Closed Drain System o4e23

CONTENTS

FLOW PLAN ABBREVIATION TABLE- sheet 1.......................................................................3 COLOR CODING...........................................................................................................................9 1.

GENERAL DESCRIPTION.........................................................................................................11 A. INTRODUCTION.................................................................................................................11 B. DUTY OF UNIT....................................................................................................................12 C. DESCRIPTION OF THE FLOW........................................................................................13 D. DESIGN BASIS.....................................................................................................................15 E. UTILITIES AND CHEMICALS-DESIGN BASIS............................................................18

2. OPERATING CONDITIONS AND CONTROLS.........................................................................21 A. HYDROCARBON DRAIN DRUM.....................................................................................21 B. C. D.

AMINE DRAIN DRUM.......................................................................................................22 HM DRAIN DRUM..............................................................................................................23 PRODUCED WATER DRAIN DISPOSAL SYSTEM......................................................25

3. EMERGENCY EQUIPMENT.........................................................................................................27 A. GENERAL.............................................................................................................................27 B. PRESSURE SAFETY VALVES...........................................................................................27 C. REMOTE OPERATED VALVES........................................................................................28 D. EMERGENCY ALARMS....................................................................................................28 E. CAR SEALED VALVES.......................................................................................................29 4. PREPARING UNIT FOR INITIAL START UP............................................................................32 A. GENERAL.............................................................................................................................32 B. PRE START UP PROCEDURES........................................................................................32 C. PREPARATION FOR START UP......................................................................................35 D. SDVs, BDVs, HCVs, PSVs....................................................................................................40 5. START UP..........................................................................................................................................42 A. GENERAL.............................................................................................................................42 B. PRELIMINARY CHECK....................................................................................................42 6. NORMAL SHUTDOWN..................................................................................................................44 A. GENERAL.............................................................................................................................44 B. SCHEDULED SHUTDOWN FOR SHORT DURATION................................................44 C. SHUTDOWN FOR MAINTENANCE................................................................................44

4.Closed Drain System

Page 1 of 154

7. EMERGENCY SHUTDOWN..........................................................................................................47 A. GENERAL.............................................................................................................................47 B. UTILITY FAILURE.............................................................................................................50 C. OTHER FAILURES.............................................................................................................52 8. MAJOR EQUIPMENT....................................................................................................................54 A. EQUIPMENT SPECIFICATIONS.....................................................................................54 B. INSTRUMENT SUMMARY.............................................................................................125 9. DRAWINGS.....................................................................................................................................132 10. SAFETY.........................................................................................................................................134 A. GENERAL...........................................................................................................................134 B. GOOD HOUSE KEEPING................................................................................................135 C. MAINTENANCE OF EQUIPMENT................................................................................135 D. USE OF SAFETY ITEMS..................................................................................................136 11. APPENDIX....................................................................................................................................138 A. CONVERSION TABLE.....................................................................................................138 B. GENERAL PRE START UP PROCEDURES..................................................................140 C. OPERATIONAL PROBLEMS – POSSIBLE CAUSES AND REMEDIES..................149 D. MISCELLANEOUS............................................................................................................153


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FLOW PLAN ABBREVIATION TABLE- sheet 1 ABBREVIATION

WHOLE WORDING

A/G

Above ground

AAH

Analyser Alarm High

AE

Analyser Element

AI

Analyser Indicator

AI

Acoustic insulation

A/M

Auto/ Manual

AT

Analyser Transmitter

AIC

Analyser Indicating Controller

ASC

Anti surge controller

ARWU AGC

Anti-reset wind up Automatic gain control

BA

Burner Alarm

BC

Burner Controller

BD

Blowdown

BDV

Blowdown Valve

BE

Burner Element

BG

Blanket gas

BRV

Breathing Valve

BI

Burner Indication

BMS

Burner Management System

BS&W

Bottom sediment and water

C

Compressor

CA

Combustion air

CC

Insulation for cold conservation

CAD

Closed amine drain

CHD

Closed Hydrocarbon drain

CSC

Car Seal Close

CSO

Car Seal Open

CC

Corrosion Coupon

CD

Continuous drainer

CG

Calibration Gauge

Corrosion Probe

CO

Carbon dioxide

CW

Cooling water


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CCR

Central control room

CVA

Choke Valve Adjustable

DF

Diesel fuel

D

Drain (HC drain, acid water)

D

Drum

DG

Diesel engine generator

DR

Drier

DT

Drain trap

DW

Potable water

DCS

Distributed Control System

E

Exchanger

EM

Elevated monitor

EH

Electric heater

EAL

Voltage Low Alarm

EI

Voltage Indicator

EL

Elevation

ET

Electric traced line


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WHOLE WORDING

ERV

Emergency relief vent

EW

Eye wash

ESD

Emergency shutdown system

FA

Flame arrester

F

Flare

F

Fired heater

FA

Fresh amine

FB

Full bore

FC

Fail closed

FG

Fuel gas

FL

Flare

FN

Fan

FM

Fixed monitor

FO

Fail open

FL

Fail locked

FW

Fire water, rain water

FAH

Flow Alarm High

FIL

Filter

FAHH FAL FALL FC FCV FE FFIC

Flow Alarm High-High Flow Alarm Low Flow Alarm Low-Low Flow Controller Flow Control Valve Flow Element Flow Ratio Indicating Controller

FG

Flow Glass

FI

Flow Indicator

FIC

Flow Indicating Controller

FM

Flow Meter

FOI

Flow Quantity Indicator (Totalizer)

FR

Flow Recorder

FRC FS FSH


Flow Recording Controller Flow Switch Flow Switch High

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FSHH

Flow Switch High-High

FSL

Flow Switch Low

FSLL

Flow Switch Low-Low

FPP

Fuel preparation

FT

Flow Transmitter

FX

Flow Straightening Vanes

GL

Glycol, MEG

GAP

Gap control

GEN

Generator

H

Heater

HB

Hose box for fire water

HD

Hydrant for fire water

HC

Insulation for heat conservation

HM

Heating medium

HBF

Hose box foam

HDF

Hydrant for foam

HMD

Heating medium drain

HIC

Hand Indicating Controller

HCV

Hand Control Valve

HOA

Hand-Off-Automatic

HS


Hand Switch

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WHOLE WORDING

HY

Hand Transducer or Function

HZ

Hand Positioner

HP Fuel Gas K LP Fuel Gas

High Pressure Fuel Gas Chemical Low Pressure Fuel Gas

IA

Instrument air

II

Current Indicator

IP

Injection point

I/P

Current to Pneumatic Converter

I/F

Interface

L

Liquid

LA

Lean amine

LO

Lube oil

LAH LAHH

Level Alarm High Level Alarm High-High

LAL

Level Alarm Low

LALL

Level Alarm Low-Low

LBV

Line break valve

LC

Level Controller

LC

Locked closed

LO

Locked open

L

Local Control

LCS

Local control station

LCV

Level Control Valve

LG

Level Gauge (Glass)

LI

Level Indicator

LIC

Level Indicator Controller

LR

Level Recorder

LRC LS LSH LSHH

Level Recorder Controller Level Switch Level Switch High Level Switch High-High

LSL

Level Switch Low

LSLL

Level Switch Low-Low


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LT

Level Transmitter

LY

Level Transducer or Function

M

Electric motor drive

MA

Motor Alarm (Fault)

MA

Mechanical agitator

MM

Mobile monitor

MCC

Motor control center

MFD

Manifold

MW

Demineralised make-up water, process water

MOV

Motor Operated Valve

MPBC

MOV Push Button Close

MPBO

MOV Push Button Open

MPBS

MOV Push Button Stop

MV

Measurement Variable

MY

MOV Logic Function

MZLC

MOV Position Indicator Light Closed

MZLO

MOV Position Indicator Light Open

MZSC

MOV Position Switch Close

MZSO

MOV Position Switch Open

N NC


Nitrogen Normally closed

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WHOLE WORDING

NNF

Normally no flow

NO

Normally open

NOC P

Net Oil Computer Pump

PA

Pressure Discrepancy Alarm

PA

Plant air

PL

Pig launcher

PP

Insulation for personnel protection

PM

Pump motor

PR

Pig receiver

PW

Produced water

PWD

Produced water drain

PAH

Pressure Alarm High

PAHH

Pressure Alarm High-High

PAL

Pressure Alarm Low

PALL

Pressure Alarm Low-Low

PB

Push Button (May be prefixed)

PBC

Push Button Close

PBO

Push Button Open

PC

Pressure Controller

PCV PD

Pressure Control Valve Pulsation Dampner

PDAH

Pressure Differential Alarm High

PDAL

Pressure Differential Alarm Low

PDC

Pressure Differential Controller

PDCV

Pressure Differential Control Valve

PDI

Pressure Differential Indicator

PDR

Pressure Differential Recorder

PDSH

Pressure Differential Switch High

PDSL

Pressure Differential Switch Low

PDT

Pressure Differential Transmitter

PI

Pressure Indicator

P/I

Pneumatic to Current converter

PIC

Pressure Indicating Controller


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PR PRC PS

Pressure Recorder Pressure Recorder Controller Pressure Switch

PSE

Bursting Disc

PSH

Pressure Switch High

PSHH

Pressure Switch High-High

PSL

Pressure Switch Low

PSLL

Pressure Switch Low-Low

PSV

Pressure Safety Valve

PP

Personnel protection

PT

Pressure Transmitter

PY

Pressure Transducer

R

Refrigerant (propane)

RA

Rich amine

RW

Raw water

RO

Restriction Orifice

RS

Removable spool

RTD

Resistance temperature detector

ROV

Remote Operated Valve

RSP

Remote setpoint


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SBY

WHOLE WORDING

Stand by

SC

Sample Connection

SE

Speed Element

SI

Speed Indicator

SO

Seal oil

SDV

Shutdown Valve

SOV

Solenoid Operated Valve

SY

Shutdown Relay

SP

Special piping

SR

Stress relieved

SP

Setpoint

SS

Safety shower

T

Tower

TK TAH TAHH

Tankage Temperature Alarm High Temperature Alarm High-High

TAL

Temperature Alarm Low

TALL

Temperature Alarm Low-Low

TC

Temperature Controller

T/C

Thermocouple

TCV

Temperature Control Valve

TE

Temperature Element

TI

Temperature Indicator

TIC

Temperature Indicating Controller

TR

Temperature Recorder

TRC

Temperature Recorder Controller

TSH

Temperature Switch High

TSO

Tight shut-off

TSHH

Temperature Switch High-High

TSL

Temperature Switch Low

TSLL

Temperature Switch Low-Low

TT

Temperature Transmitter

TV

Temperature Valve

TW

Thermowell


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TY

Temperature Transducer or Relay

UA

Common Alarm

U

Unit control

UW

Treated water, filtered water

WF

Wellhead fluid

WH

Wellhead

WW

Waste water

WV

Wing valve

WWD

Waste water drain

UASD

Common Shutdown Alarm

V VAH VAHH VE VSH VSHH X

Vent Vibration Alarm High Vibration Alarm High-High Vibration Element Vibration Switch High Vibration Switch High-High Unidentified Special Equipment

XA

Miscellaneous Alarm

XCE

Corrosion Probe Element

XCF

Corrosion Fitting

XCI

Corrosion Indicator


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WHOLE WORDING

X

Corrosion Fitting Point

XI

Miscellaneous Indicator

XPA

PIG Alarm

XPI

PIG Indicator

XPS

PIG Switch

XS

Miscellaneous Switch

XSP

Sand Probe

XSV

Solenoid Operated Valve (May be prefixed)

XV

Miscellaneous Valve

XY

Miscellaneous Transducer or Function

ZA

Position Fault Alarm

ZLC

Position Indicator Light Closed (May be prefixed)

ZLO

Position Indicator Light Open (May be prefixed)

ZSC

Position Switch Closed (May be prefixed)

ZSO

Position Switch Open (May be prefixed)

A/M

Auto / Manual

AGC

Automatic Gain Control

ARWU

Anti-Reset Wind Up

ASC

Anti Surge Controller

BS&W

Bottom Sediment And Water

CCR

Central Control Room

ESD

Emergency Shutdown System

FC

Fail Closed

FL

Fail Locked

FO

Fail Open

FPP

Fuel Preparation

GAP

GAP Control

IA

Instrument Air

I/F

Interface

LCS

Local Control Station

MCC

Motor Control Center

RTD

Resistance Temperature Detector

RSP

Remote Setpoint

SBY

Stand By


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SP

Setpoint

T/C

Thermocouple

TSO

Tight Shut-Off

U

Unit Control

May be prefixed: ABBREVIATION

LETTER DESIGNATION

B

Blowdown

F

Flow

H

Hand

L

Level

M

MOV

P

Pressure

T

Temperature

S

Shutdown

X

Miscellaneous


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COLOR CODING NO

01

02

03

04

05

FACILITY

COLOUR

COLOUR DENOMINATION PER BRITISH STANDARD BS-5252

Light Gray

BS 00 A 03

White

BS 00 E 55

Rotating equipment, electric motors, and power transformers.

Dark Gray

BS 00 A 09

Safety valves, railing, ladders and ladder cages, cranes, monorails, tail pipes, car seal valves, showers.

Yellow

BS 10 E 53

Bonnets of instrumentation control valves, instrumentation piping (where applicable).

Green

BS 14 D 43

Steel Structures, walkways, stairways and platforms, vessels, exchangers, plant piping and associated valves Tanks, including firewater tanks, stairways and platforms associated with the tank, wellheads and accessories.

06

Transmission pipelines, valves and accessories.

White

BS 00 E 55

07

Breathing apparatus station, smoking pens, water fountains.

Green

BS 14 D 43

08

Boiler stacks, bonnets of boiler superheated safety valves.

Aluminum

BS 02 A 03

09

Valve handwheels

Black

BS 00 E 53

10

Cathodic protection, transformer rectifiers, solar power units, junction boxes, groundbed casings.

White Yellow-Red (Band)

BS 00 E 55 BS 06 E 55


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11

Road barriers, specified curbs, trip hazards, width and height limits, access Black/Yellow grounds

12

Fire fighting equipment and piping (firewater tanks to be white red horizontal band)

1.

A. B. C. D. E.

Sirte Red

BS 00 E 53 BS 10 E 55

SC 127

GENERAL DESCRIPTION

INTRODUCTION……………………………………………………………………….11 DUTY OF UNIT…………………………………………………………………………12 DESCRIPTION OF THE FLOW..……………………………………….………………13 DESIGN BASIS……………………………………………….…………………………15 UTILITIES AND CHEMICALS-DESIGN BASIS……………….……….…………….18


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1. GENERAL DESCRIPTION

A. INTRODUCTION For environment protection and to recover valorous products (heating medium and amine) the plant was provided with closed drain systems. Each type of product that usually will be drained from the system was provided with a Closed Drain System. All quantity of hydrocarbons drained from the two Production Trains are collected in two separated Hydrocarbon Drain Headers (See P&ID C2-0188) and delivered to Hydrocarbon Drain Drums D-9101 and D-9201 (See P&IDs C2-0189, C2-0289). From these vessels, with pumps P-9101A/B and P9201A/B liquid hydrocarbons are pumped to LP Flare Header, and eventually gases are routed also to LP Flare Header. Each Production Train has its own Closed Amine Drain System. All amine drain points from the plant are connected to Closed Amine Drain Headers (See P&IDs C2-0148 and C2-0248). From these headers amine is routed to Amine Drain Drums D-3102 and D-3202 (See P&IDs C2-0134 and C20234). From these vessels with pumps P-3104A/B and P-3204A/B through filters FIL-3104 and FIL3204 the amine is recovered and delivered to Amine Surge Drums D-3105 / D-3205 or to Amine Storage Tank TK-3001. All quantity of drained heating medium from the system are collected in Heating Medium Drain System (See P&ID C2-0147) and delivered to Heating Medium Drain Drum D-3003 (See P&ID C20144). From this vessel with pumps P-3003A/B through FIL-3003 heating medium is returned to Heating Medium Expansion Drum D-3002 or Heating Medium Storage Tank TK-3002. Produced water separated from process and the water resulted on backwash of the filters are collected on Water Disposal System (See P&ID C2-0181).


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Waters collected are delivered to Burn Pit (See P&ID C2-0194) in order to burn all de hydrocarbons carried-over. From Burn Pit waters free of hydrocarbons are routed to Evaporation Pond where, from sun heat is evaporated.

B. DUTY OF UNIT All Closed Drain System from the Plant has the job to recover or route drain products in specific place in order to keep the stock of chemical (heating medium and amine) or to keep clean the environment by eliminated as much as possible the discharge of pollutants in the environment (hydrocarbon products). a)

Hydrocarbon Drain System

Hydrocarbon Drain System is formatted from two Hydrocarbon Drain Headers, one for each Production Train. Collected liquids are routed through those headers to Hydrocarbon Drain Drums. Hydrocarbon Drain Drums, D-9101/9201, are pumped out. Hydrocarbons drains throughout each train are routed to these drums via a header system and gas in these streams vents to the LP header on which these drums float. b)

Amine Drain System

Amine Drain System is formatted from two Amine Drain Headers, one for each Production Train. Each headers deliver collected drain amine to a separate Amine Drain Drum D-3102 / D-3202. Amine collected in those vessels can be recovered and returned into the normal circuits if its analyses after filtration (in FIL-3104, FIL-3204) are in accordance with the specifications. The water looses from the amine solution can be replaced in Amine Drain Drums with demin-water from deminwater make-up (on lines 2”-A10-MW-31014, 2”-A10-MW-32014). c)

Heating Medium Drain System

Heating Medium Drain System is formatted from a header (6”-A7-HM-30135) who collects all heating medium drained from the Heating Medium System and delivers it to Heating Medium Drain Drum D-3003.


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Recovered heating medium, if its analyses after filtration in FIL-3003 are in accordance with specification, can be reintroduced in normal circuit.

d)

Produced Water Drain System

Produced Water Drain System collect all aqueous drains from the plant and delivers it to Burn Pit. After the hydrocarbon products are separated and burnt, the aqueous flow is routed through three 6” pipes to Evaporation Pond where water is evaporated from sun heat.

C. DESCRIPTION OF THE FLOW a)


See P&IDs C2-0188, C2-0189, C2-0289 All hydrocarbons drain points from the Attahaddy Gas Plant are connected at two separated Hydrocarbon Drain Headers, one for each Production Trains (See P&ID C2-0188). The common equipments for both trains are connected to both Hydrocarbon Drain Headers (Test Separator D-2001, Heater Fuel Gas K.O. Drums D-3005A/B/C and Fuel Gas K.O. Drum D-6401). Hydrocarbon Drain Header for Production Train 1 is build up from lines 2”-A8-D-91008, 2”A8-D91009 and 3”-A8-D-91005. Hydrocarbon Drain Header for Production Train 2 is build up from lines 2”-A8-D-92013, 2”A8-D92010 and 3”-A8-D-92005. The two Drain Headers are interconnected through a 2”line with a block valve 2”VB001 but each system can be operated individually. Hydrocarbons collected into drains headers are delivered to Hydrocarbon Drain Drums D-9101 and D-9201 (See P&IDs C2-0189, C2-0289). From these vessels, on controlled level, with pumps P-9101A/B and P-9201A/B liquid hydrocarbons are pumped to HP Flare Header, and eventually gases are routed to LP Flare Header. The vessels are operated at flare pressure and they are provided with internal coils with heating medium in order to avoid wax formation. The temperature in the liquid must be maintained above the wax formation temperature (70F). The temperature can be read at local temperature indicator 910/ 920-TI-01 and can be controlled by adjusting manually the globe valves 2”VGL004 on heating medium outlet from the internal heating coils.

b)

Amine Drain System


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See P&Ids C2-0134, C2-0148, C2-0234, C2-0248 Each Production Train has its own Closed Amine Drain System. All amine drain points from the Attahaddy Gas Plant are connected to Closed Amine Drain Headers (See P&Ids C2-0148 and C20248). Amine Drain Header for Train 1 is a 6” underground line 6”-A17-RA-31146 who deliver collected drained amine to Amine Drain Drum D-3102. In this vessel are routed also the outlets from Lean /Rich Amine Exchangers E-3101A/B/C PSVs and Amine Drain Drum Filter FIL-3104 PSVs. Amine Drain Header for Train 2 is a 6” underground line 6”-A17-RA-32146 who deliver collected drained amine to Amine Drain Drum D-3202. In this vessel are routed also the outlets from Lean /Rich Amine Exchangers E-3201A/B/C PSVs and Amine Drain Drum Filter FIL-3204 PSVs. Amine Drain Drums are cylindrical horizontal underground vessels. (See P&Ids C2-0134 and C20234). From these vessels with pumps P-3104A/B and P-3204A/B through filters FIL-3104 and FIL-3204 the amine is recovered and delivered to Amine Surge Drums D-3105 / D-3205 or to Amine Storage Tank TK-3001. The two Closed Amine Drain System are not interconnected and each system can be operated individually. c)


See P&ID C2-0144 and C2-0147 All quantity of drained heating medium from the system are collected in Heating Medium Drain System (See P&ID C2-0147) and delivered through 6”-A7-HM-30135 to Heating Medium Drain Drum D-3003 (See P&ID C2-0144). Heating Medium Drain Drum D-3003 is a cylindrical horizontal vessel above ground. From this vessel with pumps P-3003A/B through FIL-3003 heating medium is returned to Heating Medium Storage Tank or Heating Medium Expansion Drum. d)


See P&ID C2-0181 and C2-0194 Produced Water and other aqueous plant streams go to the plant’s Burn Pit and then drain to an evaporation pond. Exceptionally the solids washings from the Separators go direct to a separate, smaller evaporation pond. Produced water, knocked out water and vessel or bridle drains go to the Burn Pit via a produced water header (See P&ID C2-0181). Liquid accumulations from the Flare K.O. Drum, D-9002, and waste water from the Water Treatment Plant Sump Drum, D-6501 are pumped to


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the Burn Pit also. The Burn Pit is a final oil separator, and any oil collected there is burned (See P&ID C2-0194). The water exits the pit through three 6-inch pipes with inverted bell-bottom entries at 4-inches from the pit bottom. A liquid seal piping arrangement in each drain retains a minimum level of two foot in the pit. At a level of five foot in the pit there are liquid overflows into the three drains to the evaporation pond.

D. DESIGN BASIS a)


Two independent header systems, one per train, collecting manually drained hydrocarbon condensates routed to above ground Hydrocarbon Drain Drums, D-9101 / D-9201. The collection header is on pipe rack routed to the drain drums. Drainage from equipment: i) Under normal operating conditions, all drain points are under sufficient process pressure and the hydrocarbons can easily be “blown out” to the drain header. ii) Under controlled plant shut down, plant should be blown down to flare leaving, approximately, 50 psig in the train/s to allow, if required, the remaining liquid hydrocarbons to be “blown out” to the drain header. iii) After ESD 1 trip and plant / train is at atmospheric pressure, a blanket / purge fuel gas connection is available at the inlet lines to the Test and Production Separators to allow the train/s, or Test Separator to be pressurized to, approximately 50 psig to allow any liquids to be “blown out” to the drain header. There are no continuous feeds to the drain drum. The only regular feed is an intermittent flow from the Rich Amine Flash Drum. The Hydrocarbon Drain Drum has two centrifugal pumps, which are auto-start/stop on level. The duty pump starts at high level and the second pump starts on increasing level at high-high level. Both pumps stop at low level and both pumps trip at low-low level. Pump out is to the LP flare header. From the LP flare header, the hydrocarbons are eventually, sent to the burn pit via the Flare KO Drum Pumps.


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The Drain Drum is open to the LP flare header, hence the normal operating pressure in the drum is a nominal 0.1 psig. There is a fuel gas supply, normally blinded, to the vessel which is used to completely empty the drum to the LP flare header when maintenance / vessel entry is required. The system collection piping is carbon steel, 3.0 mm corrosion allowance. b)

Amine Drain System

Two independent systems, one per train, manually drained amine solution from Unit 310 and 320. Drainage from equipment is by gravity to an underground collection header sloped to a drain drum, D3102 / D-3202 located in a pit. A separate dedicated underground line is run from auto drain line from the pre-coat filter to the Drain Drum. Above ground lines routed to the drain drum are: PSV’s discharge from filters (fire case) and the lean / rich exchangers (thermal expansion case) Demineralised water make-up line Only the underground collection header and the auto drain line from the pre-coat filter have a dip pipe in the drain drum to provide a liquid seal. Only the pre-coat filter line may have a regular, intermittent, flow every time the filter cake removed & pre-coat added. The Drain Drum has two internal submerged sump pumps which are auto-start / stop on level. The duty pump starts at high level and the second pump starts on increasing level at high-high level. Both pumps stop at low level and both pumps trip at low-low level. Pump out is via the Amine Drain Drum Filter, FIL-3104, to either back into the amine circuit at the Amine Surge Drum, to the Amine Storage Tank TK-3001 or to the evaporation pond via the produced water header. The selection of pump out routing is manual and based on regular sampling of the drum contents. A type 5 sample connection is available at each pump min flow recycle lines. The normal routing of the pump out is back into the amine circuit at the Amine Surge Drum. The Drain Drum is blanketed with fuel gas (from the treated gas supply) to avoid amine degradation in with air. The normal operating pressure in the drum is a nominal 2 psig. Above ground piping is carbon steel, 1.5 mm corrosion allowance, below ground is carbon steel wrapped, 3.0 mm corrosion allowance. All carbon steel piping and equipment are stress relieved for amine service. The minimum size for underground piping is 2”. All underground lines shall be cathodically protected complete with an insulation gasket set at the above / underground flange connection. The cover for buried lines shall be 900 mm plant area, 1000 mm under roads. c)


One common drainage system serving both process trains collects manually drained TEG heating medium solution from s. The collection header is located above ground on the pipe rack.


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Drainage from equipment is: i) ii) iii) iv)

v)

Under normal operating conditions, drain points on the expansion drum are under sufficient pressure from the blanket gas for the HM can easily be “blown out” to the drain header. The Amine Regenerator Reboilers are at a sufficient elevation to allow gravity draining to the drain drum. HM recirculation pumps, located at grade, will be “blown out” to the drain header using nitrogen from a bottle to achieve the required 10 psig. To drain down a HM heater while the other / s are in operation, the blanket gas in the HM Expansion Drum is used to “blown out” the HM to drain header. To allow this, the siphon is broken in the 10” HM recycle header line at the Expansion Drum using the 4” CSC valve and, with the header recycle MOV open, the low point drains at the heater inlet and outlet can be opened to force all the HM out. To completely drain the HM system, the HM recirculation pumps can be used to remove most of the HM, directly to the HM Storage Tank, down to LSLL trip from the Expansion Drum then use the drum blanket gas, set at a nominal 25 psig, to drain the remaining HM from the various low points to the HM Drain Drum and from there pumped to the HM Storage Tank. Alternatively, all the system can be drained solely from the low point drains with the pressure from the HM Expansion Drum blanket gas, but this will take longer and all the flow to the storage tank will be via HM Drain Drum which does gives the option of either filtering the HM before storage, or, dumping the inventory to the evaporation pond via the produced water header. In both cases the 4” CSC siphon break valve at the 10” HM recycle line on the Expansion Drum needs to be opened, as well as the heater recycle MOV’s, to allow vapour to replace the drained liquid.

There are no continous or intermittent feeds to the drain drum. Additional lines to the drain drum are: -

PSV discharge lines from filters (fire case) and the fired heaters (thermal expansion relief) - Demin water make-up line Only the header collection line and the line from PSV’s have a dip pipe in the drain drum to provide a liquid seal. The Drain Drum has two internal submerged sump pumps which are auto-start / stop on level. The duty pump starts at high level and the second pump starts on increasing level at high-high level. Both pumps stop at low level and both pumps trip at low-low level. Pump out is via the HM Drain Drum Filter, Fil-3003, to either back into the HM circuit at the HM Expansion Drum, to the HM Storage Tank TK-3002 or to the evaporation pond via the produced water header. The selection of pump out routing is manual and based on regular sampling of the drum contents. A type 6 sample connection is


Page 23 of 154

available at each of the pump min flow recycle lines. The normal routing of the pump out is back into the HM circuit at the HM Expansion Drum. The Drain Drum is blanketed with fuel gas (from the treated gas supply) to avoid HM absorption of water from atmosphere when in with air. The normal operating pressure in the drum is a nominal 2 psig. The system piping is carbon steel, 1.5 mm corrosion allowance. d)


The produced water drain collection header system is in three isolatable sections, Train 1, Train 2 and common areas and routed for disposal to the burn pit before being siphoned off to the evaporation pond. The PWD collection headers are all under ground. The headers collect: produced water from various sources washings from the HM and amine drain drum filters if either HM or amine is off-spec in their respective drain drums, contents can be sent to PWD The only continuous flow to the PWD is produced water from units U200 / 210 / 220. All others are NNF or intermittent. The entry into the burn pit is below the water level to provide a liquid seal. Normally, all inputs to the PWD are under pressure and no requirement to “blow out” liquids. During train / s shut down and plant at atmospheric pressure, drainage from equipment is by using the blanket /purge gas at the inlet to U200 / 210 / 220 to “blow out” the liquids to the PWD header in the same manner as hydrocarbons are sent to CHD. Refer item (iii) in CHD section. The above ground piping material for produced water service is duplex stainless steel on the high pressure sides and, for waste liquids other than produced water, the appropriate piping class of the liquid. All the underground sections are in GPR (RTR) for the low pressure collection header line to the burn pit. The last 25 ft is in duplex stainless steel for heat and corrosion resistance. The minimum cover for buried lines shall be 900 mm plant area, 1000 mm under roads.

E. UTILITIES AND CHEMICALS-DESIGN BASIS Instrument / Plant Air Instrument Air and Plant Air are produced in Unit 630. Plant Air is delivered in Plant Air Header from Plant Air Receiver D-6301. Instrument Air goes to distribution from Instrument Air Receiver D-6302. Specification:


Page 24 of 154

-

Dew point Particle size Pressure Pressure

-20F at 125 psig less than 5 microns (for instrumental air) 130 psig (for plant air) 125 psig (for instrument)

Electric Power Electric Power is produced in Unit 800 (GTG-8001A and GTG-8001B) or could be imported from external sources. Specifications: Frequency Voltage grade:

60 Hz 3 ph, 13.8 kV 3 ph, 4.16 kV 3 ph, 480 V 3 ph, 208 / 120 V

Blanket Gas Blanketing is used to maintain pressure in Heating Medium Storage Tank (TK-3002) and the Heating Medium Expansion Drum (D-3002). This is supplied from the export gas header because of the relatively high CO2 content of the Condensate Flash Drum gas. The blanket gas is supplied under pressure control from the pressure controller (640-PIC-11) located downstream of the pressure control valve (640-PCV-11). The required pressure for Blanket Gas is 135 psig. Demineralized Water Demineralized water is produced in Unit 650. Specification: Supply pressure Chloride Sulphate (SO4) Conductivity Suspended Solids Particle size

50 psig Max. 30 ppmw Max. 0.1 ppmw Max. 5.0 micro s/cm@20C 10 mg/l Max. 10 microns

Nitrogen N2


Page 25 of 154

-

Degree of Purity:

2.

A. B. C. D.

over 98%

OPERATING CONDITIONS AND CONTROLS

HYDROCARBON DRAIN DRUM…………………………………………………………21 AMINE DRAIN DRUM……………………………………………………….…………….22 HM DRAIN DRUM…………………………………………………….……………………23 PRODUCED WATER DRAIN DISPOSAL SYSTEM……………………………..……….25


Page 26 of 154

2. OPERATING CONDITIONS AND CONTROLS A. HYDROCARBON DRAIN DRUM See P&ID’s C2-0189 and C2-0289 There is a closed hydrocarbon drain header for each train, routed to dedicated Hydrocarbon Drain Drums (D-9101/9201); one for each processing trains. The Hydrocarbon Drain Drum D-9101/D-9201 is designed to operate at LP Flare pressure through a breather line to the LP Flare Header. This design ensures that low operating pressure equipment can discharge hydrocarbons to the hydrocarbon drain system. The liquids from the Hydrocarbon Drain Drums are pumped to the LP Flare Header using duty/standby electric motor driven Hydrocarbon Drain Drum Pumps (P-9101A/B and P-9201A/B). The pumps are start/stop from high and low level switches on the Hydrocarbon Drain Drums (910/920-LSH-01 and 910/920-LSL-01). The spare pump is started on high high level (910-LSHH01) in case of continuing rising level. A high-high-high level alarm is raised in the DCS (910-LI-01) indicating the pumps failed to start. Minimum flow recycle lines, with restriction orifices (910/920RO-01A & B), are provided back to each Hydrocarbon Drain Drum. A drum level indicator (910/920LI-01) is provided in the control room. If the liquid level falls to a low low liquid level (910-LSLL-01) the ESD system will trip the pumps and alarm in the control room. Table 1.A shows setpoints and alarm level for principal parameters of Hydrocarbon Drain System.


Page 27 of 154

TABLE 1.A P&ID

TAG/

PROC.

LOOP NO

UNITS

DCS RANGE

% OF RANGE, SETPOINT &

(0-XXX)

ALARMS Setpoint

C2-0189 910-LI-01

"WG

C2-0189 910-LAL-01

"WG

C2-0189 910-LAH-01

"WG

C2-0289 920-LI-01

"WG

C2-0289 920-LAL-01

"WG

C2-0289 920-LAH-01

"WG

45" @ 0.68

REMARKS

High

Low

50" (HHH)

9" 9" @ 0.68

12" @ 0.68 45" @ 0.68

50" (HHH)

9" 9" @ 0.68

12" @ 0.68

B. AMINE DRAIN DRUM See P&ID’s C2-0134, C2-0234 This section refers to equipment and instrument tag numbers for train #1 only. Train #2 tag numbers are pre-fixed with the digits 320 rather than 310. The manually drained amine from the various locations within the amine system is collected in each header and routed to the Amine Drain Drum (D-3102). Each train has it's own dedicated Drum. The Drum is installed in a pit below grade to enable all equipment and piping to be drained at atmospheric pressure. The amine is recovered from the Drum via an Amine Drain Drum Filter (FIL-3104), to the Amine Surge Drum (D-3105) using submersible Amine Drain Drum Pumps (P-3103A/B). The duty pump (P3103 A or B) is start/stop from the high and low liquid level switches (310-LSH-14) and (310-LSL13). In the event that liquid level still rises, the high high level switch (310-LSHH-14) starts the standby pump (P-3103A or B). A high high high level alarm is provided from the level indicator (310LI-13/1) to indicate that (P-3103A and/or B) are not operating. A local differential pressure indicator (310-PDI-09) is located across the inlet and outlet of the Amine Drain Drum Filter to enable periodic monitoring of any plugging of the filter internals. Overpressure protection on the Filter is provided by relief valves (310-PSV-15/16) routed back to the Amine Drain Drum.


Page 28 of 154

The Drum is blanketed with blanket gas under pressure control (310-PIC-03/1 and 03/2). The pressure controllers also provide high and low pressure alarms in the control room. Blanket gas from the Drum is routed to the LP flare header. Overpressure protection on the Drum is provided by relief valves (310-PSV-17/18), also relieving to the LP flare header. A minimum flow recycle line is provided back to the Drum, at the discharge of each pump. A separate low low level switch (310-LSLL-13) is installed on the Drum providing a signal to the ESD system to trip the pumps. To backwash the Amine Drain Drum Filter FIL-3104 proceed as described below: Isolate filter by closing 3”VG005 on line 3”-A17-RA-31028 and 3”VG005 on line 3”-A17RA-31043 (near filter). Open 2”VG005 on line 2”-A17-RA-31072 (on filter lid). Open slowly 2”VG008 on line 2”-A10-MW-31017 and backwash filter. From time to time open slowly vent valve 1”VG039 on 2”-A17-RA-31072 and see the water -

aspect. When water is clean close 2”VG008 on line 2”-A10-MW-31017. To drain filter open 2”VG005 on line 2”-A17-RA-31071.

Table 1.B shows setpoints and alarm level for principal parameters of Amine Drain System. TABLE 1.B P&ID

TAG/

PROC.

LOOP NO

UNITS

DCS RANGE (0-XXX)

% OF RANGE, SETPOINT & ALARMS Setpoint

High

Low

30" @1.02

42"/50"

24"

C2-0134 310-LI-13/1

"WG

C2-0134 310-LAL-13

"WG

C2-0134 310-LAHH-14

"WG

42" @1.02

C2-0134 310-LAH-14

"WG

36" @1.02

C2-0134 310-PIC-03/1

psig

50

1.5

3

0

C2-0134 310-PIC-03/2

psig

50

2.5

4

0

C2-0234 320-LI-13/1

"WG

30" @1.02

42"/50"

24"

C2-0234 320-LAL-13

"WG

C2-0234 320-LAHH-14

"WG

42" @1.02

C2-0234 320-LAH-14

"WG

36" @1.02

C2-0234 320-PIC-03/1

psig

50

1.5

3

0

C2-0234 320-PIC-03/2

psig

50

2.5

4

0


24" @1.02

24" @1.02

Page 29 of 154

REMARKS

C. HM DRAIN DRUM See P&ID C2-0144. One common drainage system serving both process trains collects manually drained TEG heating medium solution from s and routed to the Heating Medium Drain Drum (D-3003). The Drum is located above ground. There are no continuous or intermittent feeds to the Drain Drum. Additional lines to the drain drum are: -

PSV discharge lines from filters and the fired heaters (thermal expansion relief). Demin water make-up line (provides flexibility for diluting the HM solution concentration if necessary).

The Drain Drum is blanketed with fuel gas supplied through line 2”-B6-BG-30018 to avoid HM absorption of water from the atmosphere when in with air. Pressure in D-3003 is controlled by 300-PIC-04/2 acting on 300-PCV-04/2 to discharge to LP Flare on pressure increase and by 300-PIC04/1 acting on 300-PCV-04/1 to introduce fuel gas on pressure decrease; low and high pressure alarms are also provided on DCS. Overpressure protection of the drum is provided by relief valves (300-PSV07 / 08), relieving to the LP flare header. The normal operating pressure in the drum is a nominal 2 psig. Heating Medium Drain Drum D-3003 is equipped with the following: Level transmitter 300-LT-02 with indication 300-LI-02/1, high level alarm on DCS and local indication 300-LI-02. Low level switch 300-LSL-013 provides low level alarm 300-LAL-13 on DCS and stop signal for P-3003A/B pumps. Low low level switch 300-LSLL-13 provides low low level alarm 300-LALL-13 on DCS and trip signal for P-3003A/B pumps. High level switch 300-LSH-03 provides high level alarm 300-LAH-03 on DCS and start signal to P-3003 (duty pump). High high level switch 300-LSHH-03 provides high high level alarm 300-LAHH-03 on DCS and start signal to P-3003 (stand-by pump). Local pressure indicator 300-PI-11. Local temperature indicator 300-TI-16. The Drain Drum has two internal submerged sump pumps which are auto-start / stop on level. The duty pump starts at high level (300-LSH-03) and the second pump starts on increasing level at highhigh level (300-LSHH-03). Both pumps stops at low level (300-LSL-13) and both pumps trip at lowlow level. Pump out is via the HM Drain Drum Filter, FIL-3003, either back into the HM circuit at the HM Expansion Drum through 3”-A7-HM-30078, to the HM Storage Tank TK-3002 through 3”-A7-


Page 30 of 154

HM-30076 or to the evaporation pond through 2”-A7-HM-30132 via produced water header. The selection of pump out routing is manual and based on regular sampling of the drum contents. A Type 6 sample connection is available at each of the pump min flow recycle lines. The normal routing of the pump out is back into HM circuit at the HM Expansion Drum. Ensure that one pump out route is always available (because the pumps start automatically). A local differential pressure indicator (300-PDI-01) is located across the inlet and outlet of the Heating Medium Drain Filter FIL –3003 to enable periodic monitoring of any plugging of the filter internals. Overpressure protection on the filter is provided by relief valves (300-PSV-05 / 06) routed back to the Heating Medium Drain Drum. HM Drain Filter FIL –3003 is used for trap all particles greater than 10 microns from heating medium. The differential pressure across the filter should be monitored (300-PDI-01), and when it reaches 10.0 psig the filter should be taken off line and the cartridges replaced. Before remove the cartridges the filter will be taken off line, backwash with demineralized water and depressurized. To backwash the HM Filter Drain FIL-3003 proceed as described below: -

Isolate filter by closing 3”VG004 on line 3”-A7-HM-30065 and 3”VG004 on line 3”-A7-HM30078 (near filter). Open 2”VG004 on line 2”-A7-HM-30131 (on filter lid). Open slowly 2”VG008 on line 2”-A10-MW-30010 and backwash filter. From time to time open slowly vent valve 1”VG034 on 2”-A7-HM-30131 and see the water aspect. When water is clean close 2”VG008 on line 2”-A10-MW-30010. To drain filter open 2”VG004 on line 2”-A7-HM-30132.

Table 1.C shows setpoints and alarm level for principal parameters of Heating Medium Drain System. TABLE 1.C P&ID

TAG/

PROC.

LOOP NO

UNITS

DCS RANGE (0-XXX)

% OF RANGE, SETPOINT & ALARMS Setpoint

High

Low

C2-0144 300-LI-02/1

"WG

C2-0144 300-LAH-03

"WG

36" @1.05

36"

C2-0144 300-LAHH-03

"WG

42" @1.05

42"

C2-0144 300-LAL-13

"WG

18" @1.05

C2-0144 300-PIC-04/1

psig

20

1.5

3

0

C2-0144 300-PIC-04/2

psig

20

2.5

4

0


50"

Page 31 of 154

18"

REMARKS

D. PRODUCED WATER DRAIN DISPOSAL SYSTEM See P&IDs C2-0181; C2-0194 One common drainage system serving both process trains collects drained produced water from sources and routed to the Burn Pit. All aqueous flows drained from the whole plant, automatic or manual, are collected and deliver to Burn Pit through one 10” header. With produced water in Burn Pit are collected also the waste waters from Waste Water Sump Pump P-6503 A / B and liquids component comes from Flare K.O. Drum Pumps P-9002 A / B / C. The Burn Pit is a final oil separator, and any oil collected there is burned. The water exits the pit through three 6-inch pipes with inverted bell-bottom entries at 4-inches from the pit bottom. A liquid seal piping arrangement in each drain retains a minimum level of two foot in the pit. At a level of five foot in the pit there are liquid overflows into the three drains to the evaporation pond. Test Separator D-2001 and Production Separators D-2101 / D-2201 are provided also with separated lines for sand removal. Those lines conduct the mixture of water and sand near burn pit in a special evaporation pond and they are used only from time to time to eliminate the sand collected in inlet separators. Sediment/sand removal is incorporated in the production and test separators design to avoid the need to shut them down for the solids removal.

3.


EMERGENCY EQUIPMENT

Page 32 of 154

A. B. C. D. E.

GENERAL………………………………………………………………………………27 PRESURE SAFTY VALVES…………………….……………………………………..27 REMOTE OPERATED VALVES………………………………………………………28 EMERGENCY ALARMS………………………………………………………………28 CAR SEALED VALVES…………………….………………………………………….29

3. EMERGENCY EQUIPMENT A. GENERAL To ensure safe operation and to protect the unit equipment some emergency devices are provided. Vessels are provided with pressure relief valves in order to avoid overpressure. Other safety devices provided are Car Seals for valves and Emergency Alarms.

B. PRESSURE SAFETY VALVES Pressure Safety Valves for Hydrocarbon Drain System No Pressure Safety Valves are in this system. Pressure Safety Valves for Amine Drain System TAG NO.


SET

INLET

Page 33 of 154

OUTLET

Unit

Type

Serial

P&ID NO.

PRESSURE

Line No.

Size

Line No. Size

PSIG 310

PSV

15

C2-0134

130

1"-A17-RA-31051

1’’

2"-A17-RA-31067

2’’

310

PSV

16

C2-0134

130

1"-A17-RA-31052

1’’

2"-A17-RA-31068

2’’

310

PSV

17

C2-0134

50

4"-A17-BG-31022

1 ½’’

3"-A9-F-31028

3’’

310

PSV

18

C2-0134

50

4"-A17-BG-31023

1 ½’’

3"-A9-F-31033

3’’

320

PSV

15

C2-0234

130

1"-A17-RA-32051

1’’

2"-A17-RA-32067

2’’

320

PSV

16

C2-0234

130

1"-A17-RA-32052

1’’

2"-A17-RA-32068

2’’

320

PSV

17

C2-0234

50

4"-A17-BG-32022

1 ½’’

3"-A9-F-32028

3’’

320

PSV

18

C2-0234

50

4"-A17-BG-32023

1 ½’’

3"-A9-F-32033

3’’

Pressure Safety Valves for Heating Medium Drain System TAG NO. Unit

Type

SET Serial

P&ID NO.

INLET

PRESSURE

OUTLET

Line No.

Size

Line No. Size

PSIG 300

PSV

05

C2-0144

190

1 ½ "-A7-HM-30071

1’’

2"-A7-HM-30074

2’’

300

PSV

06

C2-0144

190

1 ½ "-A7-HM-30072

1’’

2"-A7-HM-30073

2’’

300

PSV

07

C2-0144

50

3"-A7-BG-30022

1 ½’’

4"-A9-F-30007

3’’

300

PSV

08

C2-0144

50

3"-A7-BG-30023

1 ½’’

4"-A9-F-30011

3’’

Pressure Safety Valves for Produced Water Drain System No Pressure Safety Valves are in this system.

C. REMOTE OPERATED VALVES Remote Operated Valves for Hydrocarbon Drain System No Remote Operated Valves are in this system. Remote Operated Valves for Amine Drain System TAG NO.

P&ID NO.

Unit

Type

Serial

310

PCV

03/1


LINE NO.

SIZE

RATING

REMARKS SETPOINT

C2-0134

2"-B6-BG-31025

Page 34 of 154

1"

300#

310

PCV

03/2

C2-0134

2"-A17-BG-31028

1 ½"

300#

320

PCV

03/1

C2-0234

2"-B6-BG-32025

1"

300#

320

PCV

03/2

C2-0234

2"-A17-BG-32028

1 ½"

300#

Remote Operated Valves for Hydrocarbon Drain System No Remote Operated Valves are in this system. Remote Operated Valves for Produced Water Drain System No Remote Operated Valves are in this system.

D. EMERGENCY ALARMS Emergency Alarms for Hydrocarbon Drain System TAG/ P&ID

LOOP NO

ESD PROC. UNITS

RANGE

PROC

REMARKS

(0-XXXX)

C2-0189 910-LALL-01

"WG

6" @ 0.68

Primary device located on D-9101

C2-0189 910-LAHH-01

"WG

41" @ 0.68


C2-0289 920-LALL-01

"WG

6" @ 0.68


C2-0289 920-LAHH-01

"WG

41" @ 0.68


Emergency Alarms for Amine Drain System TAG/ P&ID

LOOP NO

ESD PROC. UNITS

RANGE

PROC

REMARKS

(0-XXXX)

C2-0134 310-LALL-13

"WG

12" @1.02

310-P-3104A/B trip

C2-0234 320-LALL-13

"WG

12" @1.02

320-P-3104A/B trip

Emergency Alarms for Heating Medium Drain System TAG/ P&ID

LOOP NO

ESD PROC. UNITS


RANGE

PROC

(0-XXXX)

Page 35 of 154

REMARKS

C2-0144 300-LALL-13

"WG

12" @1.05

Fuel gas to HM heater

Emergency Alarms for Produced Water Drain System No Emergency Alarms are in this system.

E. CAR SEALED VALVES Car Sealed for Hydrocarbon Drain System Tag No.

P&ID No.

Line No.

Unit

Type

Serial

200

CSO

55

C2 – 0188

D – 20002

200

CSO

56

C2 – 0188

D - 20005

300

CSO

48

C2 – 0188

D – 30012

300

CSO

49

C2 - 0188

D - 30013

640

CSO

08

C2 – 0188

D – 64002

640

CSO

09

C2 - 0188

D - 64003

910

CSO

02

C2 - 0189

D – 91001

910

CSO

03

C2 - 0189

D – 91002

910

CSO

04

C2 - 0189

F - 91001

920

CSO

02

C2 - 0289

D – 92001

920

CSO

03

C2 - 0289

D – 92002

920

CSO

04

C2 - 0289

F - 92001

Remarks

Car Sealed for Amine Drain System Sheet 1 Tag No.

P&ID No.

Line No.

Unit

Type

Serial

310

CSO

84

C2 – 0134

RA – 31044

310

CSO

85

C2 – 0134

RA – 31045

310

CSO

86

C2 – 0134

BG – 31022

310

CSO

87

C2 – 0134

F – 31033

310

CSO

88

C2 – 0134

F – 31028

310

CSO

90

C2 – 0134

RA – 31052

310

CSO

91

C2 – 0134

RA – 31067

310

CSO

92

C2 – 0134

RA – 31068

310

CSC

17

C2 – 0134

BG – 31023


Page 36 of 154

Remarks

310

CSC

18

C2 – 0134

RA – 31051

320

CSO

84

C2 – 0234

RA – 32044

320

CSO

85

C2 – 0234

RA – 32045

320 CSO 86 C2 – 0234 Car Sealed for Amine Drain System Sheet 2 Tag No.

BG – 32022

P&ID No.

Line No.

Unit

Type

Serial

320

CSO

87

C2 – 0234

F – 32033

320

CSO

88

C2 – 0234

F – 32028

320

CSO

90

C2 – 0234

RA – 32052

320

CSO

91

C2 – 0234

RA – 32067

320

CSO

92

C2 – 0234

RA – 32068

320

CSC

17

C2 – 0234

BG – 32023

320

CSC

18

C2 – 0234

RA – 32051

Remarks

Car Sealed for Heating Medium Drain System Tag No.

P&ID No.

Line No.

Unit

Type

Serial

300

CSO

29

C2 - 0144

HM – 30072

300

CSO

30

C2 - 0144

HM – 30074

300

CSO

31

C2 - 0144

HM – 30073

300

CSO

32

C2 - 0144

HM – 30106

300

CSO

33

C2 - 0144

HM – 30068

300

CSO

34

C2 - 0144

BG – 30022

300

CSO

35

C2 - 0144

F – 30011

300

CSO

36

C2 - 0144

F – 30007

300

CSC

14

C2 – 0144

HM – 30071

300

CSC

15

C2 – 0144

BG – 30023

Remarks

Car Sealed for Produced Water Drain System Tag No.

P&ID No.

Line No.

Unit

Type

Serial

900

CSO

01

C2 – 0181

PW – 90005

900

CSO

02

C2 – 0181

PW – 90006

900

CSO

03

C2 – 0181

PW – 90002

900

CSO

04

C2 – 0181

PW – 90007


Page 37 of 154

Remarks

4.

PREPARING UNIT FOR START-UP

A GENERAL…………………………………………………….……………………..32 B. PRE START-UP PROCEDURE FOR……………………………………………….32 C. PREPARATION FOR START UP…………………………………………………..35 D. SDVs, BDVs, HCVs, PSVs…………………………………………………………..40


Page 38 of 154

4. PREPARING UNIT FOR INITIAL START UP A. GENERAL The normal start-up presupposes the Closed Drains System contains only air and has not been checked for leaks. This will be the case at the first start-up and for those after maintenance turnarounds. The main steps in the initial start-up of the Closed Drain Systems are the following:    



Check all blinds and car seals are placed in their operating position as per the P&ID’s. Refer to 3.E for Car Seal Schedules. Open valves for all instruments, level bridles, level gauges, instrument switches and analysers. Close all in line valves vents and drains. Some of the blind and car seal positions may require changing short term for preparations but it is most desirable to keep them in their operating position. Log any deviations as they are made for later correction. Check pumps and fans have their guards in place, are lubricated and free to rotate and bump start each pump before re-closing their MCC breakers.

Perform the following:     

Calibrate all instruments and analysers. Check all alarms. Check control valves stroke with controllers and check controller override switches trip the valves per trip setting. Witness (at the valve location) all trips by instrument switches. Check PBCs, PBOs, ESDs 1, 2 trips, witness at the valve location

Place all level controllers at 50% setpoints on auto and all pressure and temperature controllers at their setpoints on auto. Place all flow controllers on manual at minimum settings.


Page 39 of 154

B. PRE START UP PROCEDURES

a) b) c) d) e)

Pre-Start-Up procedure: Carry out vessels final inspection. Properly close up all vessel manholes and openings after final inspection. Issue Vessel Closure Certificates. Inert the system with nitrogen. Carry-out leak testing. - Hydrocarbon Drain System Draining and Purging Prior to introducing in operation the system, all water has to be drained and the system purged.    -

3”-A8-D-91005 D-9101 4”-A8-D-91011 (4”-A8-D-91012)P-9101A (P-9101B)  3”A8-D-91003 (3”-A8-D-91004) LP Flare Header and D-9101  3”-A8-F-91001 LP Flare Header For Train 1 3”-A8-D-92005 D-9201 4”-A8-D-92011 (4”-A8-D-92012)P-9201A (P-9201B)  3”A8-D-92003 (3”-A8-D-92004) LP Flare Header and D-9201  3”-A8-F-92001 LP Flare Header For Train 2  

    -

Drain water from all low points of equipment and lines Close valves on Fuel Gas Line up the following circuits concerning the hydrocarbon drain system:

Close all vents and drains. Connect a nitrogen cylinder on a vent line and pressure the system with nitrogen. Observe pressure increase in the system. When pressure reaches 30 psig close the nitrogen cylinder. Check for leaks from flange, valves, and so forth. Depressurize the system through the drains of lines and equipment. Continue pressuring / depressurizing the system until the oxygen content of samples taken from various points from the system indicate less than 2%. Pressurize the system at 20 psig and disconnect nitrogen cylinder.

Amine Drain System


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This section refers to equipment and instrument tag numbers for train #1 only. Train #2 tag numbers are pre-fixed with the digits 320 rather than 310. Draining and Purging Prior to introducing in operation the system, all water has to be drained and the system dried and purged.    -

Drain water from all low points of equipment and lines Close valves on Blanket Gas Line up the following circuits concerning the amine drain system:

6”-A7-RA-31146 D-3102 3”-A17-RA-310363”-A17-RA-31038 FIL-31043”A17-RA-31043  

   

Close all vents and drains after drain all water from the system. Connect a nitrogen cylinder on a vent line and pressure the system with nitrogen. Observe pressure increase in the system. When pressure reaches 30 psig close the nitrogen cylinder. Check for leaks from flange, valves, and so forth. Depressurize the system through the drains of lines and equipment. Continue pressuring / depressurizing the system until the oxygen content of samples taken from various points from the system indicate less than 2%. Pressurize the system at 20 psig and disconnect nitrogen cylinder.

- Heating Medium Drain System Draining and Purging Prior to introducing in operation the system, all water has to be drained and the system dried and purged.    -

Drain water from all low points of equipment and lines Close valves on Blanket Gas Line up the following circuits concerning the amine drain system:

6”-A7-HM-30135 6”-A7-HM-30135 D-3003 

Close all vents and drains after drain all water from the system.


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

    -

Connect a nitrogen cylinder on a vent line and pressure the system with nitrogen. Observe pressure increase in the system. When pressure reaches 30 psig close the nitrogen cylinder. Check for leaks from flange, valves, and so forth. Depressurize the system through the drains of lines and equipment. Continue pressuring / depressurizing the system until the oxygen content of samples taken from various points from the system indicate less than 2%. Pressurize the system at 20 psig and disconnect nitrogen cylinder.

Produced Water Drain System Prior to introducing in operation the system must be verified for leakage.   

Line up the circuits concerning the produced water drain system by ing that 900CSO-01, 900-CSO-02, 900-CSO-03, 900-CSO-04 are in the right position (Open). Close all drains valves. Check for leakages from flange, valves, and so forth.

C. PREPARATION FOR START UP - Hydrocarbon Drain System Hydrocarbon Drain Drum Pump P-9101 A, B and P-9201 A, B Operating Precautions DO NOT CLEAN PUMP IN THE VICINITY OF ROTATING PARTS WHEN PUMP IS OPERATING. IF UNUSUAL NOISE OR VIBRATIONS OCCUR, SECURE PUMP AS SOON AS POSSIBLE. 1. Never operate the pump with suction valve closed. 2. Never operate the pump with the discharge valve closed. 3. Never operate the pump unless it is completely filled with liquid and vented. 4. Never operate the pump unless an adequate liquid source is available. 5. Never operate the pump on liquids other than the one specified on the pump data sheet. Pre-Operational Checks


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The followings steps should be followed at initial start up and after the equipment has been overhauled: 1. Prior to installing the pump, flush the suction side of the system to remove all deposit (slag, bolts etc.) 2. Ensure the pump and piping is clean. Before putting the pump into operation, the piping should be thoroughly back flushed to remove any foreign matter, which may have accumulated during installation. Take all possible care not to contaminate the system. 3. Install suction strainer. 4. Fill the bearing housing with the appropriate oil to the correct level. Bearing must receive a small amount of oil prior to starting to ensure adequate lubrication at start up. 5. Turn pump rotor by hand or with a strap wrench to make sure it turns smoothly. 6. Assure that correct seal piping has been installed and has not been damaged. 7. Prior to coupling installation, bump start motor to check for correct rotation. If rotation is not correct refer to motor manual for appropriate connections to change rotation (Shut down all power prior to change). 8. Ensure coupling is correctly aligned and lubricated, and pump and driver are satisfactorily dowelled. 9. Ensure coupling guard is correctly installed. THE UNIT MUST NOT BE OPERATED UNLESS COUPLING GUARD IS SECURELY AND COMPLETELY BOLTED IN PLACE. FAILURE TO OBSERVE THE WARNING COULD RESULT IN INJURY TO OPERATING PERSONNEL. 10. Check torque of all bolting and plugs for tightness. Initial Start Up Procedure 1. Close discharge valve if valve is not already closed, and then crack open to assure minimal flow. (Do not start unit with fully closed valve). On first starts care must be taken not to cause a system water hammer. 2. Prepare the driver for start up in accordance with the driver manufacturer’s instructions. 3. Warm up pump. Avoid severe thermal shocks to the pump as the result of sudden liquid temperature changes. The pump must be preheated prior to start up. Unless otherwise specified the thermal temperature of casing must be within 100 degree F (55C) of the temperature of the liquid to be pumped at time of start up. Due to the heavy metal sections, the casing will lag the liquid temperature during such changes, and severe temperature stresses and subsequent misalignment of machined fits may result. Preheating is accomplished by circulating a small


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amount of hot fluid through the casing by utilizing vents, drains or by from discharge. Preheat pump slowly at a rate not to exceed 100 degrees F per hour (55C per hour). 4. Prime pump and ensure suction valve is open. BEFORE STARTING OR WHILE OPERATING THE PUM, THE CASING AND SUCTION LINE MUST BE COMPLETELY FILLED WITH THE LIQUID BEING PUMPED. THE ROTATING PARTS DEPEND ON THIS LIQUID FOR LUBRICATION AND THE PUMP MAY SEIZE IF OPERATED WITHOUT LIQUID. 5. Ensure pump recirculating line is open, clear and free of obstructions. 6. Check that pump is vented by observing leakage from casing vent (when fitted) and seal piping vent. Close vent when liquid is emitted. 7. Turn on cooling liquid and assure correct flow exists (to cooler, insert gland etc.) as specified. 8. Double check pump rotation by starting unit momentarily. The direction of input shaft rotation is counter clockwise when facing pump shaft from coupling end. Ensure that the pump coasts to a gradual stop. IF PUMP STOP ABRUPTLY WHEN DRIVER IS SHUT DOWN, INVESTIGATE FOR PUMP BINDING. TAKE NECESSARY REMEDIAL ACTION BEFORE RESUMING OPERATION. 9. Start the driver and bring it up to speed quickly. 10. As soon as the pump is up to rated speed slowly open discharge valve. This will avoid abrupt changes in velocity and prevent surging in the suction line. 11. Perform the operating checks. Operating checks IN THE INTEREST OF OPERATOR SAFETY THE UNIT MUST NOT BE OPERATED ABOVE THE NAMEPLATE CONDITIONS. SUCH OPERATIONS COULD RESULT IN UNIT FAILURE CAUSING INJURY TO OPERATING PERSONNEL. Immediately after start up, and frequently during running check the following: 1. 2. 3. 4. 5.

Check suction and discharge pressure gauges. Check pressure gauges on each side of suction strainer. Check for excessive leakage at seal areas. Check for unusual noises. Check oil level in bearing housing.


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OPERATION OF THE UNIT WITHOUT CORRECT LUBRICATION CAN RESULT IN OVERHEATING OF THE BEARINGS, BEARING FAILURES, PUMP SEIZURES AND ACTUAL BREAKUP OF THE EQUIPMENT EXPOSING OPERATING PERSONNEL TO PHYSICAL INJURY. 6. Check for adequate flow of cooling liquids. 7. After unit has been operated a sufficient length of time to reach normal operating temperature and condition, the unit is to be shut down and a “HOT” coupling alignment check must be made.

- Amine Drain System Amine Drain Drum Pump P-3104 A, B and P-3204 A, B Actions before Start-up: i. ii. iii. iv. v. vi.

For the first start-up of the pump, check the proper installation of the equipment. The suction tank must be filled with liquid. The minim liquid level is 50 mm above pump. The discharge valve of the pump shall be closed. The thrust bearing must be properly lubricated. Check the shaft seal. Check the alignment of the pump and driver combination and the sense of rotation of the driver. vii. It must be possible to turn the rotor by hand without any restriction. viii. All ts of the auxiliary piping must be tight. Especially tighten carefully all stainless compression fittings! Open all valves in the flushing lines and check the flow. Action during start-up: CAUTION: DO NOT OPERATE THE UNIT UNLESS SAFETY GUARD OR DEVICE ARE IN PLACE AND PROPERLY ADJUSTED! i. ii.

Start the driver for a few seconds. Watch the sense of rotation and the smooth slowing down of the rotor. Start the driver and operate the pump for 20 sec. against closed valve. Check the reading of the pressure gauge. If the pump does not deliver rated pressure, stop the pump immediately. If it is working properly, open the discharge valve very slowly, until the requested head is reached. Do not operate the pump with closed discharge valve for more than 30 sec. as the pump will overheat and may damage the main line bearing and the


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iii.

iv. v. vi.

impeller. If the pump is taking over service from another pump, both pumps running in parallel for short time, close the discharge valve of the other pump now. Check the performance of the Minimum Flow By. The flow through the by- line can be heard, with boiler feed service the by line will warm up. If the minimum flow by is working properly, there is no objection against longer operation with closed discharge valve. After some time of running, check temperature and lubrication of the thrust bearings. Check vibrations of the pump and the pipings. Check the shaft sealing: A mechanical seal must be absolutely tight, a packed stuffing box requires some leakage.

- Heating Medium Drain System Heating Medium Drain Drum Pump P-3003 A, B Actions before Start-up: i. For the first start-up of the pump, check the proper installation of the equipment. ii. The suction tank must be filled with liquid. The minim liquid level is 50 mm above pump. iii. The discharge valve of the pump shall be closed. iv. The thrust bearing must be properly lubricated. v. Check the shaft seal. vi. Check the alignment of the pump and driver combination and the sense of rotation of the driver. vii. It must be possible to turn the rotor by hand without any restriction. viii. All ts of the auxiliary piping must be tight. Especially tighten carefully all stainless compression fittings! Open all valves in the flushing lines and check the flow. Action during start-up: CAUTION: DO NOT OPERATE THE UNIT UNLESS SAFETY GUARD OR DEVICE ARE IN PLACE AND PROPERLY ADJUSTED! i. ii.

Start the driver for a few seconds. Watch the sense of rotation and the smooth slowing down of the rotor. Start the driver and operate the pump for 20 sec. against closed valve. Check the reading of the pressure gauge. If the pump does not deliver rated pressure, stop the pump immediately. If it is working properly, open the discharge valve very slowly, until the requested head is


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iii.

iv. v. vi.

reached. Do not operate the pump with closed discharge valve for more than 30 sec. as the pump will overheat and may damage the main line bearing and the impeller. If the pump is taking over service from another pump, both pumps running in parallel for short time, close the discharge valve of the other pump now. Check the performance of the Minimum Flow By. The flow through the by- line can be heard, with boiler feed service the by line will warm up. If the minimum flow by is working properly, there is no objection against longer operation with closed discharge valve. After some time of running, check temperature and lubrication of the thrust bearings. Check vibrations of the pump and the pipings. Check the shaft sealing: A mechanical seal must be absolutely tight, a packed stuffing box requires some leakage.

D. SDVs, BDVs, HCVs, PSVs In Closed Drain Systems are not SDV’s, BDV’s and HCV’s. PRESSURE SAFETY VALVES (PSV’s ) The valve should be mounted vertically in an upright position either directly on a nozzle from the pressure vessel or on a short connection fitting that provides a direct, unobstructed flow between the vessel and the valve. Installing a pressure relief valve in other than this recommended position might adversely affect its operation. A valve should never be installed on a fitting having a smaller inside diameter than the inlet connection of the valve. Both valve and the vessel and/or line on which the valve is mounted must be thoroughly cleaned of all dirt and foreign material. Discharge piping should be simple and direct. A broken connection near the valve outlet is preferred. The weight of discharge piping should be carried by a separate and be firmly braced against swaying or vibrations. Before mounting each valve must be tested (checking set pressure). PSV testing should be performed by trained personnel using the applicable test procedure. After the valves have been tested satisfactorily they must be sealed. Install only PSV’s that are sealed, in order to avoid installation of unsuitable pressure relief valve.


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5. START-UP

A. GENERAL…………………………………………………………………………………42 B. PRELIMINARY CHECK………………………………………………………………….42


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5. START UP A. GENERAL Closed Drain System must be prepared for start-up before more of the Plant systems. They will be used before start-up of the plant to drain wash water from the circuits and also they must be ready to take any products that may be drained from the Plant on start-up. To put in service a Closed Drain System means to prepare the header to be ready to take drained products from the plant and deliver them to the final destination in safe condition.

B. PRELIMINARY CHECK The following steps must be completed prior to start up the Drain Systems:             

All unnecessary blinds removed. All relief valves tested and installed. Fire-fighting facilities ready for operation. All instrument ready for service. All utilities in service All drains and vents closed. Control valves and byes blocked-in. Check pumps and fans have their guards in place, are lubricated and free to rotate before closing their breakers in the MCC. Open valves for all instruments, for level bridles/gauges and analyzers. Pumps blocked-in. Insulation reinstalled where removed or damages. Filters checked and ready for operation. Keep ageways free to avoid hindrance to personnel, working equipment and safety vehicles.


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6.

NORMAL SHUTDOWN

A. GENERAL…………………………………………………………………………………44 B. SCHEDULED SHUTDOWN FOR SHORT DURATION………………………………..44 C. SHUTDOWN FOR MAINTENANCE…………………………………………………….44


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6. NORMAL SHUTDOWN A. GENERAL Normal Unit shutdown means a scheduled shutdown, which is performed with the Plant operating at normal conditions. Since the Closed Drain Systems are fundamental to the whole Plant, a planned shutdown shall be performed together with the planned shutdown of all the other sections. During Units shutdown, if no maintenance works are programmed, all equipment shall be left in a safe condition. For short shutdowns the equipment should remain ready for start-up where possible. If maintenance work is scheduled for one Closed Drain System the equipment should be cooling down and drained. The equipment to be maintained should be blind isolated, and nitrogen and air purged before opening. During unit operation, external maintenance works could be performed wherever and whenever possible, without interfering with the normal operation of the system. A general unit shutdown is performed, in order to perform those maintenance operations that could not be performed with the system normally running.

B. SCHEDULED SHUTDOWN FOR SHORT DURATION During Unit shutdown, if no maintenance works are programmed, all equipment shall be left in safe conditions and, in case of short shutdown, ready to be started. If any maintenance work is necessary for any equipment from the system, isolated it and prepare it for intervention. If any maintenance work is necessary in another system one of drain system is possible to be used to drain the equipment that need maintenance, that why Closed Drain Systems must remain in use as time as any equipment may need to be drained.


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Is recommended that in shutdown for short duration, if no equipment from Closed Drain Systems needs any intervention, the Closed Drain Systems must remain in service.

C. SHUTDOWN FOR MAINTENANCE A planned shutdown described here is to bring the plant to where air can be introduced into vessels for inspection or repair. When this is done for both trains then everything processing or containing hydrocarbons will be shutdown except possibly gas for the GTGs and the propane may be left in the propane system. For these two instances it will be necessary to keep purging the flare with nitrogen for safety. The shut down begin with reduction of flow rates. The sequence will be to start slowly closing down the wells for each train. Use the well valves and then close down the corrosion inhibitor system blocking off all its valves. Close the flow line ball valve where the line goes underground leaving the well yard. Continue by alternatively shutting in the wells manifolded to the production headers until all the train feeds are at 30% design. Flare gas and shutdown Units 400/410/420 by pushbutton and check SDVs operate and close their MOVs. Close down the fired heaters and quickly shut down and block in all the remaining wells. Close inlet SDVs and blow off sufficient pressure at the header BDVs to demonstrate that all the well and flowline SDVs closed correctly. Retain plant pressure at an adequate level for displacing liquids from process vessels or hook up the blanket gas for this purpose if necessary. Minimise all vessel liquid inventories. Lower plant pressures to flare levels whilst checking the operation of the plant BDVs.

Removal of Hydrocarbons Purge the unit to the flare free of gaseous hydrocarbons with nitrogen, then block off from the flare and purge the plant to atmosphere with air. Blind are required for hot work and vessel entry. Operate sediment removal systems in the test and production separators, maximize filter use and water rejection; employ an external heating system for water and pump it around for cleaning purposes. Establish clean water levels in all vessels sand clean water fill all liquid lines in the plant. NEVER USE DETERGENT MIXES FOR CLEANING, AS VERY SMALL TRACES OF IT WILL CONTAMINATE THE AMINE SYSTEMS RESULTING IN SEVERE EFFICIENCY LOSS DUE TO FOAMING.


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The removal for of hydrocarbons for entry into equipment will use external hot water circulation if found needed. For this operation temporary tanks, circulating pumps and a water heating system will be required. The next step would be to purge with nitrogen and then replace with air. The Closed Drains Systems will be the last systems that will be stopped.

7.

EMERGENCY SHUTDOWN

A. GENERAL…………………………………………………………………………47 B. UTILITY FAILURE……………………………………………………………….50 C. OTHER FAILURES………………….……………………………………………52


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7. EMERGENCY SHUTDOWN A. GENERAL EMERGENCY SHUTDOWN SYSTEM (ESD) There are three levels of ESD for the plant, which will be illustrated on the Process & Emergency Cause and Effect Charts. The shutdown and depressurization philosophy shown on these charts has been developed on the basis that the plant is operational prior to some cause generating actions within the plant. The three levels of ESD are defined as follows (See Instrument Logic Diagram C2-8141/006): 1)

ESD 1 Total plant shutdown and depressurization isolation.

2)

ESD 2 Total plant shutdown (Train 1 & 2) without depressurization.

3)

ESD 31 Train 1 shutdown without depressurization. ESD 32 Train 2 shutdown without depressurization.

Emergency Shutdown Level 1 - ESD 1 Emergency shutdown at Level 1 (as detailed in the Cause and Effect Charts) is initiated by operator using the ESD push button in the Control Room (&-PB-01). The ESD push button will be used when: Fire detected in a process area main control room incorporated with gas detected in: - Any of the plant control buildings or electrical sub-stations. - MEG regeneration packages of Train 1 or Train 2.


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-

Around the Heating Medium Heaters. In Air Compressors building.

The loss of power to the plant will cause most plant electrical prime movers to trip all as detailed in the electrical system control description (13.8 Kv BUS 1 and 13.8 Kv BUS 2 loss power). The instrument air compressors will trip. At the low pressure of the IA all valves should move to their fail-safe positions and the plant will depressurize. The fuel gas system will also shutdown and depressurize.

Emergency Shutdown Level 2- ESD 2 Emergency shutdown at Level 2 (as detailed in the Cause and Effect Charts) is initiated by either: a)

the level on the Flare Knock Out Drum going high high as detected by 2 out of 3 level switches 900-LSHH-05/1,2,3. See C2-8141/158.

b)

the instrument air pressure going low low as detected by three (3) low low pressure switches (630-PT-01/1/2/3) on the main instrument air header working on a 2 out of 3 voting arrangement. See C2-8141/147.

c)

operation of the EDS 2 push button in the Control Room (7-PB-02).

d)

the level on the Heating Medium Expansion Drum going low low as detected by 2 out of 3 voting system using low low level switches (300-LSLL-01/1,2,3). See C2-8141/34.

Following an ESD 1 or ESD 2 shutdown the flowlines shutdown valves at the inlet to the plant will close with the knock on effect of closing the wells via the wellhead safety systems on each well. Also the Sales Gas and Condensate trunk pipelines will be isolated by closing the trunk pipeline shutdown valves (700-SDV-03 and 700-SDV-04). All valves closing and motors tripping on ESD 2 are detailed on the Cause and Effect Charts. Emergency Shutdown Level 3 Emergency Shutdown at Level 3 (ESD 31 for train 1 or ESD 32 for train 2) is initiated by either: a)

Operation of the ESD 31 or ESD 32 push button in the Control Room (7-PB-31 and 7-PB-32)


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b)

Treated Gas KO Drum D-3113 level going high high as detected by 310-LSHH-05 for train #1 and D-3213 / 320-LSHH 05 for train 2. See C2-8141/40 and C2-8141/68 respectively.

c)

Rich Amine LP Flush Drum D-3103 pressure going high high as detected by 310-PSHH-01 for train 1 and D-3213 / 320-PSHH-01 for train 2. See C2-8141/44 and C2-8141/72 respectively.

d)

Rich Amine LP Flush Drum D-3103 level going high high as detected by 310-LSHH-07 for train 1. Similarly, D-3203 / 320-LSHH-07 for train 2. See C2-8141/44 and C2-8141/72 respectively.

e)

Amine Regenerator T-3102 level going high high as detected by 310-LSHH-08 for train 1. Similarly T-3202 / 320-LSHH-08 for train 2. See C2-8141/44 and C2-8141/72 respectively.

f)

Amine Surge Drum D-3105 level going low low as detected by 310-LSLL-12 for train 1. Similarly D-3205 / 320-LSLL-12 for train 2. See C2-8141/52 and C2-8141/80 respectively.

g)

Gas detected within the propane compressor building will cause both ESD 31 and ESD 32 total plant shutdown. However, this total plant shutdown is different to both ESD 1 and ESD 2 shutdowns. In the case of ESD 31 or ESD 32 wells connected to train #1 or train #2 shall be diverted to flare by closing the production header shutdown valve (210-SDV-04 or 220-SDV04) and opening the production header blowdown valve (210-BDV-01 or 220-BDV-01). To prevent loss of propane inventory during an ESD 1 shutdown, the propane compressors will be blocked in and remain pressurized by closing the compressor shutdown valves (400/410/420SDV-01/02/05) with the blowdown valves (400/410/420-BDV-06) remaining closed. In the event of fire in the propane system, depressurization shall take place via the relief system. During ESD 2 and for all other cases at ESD 31 or ESD 32 initiation, the compressor shutdown valves shall remain open and the blowdown valves closed. Only when gas is detected within the propane compressor building the compressor shutdown valves should close and the blowdown valves open shutting in and depressurizing the propane compressors

h)

MEG Reboiler F-4101 burner trip will cause an ESD 31 after 4 hours if corrective action is not taken to rectify the problem and re-light the burners. Similarly, an ESD 32 will be initiated following a trip of the burner of the MEG Reboiler F-4201. See C2-8141/98 and C2-8141/117 respectively.


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Treated gas from both trains shall be diverted to flare automatically via the ESD system, by opening hand control valves 700-HCV-01 & 02 and closing shutdown valves 700-SDV-01 & 02 on the treated gas lines to the Mercury Removal unit if either of the following conditions are true; a)

b)

The sales gas trunk pipeline pressure is either low low or the rate of change of pressure exceeding a preset amount as detected by pressure transmitters 700-PT-01/1, 2 and 3 on the trunk pipeline working in a 2 out of 3 voting arrangement signifying a major leak on the trunk pipeline. The sales gas trunk pipeline pressure is high high as detected by three pressure transmitters 700-PT-02/1, 2 and 3 on the trunk pipeline working in 2 out of 3 voting arrangement signifying trunk pipeline blockage/closure downstream of the plant.

Condensate flow from both trains will be diverted to flare automatically via the ESD system, by opening blowdown valves 510-BDV-04 and 520-BDV-04 and closing shutdown valves 510-BDV-03 and 520-SDV-03 downstream of the condensate metering if the high-high pressure is detected by three pressure transmitters 500-PT-01/1/2 and /3 working in 2 out of 3 voting arrangement, installed on the condensate line to the trunk pipeline downstream of the condensate metering and upstream of the condensate launcher.

B. UTILITY FAILURE a.

Instrument Air Failure

In case of instrument air failure the pneumatic valves shall take a position such that the plant is placed in safety conditions. Hydrocarbon Drain System Flows drained to hydrocarbon drain header under control are: - Condensate from inlet filter separator FIL-3101A/B and FIL-3201A/B - Oil / water from Rich Amine Flash Drum D-3103 and D-3203 When the Instrument Air failed, the control valves will be placed in following position: a) 310-LCV-02A CLOSED b) 310-LCV-02B CLOSED c) 310-LCV-06 CLOSED d) 310-SDV-02A CLOSED e) 310-SDV-02B CLOSED f) 320-LCV-02A CLOSED g) 320-LCV-02B CLOSED


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h) i) j)

320-LCV-06 320-SDV-02A 320-SDV-02B

CLOSED CLOSED CLOSED

Amine Drain System All drained flows from Amine System are manually drained. When the Instrument Air failed, the control valves will be placed in following position: a) 310-PCV-03/1 OPEN b) 310-PCV-03/2 OPEN c) 320-PCV-03/1 OPEN d) 320-PCV-03/2 OPEN Heating Medium Drain System All drained flows from Heating Medium System are manually drained. When the Instrument Air failed, the control valves will be placed in following position: a) b)

300-PCV-04/1 300-PCV-04/2

OPEN OPEN

Produced Water Drain System When the Instrument Air failed, the control valves will be placed in following position: a) 200-LCV-01 CLOSED b) 200-SDV-05 CLOSED c) 210-LCV-01 CLOSED d) 210-SDV-05 CLOSED e) 210-LCV-04 CLOSED f) 210-SDV-06 CLOSED g) 410-LCV-02 CLOSED h) 410-SDV-06 CLOSED i) 510-LCV-02 CLOSED j) 510-SDV-04 CLOSED k) 220-LCV-01 CLOSED l) 220-SDV-05 CLOSED m) 220-LCV-04 CLOSED n) 220-SDV-06 CLOSED o) 420-LCV-02 CLOSED p) 420-SDV-06 CLOSED q) 520-LCV-02 CLOSED r) 520-SDV-04 CLOSED


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b.

Power Failure

Hydrocarbon Drain System In case of electric power failure, pumps P-9101A/B, P-9201A/B shall stop. Amine Drain System In case of electric power failure, pumps P-3104A/B and P-3204A/B shall stop. In this case is better to not drain amine to Amine Drain Drum(s) in order to keep vessel’s level under control and to avoid losing amine to LP Flare Header (if the Amine Drain Drum(s) is fill). Heating Medium Drain System In case of electric power failure, pumps P-3003A/B shall stop. In this case is better to not drain heating medium to Heating Medium Drain Drum in order to keep vessel’s level under control and to avoid losing heating medium to LP Flare Header (if the Heating Medium Drain Drum is fill). Produced Water Drain System Produced Water Drain System is not directly affected by lose of the power. c.

Blanket Gas Failure

Blanket gas is used for blanketing the Amine Drain Drums D-3102, D-3202 and the HM Drain Drum D-3003, blanket gas failure for short duration should not influence the operation of the drums.

C. OTHER FAILURES Mechanical failures Each case of mechanical failure must be very well analyzed in order to take the better solution. Depending of the gravity of the failure is possible to be forced to shut down whole Gas Plant.


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8.

MAJOR EQUIPMENT

A. EQUIPMENT SPECIFICATION………………………………………………….54 B. INSTRUMENT SUMMARY……………………………………………………...126


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8. MAJOR EQUIPMENT

A. EQUIPMENT SPECIFICATIONS a.


Hydrocarbon Drain Drum Capacity: Design Pressure: Design Temperature max/min: Insulation: Length: Internal diameter:

D-9101 / D-9201 335.49 ft3 55psig 290/25F NO 15 ft 5 ft

Hydrocarbon Drain Drum Pump Type: Capacity: Suction Pressure: Discharge Pressure: Temperature max/min:

P-9101 A, B / P-9201 A, B Centrifugal 50 USgpm 0 psig 30 psig 290/25 F

b.

Amine Drain System

Amine Drain Drum Capacity: Design Pressure: Design Temperature max/min:


D-3102 / D-3202 339 ft3 50 psig 250/25 F

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Insulation: Length: Internal diameter:

NO 15 ft 5 ft

Amine Drain Drum Pump Type: Capacity: Suction Pressure: Discharge Pressure: Temperature max/min:

P-3104 A, B / P-3204 A, B Centrifugal 50 USgpm 0 psig 40 psig 250/25 F

Amine Drain Drum Filter Flow Rate: Design Pressure: Design Temperature:

FIL-3104 / FIL-3204 100 Usgpm 130 psig 250 / 25F

c.


HM Drain Drum Capacity: Design Pressure: Design Temperature: Insulation: Length: Internal diameter:

D-3003 339 ft3 50/FV psig 370 / 25F 3 inch 15 ft 5.0 ft

HM Drain Drum Pump Type: Capacity: Suction Pressure: Discharge Pressure: Temperature:

P-3003A/B Centrifugal 50 Usgpm 0 psig 115 psig 140F

HM Drain Filter Flow Rate: Design Pressure: Design Temperature:

FIL-3003 100 Usgpm 190 psig 370 / 25F

d.



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Produced Water Header Produced Water Header is a 10” line class A14. Material: RTRP Rating: 150# RF


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DATA SHEET-Sheet 1 ATTAHADDY

LOCATION

VESSEL 900

UNIT

Rev

Date

By

Chk'd

1 2 3

28/01/00 13/06/00 10/10/00

H.J.KIM Y.S.KO Y.S.KO

SAS/JI SAS/JI

D-9101 / D-9201

Item : Service :

HYDROCARBON DRAIN DRUM Operating Pressure [psig] Max 40 Min ATM. Temperature [°F] Max AMB. Min AMB.

ASME SECTION , DIV Design [psig] 55 F.V. [°F] 290 25

Shell & Head CS(SA516 GR70) 6

Materials Corr. Allow.

Insulation Insulation Class NO Lining YES (note 4) Lower T.L.elevation above ground: Notes:

Internals CS(SA516 GR70) 3 Thickness ft.

Nozzle Data Ref A B

No. 1 1

Ø 3" 4"

SERVICE Hydrocarbon Inlet Hydrocarbon Outlet

D E F G H P

1 1 1 1 1 1

2" 6" 3" 2" 24" 2"

Drain Vent Gas Outlet Fuel Gas Inlet. (For Liquid HC Removal below Pump Suction Level) Manhole with Davit Purge Connection

K M PI

1 2 1

2" 2" 2"

Pump Minimum Flow Recycle Heating Coil Inlet/Outlet Pressure Indicator

LT01 LSH LSL LSHH LSLL TI SP

2 2 2 2 2 1 1

2" 2" 2" 2" 2" 2" 2"

Level Bridle/Level Gauge/Level Transmitter Level Switch High Level Switch Low Level Switch High High Level Switch Low Low Temperature Indicator Spare Connection with Blind


Page 64 of 154

Page

DATA SHEET-Sheet 2 LOCATION

ATTAHADDY VESSEL 900

UNIT

Item :

D-9101 / D-9201

Service :

HYDROCARBON DRAIN DRUM

PROCESS DESIGN DATA Case No. Case Description

Rev

Date

By

Chk'd

1 2 3

28/01/00 13/06/00 10/10/00


SAS/JI SAS/JI

ASME SECTION , DIV

NOMINAL note 1

Operating Pressure Temperature

psig °F

Vapour Flowrate Vapour Density @ T& P Vapour Viscosity@T, P Vapour Mol. Weight

lb/h lb/ft³

Liquid Flowrate Liquid Density @T, P Liquid Viscosity @T, P Liquid Surface Tension

lb/h lb/ft³ dyne/cm

Water Flowrate Water Density @T, P Water Viscosity @T, P Water Surface Tension


PRESSURE SETTINGS Relief Valve PAHH (Trip) PAH (Alarm) Pressure Control Normal Operating PAL (Alarm) PALL (Trip) LIQUID LEVELS

psig psig psig psig psig psig psig

ATMOSPHERIC AMBIENT

67,370 42/43.4 0.399/0.48 12/12.1

ATM

Level Settings

Overall liquid level above bottom tan line (Condensate Levels)

Interface liquid level above bottom tan line (Water Level)

inches inches inches inches inches inches inches inches inches inches


High/High High Normal Low Low/Low High/High High Normal Low Low/Low

Hold-up time

41 12 9 6

Page 65 of 154

mins. mins. mins. mins. mins. mins. mins. mins. mins. mins.

Page

DATA SHEET-Sheet 3

LOCATION

ATTAHADDY VESSEL 900

UNIT

Item :

D-9101 / D-9201

Service :

HYDROCARBON DRAIN DRUM

Rev

Date

By

Chk'd

1 2 3

28/01/00 13/06/00 10/10/00


SAS/JI SAS/JI

ASME SECTION , DIV

PROCESS SKETCH:

NOTE: 1 Drum is sized to take up the liquid content of D-2001/D2101 and other s totalling of 3000 US gallons in 15 minutes. 2 At Liquid Level Low-Low -LLLL (6" from Bottom) Trip Main & Stand-by pumps

At Liquid Level Low -LLL (9" from Bottom) Stop Main & Stand-by Pumps At Liquid Level High -HLL (12" from Bottom) Start Main Pump At Liquid Level High-High -HHLL (41" from Bottom) - Start Stand-by Pump 3 Deleted.

4 BELZONA 1591 to be applied.


Page 66 of 154

Page


Rev 1 2 3 4

ATTAHADDY DRUM

UNIT

300

Item :

D-3102/D-3202 AMINE DRAIN DRUM Operating

Service :

Pressure Max Min Temperature Max Min Materials Corr. Allow.

Date 28/01/00 12/06/00 27/09/00 10/03/01

By H.J.KIM Y.S.KO Y.S.KO Y.S.KO

ASME SECTION VIII, DIVISION . Design

[psig] 2

[psig] 50

[°F] 140 140 Shell

[°F] 250 25 Ends CS(SA516 GR70) 1.5 mm

Insulation NO Lining NO Lower T.L. elevation above ground: Stress relieve YES

ft.

Nozzle Data Ref A C F W E D BG P CL PSV PCV H PT PI LT LSL LSLL LSHH TI

No. 1 2 2 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1

Ø 6" 2" 18" 2" 6" 2" 2" 2" 3" 4" 2" 24" 2" 2" 4" 6" 6" 6" 2"

Service Amine Drains Min. flow return P-3104 A/B P-3104A/B Pumps Make-up Water Vent PSVs' discharge from FIL-3104 Blanket Gas Purge Connection Cleaning Connection Safety Valve Vent to LP Flare Manhole with Davit Pressure Transmitter Pressure Gauge Level Transmitter Stillwell Level Switch Low Stillwell Level Switch Low Low Stillwell Level Switch High High Stillwell Temperature Indicator


Vessel Dimensions

(note 4)

I.D. =5 ft, length T/T =15 ft.

Page 67 of 154

Chk'd SAS/JI SAS/JI SAS/JI

Page


Rev 1 2 3 4

ATTAHADDY DRUM

UNIT

300

Item : Service :

D-3102/D-3202 AMINE DRAIN DRUM


Date 28/01/00 12/06/00 27/09/00 10/03/01



ASME SECTION VIII, DIVISION . 2

1


psig °F

2 140

Vapour Flowrate Vapour Density Vapour Viscosity Vapour Mol. Weight

lb/h lb/ft³

0.05

3

Remarks

note 1

0.0120 18.8

Liquid Flowrate Liquid Density Liquid Viscosity Liquid Surface Tension


63.67 3.200 40.6

Water Flowrate Water Density Water Viscosity Water Surface Tension


0 -


50


High/High/High High/High High Low Low/Low High/High High Normal Low Low/Low

note 1


4 2 2 1 -

Level Settings

Liquid level above bottom tan line (Heating Medium Levels)

Liquid level above bottom line

Min. hold-up time

50 42 36 24 12

-

NOTES :

1 The process fluid are: Amine solution drains (50 % wt. of commercial MDEA) Blanket gas (Fuel Gas). 2 The drum will be located in a concrete pit below ground 3 Deleted.


Page

Page 68 of 154

-

mins. mins. mins. mins. mins.

-

mins. mins. mins. mins.


Rev 1 2 3 4

ATTAHADDY DRUM

UNIT

300

Item : Service :

Date 28/01/00 12/06/00 27/09/00 10/03/01


D-3003 HEATING MEDIUM DRAIN DRUM ASME SECTION VIII, DIV . Operating Design

Pressure

[psig] 2

Max Min Temperature Max Min

[°F] 320 140 Shell

Materials Corr. Allow.

[psig] 50/FV [°F] 370 25 Ends CS(SA516 GR70) 1.5 mm

Insulation YES (HC) Lining NO Lower T.L. elevation above ground: Stress relieving NO

ft.

Nozzle Data Ref A C A2 F W D E BG P PSV PCV H PT PI LT LSL LSLL LSHH TI

No. 1 2 1 2 1 1 1 1 1 1 1 2 1 1 1 1 1 1 1

Ø 6" 2" 4" 20" 2" 2" 6" 2" 2" 3" 2" 24" 2" 2" 4" 6" 6" 6" 2"

Service HM Drains Min. flow return P-3003 A/B Relieved liquid P-3003A/B Pumps connection Make-up Water Drain Vent Blanket Gas Purge Connection Safety Valve Vent to LP Flare Manhole with Davit Pressure Transmitter Pressure Gauge Level Transmitter Stillwell Level Switch Low Stillwell Level Switch Low Low Stillwell Level Switch High High Stillwell Temperature Indicator


Vessel Dimensions I.D. =5 ft, length T/T =15 ft.

Page 69 of 154


Page


Rev 1 2 3 4

ATTAHADDY DRUM

UNIT

300

Item : Service :

Date 28/01/00 12/06/00 27/09/00 10/03/01



D-3003 HEATING MEDIUM DRAIN DRUM ASME SECTION VIII, DIV .


2

1


psig °F

2 140

Vapour Flowrate Vapour Density Vapour Viscosity Vapour Mol. Weight

lb/h lb/ft³

0.05

3

Remarks

note 1

0.012 18.8

Liquid Flowrate Liquid Density Liquid Viscosity Liquid Surface Tension


65.54 1.9 41.5

Water Flowrate Water Density Water Viscosity Water Surface Tension


0 -


50


High/High/High High/High High Low Low/Low High/High High Normal Low Low/Low

note 1


4 2 2 1 -

Level Settings

Liquid level above bottom tan line (Heating Medium Levels)

Liquid level above bottom line

Page

Min. hold-up time

50 42 36 18 12

-

NOTES :

1 The process fluid are: Triethylene glycol / water solution drains (50/50 % wt. ), Blanket gas (Fuel Gas) 2 Deleted.


Page 70 of 154

-

mins. mins. mins. mins. mins. mins. mins. mins. mins. mins.


ATTAHADDY FILTER 300

UNIT

Rev

Date

By

Chk'd

1 2 3 4

28/01/00 16/06/00 01/02/01 27/03/01

H.J.KIM Y.S.KO Y.S.KO Y.S.KO

SAS/JI SAS/JI SAS/JI

Item Service

FIL-3104 / FIL-3204 AMINE DRAIN DRUM FILTER

Number

TWO

Type

Page

Cartridge

Operating Conditions Process Fluid Filtered Fluid Flow Rate: Operating Design Temperature Upstream Pressure Density @ T,P Viscosity @ T,P Freezing Point Nature of Impurities Impurities Content Filtration Requirement Max. Allow. Pressure Drop Clean Dirty Design Conditions : Pressure Temperature

Max./Min.

Material : Filter Body Filter Element s Filter Media Corrosion Allowance Stress Relieve

Case 1 Case 2 High Temperature Case Low Temperature Case Amine Solution (note 1) [USgpm] [USgpm] [oF] [psig] [lb/ft3] [] [oF]

100 100 140 40 63.7 3.2

100 100 140 40 63.7 3.2

-4 Sand, Scale, Salt, Corrosion products etc. 99% of particles > 10 microns

[psi] [psi]

3 10

[psig] [oF]

130 (note 2) 250 / 25

[mm]

CS CS COTTON / 316 SS 1.5 YES

Insulation Design Code


YES (PP) ASME SECTION , DIV.

Page 71 of 154



UNIT

Item Service

Rev

Date

By

Chk'd

1 2 3 4

28/01/00 16/06/00 01/02/01 27/03/01



FIL-3104 / FIL-3204 AMINE DRAIN DRUM FILTER

PROCESS SKETCH:

Vessel Dimensions:

I.D. = 1.1 ft

Length T/T = 5.3 ft

Nozzle Data Ref A F D W E PSV

No. 1 1 1 1 1 1

3" 3" 2" 2" 2" 1"

Service Amine Solution Inlet Amine Solution Outlet Drain Demin. Water Inlet Demin. Water Outlet Safety Valve

NOTES : 1 The process fluid is Amin solution (50 %wt of commercial MDEA)) The solution may contain CO2, hydrocarbons and silicone antifoaming compounds. 2 The Filters are subject to shut in pressure of the Pumps P-3104 A/B. To be confirmed by HDEC. 3 Deleted.


Page 72 of 154

Page



UNIT

Rev

Date

By

Chk'd

1 2 3 4

28/01/00 16/06/00 01/02/01 27/03/01



Item Service

FIL-3003 HEATING MEDIUM DRAIN FILTER

Number

ONE

Type

Page

Cartridge

Operating Conditions Process Fluid Filtered Fluid Flow Rate: Operating Design Temperature Max. / Min. Upstream Pressure Density @ T,P Viscosity @ T,P Freezing Point Nature of Impurities Impurities Content Filtration Requirement Max. Allow. Pressure Drop Clean Dirty Design Conditions : Pressure Temperature

Max./Min.

Material : Filter Body Filter Element s Filter Media Corrosion Allowance Insulation Design Code


Case 1 Case 2 High Temperature Case Low Temperature Case TEG/WATER Solution (note 1) [USgpm] [USgpm] [°F] [psig] [lb/ft3] [] [°F]

100 100 320 / 140 115 65.54 1.9

100 100 320 / 140 115 65.54 1.9

-8 Sand, Scale, Salt, Corrosion products etc. 99% of particles > 10 microns

[psi] [psi]

3 10 @ Design flowrate

[psig] [°F]

190 (note 2) 370 / 25

[mm]

CS CS / SS 316L COTTON / 316 SS 1.5 YES (HC) ASME SECTION , DIV.

Page 73 of 154



UNIT

Item Service

Rev

Date

By

Chk'd

1 2 3 4

28/01/00 16/06/00 01/02/01 27/03/01



FIL-3003 HEATING MEDIUM DRAIN FILTER

PROCESS SKETCH:

Vessel Dimensions:

I.D. = 1.1 ft

Length T/T = 5.3 ft

Nozzle Data Ref A F D W E PSV

No. 1 1 1 1 1 1

Ø 3" 3" 2" 2" 2" 1 1/2"

Service TEG Solution Inlet TEG Solution Outlet Drain Demin. Water Inlet Demin. Water Outlet Safety Valve

NOTES : 1 The process fluid is triethylene glycol / water solution (50 / 50 %wt) 2 The Filters are subject to shut in pressure of the Pumps P-3003 A/B. To be confirmed by HDEC. 3 Deleted.


Page 74 of 154

Page


ATTAHADDY CENTRIFUGAL PUMP

900

UNIT

Rev

Date

By

Chk'd

1 2 3

28/01/00 16/06/00 10/03/01


SAS/JI SAS/JI

P-9101A/B / P-9201A/B HYDROCARBON DRAIN DRUM PUMP

Item Service Case Case Description Fluid Corrosive / Erosive Normal Pumping Temperature@T,P Viscosity @ T, P Vapour Pressure @T Specific Gravity @ 60oF Specific Gravity @ T, P

[oF] [.] [psia]

1 NOMINAL Case Hydrocarbon Condensate Yes AMBIENT 0.62 14.7 0.72

PUMP Normal Flow Rate @T, P Design Flow Rate Discharge Pressure Suction Pressure Differential Pressure Differential Head Available NPSH Motor Power Design Temperature Max. Suction Pressure

[USgpm] [USgpm] [psig] [psig] [psi] [ft] [ft] [BHP] Max. / Min.

50 77 30 0 30 96 6.1 5.5

[oF] [psig]

290/25 56

Driver Type: Normal Spare

Electric Motor Electric Motor

Speed Control Turbine Speed Control Expected Speed Range Open Valve Start-up Materials of construction

Case Impeller Shaft

CS+3mm CA S.S S.S

NOTES : 1 Deleted.


Page 75 of 154

Page



300

UNIT

Item Service

Rev

Date

By

Chk'd

1 2 3

28/01/00 16/06/00 10/03/01


SAS/JI SAS/JI

P-3104 A/B / P-3204 A/B AMINE DRAIN DRUM PUMP

Case Case Description

1 2 High Temp Low Temp Case Case Amine Solution (50 % wt. of commercial MDEA)

Fluid Corrosive / Erosive Normal Pumping Temperature Viscosity @ T,P Vapour Pressure @ T Specific Gravity @ 60°F Specific Gravity @ T,P

[°F] [.] [psia]

140 3.2 2.94 1.05 1.02

140 3.2 2.94 1.05 1.02

50 61 40 0 40 91 25 5

50 61 40 0 40 91 25 5

PUMP Normal Flow Rate Design Flow Rate Discharge Pressure Suction Pressure Differential Pressure Differential Head Available NPSH Estimated Power

(note 2)

Design Temperature Max. Suction Pressure Estimated Shut-off Pressure

Max. / Min.

[USgpm] [USgpm] [psig] [psig] [psi] [ft] [ft] [HP] [°F] [psig] [psig]

250/25 52 100


Electric Motor (note 3) Electric Motor (note 3)

Speed Control Turbine Speed Control Expected Speed Range Open Valve Start-up Materials

None

Casing + Column Impeller Shaft

CS (1.5 mm C.A. both sides) + SR SS SS

NOTES : 1 2 3 4 5

Turndown flowrate to be 30% of normal High Temp Case flowrate. At design flow rate. 7.37 HP motor used for utility balance. Vendor to confirm. Pumps to be designed to handle solid contaminants Deleted.


Page 76 of 154

Page



300

UNIT

Item Service

Rev

Date

By

Chk'd

1 2 3

28/01/00 16/06/00 10/03/01


SAS/JI SAS/JI

P-3003 A/B HEATING MEDIUM DRAIN DRUM PUMP

Case Case Description

1 2 High Temp Low Temp Case Case Triethylene glycol / Water (50-50 % wt.)

Fluid Corrosive / Erosive Normal Pumping Temperature Viscosity @ T,P Vapour Pressure @ T Specific Gravity @ 60°F Specific Gravity @ T,P

[°F] [.] [psia]

140 1.9 2.94 1.08 1.05

140 1.9 2.94 1.08 1.05

[USgpm] [USgpm] [psig] [psig] [psi] [ft] [ft] [HP]

50 63 115 0 115 253 25 15

50 63 115 0 115 253 25 15

PUMP Normal Flow Rate Design Flow Rate Discharge Pressure Suction Pressure Differential Pressure Differential Head Available NPSH Motor Power

(note 2)

Design Temperature Max. / Min. Max. Suction Pressure Estimated Shut-off Pressure

[°F] [psig] [psig]

370 / 25 51.6 190


Electric Motor (note 3) Electric Motor (note 3)

Casing Impeller Shaft

CS CS CS

Speed Control Turbine Speed Control Expected Speed Range Open Valve Start-up Material:

NOTES : 1 2 3 4

Turndown flowrate to be 30% of normal High Temp Case flowrate. At the design flow rate. 14.8 HP motor used for utility balance. To be confirmed by vendor. Deleted.


Page 77 of 154

Page

DATA SHEET-Sheet 15 REV 0 1 2

INSTRUMENT DATA SHEETS FOR RESTRICTION ORIFICE

DATE 31/01/01 13/09/01 28/10/01

ORIFICE PLATES 1 Concentric

X

3 Bore

:

Maximum Rate

4 Material

7 Taps

:

X

304SS

Nearest 1/8" 316SS

X

Other 5 Ring Material & Type 6 MFR & Model No.

ISA / Type C

GENERAL

FLUID DATA (High temp. / Low temp.)

METER

PLATE & FLANGE

NOTES :

34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 1

Line Number P & ID No. Fluid Fluid State Maximum Flow Normal Flow Pressure (psig) Nor. Max. Temperature () Nor. Max. Specific Gravity at Base (60) Operating Spec.Gravity Supercomp. Factor Mol. Weight /Cv Operating Viscosity [] Quality % or Superheat Base Press. Base Temp. Meter Max. Min. Flow Upstream Density (lb/ft3) Pressure drop (psi) Type of Meter Diff.Range-Dry Seal sp.gr.at 15.6 Static Press. Range Chart or Scale Range Chart Multiplier

Flange

Vena Contracta

Pipe

Other

8 Tap Size

:

1/2"

Other

9 Type

:

Weld Neck

Slip On

10 Material

:

Steel

Threaded

By Other

12 Flange Rating 300-RO-04B

300-RO-05A

300-RO-05B

P-3001B Min. flow recycle

P-3003A Min. flow recycle


3"-A16-FA-30021 C2-0135 Fresh Amine Liquid

2"-A7-HM-30106 C2-0144 Heating Medium Liquid

2"-A7-HM-30068 C2-0144 Heating Medium Liquid

100 (usgpm)

1.05 1.046

13 (usgpm) 115 140 370 1.08 1.05

13 (usgpm) 115 140 370 1.08 1.05

9.2

1.9

1.9

45

115

115

60 80

212

(in-H2O)

0.29 0.12 Beta=d/D 22.7 (mm) 6.6 (mm) Orifice Bore Diameter N/A N/A Vent or Drain Hole Vent or Drain Hole Diameter Sch STD Sch STD Line I.D. 3 mm 12 mm Plate Thickness 3" 150# RF 2" 150# RF Flange Con. Size & Rating ANSI N/A Yes Solid Stellite Facing Gasket Material Bolt & Nuts Material A16 A7 Piping Material Class Unit : Pressure(psi), Temperature(), Flow(Liquid : USGPM, Gases : SCFH, Steam or Vapor : LB/h) * USGPM : US gallon per minutes, SCFH : standard cubic foot per hour


UNIT 300

Other

11 Flanges included

13 Tag No. 14 Service 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33

:

R.W.Miller

Other

CHK'D APP'D Y.N.K S.K.K Y.N.K K.C.I S.K.K S.K.K

ORIFICE FLANGES

Other

2 ISA Standard

BY J.B.R J.B.R J.B.R

Page 78 of 154

0.12 6.6 (mm) N/A Sch STD 12 mm 2" 150# RF Yes

A7



DATE 31/01/01 13/09/01 28/10/01


X

3 Bore

:

Maximum Rate

4 Material

7 Taps

:

X

304SS

Nearest 1/8" 316SS

X


ISA / Type C

GENERAL


METER

PLATE & FLANGE

NOTES :

34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 1


Flange

Vena Contracta

Pipe

Other

8 Tap Size

:

1/2"

Other

9 Type

:

Weld Neck

Slip On

10 Material

:

Steel

Other

11 Flanges included

13 Tag No. 14 Service 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33

:

R.W.Miller

Other


By Other

12 Flange Rating 910-RO-01A

910-RO-01B

D-9101A By

D-9101B By

2"-A8-D-91001 C2-0189 HC Liquids Liquid


22 (usgpm)

0.67 0.745

22 (usgpm) 30 125 290 0.67 0.745

1.23

1.23

30

30

30 125

290

(in-H2O)

0.22 0.22 Beta=d/D 11.0 (mm) 11.0 (mm) Orifice Bore Diameter N/A N/A Vent or Drain Hole Vent or Drain Hole Diameter Sch XS Sch XS Line I.D. 3 mm 3 mm Plate Thickness 2" 150# RF 2" 150# RF Flange Con. Size & Rating ANSI N/A N/A Solid Stellite Facing Gasket Material Bolt & Nuts Material A8 A8 Piping Material Class Unit : Pressure(psi), Temperature(), Flow(Liquid : USGPM, Gases : SCFH, Steam or Vapor : LB/h) * USGPM : US gallon per minutes, SCFH : standard cubic foot per hour


UNIT 910

ORIFICE FLANGES

Other

2 ISA Standard


Page 79 of 154

Threaded



DATE 31/01/01 13/09/01 28/10/01


X

3 Bore

:

Maximum Rate

4 Material

7 Taps

:

X

304SS

Nearest 1/8" 316SS

X


ISA / Type C

GENERAL


METER

PLATE & FLANGE

NOTES :

34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 1


Flange

Vena Contracta

Pipe

Other

8 Tap Size

:

1/2"

Other

9 Type

:

Weld Neck

Slip On

10 Material

:

Steel

Other

11 Flanges included

13 Tag No. 14 Service 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33

:

R.W.Miller

Other


By Other

12 Flange Rating 920-RO-01A

920-RO-01B

D-9201A By

D-9201B By



22 (usgpm)

0.67 0.745

22 (usgpm) 30 125 290 0.67 0.745

1.23

1.23

30

30

30 125

290

(in-H2O)

0.22 0.22 Beta=d/D 11.0 (mm) 11.0 (mm) Orifice Bore Diameter N/A N/A Vent or Drain Hole Vent or Drain Hole Diameter Sch XS Sch XS Line I.D. 3 mm 3 mm Plate Thickness 2" 150# RF 2" 150# RF Flange Con. Size & Rating ANSI N/A N/A Solid Stellite Facing Gasket Material Bolt & Nuts Material A8 A8 Piping Material Class Unit : Pressure(psi), Temperature(), Flow(Liquid : USGPM, Gases : SCFH, Steam or Vapor : LB/h) * USGPM : US gallon per minutes, SCFH : standard cubic foot per hour


UNIT 920

ORIFICE FLANGES

Other

2 ISA Standard


Page 80 of 154

Threaded



DATE 31/01/01 13/09/01 28/10/01


X

3 Bore

:

Maximum Rate

4 Material

7 Taps

:

X

304SS

Nearest 1/8" 316SS

X


ISA / Type C

GENERAL


METER

PLATE & FLANGE

NOTES :

34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 1


Flange

Vena Contracta

Pipe

Other

8 Tap Size

:

1/2"

Other

9 Type

:

Weld Neck

Slip On

10 Material

:

Steel

Threaded

By Other

12 Flange Rating 310-RO-01 Gas to HP flare header 4"-C1-G-31032 C2-0118 Gas Vapor

310-RO-02 Rich Amine to D-3103 2"-C9-RA-31003 C2-0118 Rich Amine / HC Liquid

74231 (lb/h) 785 117 235

15 (usgpm) 794.3 180 235 1.112 1.055

11 (usgpm) 40 140 250 1.1 1.02

0.013

1.331

3.2

2.9 770

729.3

40

19.6

310-RO-04A P-3104A Min. flow recycle 2"-A17-RA-31044 C2-0134 Amine Solution Liquid

1.2

(in-H2O)

0.36 0.08 Beta=d/D 36.5 (mm) 4.5 (mm) Orifice Bore Diameter N/A N/A Vent or Drain Hole Vent or Drain Hole Diameter Sch XS Sch XS Line I.D. 18 mm 12 mm Plate Thickness 4" 600# RF 2" 600# RF Flange Con. Size & Rating ANSI Yes Yes Solid Stellite Facing Gasket Material Bolt & Nuts Material C1 C9 Piping Material Class Unit : Pressure(psi), Temperature(), Flow(Liquid : USGPM, Gases : SCFH, Steam or Vapor : LB/h) * USGPM : US gallon per minutes, SCFH : standard cubic foot per hour


UNIT 310

Other

11 Flanges included

13 Tag No. 14 Service 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33

:

R.W.Miller

Other


ORIFICE FLANGES

Other

2 ISA Standard


Page 81 of 154

0.14 7.9 (mm) N/A Sch XS 3 mm 2" 150# RF N/A

A17



DATE 31/01/01 13/09/01 28/10/01


X

3 Bore

:

Maximum Rate

4 Material

7 Taps

:

X

304SS

Nearest 1/8" 316SS

X


ISA / Type C

GENERAL


METER

PLATE & FLANGE

NOTES :

34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 1


Flange

Vena Contracta

Pipe

Other

8 Tap Size

:

1/2"

Other

9 Type

:

Weld Neck

Slip On

10 Material

:

Steel

Threaded

By Other


310-RO-05A

310-RO-05B


HC Condensate to HP flare header


2"-A17-RA-31045 C2-0134 Amine Solution Liquid

2"-C4-D-31023 C2-0116 HC Condensate Liquid


11 (usgpm) 40 140

250

8 (usgpm) 794 140

8 (usgpm) 235

794 140

235

1.1 1.02

0.695 0.65

0.695 0.65

3.2

0.29

0.29

40

764

764

(in-H2O)

0.14 0.06 Beta=d/D 7.9 (mm) 2.9 (mm) Orifice Bore Diameter N/A N/A Vent or Drain Hole Vent or Drain Hole Diameter Sch XS Sch 160 Line I.D. 3 mm 12 mm Plate Thickness 2" 150# RF 2" 600# RF Flange Con. Size & Rating ANSI N/A Yes Solid Stellite Facing Gasket Material Bolt & Nuts Material A17 C4 Piping Material Class Unit : Pressure(psi), Temperature(), Flow(Liquid : USGPM, Gases : SCFH, Steam or Vapor : LB/h) * USGPM : US gallon per minutes, SCFH : standard cubic foot per hour


UNIT 310

Other

11 Flanges included

13 Tag No. 14 Service 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33

:

R.W.Miller

Other


ORIFICE FLANGES

Other

2 ISA Standard


Page 82 of 154

0.06 2.9 (mm) N/A Sch 160 12 mm 2" 600# RF Yes

C4



DATE 31/01/01 13/09/01 28/10/01


X

3 Bore

:

Maximum Rate

4 Material

7 Taps

:

X

304SS

Nearest 1/8" 316SS

X


ISA / Type C

GENERAL


METER

PLATE & FLANGE

NOTES :

34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 1


Flange

Vena Contracta

Pipe

Other

8 Tap Size

:

1/2"

Other

9 Type

:

Weld Neck

Slip On

10 Material

:

Steel

Threaded

By Other

12 Flange Rating 320-RO-01 Gas to HP flare header 4"-C1-G-32032 C2-0218 Gas Vapor

320-RO-02 Rich Amine to D-3203 2"-C9-RA-32003 C2-0218 Rich Amine / HC Liquid

74231 (lb/h) 785 117 235

15 (usgpm) 794.3 180 235 1.112 1.055

11 (usgpm) 40 140 250 1.1 1.02

0.013

1.331

3.2

2.9 770

729.3

40

19.6

320-RO-04A P-3204A Min. flow recycle 2"-A17-RA-32044 C2-0234 Amine Solution Liquid

1.2

(in-H2O)

0.36 0.08 Beta=d/D 36.5 (mm) 4.5 (mm) Orifice Bore Diameter N/A N/A Vent or Drain Hole Vent or Drain Hole Diameter Sch XS Sch XS Line I.D. 18 mm 12 mm Plate Thickness 4" 600# RF 2" 600# RF Flange Con. Size & Rating ANSI Yes Yes Solid Stellite Facing Gasket Material Bolt & Nuts Material C1 C9 Piping Material Class Unit : Pressure(psi), Temperature(), Flow(Liquid : USGPM, Gases : SCFH, Steam or Vapor : LB/h) * USGPM : US gallon per minutes, SCFH : standard cubic foot per hour


UNIT 320

Other

11 Flanges included

13 Tag No. 14 Service 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33

:

R.W.Miller

Other


ORIFICE FLANGES

Other

2 ISA Standard


Page 83 of 154

0.14 7.9 (mm) N/A Sch XS 3 mm 2" 150# RF N/A

A17



DATE 31/01/01 13/09/01 28/10/01


X

3 Bore

:

Maximum Rate

4 Material

7 Taps

:

X

304SS

Nearest 1/8" 316SS

X


ISA / Type C

GENERAL


METER

PLATE & FLANGE

NOTES :

34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 1


Flange

Vena Contracta

Pipe

Other

8 Tap Size

:

1/2"

Other

9 Type

:

Weld Neck

Slip On

10 Material

:

Steel

Threaded

By Other


320-RO-05A

320-RO-05B




2"-A17-RA-32045 C2-0234 Amine Solution Liquid



11 (usgpm) 40 140

250

8 (usgpm) 794 140

8 (usgpm) 235

794 140

235

1.1 1.02

0.695 0.65

0.695 0.65

3.2

0.29

0.29

40

764

764

(in-H2O)

0.14 0.06 Beta=d/D 7.9 (mm) 2.9 (mm) Orifice Bore Diameter N/A N/A Vent or Drain Hole Vent or Drain Hole Diameter Sch XS Sch 160 Line I.D. 3 mm 12 mm Plate Thickness 2" 150# RF 2" 600# RF Flange Con. Size & Rating ANSI N/A Yes Solid Stellite Facing Gasket Material Bolt & Nuts Material A17 C4 Piping Material Class Unit : Pressure(psi), Temperature(), Flow(Liquid : USGPM, Gases : SCFH, Steam or Vapor : LB/h) * USGPM : US gallon per minutes, SCFH : standard cubic foot per hour


UNIT 320

Other

11 Flanges included

13 Tag No. 14 Service 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33

:

R.W.Miller

Other


ORIFICE FLANGES

Other

2 ISA Standard


Page 84 of 154

0.06 2.9 (mm) N/A Sch 160 12 mm 2" 600# RF Yes

C4


INSTRUMENT DATA SHEETS FOR ORIFICE PLATES & FLANGES

DATE 31/01/01 13/09/01 28/10/01



X

3 Bore

:

Maximum Rate

4 Material

7 Taps

Other :

304SS

Nearest 1/8" 316SS

X

5 Ring Material & Type 6 MFR & Model No.

ISA / Type A

GENERAL

METER

PLATE & FLANGE

NOTES :

34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 1. 2.

Line Number P & ID No. Fluid Fluid State Maximum Flow Normal Flow Pressure (psig) Nor. Max. Temperature () Nor. Max. Specific Gravity at Base (60) Operating Spec.Gravity Supercomp. Factor Mol. Weight /Cv Operating Viscosity [] Quality % or Superheat Base Press. Base Temp. Meter Max. Min. Flow Upstream Density (lb/ft3)

Type of Meter Diff.Range-Dry Seal Sp.Gr.at 15.6 Static Press. Range Chart or Scale Range Chart Multiplier

Vena Contracta Other

X

8 Tap Size

:

1/2"

9 Type

:

Weld Neck X

10 Material

:

Steel

(in-H2O)

Other

X

12 Flange Rating

NPTF

Slip On Other

11 Flanges included

13 Tag No. 14 Service


X

Flange Pipe

Other

15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33

:

ISO 5167 X

Threaded See Below

By Other See Below

310-FE-13B

310-FE-13C

Lean Amine to P-3102 B

Lean Amine to P-3102 C

12"-A16-LA-31316 C2-0133A Lean Amine Liquid 1511.4 (usgpm) 1374.2 (usgpm) 40.3 170 149 250 1.056 1.02


310-FE-16 Amine to D-3105 3"-A17-RA-31043 C2-0134 Amine Liquid 110 (usgpm) 100 (usgpm) 30 100 140 250 1.05 1.02

2.63

2.63

3.2

1600 (usgpm) 302.4 (usgpm)

1600 (usgpm) 302.4 (usgpm)

120 (usgpm) 30 (usgpm)

D/P 100

D/P 100

D/P 100

0.55 0.55 Beta=d/D 172.6 (mm) 172.6 (mm) Orifice Bore Diameter Vent Vent Vent or Drain Hole 3 (mm) 3 (mm) Vent or Drain Hole Diameter Sch 120 Sch 120 Line I.D. 6 mm 6 mm Plate Thickness 12" 300# RF 12" 300# RF Flange Con. Size & Rating ASME A105 A105 Flange Material Note 2. Note 2. Gasket Material Note 2. Note 2. Bolt & Nuts Material A16 A16 Piping Material Class Unit : Pressure(psi), Temperature(), Flow(Liquid : USGPM, Gases : SCFH, Steam or Vapor : LB/h) * USGPM : US gallon per minutes, SCFH : standard cubic foot per hour Vendor shall provide the Bolt, Nut & Gasket material as per piping specification. (See attached technical note.)


UNIT 310

ORIFICE FLANGES

Other

2 ISA Standard


Page 85 of 154

0.59 46.3 (mm) Vent 2.38 (mm) Sch STD 3 mm 3" 300# RF A105 Note 2. Note 2. A17


INSTRUMENT DATA SHEETS FOR ORIFICE PLATES & FLANGES

DATE 31/01/01 13/09/01 28/10/01



X

3 Bore

:

Maximum Rate

4 Material

7 Taps

Other :

304SS

Nearest 1/8" 316SS

X

5 Ring Material & Type 6 MFR & Model No.

ISA / Type A

GENERAL

METER

PLATE & FLANGE

NOTES :

34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 1. 2.

Line Number P & ID No. Fluid Fluid State Maximum Flow Normal Flow Pressure (psig) Nor. Max. Temperature () Nor. Max. Specific Gravity at Base (60) Operating Spec.Gravity Supercomp. Factor Mol. Weight /Cv Operating Viscosity [] Quality % or Superheat Base Press. Base Temp. Meter Max. Min. Flow Upstream Density (lb/ft3)

Type of Meter Diff.Range-Dry Seal Sp.Gr.at 15.6 Static Press. Range Chart or Scale Range Chart Multiplier

Vena Contracta

(in-H2O)

Other X

8 Tap Size

:

1/2"

9 Type

:

Weld Neck X

10 Material

:

Steel

Other

12 Flange Rating

NPTF

Slip On Other

X

11 Flanges included

13 Tag No. 14 Service


X

Flange Pipe

Other

15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33

:

ISO 5167 X

Threaded See Below

By Other See Below

320-FE-13B

320-FE-13C

Lean Amine to P-3202 B

Lean Amine to P-3202 C



320-FE-16 Amine to D-3205 3"-A17-RA-32043 C2-0234 Amine Liquid 110 (usgpm) 100 (usgpm) 30 100 140 250 1.05 1.02

2.63

2.63

3.2

1600 (usgpm) 302.4 (usgpm)

1600 (usgpm) 302.4 (usgpm)

120 (usgpm) 30 (usgpm)

D/P 100

D/P 100

D/P 100

0.55 0.55 Beta=d/D 172.6 (mm) 172.6 (mm) Orifice Bore Diameter Vent Vent Vent or Drain Hole 3 (mm) 3 (mm) Vent or Drain Hole Diameter Sch 120 Sch 120 Line I.D. 6 mm 6 mm Plate Thickness 12" 300# RF 12" 300# RF Flange Con. Size & Rating ASME A105 A105 Flange Material Note 2. Note 2. Gasket Material Note 2. Note 2. Bolt & Nuts Material A16 A16 Piping Material Class Unit : Pressure(psi), Temperature(), Flow(Liquid : USGPM, Gases : SCFH, Steam or Vapor : LB/h) * USGPM : US gallon per minutes, SCFH : standard cubic foot per hour Vendor shall provide the Bolt, Nut & Gasket material as per piping specification. (See attached technical note.)


UNIT 320

ORIFICE FLANGES

Other

2 ISA Standard


Page 86 of 154

0.59 46.3 (mm) Vent 2.38 (mm) Sch STD 3 mm 3" 300# RF A105 Note 2. Note 2. A17

DATA SHEET-Sheet 24 REV DATE 0 09/06/00 1 09/11/00 2 28/08/00

INSTRUMENT DATA SHEETS FOR ROTAMETER

1. Tag No.

310-FI-14

2. Service

Demi Water to D-3102 2"-A10-MW-31014

3. Line No./Vessel No. GENERAL

C2-0134

4. P&ID No.

ABB Automation

5. Manufacturer 6. Model Number

10 A 3225

7. Tube Number

N/A N/A

8. Float Number

Local Indication Pipe (In-Line)

9. Function 10. Mounting 11. Process Conn. Size

Rating

12. Inlet Dir.

Outlet Dir.

1"

ANSI 300#RF

BOTTOM Viton

14. Packing or O-Ring Mtl. METER

TOP

316SS Ti

13. Fitting Material

N/A

15. Enclosure type 16. Size

Float Guide

17. Tube Mtl.

Float Mtl.

1/2"

Rod Guide

316SS Ti

316SS Ti

Metal Tube

18. Meter Type

0.3 ~ 3.6 (usgpm)

19. Meter Scale Range

0 ~ 100 %

20. Meter Factor

Class 6

21. Rated Accuracy

No

22. Hydraulic Calib. Required

Demi Water (Liquid)

23. Fluid 24. Color or Transparency 25. Maximum Flow Rate

(usgpm)

26. Normal Flow

(usgpm)

(usgpm) Min. Flow

FLUID DATA 27. Oper. Specific Gravity at T deg (High temp. / 28. Max. Oper. Viscosity at T () Low temp.) 29. Max. Press.(psig) Oper. Press.(psig) Oper.Temp.() 30. Max.Temp.() 31. Std. Density

3.3 3

0.9 0.993 0.76

-

50

180

125

Mol. Wgt.

32. Max. Allowable Press. Drop (psi) 33. /Cv Ratio EXT

34. Extension Well Mtl 35. Gasket Mtl 36. Transmitter Output

XMTR

37. Trans. Enclosure Class 38. Scale Range 39. No. of s

ALARM

OPTIONS

Form

40. Rating 41. :

Open

On

Incr.

Actions

Close

Flow

Decr.

42. Valve Size & Material

1/2" NPT

316SS

43. Valve Location & Type

Outlet

Needle

44. Coupling Type & Material

Flanged

316SS

45. Coupling Size & Rating

1" 300# RF x 1/2"NPT

Notes :


Page 87 of 154


CHK'D APP'D T.S.K S.K.K T.S.K S.K.K Y.N.K K.C.I

UNIT 310

DATA SHEET-Sheet 25 REV DATE 0 09/06/00 1 09/11/00 2 28/08/00

INSTRUMENT DATA SHEETS FOR ROTAMETER

1. Tag No.

320-FI-14

2. Service

Demi Water to D-3202 2"-A10-MW-32014


C2-0234

4. P&ID No.

ABB Automation

5. Manufacturer 6. Model Number

10 A 3225

7. Tube Number

N/A N/A

8. Float Number

Local Indication Pipe (In-Line)

9. Function 10. Mounting 11. Process Conn. Size

Rating

12. Inlet Dir.

Outlet Dir.

1"

ANSI 300#RF

BOTTOM Viton

14. Packing or O-Ring Mtl. METER

TOP

316SS Ti

13. Fitting Material

N/A

15. Enclosure type 16. Size

Float Guide

17. Tube Mtl.

Float Mtl.

1/2"

Rod Guide

316SS Ti

316SS Ti

Metal Tube

18. Meter Type

0.3 ~ 3.6 (usgpm)

19. Meter Scale Range

0 ~ 100 %

20. Meter Factor

Class 6

21. Rated Accuracy

No

22. Hydraulic Calib. Required

Demi Water (Liquid)

23. Fluid 24. Color or Transparency 25. Maximum Flow Rate

(usgpm)

26. Normal Flow

(usgpm)

(usgpm) Min. Flow

FLUID DATA 27. Oper. Specific Gravity at T deg (High temp. / 28. Max. Oper. Viscosity at T () Low temp.) 29. Max. Press.(psig) Oper. Press.(psig) Oper.Temp.() 30. Max.Temp.() 31. Std. Density

3.3 3

0.9 0.993 0.76

-

50

180

125

Mol. Wgt.

32. Max. Allowable Press. Drop (psi) 33. /Cv Ratio EXT

34. Extension Well Mtl 35. Gasket Mtl 36. Transmitter Output

XMTR

37. Trans. Enclosure Class 38. Scale Range 39. No. of s

ALARM

OPTIONS

Form

40. Rating 41. :

Open

On

Incr.

Actions

Close

Flow

Decr.

42. Valve Size & Material

1/2" NPT

316SS

43. Valve Location & Type

Outlet

Needle

44. Coupling Type & Material

Flanged

316SS

45. Coupling Size & Rating

1" 300# RF x 1/2"NPT

Notes :


Page 88 of 154


CHK'D APP'D T.S.K S.K.K T.S.K S.K.K Y.N.K K.C.I

UNIT 320


INSTRUMENT DATA SHEETS FOR D/P FLOW GAUGES 1 Type

:

Direct Rdg X

3~15 lb receiver

Other Yoke X

:

Surface

3 Dial

:

Diameter

4 Case

:

Cast Iron

Alumin.

Other

Stainless Steel

Screwed X

Hinged

Std

Other

:

6 Blow-out Protection

:

None

Solid Front X

Note 2. :

Flush

120mmΦ (min.) Color

Note 1.

BY CHK'D APP'D J.B.R T.S.K S.K.K J.B.R T.S.K S.K.K J.B.R T.S.K S.K.K

10 MFR. & Model No. 11 Press. Element

2 Mounting

5 Ring

DATE 25/05/00 04/10/00 26/10/00

Bourdon

Bellows

Other

Diaphragm

12 Element Mtl

:

Bronze

Steel

316 SS

Phenol

13 Socket Mtl

:

Bronze

Steel

316 SS

Slip

14 Connection

:

Other NPT X

PT 1/2" X

Back X

Disc X

Other

Bottom X 15 Movement

:

Shatterproof X

7 Lens

:

Glass

Plastic

8 Option

:

1) 5-Way Manifold (316SS) (Note 3 & 5)

1/4"

PF Other

Back SS X

Bronze

Nylon

Other 16 Diaphragm Seal MFR.

Type

Wetted Part Mtl

Other Mtl

Fill Fluid 9 Nominal Accuracy Required

±1.5% F.S.

Process Conn

Gage Conn

D/P Range

Fluid

Flow Range

Max. Press.

(in-H2O)

Status

(Note 4.)

(psig)

Rev.

Tag No.

2

300-FI-03

0-200

Liquid

0-120

190

2

300-FI-04

0-200

Liquid

0-300

151

Heating Medium to D-3002

C2-0145

2

300-FI-06A/A-H (8EA)

0-200

Liquid

0-730

209

Heating medium to F-3001A

C2-0140A

2

300-FI-06B/A-H (8EA)

0-200

Liquid

0-730

209

Heating medium to F-3001B

C2-0140B

2

300-FI-06C/A-H (8EA)

0-200

Liquid

0-730

209

Heating medium to F-3001C

C2-0140C

2

310-FI-12

0-200

Liquid

0-500

177

Lean amine to FIL-3102 A/B

C2-0128

2

310-FI-16

0-200

Liquid

0-120

100

Rich amine from FIL-3104

C2-0134

2

310-FI-17

0-200

Liquid

0-330

177

Lean amine from FIL-3102 A/B

C2-0131

2

320-FI-12

0-200

Liquid

0-500

177

Lean amine to FIL-3202 A/B

C2-0228

2

320-FI-16

0-200

Liquid

0-120

100


C2-0234

2

320-FI-17

0-200

Liquid

0-330

177

Lean amine from FIL-3202 A/B

C2-0231

2

410-FI-01

0-200

Liquid

0-10

1200

Lean MEG to E-4101

C2-0153

2

410-FI-02A/B (2EA)

0-200

Liquid

0-5

1200

Lean MEG to E-4102A/B

C2-0154

2

410-FI-03A/B (2EA)

0-200

Liquid

0-2

1200


C2-0154

2

410-FI-10A/B (2EA)

0-200

Vapor

152356

1000

Treated gas from D-4101

C2-0154

2

410-FI-11A/B (2EA)

0-200

Vapor

144256

1000


C2-0154

2

410-FI-12A

0-200

Liquid

0-2

1200

MEG to E-4103A

C2-0154

2

410-FI-12B

0-200

Liquid

0-2

1200

MEG to E-4103B

C2-0154

2

420-FI-01

0-200

Liquid

0-10

1200

Lean MEG to E-4201

C2-0253

2

420-FI-02A/B (2EA)

0-200

Liquid

0-5

1200


C2-0254

2

420-FI-03A/B (2EA)

0-200

Liquid

0-2

1200


C2-0254

2

420-FI-10A/B (2EA)

0-200

Vapor

152356

1000


C2-0254

2

420-FI-11A/B (2EA)

0-200

Vapor

144256

1000


C2-0254

2

420-FI-12A

0-200

Liquid

0-2

1200

MEG to E-4203A

C2-0254

2

420-FI-12B

0-200

Liquid

0-2

1200

MEG to E-4203B

C2-0254

140

Fire water to TK-6901

C2-0332

2 690-FI-01 0-200 Liquid 0-3500 NOTES : 1. All gauges shall have a white background with black scale markings. 2. Vendor to specify. 3. Manifold connection shall be 1/2" NPT(F). 4. Unit : Flow (Liquid : USGPM, Gases : SCFH, Steam or Vapor : LB/h) 5. Vendor shall provide the 2" pipe mounting bracket.


Page 89 of 154

Service

P&ID No.

Heating Medium to D-3002

C2-0144

DATA SHEET-Sheet 27 REV 1 2 3 4 5

INSTRUMENT DATA SHEETS FOR LEVEL SWITCHES

GENERAL

BODY OR CAGE

1. Tag No. 2. P&ID No. 3. Line No. / Vessel No. 4. Manufacturer 5. Model No. 6. Piping Material Class 7. Area Classification as per NEC 8. Type 9. Connection Size & Rating 10. Body Material [mm] 11. Center to Center 12. Connection Type 13. Case Mounting Type 14. Rotatable Head 15. Cooling Fin or Extension

SWITCH

BY J.B.R J.B.R J.B.R J.B.R J.B.R

CHK'D T.S.K T.S.K Y.N.K S.K.K S.K.K

APP'D S.K.K S.K.K K.C.IM S.K.K S.K.K

UNIT 300

300-LSHH-01 C2-0138 D-3002 Solartron Mobrey BC3FR4N1H8 / 132 A7 Weatherproof (Suitable for I.S. service) Float 2" 300# RF Carbon Steel 356 External Top-Side-Bottom Yes N/A

300-LSLL-01/1 C2-0138 D-3002 Solartron Mobrey BC3FR4N1H8 / 132 A7 Weatherproof (Suitable for I.S. service) Float 2" 300# RF Carbon Steel 356 External Top-Side-Bottom Yes N/A

300-LSLL-13 C2-0144 D-3003 Solartron Mobrey DC1DS4N1H8 / 66 A7 Weatherproof (Suitable for I.S. service) Displacer 6" 300# RF C.S Flange w/ S.S wet. Part N/A Internal Top Yes N/A

N/A 316SS Monel 500 100

N/A 316SS Monel 500 100

1437 ["A"] 316SS Nimonic 90 (Spring) -

Hermetically Sealed, Snap 1-DPDT IP-66 1/2" NPT(F) 24V DC 0.25A NON IND. YES N/A



YES

YES

[mm] 16. Dimensions [mm] 17. Insertion Depth 18. Displacer Extension [mm] FLOAT OR 19. Displacer or Float Mat'l DISPLACER 20. Tube / Union Mat'l [mm] 21. Set point (From upper flange) 22. Type 23. Form 24. Switch certification Enclosure Rating 25. Electrical Connection 26. Rating : Volts (DC / AC) 27. Amps. Watts 28. Load Type - Ind. Non-Ind. 29. Diff : Fixed Adjust 30. Adjust. : Int Ext. 31. Actions Open On Incr. Close Level Decr. 32. Upper Fluid 33. Lower Fluid 34. Specific Gravity Upper Lower

DATE 04/09/00 18/10/00 29/06/01 18/09/01 09/05/02

YES

YES YES

Heating Medium (L)

Heating Medium (L)

0.98

YES Heating Medium (L)

0.98

1.05

SERVICE CONDITION 35. Minimum Sp. Gr. Diff. (High temp. 36. Pressure (psig) / Low temp.) Operating Maximum

80

95

80

95

2

50

37. Temperature () Operating Maximum

265

370

265

370

140

370

Notes :

"218" SET POINT OF SWITCH


Page 90 of 154

"A"



GENERAL

BODY OR CAGE


SWITCH




UNIT 300

300-LSLL-10 C2-0135 TK-3001 Solartron Mobrey BC3FR4N1H8 / 132 A16 Weatherproof (Suitable for I.S. service) Float 2" 300# RF Carbon Steel 356 External Top-Side-Bottom Yes N/A

300-LSLL-03 C2-0145 TK-3002 Solartron Mobrey BC3FR4N1H8 / 132 A7 Weatherproof (Suitable for I.S. service) Float 2" 300# RF Carbon Steel 356 External Top-Side-Bottom Yes N/A

300-LSHH/H-03 C2-0144 D-3003 Solartron Mobrey DC8DS4N2H4 / 66 A7 Weatherproof (Suitable for I.S. service) Displacer 6" 300# RF Carbon Steel (Flange) N/A Internal Top Yes N/A

N/A 316SS Monel 500 100

N/A 316SS Monel 500 100

H:827.6 ["B"], HH:675 ["A"] 316SS Nimonic 90 (Spring) -



Hermetically Sealed, Snap 2-SPDT IP-66 1/2" NPT(F) 24V DC 0.25A NON IND. YES N/A

YES

YES


DATE 04/09/00 18/10/00 29/06/01 18/09/01 09/05/02

YES

YES Fresh Amine (L)

YES


1.04

Heating Medium (L)

1.07

1.05


ATM

0.3

ATM

0.3

2

50


125

212

125

212

140

370

Notes :



Page 91 of 154

"A" "B"



GENERAL

BODY OR CAGE


[mm] 16. Dimensions [mm] 17. Insertion Depth 18. Displacer Extension [mm] FLOAT OR 19. Displacer or Float Mat'l DISPLACER 20. Tube / Union Mat'l [mm] 21. Set point

SWITCH

(From upper flange) 22. Type 23. Form 24. Switch certification Enclosure Rating 25. Electrical Connection 26. Rating : Volts (DC / AC) 27. Amps. Watts 28. Load Type - Ind. Non-Ind. 29. Diff : Fixed Adjust 30. Adjust. : Int Ext. 31. Actions Open On Incr. Close Level Decr. 32. Upper Fluid 33. Lower Fluid 34. Specific Gravity Upper Lower

SERVICE CONDITION 35. Minimum Sp. Gr. Diff. (High temp. 36. Pressure (psig) / Low temp.) Operating Maximum 37. Temperature () Operating Maximum

DATE 04/09/00 18/10/00 29/06/01 18/09/01 09/05/02




UNIT 300

300-LSL-13 C2-0144 D-3003 Solartron Mobrey DC1DS4N1H8 / 66 A7 Weatherproof (Suitable for I.S. service) Displacer 6" 300# RF C.S Flange w/ S.S wet. Part N/A Internal Top Yes N/A

300-LSL-04 C2-0142 Solartron Mobrey BC3FR4N1H8 / 132 A7 Weatherproof (Suitable for I.S. service) Float 2" 300# RF Carbon Steel 356 External Top-Side-Bottom Yes N/A

300-LSH-01A C2-0139C D-3005A/B/C Solartron Mobrey BC3FR4N1H8 / 132 B7 Weatherproof (Suitable for I.S. service) Float 2" 300# RF Carbon Steel 356 External Top-Side-Bottom Yes N/A

1284.8 ["A"] 316SS Nimonic 90 (Spring) -

N/A 316SS Monel 500 100

N/A 316SS Monel 500 100




YES

YES

YES


YES


1.05

Drain (L)

0.98

0.82 / 0.84

2

50

102.3 / 88.3

209

55.3

500

140

370

265

370

214/168.6

320

Notes :



Page 92 of 154

"A"



GENERAL

BODY OR CAGE


SWITCH




UNIT 910

910-LSL-01 C2-0189 D-9101 Solartron Mobrey BC3FR4N1H8 / 132 A8 Weatherproof (Suitable for I.S. service) Float 2" 300# RF Carbon Steel 356 External Top-Side-Bottom Yes N/A


910-LSH-01 C2-0189 D-9101 Solartron Mobrey BC3FR4N1H8 / 132 A8 Weatherproof (Suitable for I.S. service) Float 2" 300# RF Carbon Steel 356 External Top-Side-Bottom Yes N/A

N/A 316SS Monel 500 100

N/A 316SS Monel 500 100

N/A 316SS Monel 500 100




YES

YES


DATE 04/09/00 18/10/00 29/06/01 18/09/01 09/05/02

YES

YES

YES

YES Condensate (L)

Condensate (L)

0.67 / 0.69

Condensate (L)

0.67 / 0.69

0.67 / 0.69


ATM

55

ATM

55

ATM

55


125

290

125

290

125

290

Notes :


Page 93 of 154



GENERAL

BODY OR CAGE


SWITCH


910-LSLL-01 C2-0189 D-9101 Solartron Mobrey BC3FR4N1H8 / 132 A8 Weatherproof (Suitable for I.S. service) Float 2" 300# RF Carbon Steel 356 External Top-Side-Bottom Yes N/A


DATE 04/09/00 18/10/00 29/06/01 18/09/01 09/05/02

N/A 316SS Monel 500 150 Hermetically Sealed, Snap 1-DPDT IP-66 1/2" NPT(F) 24V DC 0.25A NON IND. YES N/A YES YES Heating Medium (L) 0.67 / 0.69


ATM

55


125

290

Notes :


Page 94 of 154



UNIT 910



GENERAL

BODY OR CAGE


SWITCH




UNIT 920

920-LSL-01 C2-0289 D-9201 Solartron Mobrey BC3FR4N1H8 / 132 A8 Weatherproof (Suitable for I.S. service) Float 2" 300# RF Carbon Steel 356 External Top-Side-Bottom Yes N/A


920-LSH-01 C2-0289 D-9201 Solartron Mobrey BC3FR4N1H8 / 132 A8 Weatherproof (Suitable for I.S. service) Float 2" 300# RF Carbon Steel 356 External Top-Side-Bottom Yes N/A

N/A 316SS Monel 500 100

N/A 316SS Monel 500 100

N/A 316SS Monel 500 100




YES

YES


DATE 04/09/00 18/10/00 29/06/01 18/09/01 09/05/02

YES

YES

YES

YES Condensate (L)

Condensate (L)

0.67 / 0.69

Condensate (L)

0.67 / 0.69

0.67 / 0.69


ATM

55

ATM

55

ATM

55


125

290

125

290

125

290

Notes :


Page 95 of 154



GENERAL

BODY OR CAGE


SWITCH




DATE 04/09/00 18/10/00 29/06/01 18/09/01 09/05/02

N/A 316SS Monel 500 150 Hermetically Sealed, Snap 1-DPDT IP-66 1/2" NPT(F) 24V DC 0.25A NON IND. YES N/A YES YES Heating Medium (L) 0.67 / 0.69


ATM

55


125

290

Notes :


Page 96 of 154



UNIT 920



GENERAL

BODY OR CAGE


SWITCH





UNIT 310



310-LSHH-03A C2-0116 FIL-3101A Solartron Mobrey BM7DS4N1H8 / 233 C6 Weatherproof (Suitable for I.S. service) Float 1 1/2" 600# RF Monel 400 356 External Side-Side Yes N/A

N/A 316SS Monel 500 100


N/A Monel 400 Monel 500 100




YES

YES


DATE 04/09/00 18/10/00 29/06/01 18/09/01 09/05/02

YES

YES

YES

YES Lean Amine (L)

Rich Amine (L)

0.99 / 1.0

Condensate (L)

1.02

0.65 / 1.00

1.5

50

2

50

799.3

1000

207/190

250

140

250

140/90

235

Notes :



Page 97 of 154

"A" "B"



GENERAL

BODY OR CAGE



SWITCH



DATE 04/09/00 18/10/00 29/06/01 18/09/01 09/05/02




UNIT 310



310-LSHH-03B C2-0117 FIL-3101B Solartron Mobrey BM7DS4N1H8 / 233 C6 Weatherproof (Suitable for I.S. service) Float 1 1/2" 600# RF Monel 400 356 External Side-Side Yes N/A







YES

YES

YES

YES Lean Amine (L)

YES

YES Rich Amine (L)

1.02

Condensate (L)

1.02

0.65 / 1.00

2

50

2

50

799.3

1000

140

250

140

250

140/90

235

Notes :



Page 98 of 154

"A"



GENERAL

BODY OR CAGE


SWITCH





UNIT 320



320-LSHH-03A C2-0216 FIL-3201A Solartron Mobrey BM7DS4N1H8 / 233 C6 Weatherproof (Suitable for I.S. service) Float 1 1/2" 600# RF Monel 400 356 External Side-Side Yes N/A

N/A 316SS Monel 500 100






YES

YES


DATE 04/09/00 18/10/00 29/06/01 18/09/01 09/05/02

YES

YES

YES

YES Lean Amine (L)

Rich Amine (L)

0.99 / 1.0

Condensate (L)

1.02

0.65 / 1.00

1.5

50

2

50

799.3

1000

207/190

250

140

250

140/90

235

Notes :



Page 99 of 154

"A" "B"



GENERAL

BODY OR CAGE



SWITCH



DATE 04/09/00 18/10/00 29/06/01 18/09/01 09/05/02




UNIT 320



320-LSHH-03B C2-0217 FIL-3201B Solartron Mobrey BM7DS4N1H8 / 233 C6 Weatherproof (Suitable for I.S. service) Float 1 1/2" 600# RF Monel 400 356 External Side-Side Yes N/A







YES

YES

YES

YES Lean Amine (L)

YES

YES Rich Amine (L)

1.02

Condensate (L)

1.02

0.65 / 1.00

2

50

2

50

799.3

1000

140

250

140

250

140/90

235

Notes :



Page 100 of 154

"A"

DATA SHEET-Sheet 38 INSTRUMENT DATA SHEETS FOR LEVEL TRANSMITTERS (DISPLACER TYPE) 1. Tag No. 2. Service

REV DATE 0 16/05/00 1 05/09/00 2 28/05/01


"A"

HHH HH L


APP'D S.K.K S.K.K K.C.IM UNIT 300

300-LT-02 Heating Medium Drain Drum D-3003 C2-0144 Krohne

3. Line No./Vessel No. 4. P&ID NO. 5. Manufacturer BW25/R/N/M9/ESK/EEx/Z0 6. Model Number Class , Div 1, Gr B 7. Area Classification as per NEC Carbon Steel (Flange) 8. Body or Cage Material ANSI 300# RF Rating & Type 4" 9. Conn. Size & Location Upper 10. Conn. Size & Location Center 11. Conn. Size & Location Lower 12. Conn. Dim. (Upper flange~Lower flange) BODY/CAGE Top Mounting 13. Case Mounting Type Yes 14. Rotatable Head N/A 15. Cooling Fin or Extension Displacer 16. Sensing Method Internal 17. Connection Type [mm] 914.4 (Note 1.) 18. Measuring Range 48" (1219mm) 19. Dimensions [mm] See below drawing 20. Insertion Depth DISPLACER 21. Displacer Extension [mm] 316SS Ti 22. Displacer or Float Material ATS 340 23. Displacer Spring Mtl Transmitter 24. Function 4 ~ 20 mA DC 25. Output Signal 26. Differential 27. Output Action : Level Rise XMTR/CONT. 28. Mounting Integral EExia IIC T6 Zone 0 29. Certification IP-65 Enclosure Rating DC 24 V 30. Elec. Power or Air Supply 1/2" NPT (F) 31. Electrical Entry 32. Upper Liquid Heating Medium (L) SERVICE 33. Lower Liquid 1.05 CONDITION 34. Sp. Gr. : Upper Lower (High temp. 35. Press. (psig) : 50 2 Max. Normal / Low temp.) 36. Temp. () : 370 140 Max. Normal 37. Interface Level N/A N/A 38. Airset Supply Gage N/A 39. Gage Glass Connections N/A 40. Gage Glass Model No. OPTIONS 41. s No. N/A N/A Form N/A 42. Rating N/A 43. Action of s Note 2. 44. Remote Local Indicator Notes : 1. 1. "A" Vendor : 422,shall "B" provide : 625.2, the "C" cooling : 1234.8fin or extension as per following requirement. 2. Vendor shall provide the remote indicator with 2" pipe mounting bracket. (300-LI-02) 3. N/A : Not Applicable "168" GENERAL

CHK'D T.S.K T.S.K Y.N.K

Page 101 of 154

"B"

"C"


REV DATE 0 16/05/00 1 05/09/00 2 28/05/01

910-LT-01 Hydrocarbon Drain Drum

D-9101 3. Line No./Vessel No. C2-0189 4. P&ID NO. Krohne 5. Manufacturer BW25/R/B/M9/ESK/EEx/Z0 6. Model Number Class , Div 1, Gr B 7. Area Classification as per NEC Carbon Steel 8. Body or Cage Material ANSI 300# RF Rating & Type 1 1/2" 9. Conn. Size & Location Upper 10. Conn. Size & Location Center 1 1/2" 11. Conn. Size & Location Lower 52" (1321mm) 12. Conn. Dim. (Upper flange~Lower flange) BODY/CAGE Top-Side-Bottom 13. Case Mounting Type Yes 14. Rotatable Head N/A 15. Cooling Fin or Extension Displacer 16. Sensing Method External 17. Connection Type [mm] 1143 (Note 1.) 18. Measuring Range 48" (1219mm) 19. Dimensions [mm] N/A 20. Insertion Depth DISPLACER 21. Displacer Extension [mm] 316SS Ti 22. Displacer or Float Material ATS 340 23. Displacer Spring Mtl Transmitter 24. Function 4 ~ 20 mA DC 25. Output Signal 26. Differential 27. Output Action : Level Rise XMTR/CONT. 28. Mounting Integral EExia IIC T6 Zone 0 29. Certification IP-65 Enclosure Rating DC 24 V 30. Elec. Power or Air Supply 1/2" NPT (F) 31. Electrical Entry 32. Upper Liquid Condensate (L) 33. Lower Liquid SERVICE 0.67 / 0.69 CONDITION 34. Sp. Gr. : Upper Lower (High temp. 35. Press. (psig) : 55 ATM Max. Normal / Low temp.) 36. Temp. () : 290 125 Max. Normal 37. Interface Level N/A N/A 38. Airset Supply Gage N/A 39. Gage Glass Connections N/A 40. Gage Glass Model No. OPTIONS 41. s No. N/A N/A Form N/A 42. Rating N/A 43. Action of s N/A 44. Remote Local Indicator Notes : 1. 1. Top Vendor Level shall (HHHLL) provide: 1270mm, the coolingBottom fin or extension Level (LLL) as: per 228.6mm following requirement. 2. N/A : Not Applicable GENERAL


Page 102 of 154

BY CHK'D APP'D J.B.R T.S.K S.K.K J.B.R T.S.K S.K.K J.B.R Y.N.K K.C.IM UNIT 910

DATA SHEET-Sheet 40

INSTRUMENT DATA SHEETS FOR LEVEL TRANSMITTERS (DISPLACER TYPE) 1. Tag No. 2. Service

REV DATE 0 16/05/00 1 05/09/00 2 28/05/01

920-LT-01 Hydrocarbon Drain Drum

D-9201 3. Line No./Vessel No. C2-0289 4. P&ID NO. Krohne 5. Manufacturer BW25/R/B/M9/ESK/EEx/Z0 6. Model Number Class , Div 1, Gr B 7. Area Classification as per NEC Carbon Steel 8. Body or Cage Material ANSI 300# RF Rating & Type 1 1/2" 9. Conn. Size & Location Upper 10. Conn. Size & Location Center 1 1/2" 11. Conn. Size & Location Lower 52" (1321mm) 12. Conn. Dim. (Upper flange~Lower flange) BODY/CAGE Top-Side-Bottom 13. Case Mounting Type Yes 14. Rotatable Head N/A 15. Cooling Fin or Extension Displacer 16. Sensing Method External 17. Connection Type [mm] 1143 (Note 1.) 18. Measuring Range 48" (1219mm) 19. Dimensions [mm] N/A 20. Insertion Depth DISPLACER 21. Displacer Extension [mm] 316SS Ti 22. Displacer or Float Material ATS 340 23. Displacer Spring Mtl Transmitter 24. Function 4 ~ 20 mA DC 25. Output Signal 26. Differential 27. Output Action : Level Rise XMTR/CONT. 28. Mounting Integral EExia IIC T6 Zone 0 29. Certification IP-65 Enclosure Rating DC 24 V 30. Elec. Power or Air Supply 1/2" NPT (F) 31. Electrical Entry 32. Upper Liquid Condensate (L) 33. Lower Liquid SERVICE 0.67 / 0.69 CONDITION 34. Sp. Gr. : Upper Lower (High temp. 35. Press. (psig) : 55 ATM Max. Normal / Low temp.) 36. Temp. () : 290 125 Max. Normal 37. Interface Level N/A N/A 38. Airset Supply Gage N/A 39. Gage Glass Connections N/A 40. Gage Glass Model No. OPTIONS N/A N/A 41. s No. Form N/A 42. Rating N/A 43. Action of s N/A 44. Remote Local Indicator Notes : 1. 1. Top Vendor Level shall (HHHLL) provide: 1270mm, the coolingBottom fin or extension Level (LLL) as: per 228.6mm following requirement. 2. N/A : Not Applicable GENERAL


Page 103 of 154


DATA SHEET-Sheet 41

INSTRUMENT DATA SHEETS FOR LEVEL TRANSMITTERS (DISPLACER TYPE) 1. Tag No. 2. Service

REV DATE 0 16/05/00 1 05/09/00 2 28/05/01

310-LT-10 Regenerator Reflux Drum D-3104 C2-0123 Krohne


310-LT-13 Amine Drain Drum

D-3102 3. Line No./Vessel No. C2-0134 4. P&ID NO. Krohne 5. Manufacturer BW25/R/B/M9/ESK/EEx/Z0 BW25/R/N/M9/ESK/EEx/Z0 6. Model Number Class , Div 1, Gr B Class , Div 1, Gr B 7. Area Classification as per NEC 316SS Ti Carbon Steel (Flange) 8. Body or Cage Material ANSI 300# RF ANSI 300# RF Rating & Type 1 1/2" 4" 9. Conn. Size & Location Upper 10. Conn. Size & Location Center 1 1/2" 11. Conn. Size & Location Lower 36" (914mm) 12. Conn. Dim. (Upper flange~Lower flange) BODY/CAGE Top-Side-Bottom Top Mounting 13. Case Mounting Type Yes Yes 14. Rotatable Head N/A N/A 15. Cooling Fin or Extension Displacer Displacer 16. Sensing Method External Internal 17. Connection Type [mm] 457.2 (Note 1.) 762 (Note 2.) 18. Measuring Range 32" (813mm) 32" (813mm) 19. Dimensions [mm] N/A See below drawing 20. Insertion Depth DISPLACER 21. Displacer Extension [mm] 316SS Ti 316SS Ti 22. Displacer or Float Material ATS 340 ATS 340 23. Displacer Spring Mtl Transmitter Transmitter 24. Function 4 ~ 20 mA DC 4 ~ 20 mA DC 25. Output Signal 26. Differential 27. Output Action : Level Rise XMTR/CONT. 28. Mounting Integral Integral EExia IIC T6 Zone 0 EExia IIC T6 Zone 0 29. Certification IP-65 IP-65 Enclosure Rating DC 24 V DC 24 V 30. Elec. Power or Air Supply 1/2" NPT (F) 1/2" NPT (F) 31. Electrical Entry 32. Upper Liquid Lean Amine (L) Rich Amine (L) 33. Lower Liquid SERVICE 0.97 / 0.98 1.02 CONDITION 34. Sp. Gr. : Upper Lower (High temp. 35. Press. (psig) : 50 2.3 50 2 Max. Normal / Low temp.) 36. Temp. () : 300 140 / 110 250 140 Max. Normal 37. Interface Level N/A N/A N/A N/A 38. Airset Supply Gage N/A N/A 39. Gage Glass Connections N/A N/A 40. Gage Glass Model No. OPTIONS N/A N/A N/A N/A 41. s No. Form N/A N/A 42. Rating N/A N/A 43. Action of s N/A Note 3. 44. Remote Local Indicator Notes : 1. 1. Top Vendor Level shall (HLL) provide : 660.4mm, the cooling Bottom fin or Level extension (LLL) :as 304.8mm per following requirement. 2. "A" : 422, "B" : 625.2, "C" : 1082.4 3. Vendor shall provide the remote indicator with 2" pipe mounting bracket. (320-LI-13)"168" 4. N/A : Not Applicable GENERAL

HHH HH L


Page 104 of 154

"A" "B"

"C"


REV DATE 0 16/05/00 1 05/09/00 2 28/05/01

320-LT-10 Regenerator Reflux Drum D-3204 C2-0223 Krohne


320-LT-13 Amine Drain Drum

D-3202 3. Line No./Vessel No. C2-0234 4. P&ID NO. Krohne 5. Manufacturer BW25/R/B/M9/ESK/EEx/Z0 BW25/R/N/M9/ESK/EEx/Z0 6. Model Number Class , Div 1, Gr B Class , Div 1, Gr B 7. Area Classification as per NEC 316SS Ti Carbon Steel (Flange) 8. Body or Cage Material ANSI 300# RF ANSI 300# RF Rating & Type 1 1/2" 4" 9. Conn. Size & Location Upper 10. Conn. Size & Location Center 1 1/2" 11. Conn. Size & Location Lower 36" (914mm) 12. Conn. Dim. (Upper flange~Lower flange) BODY/CAGE Top-Side-Bottom Top Mounting 13. Case Mounting Type Yes Yes 14. Rotatable Head N/A N/A 15. Cooling Fin or Extension Displacer Displacer 16. Sensing Method External Internal 17. Connection Type [mm] 457.2 (Note 1.) 762 (Note 2.) 18. Measuring Range 32" (813mm) 32" (813mm) 19. Dimensions [mm] N/A See below drawing 20. Insertion Depth DISPLACER 21. Displacer Extension [mm] 316SS Ti 316SS Ti 22. Displacer or Float Material ATS 340 ATS 340 23. Displacer Spring Mtl Transmitter Transmitter 24. Function 4 ~ 20 mA DC 4 ~ 20 mA DC 25. Output Signal 26. Differential 27. Output Action : Level Rise XMTR/CONT. 28. Mounting Integral Integral EExia IIC T6 Zone 0 EExia IIC T6 Zone 0 29. Certification IP-65 IP-65 Enclosure Rating DC 24 V DC 24 V 30. Elec. Power or Air Supply 1/2" NPT (F) 1/2" NPT (F) 31. Electrical Entry 32. Upper Liquid Lean Amine (L) Rich Amine (L) 33. Lower Liquid SERVICE 0.97 / 0.98 1.02 CONDITION 34. Sp. Gr. : Upper Lower (High temp. 35. Press. (psig) : 50 2.3 50 2 Max. Normal / Low temp.) 36. Temp. () : 300 140 / 110 250 140 Max. Normal 37. Interface Level N/A N/A N/A N/A 38. Airset Supply Gage N/A N/A 39. Gage Glass Connections N/A N/A 40. Gage Glass Model No. OPTIONS 41. s No. N/A N/A N/A N/A Form N/A N/A 42. Rating N/A N/A 43. Action of s N/A Note 3. 44. Remote Local Indicator Notes : 1. 1. Top Vendor Level shall (HLL) provide : 660.4mm, the cooling Bottom fin or Level extension (LLL) :as 304.8mm per following requirement. 2. "A" : 422, "B" : 625.2, "C" : 1082.4 3. Vendor shall provide the remote indicator with 2" pipe mounting bracket. (320-LI-13)"168" 4. N/A : Not Applicable GENERAL

HHH HH LL


Page 105 of 154

"A" "B"

"C"


INSTRUMENT DATA SHEETS FOR LEVEL GAUGES

X 1 Gauge Column Assembled with Nipples

X Cocks X Unassembled

4 5 6

19/08/00 25/06/01


CHK'D APP'D T.S.K S.K.K T.S.K S.K.K Y.N.K K.C.IM

GAUGE COCKS X Offset Straight Vessel 1" 300# RF Gage 3/4" NPT (M) Vent 3/4" NPT (F) + Plug Drain 3/4" NPT (F) + Plug CS Material Body Trim 316 SS 550 600 Min. Rating psig at Construction : Quick closing Bonnet : Union Options : Ball Checks X Renewable Seats Other Manufacturer : Jerguson Model No. : 66

7 Type : 8 Conn :

GAUGE GLASSES X Transparent Reflex Tubular Large Chamber Weld Pad Conn : Size and Type : 1" 300# RF Top & Bot. Side X Back Vent : 3/4" NPT Drain : 3/4" NPT Material FORGED CARBON STEEL (Except as note 3,4) 550 600 Min. Rating psig at Options : Internal Tube Mica Shield Non-Frost External Jkt Calb.Scale Ext-Length Illuminator

2 Type : 3

DATE 16/05/00

9 10 11 12 13 14 15

- Power Supply : - Area Classification : - Enclosure : - Cable entry : Other Rev.

Tag No.

Visible

C to C

Glass

Operating (Note 2.)

Length

Length

Model

Press.

Temp.

(mm)

(mm)

No.

(psig)

()

Service (Equipment)

P&ID No.

2

320-LG-06B (Note 3.)

1397

1401

49 RCH-20

65.3

179/147

D-3203

C2-0219

2

400-LG-12 (Note 4.)

559

560

27 RCH-20

99.3

61.3/60.2

D-4010

C2-0159

2

410-LG-07A (Note 4.)

1038

1042

39 RCH-20

99.3

61.3/60.2

D-4105

C2-0157

2

410-LG-07B (Note 4.)

1038

1042

39 RCH-20

99.3

61.3/60.2

D-4105

C2-0157

2

410-LG-12 (Note 4.)

559

560

27 RCH-20

99.3

61.3/60.2

D-4110

C2-0158

2

420-LG-07A (Note 4.)

1038

1042

39 RCH-20

99.3

61.3/60.2

D-4205

C2-0257

2

420-LG-07B (Note 4.)

1038

1042

39 RCH-20

99.3

61.3/60.2

D-4205

C2-0257

2

420-LG-12 (Note 4.)

559

560

27 RCH-20

99.3

61.3/60.2

D-4210

C2-0258

2

510-LG-01

1756

1759

59 RCH-20

350.3

130/86.1

D-5101

C2-0172

2

520-LG-01

1756

1759

59 RCH-20

350.3

130/86.1

D-5201

C2-0272

2

630-LG-01

679

683

29 RCH-20

130 (max)

AMB

D-6301

C2-0302

2

640-LG-01

679

683

29 RCH-20

325.3

229/185

D-6401

C2-0184

2

800-LG-01

1038

1042

39 RCH-20

350

260

D-8001

C2-0801

2

910-LG-01

1397

1401

49 RCH-20

ATM

AMB

D-9101

C2-0189

2

920-LG-01

1397

1401

49 RCH-20

ATM

AMB

D-9201

C2-0289

2

900-LG-01A (Note 4.)

1756

1759

59 RCH-20

0

118 / 39

D-9002

C2-0192

2

900-LG-01B (Note 4.)

1756

1759

59 RCH-20

0

118 / 39

D-9002

C2-0192

NOTES : 1. All gauge glasses shall be armoured type. 2. High Temp Case / Low Temp. Case 3. Chamber Material : 316LSS, Gauge cock body & trim Material : 316LSS 4. Chamber Material : LTCS, Gauge cock body Material : LTCS, Gauge cock trim Material : 316SS


Page 106 of 154

X

DATA SHEET-Sheet 44 REV 0 1 2 3

INSTRUMENT DATA SHEETS FOR PRESSURE GAUGES (DIRECT MOUNTING) Direct Rdg X

1 Type

:

3~15 lb receiver

2 Mounting

:

Surface

Local X

3 Dial

:

Diameter

160mm Φ

4 Case

:

Cast Iron

Alumin.

5 Ring

:

11 Press. Element

:

Screwed X

Hinged

Std

Other

Note 1.

12 Element Mtl

:

Bronze

Steel

316 SS Ti

Phenol

13 Socket Mtl

:

Bronze

Steel

316 SS Ti

Slip

14 Connection

:

15 Movement

:

Shatterproof X

:

Glass

8 Option

:

1. Siphon

Material

2. Snubber

Material

MFR.

3. Pressure Limit Valve

Material

Wetted Part Mtl

4. Movement Damping

Material

Fill Fluid

Rev.

Tag No.

3 3 3

Back SS X

Bronze

PF NPT(M)

Other

Nylon

Other 16 Diaphragm Seal

±1.0% F.S. Range

1/4"

Bottom X

Disc

7 Lens

9 Nominal Accuracy Required

NPT X

PT 1/2" X

Other Plastic ?

Bellows

Other

Back X

None

Solid Front X

Bourdon X Other

304SS

Other

:

WIKA / 232.30.160

Flush Color

BY CHK'D APP'D J.B.R T.S.K S.K.K J.B.R T.S.K S.K.K J.B.R T.S.K S.K.K J.B.R Y.N.K K.C.I

10 MFR. & Model No.

Other


DATE 25/05/00 04/10/00 26/10/00 13/09/01

Type

Process Conn

Pressure (psig)

Other Mtl Gage Conn

Temperature ()

Service

P&ID No.

212

P-3004A Discharge

C2-0145

212

P-3004B Discharge

C2-0145

214

260

Fuel gas to Fuel gas K.O pot

C2-0139C

100

214

260


C2-0139C

100

214

260


C2-0139C

60

90

80

212

P-3001A Discharge

C2-0135

60

90

80

212

P-3001B Discharge

C2-0135

135.3

160

95

260

Blanket gas to TK-3001

C2-0135

60

85

140

212

Fresh amine from FIL-3002

C2-0135

130

190

320

370

Heating medium from FIL-3003

C2-0144

137

151

80

212


C2-0145

0 - 300

145

190

265

370


C2-0140A

0 - 300

145

190

265

370


C2-0140B

300-PI-51C/A-H (8EA)

0 - 300

145

190

265

370


C2-0140C

3

300-PI-59A/A-H (8EA)

0 - 300

209

260

55

500

Fuel Gas to F-3001A

C2-0140A

3

300-PI-59B/A-H (8EA)

0 - 300

209

260

55

500

Fuel Gas to F-3001B

C2-0140B

3

300-PI-59C/A-H (8EA)

0 - 300

209

260

55

500

Fuel Gas to F-3001C

C2-0140C

3

300-PI-60A/A-H (8EA)

0 - 300

160.2

209

265

370


C2-0140A

3

300-PI-60B/A-H (8EA)

0 - 300

160.2

209

265

370


C2-0140B

3

300-PI-60C/A-H (8EA)

0 - 300

160.2

209

265

370


C2-0140C

3

310-PI-08

0 - 100

65.3

78.4

179.1

235

D-3103

C2-0119

3

310-PI-10A

0 - 100

65.3

78.4

178.9

300

Rich amine to E-3101A

C2-0120

3

310-PI-10B

0 - 100

65.3

78.4

178.9

300

Rich amine to E-3101B

C2-0120

3

310-PI-10C

0 - 100

65.3

78.4

178.9

300

Rich amine to E-3101C

C2-0120

(psig)

Nor.

Max.

Nor.

Max.

300-PI-16A

0 - 200

137

175

80

300-PI-16B

0 - 200

137

175

80

300-PI-18A

0 - 100

55.3

100

3

300-PI-18B

0 - 100

55.3

3

300-PI-18C

0 - 100

55.3

3

300-PI-19A

0 - 120

3

300-PI-19B

0 - 120

3

300-PI-20

0 - 200

3

300-PI-28

0 - 100

3

300-PI-29

0 - 200

3

300-PI-30

0 - 200

3

300-PI-51A/A-H (8EA)

3

300-PI-51B/A-H (8EA)

3

NOTES : 1. All gauges shall have a white background with black scale markings.


Page 107 of 154



1 Type

:

3~15 lb receiver

2 Mounting

:

Surface

Local X

3 Dial

:

Diameter

160mmΦ

4 Case

:

Cast Iron

Alumin.

5 Ring

:

11 Press. Element

:

Screwed X

Note 1.

12 Element Mtl

:

Bronze

Steel

316 SS Ti

Phenol

13 Socket Mtl

:

Bronze

Steel

316 SS Ti

Slip

14 Connection

:

Back X

None

Solid Front X

15 Movement

:

Shatterproof X

7 Lens

:

Glass

8 Option

:

1. Siphon

Material

2. Snubber

Material

MFR.


Material

Wetted Part Mtl

4. Movement Damping

Material

Fill Fluid

9 Nominal Accuracy Required Tag No.

3 3

Other Back SS X

Bronze

PF NPT(M) Nylon


±1.0% F.S. Range

1/4"

Bottom X

Disc

Other Plastic

NPT X

PT 1/2" X

Other :

Bellows

Other

Hinged

Std

Bourdon X Other

304SS

Other

Rev.

WIKA / 232.30.160

Flush Color


10 MFR. & Model No.

Other


DATE 25/05/00 04/10/00 26/10/00 13/09/01

Type

Process Conn

Pressure (psig)

(psig)

Nor.

Max.

300-PI-01

0 - 120

80

300-PI-02

0 - 120

80

3

300-PI-03

0 - 120

3

300-PI-04A

0 - 150

3

300-PI-04B

0 - 150

3

300-PI-04C

3

300-PI-05A

3

Other Mtl Gage Conn

Temperature ()

Service

P&ID No.

260

PCV-01/1 By

C2-0138

370

Blanket gas to LP flare header

C2-0138

Nor.

Max.

95

95

95

265

80

95

265

370

D-3002

C2-0138

108.3

115

265

370

P-3002A Suction

C2-0139A

108.3

115

265

370

P-3002B Suction

C2-0139A

0 - 150

108.3

115

265

370

P-3002C Suction

C2-0139A

0 - 250

153

213

265

370

P-3002A Discharge

C2-0139A

300-PI-05B

0 - 250

153

213

265

370

P-3002B Discharge

C2-0139A

3

300-PI-05C

0 - 250

153

213

265

370

P-3002C Discharge

C2-0139A

3

300-PI-06A

0 - 250

142

209

265

370


C2-0140A

3

300-PI-06B

0 - 250

142

209

265

370


C2-0140B

3

300-PI-06C

0 - 250

142

209

265

370


C2-0140C

3

300-PI-08A

0 - 250

123

210

320

370

Heating medium to HM header

C2-0140A

3

300-PI-08B

0 - 250

123

210

320

370


C2-0140B

3

300-PI-08C

0 - 250

123

210

320

370


C2-0140C

3

300-PI-09A

0 - 40

21

35

209

260

Fuel gas to F-3001A

C2-0141A

3

300-PI-09B

0 - 40

21

35

209

260

Fuel gas to F-3001B

C2-0141B

3

300-PI-09C

0 - 40

21

35

209

260

Fuel gas to F-3001C

C2-0141C

3

300-PI-10A

0 - 40

21

35

95

260

Pilot gas to F-3001A

C2-0141A

3

300-PI-10B

0 - 40

21

35

95

260

Pilot gas to F-3001B

C2-0141B

3

300-PI-10C

0 - 40

21

35

95

260

Pilot gas to F-3001C

C2-0141C

3

300-PI-12A

0 - 250

130

210

140

370

P-3003A Discharge

C2-0144

3

300-PI-12B

0 - 250

130

210

140

370

P-3003B Discharge

C2-0144

3

300-PI-13

0 - 200

135.3

160

95

260

Blanket gas to TK-3002

C2-0145



Page 108 of 154



1 Type

:

3~15 lb receiver

2 Mounting

:

Surface

Local X

3 Dial

:

Diameter

160mm Φ

4 Case

:

Cast Iron

Alumin.

5 Ring

:

11 Press. Element

:

Screwed X Std

Note 1.

:

Bronze

Steel

316 SS Ti

Phenol

13 Socket Mtl

:

Bronze

Steel

316 SS Ti

Slip

14 Connection

:

Other

Hinged

Solid Front X

15 Movement

:

Shatterproof X

7 Lens

:

Glass

8 Option

:

1. Siphon

Material

2. Snubber

Material

MFR.


Material

Wetted Part Mtl

4. Movement Damping

Material

Fill Fluid


3 3

Other Back SS X

Bronze

PF NPT(M) Nylon


±1.0% F.S. Range

1/4"

Bottom X

Disc

Other Plastic

NPT X

PT 1/2" X

Back X

None

Bellows

12 Element Mtl

Other :

Bourdon X Other

304SS

Other

Rev.

WIKA / 232.30.160

Flush Color


10 MFR. & Model No.

Other


DATE 25/05/00 04/10/00 26/10/00 13/09/01

Type

Process Conn

Pressure (psig)

Other Mtl Gage Conn

Temperature ()

Service

P&ID No.

180

Sales gas to trunkline

C2-0170

180

PL-7001

C2-0171

127.7

180

Sales gas to D-7001

C2-0171

125

180

P-8001A Discharge

C2-0802

150

125

180

P-8001B Discharge

C2-0802

114

150

125

180

P-8001C Discharge

C2-0802

290

350

132

260

Fuel gas to D-8001

C2-0801

0 - 400

290

350

132

260

D-8001

C2-0801

800-PI-05

0 - 400

290

350

56.6

260

EH-8001A

C2-0801

800-PI-06

0 - 400

290

350

56.6

260

EH-8001B

C2-0801

800-PI-11

0 - 35

20

30

146

180

Diesel fuel to GTG-8001A/B

C2-0802

(psig)

Nor.

Max.

Nor.

Max.

700-PI-02

0 - 1000

670.3

720

127.7

700-PI-07

0 - 1000

670.3

720

127.7

3

700-PI-08

0 - 1000

670.3

720

3

800-PI-01A

0 - 200

114

150

3

800-PI-01B

0 - 200

114

3

800-PI-01C

0 - 200

3

800-PI-03

0 - 400

3

800-PI-04

3 3 3 3

900-PI-01

0 - 35

18

33

118

150

D-9002

C2-0192

3

900-PI-02A/B/C (3EA)

0 - 100

48.3

100

123

150

P-9002A/B/C Discharge

C2-0192

3

900-PI-07A/B/C (3EA)

0 - 50

27.2

50

134

290

P-9002A/B/C Suction

C2-0192

3

910-PI-01

0 - 50

10

40

125

180

D-9101

C2-0189

3

910-PI-02A/B (2EA)

0 - 50

25

50

125

180

P-9101A/B Discharge

C2-0189

3

920-PI-01

0 - 50

10

40

125

180

D-9201

C2-0289

3

920-PI-02A/B (2EA)

0 - 50

25

50

125

180

P-9201A/B Discharge

C2-0289



Page 109 of 154


INSTRUMENT DATA SHEETS FOR PRESSURE GAUGES (DIRECT MOUNTING) 1 Type

:

Direct Rdg X

3~15 lb receiver

:

Surface

Local X

3 Dial

:

Diameter

160mm Φ

4 Case

:

Cast Iron

Alumin.

:

Screwed X

Hinged

Std

Other


:

:

Phenol

12 Element Mtl

:

Bronze

Steel

316 SS Ti

13 Socket Mtl

:

Bronze

Steel

316 SS Ti

Other Slip

Solid Front X

14 Connection

:

15 Movement

:

Shatterproof X

7 Lens

:

Glass

8 Option

:

1. Siphon

Material

2. Snubber

Material

MFR.


Material

Wetted Part Mtl

4. Movement Damping

Material

Fill Fluid

9 Nominal Accuracy Required Rev.

Tag No.

3 3

Back SS X

Bronze

PF NPT(M)

Other

Nylon


±1.0% F.S. Range

1/4"

Bottom X

Disc

Other Plastic

NPT X

PT 1/2" X

Back X

None

Bellows

Other Note 1.

304SS

Other 5 Ring

WIKA / 232.30.160 Bourdon X

11 Press. Element Flush Color


10 MFR. & Model No.

Other 2 Mounting

DATE 25/05/00 04/10/00 26/10/00 13/09/01

Type

Process Conn

Pressure (psig)

Other Mtl Gage Conn

Temperature ()

Service

P&ID No.

250

P-3101A Suction

C2-0127

250

P-3101B Suction

C2-0127

207.2

250

P-3101C Suction

C2-0127

170

207.2

250

P-3101A Discharge

C2-0127

170

207.2

250

P-3101B Discharge

C2-0127

99

170

207.2

250

P-3101C Discharge

C2-0127

0 - 200

99

177

207.4

250

Lean amine to E-3104

C2-0128

0 - 200

80.3

177

149.2

250

Lean amine from E-3104

C2-0128

310-PI-37A

0 - 200

70.3

177

149

200

D-3109A

C2-0131

3

310-PI-37B

0 - 200

70.3

177

149

200

D-3109B

C2-0131

3

310-PI-39A

0 - 100

50.3

100

149

200

Lean amine from FIL-3103A

C2-0132

3

310-PI-39B

0 - 100

50.3

100

149

200

Lean amine from FIL-3103B

C2-0132

3

310-PI-40A

0 - 100

40.3

100

149

250

P-3102A Suction

C2-0133A

3

310-PI-40B

0 - 100

40.3

100

149

250

P-3102B Suction

C2-0133A

3

310-PI-40C

0 - 100

40.3

100

149

250

P-3102C Suction

C2-0133A

3

310-PI-41A

0 - 1400

862

1000

150.7

250

P-3102A Discharge

C2-0133A

3

310-PI-41B

0 - 1400

862

1000

150.7

250

P-3102B Discharge

C2-0133A

3

310-PI-41C

0 - 1400

862

1000

150.7

250

P-3102C Discharge

C2-0133A

3

310-PI-43A

0 - 150

60

130

140

250

P-3104A Discharge

C2-0134

3

310-PI-43B

0 - 150

60

130

140

250

P-3104B Discharge

C2-0134

(psig)

Nor.

Max.

Nor.

Max.

310-PI-29A

0 - 10

4

5

207.2

310-PI-29B

0 - 10

4

5

207.2

3

310-PI-29C

0 - 10

4

5

3

310-PI-30A

0 - 200

99

3

310-PI-30B

0 - 200

99

3

310-PI-30C

0 - 200

3

310-PI-31

3

310-PI-32

3



Page 110 of 154



1 Type

:

3~15 lb receiver

2 Mounting

:

Surface

Local X

3 Dial

:

Diameter

160mm Φ

4 Case

:

Cast Iron

Alumin.

11 Press. Element

Screwed X

Hinged

Std

Other


:

:

Note 1. Phenol

Solid Front X

Slip

12 Element Mtl

:

Bronze

Steel

316 SS Ti

13 Socket Mtl

:

Bronze

Steel

316 SS Ti

14 Connection

:

:

Shatterproof X

:

Glass

8 Option

:

1. Siphon

Material

2. Snubber

MFR.

Material

Wetted Part Mtl

4. Movement Damping

Material

Fill Fluid

Tag No.

3

Nylon

16 Diaphragm Seal

Material

Rev.

NPT(M)

Other Back SS X

Bronze

PF

Other


±1.0% F.S. Range

1/4"

Bottom X 15 Movement

7 Lens


NPT X

PT 1/2" X

Disc

Other Plastic

Bellows

Other

Back X

None

Bourdon X Other

304SS

Other :

WIKA / 232.30.160

Flush Color


10 MFR. & Model No.

Other

5 Ring

DATE 25/05/00 04/10/00 26/10/00 13/09/01

Type

Process Conn

Pressure (psig)

Other Mtl Gage Conn

Temperature ()

Service

P&ID No.

260

24"-A8-D-31026

C2-0123

140

250


C2-0134

179.1

235

D-3203

C2-0219

178.9

300

Rich amine to E-3201A

C2-0220

78.4

178.9

300

Rich amine to E-3201B

C2-0220

78.4

178.9

300

Rich amine to E-3201C

C2-0220

60.3

72.4

210

300

Rich amine from E-3201A

C2-0220

0 - 100

60.3

72.4

210

300

Rich amine from E-3201B

C2-0220

0 - 100

60.3

72.4

210

300

Rich amine from E-3201C

C2-0220

320-PI-12A

0 - 15

9.3

11.2

243.7

300

Lean amine from E-3201A

C2-0220

320-PI-12B

0 - 15

9.3

11.2

243.7

300

Lean amine from E-3201B

C2-0220

3

320-PI-12C

0 - 15

9.3

11.2

243.7

300

Lean amine from E-3201C

C2-0220

3

320-PI-13A

0 - 10

4.3

5.2

207.2

300


C2-0220

3

320-PI-13B

0 - 10

4.3

5.2

207.2

300


C2-0220

3

320-PI-13C

0 - 10

4.3

5.2

207.2

300


C2-0220

(psig)

Nor.

Max.

Nor.

Max.

310-PI-51

0 - 100

55.3

100

214

3

310-PI-58

0 - 100

60

100

3

320-PI-08

0 - 100

65.3

78.4

3

320-PI-10A

0 - 100

65.3

78.4

3

320-PI-10B

0 - 100

65.3

3

320-PI-10C

0 - 100

65.3

3

320-PI-11A

0 - 100

3

320-PI-11B

3

320-PI-11C

3 3

3

320-PI-18

0 - 10

4.3

5.2

196.2

300

Rich amine to E-3203

C2-0222

3

320-PI-21A

0 - 100

66

79

140

300

P-3203A Discharge

C2-0223

3

320-PI-21B

0 - 100

66

79

140

300

P-3203B Discharge

C2-0223

3

320-PI-24A

0 - 250

109.3

209

320

370

Heating Medium to E-3202A

C2-0224

3

320-PI-24B

0 - 250

109.3

209

320

370

Heating Medium to E-3202B

C2-0224



Page 111 of 154


INSTRUMENT DATA SHEETS FOR PRESSURE GAUGES (DIRECT MOUNTING) 1 Type

:

Direct Rdg X

3~15 lb receiver

:

Surface

Local X

3 Dial

:

Diameter

160mm Φ

4 Case

:

Cast Iron

Alumin.

:

Screwed X

Hinged

Std

Other


:

:

Phenol

12 Element Mtl

:

Bronze

Steel

316 SS Ti

13 Socket Mtl

:

Bronze

Steel

316 SS Ti

Other Slip

Solid Front X

14 Connection

:

15 Movement

:

Shatterproof X

7 Lens

:

Glass

8 Option

:

1. Siphon

Material

2. Snubber

MFR.

Material

Wetted Part Mtl

4. Movement Damping

Material

Fill Fluid

Tag No.

3 3

±1.0% F.S. Range

Nylon

16 Diaphragm Seal

Material

Rev.

Back SS X

Bronze

PF NPT(M)

Other

Other

3. Pressure Limit Valve 9 Nominal Accuracy Required

1/4"

Bottom X

Disc

Other Plastic

NPT X

PT 1/2" X

Back X

None

Bellows

Other Note 1.

304SS

Other 5 Ring




10 MFR. & Model No.

Other 2 Mounting

DATE 25/05/00 04/10/00 26/10/00 13/09/01

Type Other Mtl

Process Conn

Pressure (psig)

Gage Conn

Temperature ()

Service

P&ID No.

250

P-3204A Discharge

C2-0234

250

P-3204B Discharge

C2-0234

214

260

SP-3201

C2-0223

100

140

250


C2-0234

31

5.3

20

D-4003

C2-0159

24

29

4.8

20

Propane from D-4003

C2-0159

0 - 150

99.3

119.2

61.3

100

Propane from D-4010

C2-0159

0 - 150

99.3

119.2

61.3

100

D-4010

C2-0159

400-PI-34

0 - 400

310.3

372.4

185

225

Propane from C-4001

C2-0159

3

410-PI-02

0 - 1200

725.3

1000

50.8

100

Chilled gas to E-4101

C2-0153

3

410-PI-03

0 - 1200

710.3

1000

130

180

Treated gas from E-4101

C2-0153

3

410-PI-04

0 - 1200

776.3

1000

88

180

Liquid from E-4101

C2-0153

3

410-PI-05

0 - 1400

785.3

1200

98.5

180

MEG to E-4101

C2-0153

3

410-PI-06

0 - 1200

774.3

1000

87.9

180

D-4101

C2-0153

3

410-PI-07A

0 - 1200

774.3

1000

87.9

180

Treated gas to E-4102A

C2-0154

3

410-PI-07B

0 - 1200

774.3

1000

87.9

180

Treated gas to E-4102B

C2-0154

3

410-PI-08A

0 - 1200

734.3

1000

14.5

35

Treated gas to E-4102A

C2-0154

3

410-PI-08B

0 - 1200

734.3

1000

14.5

35

Treated gas to E-4102B

C2-0154

3

410-PI-09A

0 - 1200

725.3

1000

50.8

100

Treated gas from E-4102A

C2-0154

3

410-PI-09B

0 - 1200

725.3

1000

50.8

100

Treated gas from E-4102B

C2-0154

3

410-PI-10A

0 - 1200

761.8

1000

62.6

100

Treated gas from E-4102A

C2-0154

3

410-PI-10B

0 - 1200

761.8

1000

62.6

100

Treated gas from E-4102B

C2-0154

(psig)

Nor.

Max.

Nor.

Max.

320-PI-43A

0 - 150

60

130

140

320-PI-43B

0 - 150

60

130

140

3

320-PI-51

0 - 100

55.3

100

3

320-PI-58

0 - 100

60

3

400-PI-29

0 - 50

26

3

400-PI-30

0 - 50

3

400-PI-32

3

400-PI-33

3



Page 112 of 154


INSTRUMENT DATA SHEETS FOR PRESSURE GAUGES (SAMPLE CONNECTION) Direct Rdg X

1 Type

:

3~15 lb receiver

2 Mounting

:

Surface

Local X

3 Dial

:

Diameter

160mmΦ

4 Case

:

Cast Iron

Alumin.

5 Ring

:

11 Press. Element

:

Screwed X

Hinged

Std

Other

Note 1.

12 Element Mtl

:

Bronze

Steel

316 SS Ti

Phenol

13 Socket Mtl

:

Bronze

Steel

316 SS Ti

Slip

14 Connection

:

15 Movement

:

Shatterproof X

:

Glass

8 Option

:

1. Siphon

Material

2. Snubber

Material

MFR.


Material

Wetted Part Mtl

4. Movement Damping

Material

Fill Fluid

Rev.

Tag No.

3 3

Back SS X

Bronze

PF NPT(M)

Other

Nylon


±1.0% F.S. Range

1/4"

Bottom X

Disc

7 Lens


NPT X

PT 1/2" X

Other Plastic

Bellows

Other

Back X

None

Solid Front X

Bourdon X Other

304SS

Other

:

WIKA / 232.30.160

Flush Color


10 MFR. & Model No.

Other


DATE 09/09/00 04/10/00 26/10/00 13/09/01

Type

Process Conn

Pressure (psig)

Other Mtl Gage Conn

Temperature ()

Service

P&ID No.

212


C2-0135

212


C2-0135

125

180

X-3001

C2-0136

125

180

X-3001

C2-0136

190

320

370


C2-0144

120

190

320

370


C2-0144

137

175

320

370

Heating medium to TK-3002

C2-0145

137

175

320

370


C2-0145

0 - 150

105

131

125

180

X-3004

C2-0146

0 - 250

102.3

209

320

370

Heating medium circulation system

C2-0142

310-PI-102A

0 - 1200

785.3

1000

151.1

235

Filtered gas to flare header

C2-0118

310-PI-102B

0 - 1200

785.3

1000

151.1

235


C2-0118

3

310-PI-103A

0 - 1200

785.3

1000

151.1

235

Treated gas to flare header

C2-0118

3

310-PI-103B

0 - 1200

785.3

1000

151.1

235


C2-0118

3

310-PI-104A

0 - 100

65.2

78

153.3

235

Flash gas to flare header

C2-0119

3

310-PI-104B

0 - 100

65.2

78

153.3

235


C2-0119

3

310-PI-105A

0 - 100

65.3

78

178.9

235

Rich amine to E-3101A/B/C

C2-0119

3

310-PI-105B

0 - 100

65.3

78

178.9

235


C2-0119

3

310-PI-107A

0 - 100

66

79

140

300

Reflex to T-3102

C2-0123

3

310-PI-107B

0 - 100

66

79

140

300

Reflex to T-3102

C2-0123

3

310-PI-108A

0 - 10

4.3

5.2

207

250

Lean amine to D-3105

C2-0126

3

310-PI-108B

0 - 10

4.3

5.2

207

250


C2-0126

3

310-PI-109A

0 - 150

80

100

149

250

X-3101

C2-0129

3

310-PI-109B

0 - 150

80

100

149

250

X-3101

C2-0129

(psig)

Nor.

Max.

Nor.

Max.

300-PI-110A

0 - 100

60

85

140

300-PI-110B

0 - 100

60

85

140

3

300-PI-111A

0 - 50

25

35

3

300-PI-111B

0 - 50

25

35

3

300-PI-112A

0 - 250

120

3

300-PI-112B

0 - 250

3

300-PI-115A

0 - 200

3

300-PI-115B

0 - 200

3

300-PI-116A/B (2EA)

3

300-PI-117A/B (2EA)

3 3



Page 113 of 154


INSTRUMENT DATA SHEETS FOR PRESSURE GAUGES (SAMPLE CONNECTION) 1 Type

:

Direct Rdg X

3~15 lb receiver

:

Surface

Local X

3 Dial

:

Diameter

160mmΦ

4 Case

:

Cast Iron

Alumin.

:

Screwed X

Hinged

Std

Other


:

:

Phenol

12 Element Mtl

:

Bronze

Steel

316 SS Ti

13 Socket Mtl

:

Bronze

Steel

316 SS Ti

Other Slip

Solid Front X

14 Connection

:

15 Movement

:

Shatterproof X

7 Lens

:

Glass

8 Option

:

1. Siphon

Material

2. Snubber

MFR.

Material

Wetted Part Mtl

4. Movement Damping

Material

Fill Fluid

Tag No.

3 3

±1.0% F.S. Range

Nylon

16 Diaphragm Seal

Material

Rev.

Back SS X

Bronze

PF NPT(M)

Other

Other


1/4"

Bottom X

Disc

Other Plastic

NPT X

PT 1/2" X

Back X

None

Bellows

Other Note 1.

304SS

Other 5 Ring




10 MFR. & Model No.

Other 2 Mounting

DATE 09/09/00 04/10/00 26/10/00 13/09/01

Type

Process Conn

Pressure (psig)

Other Mtl Gage Conn

Temperature ()

Service

P&ID No.

250

X-3101

C2-0129

250

X-3101

C2-0129

149

250

X-3101

C2-0129

100

149

250

X-3101

C2-0129

100

149

250

X-3101

C2-0129

77

100

149

250

X-3101

C2-0129

0 - 150

77

100

149

250

X-3101

C2-0129

0 - 150

77

100

149

250

X-3101

C2-0129

310-PI-114A

0 - 100

60

72

149.2

200

Lean amine from D-3109A/B

C2-0132

3

310-PI-114B

0 - 100

60

72

149.2

200


C2-0132

3

310-PI-115A

0 - 100

60

72

140

250


C2-0134

3

310-PI-115B

0 - 100

60

72

140

250


C2-0134

3

320-PI-102A

0 - 1200

785.3

1000

151.1

235


C2-0218

3

320-PI-102B

0 - 1200

785.3

1000

151.1

235


C2-0218

3

320-PI-103A

0 - 1200

785.3

1000

151.1

235


C2-0218

3

320-PI-103B

0 - 1200

785.3

1000

151.1

235


C2-0218

3

320-PI-104A

0 - 100

65.2

78

153.3

235


C2-0219

3

320-PI-104B

0 - 100

65.2

78

153.3

235


C2-0219

3

320-PI-105A

0 - 100

65.3

78

178.9

235


C2-0219

3

320-PI-105B

0 - 100

65.3

78

178.9

235


C2-0219

3

320-PI-107A

0 - 100

66

79

140

300

Reflex to T-3202

C2-0223

3

320-PI-107B

0 - 100

66

79

140

300

Reflex to T-3202

C2-0223

(psig)

Nor.

Max.

Nor.

Max.

310-PI-110A

0 - 150

80

100

149

310-PI-110B

0 - 150

80

100

149

3

310-PI-111A

0 - 150

77

100

3

310-PI-111B

0 - 150

77

3

310-PI-112A

0 - 150

77

3

310-PI-112B

0 - 150

3

310-PI-113A

3

310-PI-113B

3



Page 114 of 154


INSTRUMENT DATA SHEETS FOR PRESSURE GAUGES (SAMPLE CONNECTION) Direct Rdg X

1 Type

:

3~15 lb receiver

2 Mounting

:

Surface

Local X

3 Dial

:

Diameter

160mmΦ

4 Case

:

Cast Iron

Alumin.

5 Ring

:

11 Press. Element

:

Screwed X Std

Note 1.

:

Bronze

Steel

316 SS Ti

Phenol

13 Socket Mtl

:

Bronze

Steel

316 SS Ti

Slip

14 Connection

:

Other

Hinged

Solid Front X

Bottom X

Disc

Other

15 Movement

:

Shatterproof X

Plastic

7 Lens

:

Glass

8 Option

:

1. Siphon

Material

2. Snubber

Material

MFR.


Material

Wetted Part Mtl

4. Movement Damping

Material

Fill Fluid


3 3

Bronze

1/4"

PF NPT(M)

Other Back SS X

Nylon


±1.0% F.S. Range

NPT X

PT 1/2" X

Back X

None

Bellows

12 Element Mtl

Other :

Bourdon X Other

304SS

Other

Rev.

WIKA / 232.30.160

Flush Color


10 MFR. & Model No.

Other


DATE 09/09/00 04/10/00 26/10/00 13/09/01

Type Other Mtl

Process Conn

Pressure (psig)

Gage Conn

Temperature ()

Service

P&ID No.

250


C2-0226

250


C2-0226

149

250

X-3201

C2-0229

149

250

X-3201

C2-0229

100

149

250

X-3201

C2-0229

80

100

149

250

X-3201

C2-0229

77

100

149

250

X-3201

C2-0229

0 - 150

77

100

149

250

X-3201

C2-0229

320-PI-112A

0 - 150

77

100

149

250

X-3201

C2-0229

320-PI-112B

0 - 150

77

100

149

250

X-3201

C2-0229

3

320-PI-113A

0 - 150

77

100

149

250

X-3201

C2-0229

3

320-PI-113B

0 - 150

77

100

149

250

X-3201

C2-0229

3

320-PI-114A

0 - 100

60

72

149.2

200


C2-0232

3

320-PI-114B

0 - 100

60

72

149.2

200


C2-0232

3

320-PI-115A

0 - 100

60

72

140

250


C2-0234

3

320-PI-115B

0 - 100

60

72

140

250


C2-0234

3

410-PI-101A

0 - 1200

774.3

1000

87.9

180


C2-0153

3

410-PI-101B

0 - 1200

774.3

1000

87.9

180


C2-0153

3

410-PI-102A

0 - 500

350.3

500

87.9

180

Condensate to closed drain

C2-0153

3

410-PI-102B

0 - 500

350.3

500

87.9

180


C2-0153

3

410-PI-103A

0 - 1200

710.3

1000

130

180


C2-0153

3

410-PI-103B

0 - 1200

710.3

1000

130

180


C2-0153

3

410-PI-104A

0 - 1200

734.3

1000

14.5

35

Chilled gas to flare header

C2-0155

3

410-PI-104B

0 - 1200

734.3

1000

14.5

35

Chilled gas to flare header

C2-0155

3

410-PI-105A

0 - 1200

734.3

1000

14.5

35


C2-0155

(psig)

Nor.

Max.

Nor.

Max.

320-PI-108A

0 - 10

4.3

5.2

207

320-PI-108B

0 - 10

4.3

5.2

207

3

320-PI-109A

0 - 150

80

100

3

320-PI-109B

0 - 150

80

100

3

320-PI-110A

0 - 150

80

3

320-PI-110B

0 - 150

3

320-PI-111A

0 - 150

3

320-PI-111B

3 3



Page 115 of 154


INSTRUMENT DATA SHEETS FOR PRESSURE GAUGES (CAPSULE TYPE) 1 Type

:

Direct Rdg X

3~15 lb receiver

11 Press. Element

2 Mounting

:

Surface

Local X

3 Dial

:

Diameter

160mmΦ

4 Case

:

Cast Iron

Alumin.

Screwed X

Hinged

Std

Other


:

None

12 Element Mtl

:

Bronze

Steel

316 SS Ti

13 Socket Mtl

:

Bronze

Steel

316 SS Ti

Other Slip

14 Connection

:

Disc X 15 Movement

:

Shatterproof X

:

Glass

8 Option

:

1. Siphon

Material

2. Snubber

MFR.

Material

Wetted Part Mtl

4. Movement Damping

Material

Fill Fluid

Tag No.

Nylon ?

16 Diaphragm Seal

Material

±1.6% F.S. Range

Back SS X

Bronze

PF NPT(M)

Other

Other


1/4"

Bottom X

Other Plastic

NPT X

PT 1/2" X

7 Lens

Rev.

Note 1. Phenol

Back

Solid Front

Bellows X

Bourdon Other

304SS

Other :

WIKA / 632.50.160 :

Flush Color


10 MFR. & Model No.

Other

5 Ring

DATE 25/05/00 04/10/00 26/10/00 13/09/01

Type

Process Conn

Pressure (psig)

Other Mtl Gage Conn

Temperature ()

(psig)

Nor.

Max.

Nor.

Max.

Service

P&ID No.

3

300-PI-11

0-5

2

3

140

370

D-3003

C2-0144

3

300-PI-18/1

0-5

2

3

95

260

PCV-04/1 By

C2-0144

3

300-PI-18/2

0-5

2

3

140

370

PCV-04/2 By

C2-0144

3

310-PI-19

0-5

2.3

2.8

140

300

Rich amine from E-3103

C2-0122

3

310-PI-20

0-5

2.3

2.8

140

300

D-3104

C2-0123

3

310-PI-22A

0-5

2.3

2.8

140

300

P-3103A Suction

C2-0123

3

310-PI-22B

0-5

2.3

2.8

140

300

P-3103B Suction

C2-0123

3

310-PI-28

0-5

1.5

2.5

207

250

D-3105

C2-0126

3

310-PI-42

0-5

2

3

140

250

D-3102

C2-0134

3

310-PI-44/1

0-5

2

3

95

250

PCV-03/1 By

C2-0134

3

310-PI-44/2

0-5

2

3

140

250

PCV-03/2 By

C2-0134

3

320-PI-19

0-5

2.3

2.8

140

300


C2-0222

3

320-PI-20

0-5

2.3

2.8

140

300

D-3204

C2-0223

3

320-PI-22A

0-5

2.3

2.8

140

300

P-3203A Suction

C2-0223

3

320-PI-22B

0-5

2.3

2.8

140

300

P-3203B Suction

C2-0223

3

320-PI-28

0-5

1.5

2.5

207

250

D-3205

C2-0226

3

320-PI-42

0-5

2

3

140

250

D-3202

C2-0234

3

320-PI-44/1

0-5

2

3

95

250

PCV-03/1 By

C2-0234

3

320-PI-44/2

0-5

2

3

140

250

PCV-03/2 By

C2-0234

3

310-PI-106A

0-5

2.3

2.8

140

300

Carbon Dioxide to flare header

C2-0123

3

310-PI-106B

0-5

2.3

2.8

140

300


C2-0123

3

320-PI-106A

0-5

2.3

2.8

140

300


C2-0223

3

320-PI-106B

0-5

2.3

2.8

140

300


C2-0223



Page 116 of 154


INSTRUMENT DATA SHEETS FOR DIFFERENTIAL PRESSURE GAUGES 1 Type

:

Direct Rdg X

3~15 lb receiver

Other Yoke X

2 Mounting

:

Surface

3 Dial

:

Diameter

4 Case

:

Cast Iron

Alumin.

Other

Stainless Steel

Screwed X

Hinged

Std

Other

5 Ring

:


:

Solid Front X

Note 1. Phenol

BY CHK'D APP'D J.B.R T.S.K S.K.K J.B.R T.S.K S.K.K J.B.R T.S.K S.K.K Note 2.

10 MFR. & Model No. 11 Press. Element

:

12 Element Mtl

:

Bronze

Steel

316 SS

13 Socket Mtl

:

Bronze

Steel

316 SS

Flush

120mmΦ (min.) Color

None

DATE 25/05/00 04/10/00 26/10/00

Bourdon

Diaphragm

Other

Other Slip

14 Connection

:

NPT X

PT 1/2" X

Back X

Disc X

Other

15 Movement

7 Lens

:

Glass

8 Option

:

1) 5-Way Manifold (316SS) (Note 3 & 4)

1/4"

Bottom X :

Shatterproof X

Plastic

Bellows

Bronze

PF

Other

Back SS X

Nylon

Other 16 Diaphragm Seal MFR.

Type

Wetted Part Mtl

Other Mtl

Fill Fluid 9 Nominal Accuracy Required

±1.5% F.S.

Process Conn

Gage Conn

Range

Fluid

(psi)

Status

Nor.

Max.

()

1

0 - 20

Liquid

130

190

1

0 - 20

Liquid

137

151

300-PDI-03

1

0 - 20

Liquid

60

2

310-PDI-09

1

0 - 20

Liquid

2

320-PDI-09

1

0 - 20

2

700-PDI-01

1

0 - 20

Rev.

Tag No.

Q'ty

2

300-PDI-01

2

300-PDI-02

2

Pressure (psig) Temp. Oper.

Service

P&ID No.

140

Heating Medium from/to FIL-3003

C2-0144

80

Heating Medium from/to FIL-3004

C2-0145

85

80

Fresh amine from/to FIL-3002

C2-0135

60

100

140

Rich amine from/to FIL-3104

C2-0134

Liquid

60

100

140

Rich amine from/to FIL-3204

C2-0234

Vapor

690.3

720

129

Treated gas from/to D-7001

C2-0170

NOTES : 1. All gauges shall have a white background with black scale markings. 2. Vendor to specify. 3. Manifold connection shall be 1/2" NPT(F). 4. Vendor shall provide the 2" pipe mounting bracket.


Page 117 of 154


INSTRUMENT DATA SHEETS FOR PRESSURE TRANSMITTERS (1/2" NPT) 1 Tag No. SEE PAGE 24,25,26 Hartmann & Braun Manufacturer See Note 1. Model No.

Service

2 Function

Record

Indicate

3 Case

MFR STD X

4 Mounting

Flush

5 Enclosure Class

Area Classification

DATE 25/05/00 18/10/00 19/04/01


X

Control

Nom. Size

Color : Yoke X

Surface

IP-65 Other

AC

DC

24

Roll

Fold

Circular

Range Speed

9 Scale

Type

XMTR

Output 11 Control Modes

Volts Time Marks

Number Power Actual Reading (Model : 416)

Range 10 Transmitter

Other

Class , Div 1, Gr B

Strip

8 Chart Drive

MFR STD X

Other

EExia IIC T6 Zone 0

117V 60Hz

7 Chart

Trans X

Blind

Certification 6 Power Supply

APP'D S.K.K S.K.K K.C.IM

SEE PAGE 24,25,26

Enclosure Rating

GENERAL

CHK'D T.S.K T.S.K Y.N.K

1

2

4~20mA X

10~50mA

For Receiver

See Spec. Sheet

P=Prop (Gain) Sub

3

4

0.2~1.0 Kg/Cm2G (3~15 psig)

I=Integral (Auto-Reset) :

P

s=Slow PI

Other

D=Derivative (Rate)

f=Fast PD

PID

If

Df

Is

Ds

Other CONTROLLER

12 Action

On Meas. increase Output

:

13 Auto-Man. SW

None

Other

14 Set Point Adj.

Manual

15 Manual Reg.

None

16 Output

4~20mA

17 Service

Gage Press X

18 Element Type

Diaphragm

19 Material

Body (Cover flange)

20 Range

Fixed

ELEMENT

MFR STD External

22 Process Conn.

1/4" NPT

Absolute Bourdon

Other

Element (Isolating diaphragm)

SEE PAGE 24,25,26

Set at

Bottom X

Other Back

Other

23 Alarm Switches

Quantity

24 Function

Meas. Var.

25 Options

Filt-Reg

Supply Gage

Output Gage

Diaph Seal

Type

Diaph

Bot Bowl

Form

Length

Material

Conn OPTIONS

Other

Rating

Deviation

Capillary

Valve Manifold

See Note 1.

SEE PAGE 24,25,26

130% of Maximum pressure

1/2" NPT X :

Other

Compound Bellows

316SS Ti

Overrange protection to 1/2" NPT-F X

0.2~1.0 Kg/Cm2G (3~15 psig)

Vacuum Helix Adj. Range

21 Elect. Conn.

Other

Other

10~50mA

X

Decrease

Remote

MFR STD

Location

ALARM

Increase

s To

:

on Inc Press. Charts

2-WAY (316LSS)

1) 2" MOUNTING BRACKET WITH-BOLT & NUTS 2) S.S NAME PLATE

Notes : 1) 5 - 100 mmH2O Range : ASA 800/V15943A-13XX06-Y04-050-157-064-070-023-270/557/244/202/142/376/395/Z2E (Element : 316LSS) 2) 20 - 600 mmH2O Range : ASD 800/V15956A-10XX10-Y04-057-160-170-023-270/557/244/202/142/Z2E (Element : Ceramic) 3) 1.2 - 36.25 psig Range : ASD 800/V15936A-30XX18-Y04-153-170-070-023-270/557/244/202/142/Z2E (Element : Hastelloy "C") 4) 7.6 - 227 psig Range : ASD 800/V15936A-30XX22-Y04-054-170-070-023-270/557/244/202/142/Z2E (Element : Hastelloy "C") 5) 19.2 - 568 psig Range : ASD 800/V15936A-20XX24-Y04-054-170-070-023-270/557/244/202/142/Z2E (Element : Hastelloy "C") 6) 47.4 - 1422 psig Range : ASD 800/V15936A-20XX26-Y04-054-170-070-023-270/557/244/202/142/Z2E (Element : Hastelloy "C")


Page 118 of 154

DATA SHEET-Sheet 56 REV 0 1 2 2b

INSTRUMENT DATA SHEETS FOR PRESSURE TRANSMITTERS (1/2" NPT)

DATE 25/05/00 18/10/00 19/04/01 09/12/02

Set Range

Adj. Range

(psig)

(psig)

Nor.

Max.

()

300-PT-01/1

0 - 200

19.2 - 568

80

95

300-PT-01/2

0 - 200

19.2 - 568

80

95

300-PT-01A

0 - 60

7.6 - 227

21

2

300-PT-01B

0 - 60

7.6 - 227

2

300-PT-01C

0 - 60

7.6 - 227

2

300-PT-12A

0 - 300

2

300-PT-12B

0 - 300

2

300-PT-12C

0 - 300

Rev.

Tag No.

2 2 2

Press. (psig)

BY J.B.R J.B.R J.B.R J.B.R

Temp. Oper.

CHK'D T.S.K T.S.K Y.N.K T.S.K

APP'D S.K.K S.K.K K.C.IM S.K.K

Service

P&ID No.

265

Blanket gas from D-3002

C2-0138

265

Blanket gas to flare header

C2-0138

55

209

Fuel gas to F-3001A

C2-0141A

21

55

209

Fuel gas to F-3001B

C2-0141B

21

55

209

Fuel gas to F-3001C

C2-0141C

19.2 - 568

146.8

213

265

Heating medium from P-3002A/B/C

C2-0140A

19.2 - 568

146.8

213

265


C2-0140B

19.2 - 568

146.8

213

265


C2-0140C

2

300-PT-04

0 - 20

1.2 - 36.5

2

17

140

D-3003

C2-0144

2

300-PT-07A

0 - 250

19.2 - 568

125.3

210

320

Heating medium from F-3001A

C2-0140A

2

300-PT-07B

0 - 250

19.2 - 568

125.3

210

320

Heating medium from F-3001B

C2-0140B

2

300-PT-07C

0 - 250

19.2 - 568

125.3

210

320

Heating medium from F-3001C

C2-0140C

2b

300-PT-11A

0 -250 mmH2O

20 - 600 mmH2O

130

FN-3001A Discharge

C2-0139B

2b

300-PT-11B

0 -250 mmH2O

130

FN-3001B Discharge

C2-0139B

2b

300-PT-11C

0 -250 mmH2O

130

FN-3001C Discharge

C2-0139B

2b

300-PT-52A

-10 - +10mmH2O

5 - 100 mmH2O

-2mm H2O

2 mmH2O

1033

F-3001A

C2-0140A

2b

300-PT-52B

-10 - +10mmH2O

5 - 100 mmH2O

-2mm H2O

2 mmH2O

1033

F-3001B

C2-0140B

2b

300-PT-52C

-10 - +10mmH2O

5 - 100 mmH2O

-2mm H2O

2 mmH2O

1033

F-3001C

C2-0140C

2b

300-PT-54A

-10 - +10mmH2O

5 - 100 mmH2O

-2mm H2O

1mmH2O

1033

F-3001A

C2-0140A

2b

300-PT-54B

-10 - +10mmH2O

5 - 100 mmH2O

-2mm H2O

1mmH2O

1033

F-3001B

C2-0140B

2b

300-PT-54C

-10 - +10mmH2O

5 - 100 mmH2O

-2mm H2O

1mmH2O

1033

F-3001C

C2-0140C

2b

300-PT-56A

-10 - +10mmH2O

5 - 100 mmH2O -2.5mm H2O 5 mmH2O

1033

F-3001A

C2-0140A

2b

300-PT-56B

-10 - +10mmH2O

5 - 100 mmH2O -2.5mm H2O 5 mmH2O

1033

F-3001B

C2-0140B

2b

300-PT-56C

-10 - +10mmH2O

5 - 100 mmH2O -2.5mm H2O 5 mmH2O

1033

F-3001C

C2-0140C

2

300-PT-61A

0 - 150

7.6 - 227

21

135

130

Fuel gas to F-3001A

C2-0141A

2

300-PT-61B

0 - 150

7.6 - 227

21

135

130

Fuel gas to F-3001B

C2-0141B

2

300-PT-61C

0 - 150

7.6 - 227

21

135

130

Fuel gas to F-3001C

C2-0141C

2

310-PT-01/1

0 - 300

19.2 - 568

65.3

150

179

D-3103

C2-0119

2

310-PT-01/2

0 - 300

19.2 - 568

65.2

150

153.3

Fuel gas from D-3103

C2-0119

2

310-PT-02/1

0 - 50

7.6 - 227

1.5

16.5

207


C2-0126

2

310-PT-02/2

0 - 50

7.6 - 227

1.5

16.5

207


C2-0126

2

310-PT-03

0 - 50

7.6 - 227

2

17

140

Blanket gas to D-3102

C2-0134

2

310-PT-07

0 - 300

19.2 - 568

65.2

150

153.3


C2-0119

2

310-PT-08

0 - 1600

119 - 3555

785.3

1000

151.1

Treated gas from T-3101

C2-0118

2

310-PT-14

0 - 50

7.6 - 227

9.3

24.3

243.7

T-3102

C2-0121

2

310-PT-16

0 - 50

7.6 - 227

4.3

19.3

196


C2-0121

2

310-PT-23A

0 - 300

19.2 - 568

109.3

209

320

Heating medium to E-3102A

C2-0124

2

310-PT-23B

0 - 300

19.2 - 568

109.3

209

320

Heating medium to E-3102B

C2-0124

2

310-PT-57

0 - 200

19.2 - 568

40.3

100

149


C2-0133A

2

320-PT-01/1

0 - 300

19.2 - 568

65.3

150

179

D-3203

C2-0219

2

320-PT-01/2

0 - 300

19.2 - 568

65.2

150

153.3


C2-0219

2

320-PT-02/1

0 - 50

7.6 - 227

1.5

16.5

207


C2-0226

2

320-PT-02/2

0 - 50

7.6 - 227

1.5

16.5

207


C2-0226

2

320-PT-03

0 - 50

7.6 - 227

2

17

140

Blanket gas to D-3202

C2-0234

2

320-PT-07

0 - 300

19.2 - 568

65.2

150

153.3


C2-0219

Notes

150mmH2 O 150mmH2 20 - 600 mmH2O O 150mmH2 20 - 600 mmH2O O

216mm H2O 216mm H2O 216mm H2O

:


Page 119 of 154

DATA SHEET-Sheet 57 REV 0 1 2 2a

INSTRUMENT DATA SHEETS FOR TEMPERATURE GAUGES

DATE 25/05/00 25/10/00 13/09/01 09/03/03

BY CHK'D APP'D J.B.R T.S.K S.K.K J.B.R T.S.K S.K.K J.B.R Y.N.K S.K.K J.B.R Y.N.K S.K.K WELL

THERMOMETER 1 Stem :

Threaded X

Plain

Union

10 None

Material

11 Material

2 Stem or Union

:

1/2" X

3/4"

PT

3 Stem Diameter

:

STD X

.250"

.375"

4 Case Material

:

STD 5" (127mm)

5 Dial Size 6 Scale Length 7 Form :

MFR STD 1

Fig. No.

8 External Calibrator X

Other

304SS

Color

Note 1.

Color

Note 1.

Stem Length (mm)

210-TI-11

1 1/2" 300#RF

270

220-TI-11

1 1/2" 300#RF

270

2

316LSS Tapered X

12 Construction

:

Drilled X

Built-Up

Straight

Closed-End Tube

Well Length Must Suit Stem Length. 13 Accuracy

:

±1.0

% of F.S.

Herm Sealed Case

Process

2

316 SS

Other

Adjustable X

Connection

Tag No.

NPT X

By Others

304 SS

WIKA / S5301/4

9 MFR & Model No.

Rev.

:

Included X

Line No.

Range

Temp. ()

Service

P&ID No.

290

Condensate to E-5101

C2-0172

290

Condensate to E-5201

C2-0272

()

Nor.

Max.

8"-B8-L-21005

0 - 400

214.4

8"-B8-L-22005

0 - 400

214.4

2

300-TI-01

2" 300# RF

500

-

0 - 500

265

370

D-3002

C2-0138

2

300-TI-04A

1 1/2" 300#RF

370

16"-A7-HM-30027

0 - 500

265

370


C2-0140A

2

300-TI-04B

1 1/2" 300#RF

370

16"-A7-HM-30035

0 - 500

265

370


C2-0140B

2

300-TI-04C

1 1/2" 300#RF

370

16"-A7-HM-30043

0 - 500

265

370


C2-0140C

2

300-TI-07A

1 1/2" 300#RF

370

16"-A7-HM-30029

0 - 500

320

370

Heating medium from F-3001A

C2-0140A

2

300-TI-07B

1 1/2" 300#RF

370

16"-A7-HM-30039

0 - 500

320

370

Heating medium from F-3001B

C2-0140B

2

300-TI-07C

1 1/2" 300#RF

370

16"-A7-HM-30051

0 - 500

320

370

Heating medium from F-3001C

C2-0140C

2

300-TI-16

2" 300# RF

500

-

0 - 500

140

370

D-3003

C2-0144

2

300-TI-17

1 1/2" 300#RF

220

3"-A7-HM-30076

0 - 500

140

370


C2-0144

2

300-TI-18

2" 300# RF

500

-

0 - 250

125

212

TK-3002

C2-0145

2

300-TI-19

2" 300# RF

500

-

0 - 250

125

212

TK-3001

C2-0135

2

310-TI-05

2" 600# RF

500

-

0 - 300

151

235

D-3113

C2-0118

2

310-TI-15

2" 300# RF

500

-

0 - 300

179

235

D-3103

C2-0119

2

310-TI-17

1 1/2" 300#RF

400

24"-A18-RA-31006

0 - 300

178.9

235


C2-0119

2

310-TI-20

1 1/2" 300#RF

400

24"-A18-RA-31006

0 - 400

178.9

300

Rich amine from D-3103

C2-0120

2

310-TI-22

1 1/2" 300#RF

400

20"-A17-LA-31001

0 - 500

243.7

300

Lean amine from T-3102

C2-0120

2

310-TI-21A

1 1/2" 300#RF

370

16"-A10-RA-31011

0 - 400

210

300


C2-0120

2

310-TI-21B

1 1/2" 300#RF

370

16"-A10-RA-31013

0 - 400

210

300


C2-0120

2

310-TI-21C

1 1/2" 300#RF

370

16"-A10-RA-31014

0 - 400

210

300

Rich amine from E-3101C

C2-0120

2

310-TI-23A

1 1/2" 300#RF

370

16"-A16-LA-31004

0 - 400

207.2

300


C2-0120

2

310-TI-23B

1 1/2" 300#RF

370

16"-A16-LA-31005

0 - 400

207.2

300


C2-0120

2

310-TI-23C

1 1/2" 300#RF

370

16"-A16-LA-31006

0 - 400

207.2

300


C2-0120

2

310-TI-28

2" 300# RF

500

-

0 - 400

196

300

T-3102

C2-0121

2

310-TI-48

1 1/2" 300#RF

220

30"-A10-RA-31026

0 - 400

196.2

300


C2-0122

2

310-TI-49

1 1/2" 300#RF

240

24"-A10-RA-31032

0 - 300

140

300


C2-0122

NOTES :

1. Black characters on white background.


Page 120 of 154



2a

DATE 25/05/00 25/10/00 13/09/01 09/03/03



Threaded X

Plain

Union

10 None

Material

11 Material

2 Stem or Union

:

1/2" X

3/4"

3 Stem Diameter

:

STD X

.250"

4 Case Material

:

STD 5" (127mm)


MFR STD 1

Fig. No.


304SS

Color

Note 1.

Color

Note 1.

316LSS Tapered X

12 Construction

:

Drilled X

Built-Up

Straight

Closed-End Tube

Well Length Must Suit Stem Length.

Adjustable X

13 Accuracy

:

±1.0

% of F.S.

WIKA / S5301/4

Process

Stem Length (mm)

310-TI-51

2" 300# RF

500

2

310-TI-53A

1 1/2" 300#RF

2

310-TI-53B

1 1/2" 300#RF

2

310-TI-54A

2

2

316 SS

Other

.375"

Other

Connection

Tag No.

NPT X

PT

By Others

304 SS

Herm Sealed Case

9 MFR & Model No.

Rev.

:

Included X

Line No.

Range

Temp. ()

Service

P&ID No.

300

D-3104

C2-0123

320

370


C2-0124

320

370


C2-0124

0 - 400

243.7

300


C2-0124

30"-A10-RA-31034

0 - 400

243.7

300


C2-0124

370

16"-A17-LA-31050

0 - 400

243.7

300


C2-0124

1 1/2" 300#RF

370

16"-A17-LA-31049

0 - 400

243.7

300


C2-0124

1 1/2" 300#RF

300

10"-A7-HM-31004

0 - 400

265

370

Heating medium from E-3102A

C2-0124

310-TI-56B

1 1/2" 300#RF

300

10"-A7-HM-31005

0 - 400

265

370

Heating medium from E-3102B

C2-0124

2

310-TI-57A

1 1/2" 300#RF

370

16"-A18-RA-31025

0 - 400

241.8

300

Rich amine from T-3102

C2-0124

2

310-TI-57B

1 1/2" 300#RF

370

16"-A18-RA-31024

0 - 400

241.8

300


C2-0124

2

310-TI-58

2" 300# RF

500

-

0 - 400

207

250

D-3105

C2-0126

2

310-TI-59

1 1/2" 300#RF

400

20"-A16-LA-31015

0 - 400

207.2

250

Lean amine from D-3105

C2-0126

2

310-TI-68

1 1/2" 300#RF

400

18"-A16-LA-31027

0 - 400

207.4

250


C2-0128

2

310-TI-69

1 1/2" 300#RF

400

18"-A16-LA-31029

0 - 300

149

250


C2-0128

2

310-TI-71A

2" 300# RF

500

-

0 - 300

149

200

D-3109A

C2-0131

2

310-TI-71B

2" 300# RF

500

-

0 - 300

149

200

D-3109B

C2-0131

2

310-TI-72 (Note 2.)

2" 300# RF

1500

-

0 - 300

140

250

D-3102

C2-0134

2

320-TI-05

2" 600# RF

500

-

0 - 300

151

235

D-3213

C2-0218

2

320-TI-15

2" 300# RF

500

-

0 - 300

179

235

D-3203

C2-0219

2

320-TI-17

1 1/2" 300#RF

400

24"-A18-RA-32006

0 - 300

178.9

235


C2-0219

2

320-TI-20

1 1/2" 300#RF

400

24"-A18-RA-32006

0 - 400

178.9

300

Rich amine from D-3203

C2-0220

2

320-TI-22

1 1/2" 300#RF

400

20"-A17-LA-32001

0 - 500

243.7

300


C2-0220

2

320-TI-21A

1 1/2" 300#RF

370

16"-A10-RA-32011

0 - 400

210

300


C2-0220

2

320-TI-21B

1 1/2" 300#RF

370

16"-A10-RA-32013

0 - 400

210

300


C2-0220

2

320-TI-21C

1 1/2" 300#RF

370

16"-A10-RA-32014

0 - 400

210

300

Rich amine from E-3201A/B/C

C2-0220

2

320-TI-23A

1 1/2" 300#RF

370

16"-A16-LA-32004

0 - 400

207.2

300


C2-0220

()

Nor.

Max.

-

0 - 300

140

300

10"-A7-HM-31008

0 - 500

300

10"-A7-HM-31007

0 - 500

1 1/2" 300#RF

250

30"-A10-RA-31030

310-TI-54B

1 1/2" 300#RF

250

2

310-TI-55A

1 1/2" 300#RF

2

310-TI-55B

2

310-TI-56A

2

NOTES :

1. Black characters on white background. 2. Vendor to provide capillary type gauge and well construction shall be straight type.


Page 121 of 154



DATE 25/05/00 25/10/00 13/09/01 09/03/03



Threaded X

Plain

Union

10 None

Material

11 Material

2 Stem or Union

:

1/2" X

3/4"

3 Stem Diameter

:

STD X

.250"

4 Case Material

:

STD 5" (127mm)


MFR STD 1

Fig. No.


304SS

Color

Note 1.

Color

Note 1.

316LSS Tapered X

12 Construction

:

Drilled X

Built-Up

Straight

Closed-End Tube

Well Length Must Suit Stem Length.

Adjustable X

13 Accuracy

:

±1.0

% of F.S.

WIKA / S5301/4

Process

Stem Length (mm)

320-TI-23B

1 1/2" 300#RF

370

2

320-TI-23C

1 1/2" 300#RF

2

320-TI-28

2" 300# RF

2

320-TI-48

2

2

316 SS

Other

.375"

Other

Connection

Tag No.

NPT X

PT

By Others

304 SS

Herm Sealed Case

9 MFR & Model No.

Rev.

:

Included X

Line No.

Range

Temp. ()

Service

P&ID No.

300


C2-0220

207.2

300


C2-0220

196

300

T-3202

C2-0221

0 - 400

196.2

300


C2-0222

24"-A10-RA-32032

0 - 300

140

300


C2-0222

500

-

0 - 300

140

300

D-3204

C2-0223

1 1/2" 300#RF

300

10"-A7-HM-32008

0 - 500

320

370


C2-0224

1 1/2" 300#RF

300

10"-A7-HM-32007

0 - 500

320

370


C2-0224

320-TI-54A

1 1/2" 300#RF

250

30"-A10-RA-32030

0 - 400

243.7

300


C2-0224

2

320-TI-54B

1 1/2" 300#RF

250

30"-A10-RA-32034

0 - 400

243.7

300


C2-0224

2

320-TI-55A

1 1/2" 300#RF

370

16"-A17-LA-32050

0 - 400

243.7

300


C2-0224

2

320-TI-55B

1 1/2" 300#RF

370

16"-A17-LA-32049

0 - 400

243.7

300


C2-0224

2

320-TI-56A

1 1/2" 300#RF

300

10"-A7-HM-32004

0 - 400

265

370


C2-0224

2

320-TI-56B

1 1/2" 300#RF

300

10"-A7-HM-32005

0 - 400

265

370


C2-0224

2

320-TI-57A

1 1/2" 300#RF

370

16"-A18-RA-32025

0 - 400

241.8

300


C2-0224

2

320-TI-57B

1 1/2" 300#RF

370

16"-A18-RA-32024

0 - 400

241.8

300


C2-0224

2

320-TI-58

2" 300# RF

500

-

0 - 400

207

250

D-3205

C2-0226

2

320-TI-59

1 1/2" 300#RF

400

20"-A16-LA-32015

0 - 400

207.2

250

Lean amine from D-3205

C2-0226

2

320-TI-68

1 1/2" 300#RF

400

18"-A16-LA-32027

0 - 400

207.4

250


C2-0228

2

320-TI-69

1 1/2" 300#RF

400

18"-A16-LA-32029

0 - 300

149

250


C2-0228

2

320-TI-71A

2" 300# RF

500

-

0 - 300

149

200

D-3209A

C2-0231

2

320-TI-71B

2" 300# RF

500

-

0 - 300

149

200

D-3209B

C2-0231

2

320-TI-72 (Note 2.)

2" 300# RF

1500

-

0 - 300

140

250

D-3202

C2-0234

2

400-TI-48

1 1/2" 300#RF

270

8"-B5-R-40004

0 - 300

185

225

Propane from C-4001

C2-0159

2

400-TI-56

1 1/2" 300#RF

250

14"-B9-R-40001

0 - 140

4.8

20

Propane from D-4003

C2-0159

2

400-TI-57

1 1/2" 300#RF

250

6"-B9-R-40003

0 - 140

61.3

100

Propane to C-4001

C2-0159

2

400-TI-61

2" 300# RF

500

-

0 - 140

5.3

20

D-4003

C2-0159

()

Nor.

Max.

16"-A16-LA-32005

0 - 400

207.2

370

16"-A16-LA-32006

0 - 400

500

-

0 - 400

1 1/2" 300#RF

220

30"-A10-RA-32026

320-TI-49

1 1/2" 300#RF

240

2

320-TI-51

2" 300# RF

2

320-TI-53A

2

320-TI-53B

2

NOTES :

1. Black characters on white background. 2. Vendor to provide capillary type gauge and well construction shall be straight type.


Page 122 of 154



DATE 25/05/00 25/10/00 13/09/01 09/03/03



Threaded X

Plain

Union

10 None

Material

11 Material

2 Stem or Union

:

1/2" X

3/4"

PT

3 Stem Diameter

:

STD X

.250"

.375"

4 Case Material

:

STD 5" (127mm)


MFR STD 1

Fig. No.


Other

304SS

Color

Note 1.

Color

Note 1.

316LSS Tapered X

12 Construction

:

Drilled X

Built-Up

Straight

Closed-End Tube


:

±1.0

% of F.S.

WIKA / S5301/4

Process

Stem Length (mm)

640-TI-04

1 1/2" 300#RF

250

2

640-TI-05

2" 300# RF

2

640-TI-06

1 1/2" 300#RF

2

640-TI-10A

2

2

316 SS

Other

Adjustable X

Connection

Tag No.

NPT X

By Others

304 SS

Herm Sealed Case

9 MFR & Model No.

Rev.

:

Included X

Line No.

Range

Temp. ()

Service

P&ID No.

Fuel gas to D-6401

C2-0184

260

D-6401

C2-0184

260

Fuel gas to E-6401A

C2-0184

320

400


C2-0184

0 - 500

320

400


C2-0184

2"-B7-HM-64005

0 - 500

265

400


C2-0184

2"-B7-HM-64005

0 - 500

265

400


C2-0184

290

18"-C2-G-70002

0 - 250

128.8

180

Propane to D-7001

C2-0170

1 1/2" 300#RF

250

6"-B7-FG-80003

0 - 300

132

260

Fuel gas to FIL-8001

C2-0801

1 1/2" 300#RF

250

6"-B9-FG-80004

0 - 300

132

260


C2-0801

800-TI-04

1 1/2" 300#RF

250

6"-B9-FG-80007

0 - 300

132

260

Fuel gas to GTG-8001A/B

C2-0801

2

800-TI-06

2" 300# RF

500

-

0 - 250

125

180

TK-8001

C2-0802

2

900-TI-01

2" 300# RF

500

-

0 - 300

141

290

D-9002

C2-0192

2

910-TI-01

2" 300# RF

500

-

0 - 250

125

180

D-9101

C2-0189

2

920-TI-01

2" 300# RF

500

-

0 - 250

125

180

D-9201

C2-0289

()

Nor.

Max.

6"-B7-FG-64007

0 - 400

229

260

500

-

0 - 400

229

250

6"-B9-FG-64009

0 - 300

129

1 1/2" 300#RF

220

2"-B7-HM-64002

0 - 500

640-TI-10B

1 1/2" 300#RF

220

2"-A7-HM-64003

2

640-TI-11A

1 1/2" 300#RF

220

2

640-TI-11B

1 1/2" 300#RF

220

2

700-TI-04

1 1/2" 600#RF

2

800-TI-01

2

800-TI-03

2

NOTES :



Page 123 of 154


INSTRUMENT DATA SHEETS FOR TEMPERATURE GAUGES (SAMPLE CONNECTION)

DATE BY CHK'D APP'D 09/09/00 J.B.R T.S.K S.K.K 25/10/00 J.B.R T.S.K S.K.K 13/09/01 J.B.R Y.N.K S.K.K WELL


Threaded X

Plain

Union

10 None

Material

11 Material

2 Stem or Union

:

1/2" X

3/4"

PT

3 Stem Diameter

:

STD X

.250"

.375"

4 Case Material

:

STD 5" (127mm)


MFR STD 1

Fig. No.


Other

304SS

Color

Note 1.

Color

Note 1.

Stem Length (mm)

:

Drilled X

Built-Up

Straight

Closed-End Tube


300-TI-111

1 1/2" 300# RF

220

2

300-TI-117

1 1/2" 300# RF

2

310-TI-101

1 1/2" 300# RF

2

310-TI-102

2

Line No.

Range

Temp. ()

:

±1.0

% of F.S.

Service

P&ID No.

370


C2-0144

320

370

Heating medium circulation system

C2-0142

179

235


C2-0119

0 - 300

207

250


C2-0126

-

0 - 300

179

235


C2-0219

220

-

0 - 300

207

250


C2-0226

220

-

0 - 300

185

225

Propane to flare header

C2-0158

1 1/2" 300# RF

220

-

0 - 300

185

225

Propane to flare header

C2-0258

1 1/2" 300# RF

220

-

0 - 300

214

260

Fuel gas to flare header

C2-0184

()

Nor.

Max.

-

0 - 500

320

220

-

0 - 500

220

-

0 - 300

1 1/2" 300# RF

220

-

320-TI-101

1 1/2" 300# RF

220

2

320-TI-102

1 1/2" 300# RF

2

410-TI-101

1 1/2" 300# RF

2

420-TI-101

2

640-TI-101

NOTES :

316LSS Tapered X

12 Construction

WIKA / S5301/4

Process

2

316 SS

Other

Adjustable X

Connection

Tag No.

NPT X

By Others

304 SS

Herm Sealed Case

9 MFR & Model No.

Rev.

:

Included X



Page 124 of 154

DATA SHEET-Sheet 62 REV

DATE

BY

0 1 2

15/12/00 20/07/01 06/10/01

D.G.L. K.B.M. K.B.M.

INSTRUMENT DATA SHEETS FOR CONTROL VALVES 1 Tag No. : 300-PCV-04/1 2 Service : BLANKET GAS TO D-3003

SINGLE PORT / STEM GUIDING Type 10 mm 16 mm Size Rated Travel EQ% Characteristic UNBALANCED Balanced/Unbalanced Cg 99.3 FL 0.910 XT 0.559 Rated DIN 1.4571 (316L SS) Plug/Ball/Disk Material DIN 1.4571 (316L SS) Seat Material 316L SS / PTFE Liner Cage/Guide Material DIN 1.4571 (316L SS) Stem Material NEC Class Tube Material Fitting Material

I

Group

D

AISI 316SS AISI 316SS (SWAGELOK)

Solenoid Valve Tag No. N/A No Supply Voltage N/A Enclosure Protection N/A Others N/A Body Material N/A

Notes :

Div 2

1.253 / -

47.157 82 85 57 58 59 60 61 62 63 64 65 66 67 68 69 70 71 72 73 74 75 76 77 78 79 80 81 82 83 84 85 86 87 88 89 90 91 92 93 94 95 96 97 98

76

(0.485/0.555)/ - /(18.71/18.99)

0.012/0.0106 1.253/1.263

UNIT

Min. - / 120 - / 135.2 - / 2.3 - / 38

( - /0.555) / - / ( - /18.99)

- / 0.0106

42.496 79 75.1 85

300

- / 1.263

12.655 50 85

64.6

-

Shut-Off -

-

4~20mA Input Signal Electro-Pneumatic Type FISHER & 3582i Mfr & Model Increase On Incr Signal Output Incr / Decr Yes (supply / output) By- Gauges Enclosure Protection EExib IIA T4 Zone2 (IP 65) Limit Switch Mfr & Model s / Rating Actuation Points Tag No. Enclosure Protection Mfr & Model Set Pressure Supply Gauge

N/A N/A N/A N/A N/A N/A FISHER & 67CFR 35 PSIG Yes

Hydro Pressure ANSI/FCI Leakage Class

1. High/Low temperature. 2. Deleted. 3. Deleted.


S.K.K. S.K.K. S.K.K.

-

SPRING & DIAPHRAGM Type FISHER & 657 Mfr & Model 30 Size Eff Area 46 INCH2 MODULATING Application Type FO(Open) Spring Action Open/Close Max Allowable Pressure Min Required Pressure Available Air Supply Pressure 125 psig Max Min 80 PSIG 6 - 30 PSIG Bench Range TOP Actuator Orientation No Handwheel Type No No Air Failure Valve Set at

A C T U A T O R

Pipe Line Insulation Globe Type 1" 300# Size ANSI Class 500 psi 370/25 ? Design Temp Shut Off ? P FISHER & 1018S.00 Mfr & Model ASTM A216 WCC Body Material ASTM A216 WCC Bonnet Material End In 1" , 300# RF Connection Out 1" , 300# RF ANSI B16.5 , B16.10 Flg Face Finish UP Flow Direction BOLTED BONNET (PLAIN) Type of Bonnet NONE Lube NONE Lub & Iso Valve SINGLE PTFE / GRAPHITE Packing Material V-RING Packing Type

0.012 / -

P O S I T I O N E R

In 2"/SchSTD/2.067 Out 2"/SchSTD/2.067

(0.485/ - ) / - / (18.71/ - )

S W I T C H E S

% dBA

State : Vapor Normal 400 / 400 134.1 / 134.2 2/2 95 / 38

Max. 440 / 133.9 / 2.5 / 95 / -

A I R F I L T E R

Flow Rate (Note 1) Inlet Pressure (Note 1) Outlet Pressure (Note 1) Inlet Temperature (Note 1) Density/Spec. Grav./Mol Wt. (Note 1) Viscosity (Note 1) Spec Heats Ratio Vapor Pressure PV Required Cg Travel Allowable Predicted SPL

Units lb/h psig psig deg F 3 lb/ft / / psia

R E G U L A T O

: BLANKET GAS

Pipe Line Size/Sch/ID

T.S.K. T.S.K. T.S.K.

Line No. : 2"-B6-BG-30018 P&ID No. : PP-17-7-C2-0144

T E S T S

L I N E V A L V E B O D Y / B O N N E T T R I M

15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56

S P E C I A L S / A C C E S S O R I E S

4 5 6 7 8 9 10 11 12 13 14

S E R V I C E C O N D I T I O N S

3 Fluid

CHK'D APP'D

Page 125 of 154

1125 PSIG / 1 MINUTE Class IV

No

-

-

DATA SHEET-Sheet 63 REV INSTRUMENT DATA SHEETS FOR CONTROL VALVES

SINGLE PORT / CAGE GUIDING Type 1 7/8 INCH 3/4 INCH Size Rated Travel EQ% Characteristic BALANCED Balanced/Unbalanced Cg 1170 FL 0.839 XT 0.685 Rated 416 SS HD Plug/Ball/Disk Material 416 SS Seat Material 17-4 PH Cage/Guide Material 316 SS Stem Material NEC Class Tube Material Fitting Material

I

Group

Div 2


Solenoid Valve No Supply Voltage N/A Enclosure Protection N/A Others N/A Body Material N/A

Notes :

D

Tag No. N/A

57 58 59 60 61 62 63 64 65 66 67 68 69 70 71 72 73 74 75 76 77 78 79 80 81 82 83 84 85 86 87 88 89 90 91 92 93 94 95 96 97 98

BY

UNIT

Min. - / 120 -/2 - / 0.1 - / 140

( - /0.049) / - / ( - /18.99) 1.251/1.252 - / 0.0124 - / 1.252

(0.049/0.049)/ - /(18.71/18.99) 0.0123/0.0124

724.347 76 59.2 85

224.518 45 <50 85

-

300

Shut-Off -

-

4~20mA Input Signal Electro-Pneumatic Type FISHER & 3582i Mfr & Model Increase On Incr Signal Output Incr / Decr Yes (supply / output) By- Gauges Enclosure Protection EExib IIA T4 Zone2 (IP 65) Limit Switch Mfr & Model s / Rating Actuation Points Tag No. Enclosure Protection Mfr & Model Set Pressure Supply Gauge





CHK'D APP'D

-


A C T U A T O R

Pipe Line Insulation Globe Type 1 1/2" 300# Size ANSI Class 500 psi 370/25 ? Design Temp Shut Off ? P FISHER & ET Mfr & Model ASTM A216 WCC Body Material ASTM A105 Bonnet Material End In 1 1/2" , 300# RF Connection Out 1 1/2" , 300# RF ANSI B16.5 , B16.10 Flg Face Finish DOWN Flow Direction BOLTED BONNET (PLAIN) Type of Bonnet NONE Lube NONE Lub & Iso Valve PTFE Packing Material V-RING Packing Type

802.721 79 60.1 85

P O S I T I O N E R


1.251 / -

S W I T C H E S

% dBA

(0.049/ - ) / - / (18.71/ - )

0.0123 / -

DATE

15/12/00 D.G.L. T.S.K. S.K.K. 20/07/01 K.B.M. T.S.K. S.K.K. 06/10/01 K.B.M. T.S.K. S.K.K. 20/09/02 K.B.M. T.S.K. S.K.K. Line No. : 2"-A7-BG-30045 P&ID No. : PP-17-7-C2-0144 State : Vapor Normal 400 / 400 2/2 0.1 / 0.1 140 / 140

Max. 440 / 2/0.1 / 140 / -

A I R F I L T E R

V A L V E B O D Y / B O N N E T ( N o t e 3 )


T R I M

15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56



4 5 6 7 8 9 10 11 12 13 14


R E G U L A T O

: BLANKET GAS

T E S T S

3 Fluid S E R V I C E C O N D I T I O N S

: 300-PCV-04/2 : BLANKET GAS TO LP FLARE HEADER

L I N E

1 Tag No. 2 Service

0 1 2 3

Page 126 of 154


No

-

-


DATE

BY

0 1 2

15/12/00 20/07/01 06/10/01

D.G.L. K.B.M. K.B.M.

INSTRUMENT DATA SHEETS FOR CONTROL VALVES


Pipe Line Insulation Globe Type 1" 300# Size ANSI Class 500 psi 250/25 ? Design Temp Shut Off ? P FISHER & 1018S.00 Mfr & Model ASTM A216 WCC Body Material ASTM A216 WCC Bonnet Material End In 1" , 300# RF Connection Out 1" , 300# RF ANSI B16.5 , B16.10 Flg Face Finish UP Flow Direction BOLTED BONNET (PLAIN) Type of Bonnet NONE Lube NONE Lub & Iso Valve SINGLE PTFE / GRAPHITE Packing Material V-RING Packing Type SINGLE PORT / STEM GUIDING Type 15 mm 16 mm Size Rated Travel EQ% Characteristic UNBALANCED Balanced/Unbalanced Cg 147 FL 0.901 XT 0.536 Rated DIN 1.4571 (316L SS) Plug/Ball/Disk Material DIN 1.4571 (316L SS) Seat Material 316L SS / PTFE Liner Cage/Guide Material DIN 1.4571 (316L SS) Stem Material NEC Class Tube Material Fitting Material

I

Group

Div 2


Solenoid Valve No Supply Voltage N/A Enclosure Protection N/A Others N/A Body Material N/A

Notes :

D

Tag No. N/A

0.012/ -

1.253 / -

49.718 73 76.4 85 57 58 59 60 61 62 63 64 65 66 67 68 69 70 71 72 73 74 75 76 77 78 79 80 81 82 83 84 85 86 87 88 89 90 91 92 93 94 95 96 97 98

(0.485/0.555)/ - /(18.71/18.99)

0.012/0.0106

1.253/1.263

UNIT 310/320

Min. - / 120 - / 135.3 - / 2.3 - / 38

Shut-Off -

( - /0.555) / - / ( - /18.99)

- /0.0106

45.137 71 75.6 85

- /1.263

12.646 40 85

64.6

-

-

-

4~20 mA Input Signal Electro-Pneumatic Type FISHER & 3582i Mfr & Model Increase On Incr Signal Output Incr / Decr Yes (supply / output) By- Gauges Enclosure Protection EExib IIA T4 Zone2 (IP 65) Limit Switch Mfr & Model s / Rating Actuation Points Tag No. Enclosure Protection Mfr & Model Set Pressure Supply Gauge





S.K.K. S.K.K. S.K.K.

Page 127 of 154


-

-


A C T U A T O R


% dBA

(0.485/ - ) / - / (18.71/ - )

P O S I T I O N E R


State : Vapor Normal 400 / 400 134.3 / 134.4 2/2 95 / 38

Max. 440 / 134.1 / 2.5 / 95 / -

S W I T C H E S


15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56


4 5 6 7 8 9 10 11 12 13 14


A I R F I L T E R

: BLANKET GAS

R E G U L A T O

3 Fluid

T.S.K. T.S.K. T.S.K.

Line No. : 2"-B6-BG-31025 / 32025 P&ID No. : PP-17-7-C2-0134 / 0234

T E S T S

: 310 / 320-PCV-03/1 : BLANKET GAS TO D-3102 / D-3202


1 Tag No. 2 Service

CHK'D APP'D

No

DATA SHEET-Sheet 65 REV INSTRUMENT DATA SHEETS FOR CONTROL VALVES

Pipe Line Insulation Type Size Shut Off ? P Mfr & Model Body Material Bonnet Material End Connection Flg Face Finish Flow Direction Type of Bonnet Lub & Iso Valve Packing Material Packing Type

In 2"/SchXS/1.939 Out 2"/SchXS/1.939

Globe 1 1/2" 300# ANSI Class 50 psi 250/25 ? Design Temp FISHER & ET ASTM A216 WCC ASTM A105 In 1 1/2" , 300# RF Out 1 1/2" , 300# RF ANSI B16.5 , B16.10 DOWN BOLTED BONNET (PLAIN) NONE Lube NONE SINGLE PTFE / GRAPHITE V-RING

SINGLE PORT / CAGE GUIDING Type 1 7/8 INCH 3/4 INCH Size Rated Travel EQ% Characteristic BALANCED Balanced/Unbalanced Cg 1170 FL 0.839 XT 0.685 Rated 416 SS HD Plug/Ball/Disk Material 416 SS Seat Material 17-4 PH Cage/Guide Material 316 SS Stem Material NEC Class Tube Material Fitting Material

I

Group

D


Solenoid Valve Tag No. N/A No Supply Voltage N/A Enclosure Protection N/A Others N/A Body Material N/A

Notes :

Div 2

0.0123 / -

802.734 79 57.1 85 57 58 59 60 61 62 63 64 65 66 67 68 69 70 71 72 73 74 75 76 77 78 79 80 81 82 83 84 85 86 87 88 89 90 91 92 93 94 95 96 97 98

(0.049/0.049)/ - /(18.71/18.99)

CHK'D APP'D

UNIT 310/320

Min. - / 120 -/2 - / 0.1 - / 140

( - /0.049) / - / ( - /18.99)

- / 0.0124

729.758 76 56.3 85

- / 1.252

224.523 45 <50 85

-

Shut-Off -

-

-

SPRING & DIAPHRAGM Type FISHER & 657 Mfr & Model 30 Size Eff Area 46 INCH2 MODULATING Application Type FO(Open) Spring Action Open/Close Max Allowable Pressure Min Required Pressure Available Air Supply Pressure 125 psig Max Min 80 PSIG 6 - 22 PSIG Bench Range TOP Actuator Orientation No Handwheel Type No No Air Failure Valve Set at 4~20 mA Input Signal Electro-Pneumatic Type FISHER & 3582i Mfr & Model Increase On Incr Signal Output Incr / Decr Yes (supply / output) By- Gauges Enclosure Protection EExib IIA T4 Zone2 (IP 65) Limit Switch Mfr & Model s / Rating Actuation Points Tag No. Enclosure Protection Mfr & Model Set Pressure Supply Gauge





BY

1.251 / - 0.0123/0.01241.251/1.252

A C T U A T O R


% dBA

(0.049/ - ) / - / (18.71/ - )

P O S I T I O N E R


DATE

15/12/00 D.G.L. T.S.K. S.K.K. 20/07/01 K.B.M. T.S.K. S.K.K. 06/10/01 K.B.M. T.S.K. S.K.K. 20/09/02 K.B.M. T.S.K. S.K.K. Line No. : 2"-A17-BG-31028 / 32028 P&ID No. : PP-17-7-C2-0134 / 0234 State : Vapor Normal 400 / 400 2/2 0.1 / 0.1 140 / 140

Max. 440 / 2/0.1 / 140 / -

S W I T C H E S


15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56


4 5 6 7 8 9 10 11 12 13 14


A I R F I L T E R

: BLANKET GAS

R E G U L A T O

3 Fluid

T E S T S

: 310 / 320-PCV-03/2 : BLANKET GAS TO LP FLARE HEADER


1 Tag No. 2 Service

0 1 2 3

Page 128 of 154


No

-

-


DATE

BY

0

13/11/00

D.G.L.

T.S.K.

S.K.K.

1

15/01/01

K.B.M.

T.S.K.

S.K.K.

2

16/08/01

K.B.M.

T.S.K.

S.K.K.

INSTRUMENT DATA SHEETS FOR PRESSURE SAFETY VALVES 1. Tag No. 2. Service 3. Line No./Vessel No. GENERAL

CONNECTION

MATERIALS

OPTIONS

BASIS

FLUID DATA

4. P&ID No. 5. Full/Semi Nozzle 6. Safety or Relief 7. Conv., Bellow, Pilot Operated 8. Bonnet Type 9. Size : Inlet Outlet 10. Flange Rating or Screwed 11. Type of Facing 12. Body and Bonnet 13. Seat and Disc 14. Resilient Seat Seal 15. Guide and Rings 16. Spring 17. Bellows 18. Cap : Screwed or Bolted 19. Lever : Plain or Packed 20. Test Gag 21. 22. 23. 24. Code 25. Fire 26. Others 27. Corrosive / Erosive Component 28. Fluid and State 29. Required Capacity 30. Mol. Wt. Oper. sp.gr. 31. Oper. Press. Set Press. (psig) 32. Oper. Temp.(? ) Rel. Temp. (? ) 33. Back Press. Constant 34. (psig) Variable 35. Total 36. % Allowable Overpressure (Note 2) 37. Overpressure Factor 38. Compressibility Factor 39. Latent Heat of Vaporization 40. Ratio of Specific Heats 41. Operating Viscosity () 42. Barometric Pressure 3

43. Density (lb/ft ) 44. Flashing (%) 45. Calc. Area sq in. 46. Selected Area sq in. 47. Orifice Designation 48. Manufacturer 49. Model No. 50. Notes :

UNIT

300

300-PSV-04B HEATING MEDIUM TO D-3003

300-PSV-04C HEATING MEDIUM TO D-3003

3"-A7-HM-30041 / 3"-A7-HM-30042

3"-A7-HM-30047 / 3"-A7-HM-30048

PP-17-7-C2-0140B Full Relief Conventional (Note 1) Closed 2" 1 1/2" 150# 150# RF RF ASME SA216 WCC 316SS 316SS ALLOY STEEL Screwed No

PP-17-7-C2-0140C Full Relief Conventional (Note 1) Closed 2" 1 1/2" 150# 150# RF RF ASME SA216 WCC 316SS 316SS ALLOY STEEL Screwed No

PP-17-7-C2-0144 Full Safety Conventional (Note 1) Closed 1" 2" 150# 150# RF RF ASME SA216 WCC 316SS 316SS ALLOY STEEL

-

-

-

API RP 520,526,527 -

API RP 520,526,527 -

Hydraulic Expansion

Hydraulic Expansion

No TEG+H2O / Liquid

No TEG+H2O / Liquid

114 (usgpm) 0.97 209 320 320 2 0 ~ 18.9 2 ~ 20.9 10% 0.496 60.5 0.2748 0.307 F Dresser (Consolidated)

114 (usgpm) 0.97 209 320 320 2 0 ~ 18.9 2 ~ 20.9 10% 0.496 60.5 0.2748 0.307 F Dresser (Consolidated)

API RP 520,526,527 Yes No TEG+Steam / Vapor 440 (lb/h) 18.3 190 140 400 2 0 ~ 17 2 ~ 19 21% 0.92 1.27 0.013 0.53 0.0358 0.11 D Dresser (Consolidated)

1905-00FC-1-CC-MS-31-RF-LA

1905-00FC-1-CC-MS-31-RF-LA

1905-00DC-2-CC-MS-31-RF-GS-HP

1. Conventional : Up to 10% back pressure. Balanced Bellows : Up to 50% back pressure (Vendor to confirm). Pilot operated : Up to 100% back pressure (Internal pick-up with non flowing type). 2. 10% for blocked discharged , 21% for fire.


CHK'D APP'D

Page 129 of 154

300-PSV-05 HEATING MEDIUM TO D-3003 1 1/2"-A7-HM-30071/2"-A7-HM-30074

Screwed No

DATA SHEET-Sheet 67 INSTRUMENT DATA SHEETS FOR PRESSURE SAFETY VALVES 1. Tag No. 2. Service

CONNECTION

MATERIALS

OPTIONS

BASIS

FLUID DATA



DATE

BY

0

13/11/00

D.G.L.

T.S.K.

S.K.K.

1

15/01/01

K.B.M.

T.S.K.

S.K.K.

2

16/08/01

K.B.M.

T.S.K.

S.K.K.

300-PSV-06 HEATING MEDIUM TO D-3003


REV

UNIT

300

300-PSV-07 BLANKET GAS TO L.P FLARE HEADER

300-PSV-08 BLANKET GAS TO L.P FLARE HEADER

3"-A7-BG-30022 / 4"-A9-F-30007

3"-A7-BG-30023 / 4"-A9-F-30011

Screwed No

PP-17-7-C2-0144 Full Safety Balanced Bellows (Note 1) Closed 1 1/2" 3" 150# 150# RF RF ASME SA216 WCC 316SS 316SS ALLOY STEEL INCONEL Screwed No

PP-17-7-C2-0144 Full Safety Balanced Bellows (Note 1) Closed 1 1/2" 3" 150# 150# RF RF ASME SA216 WCC 316SS 316SS ALLOY STEEL INCONEL Screwed No

-

-

-

API RP 520,526,527 Yes No TEG+Steam / Vapor 440 (lb/h) 18.3 190 140 400 2 0 ~ 17 2 ~ 19 21% 0.92 1.27 0.013 0.53 0.0358 0.11 D Dresser (Consolidated)

API RP 520,526,527 Yes No TEG+Steam / Vapor 2186 (lb/h) 18 50 140 308 0 ~ 15 0 ~ 15 21%

API RP 520,526,527 Yes No TEG+Steam / Vapor 2186 (lb/h) 18 50 140 308 0 ~ 15 0 ~ 15 21%

0.97 1.3 0.014 0.17 0.5527 0.785 H Dresser (Consolidated)

0.97 1.3 0.014 0.17 0.5527 0.785 H Dresser (Consolidated)


1905-30HC-1-CC-MS-31-RF-GS-LP

1905-30HC-1-CC-MS-31-RF-GS-LP

1 1/2"-A7-HM-30072/2"-A7-HM-30073

PP-17-7-C2-0144 Full Safety Conventional (Note 1) Closed 1" 2" 150# 150# RF RF ASME SA216 WCC 316SS 316SS ALLOY STEEL

1. Conventional : Up to 10% back pressure. Balanced Bellows : Up to 50% back pressure (Vendor to confirm). Pilot operated : Up to 100% back pressure (Internal pick-up with non flowing type). 2. 10% for blocked discharged , 21% for fire.


CHK'D APP'D

Page 130 of 154

DATA SHEET-Sheet 68 INSTRUMENT DATA SHEETS FOR PRESSURE SAFETY VALVES

GENERAL

CONNECTION

MATERIALS

OPTIONS

BASIS

FLUID DATA

DATE

BY

0

13/11/00

D.G.L.

CHK'D APP'D T.S.K.

S.K.K.

1

15/01/01

K.B.M.

T.S.K.

S.K.K.

2

16/08/01

K.B.M.

T.S.K.

S.K.K.

UNIT 310/320

1. Tag No. 2. Service

310 / 320-PSV-15 (Note3) RICH AMINE TO AMINE DRAIN DRUM

310 / 320-PSV-16 (Note3) RICH AMINE TO AMINE DRAIN DRUM

310 / 320-PSV-17 (Note3) BLANKET GAS TO L.P FLARE HEADER

3. Line No./Vessel No.

1"-A17-RA-31051 / 2"-A17-RA-31067

1"-A17-RA-31052 / 2"-A17-RA-31068

4"-A17-BG-31022 / 3"-A9-F-31028

1"-A17-RA-32051 / 2"-A17-RA-32067

1"-A17-RA-32052 / 2"-A17-RA-32068

4"-A17-BG-32022 / 3"-A9-F-32028

PP-17-7-C2-0134 / 0234 Full Safety Conventional (Note 1) Closed 1" 2" 150# 150# RF RF ASME SA216 WCC 316SS 316SS ALLOY STEEL Screwed No -

PP-17-7-C2-0134 / 0234 Full Safety Conventional (Note 1) Closed 1" 2" 150# 150# RF RF ASME SA216 WCC 316SS 316SS ALLOY STEEL Screwed No -

PP-17-7-C2-0134 / 0234 Full Safety Balanced Bellows (Note 1) Closed 1 1/2" 3" 150# 150# RF RF ASME SA216 WCC 316SS 316SS ALLOY STEEL INCONEL Screwed No -

API RP 520,526,527 Yes No Amine+Steam / Vapor 476 (lb/h) 20.65 130 140 373 2 0 ~ 11 2 ~ 13 21% 0.946 1.278 0.013 0.42 0.05083 0.11 D Dresser (Consolidated)

API RP 520,526,527 Yes No Amine+Steam / Vapor 476 (lb/h) 20.65 130 140 373 2 0 ~ 11 2 ~ 13 21% 0.946 1.278 0.013 0.42 0.05083 0.11 D Dresser (Consolidated)

API RP 520,526,527 Yes No Amine+Steam / Vapor 2593 (lb/h) 20 50 140 312 0 ~ 15 0 ~ 15 21% 0.97 1.3 0.014 0.19 0.6236 0.785 H Dresser (Consolidated)



1905-30HC-1-CC-MS-31-RF-GS-HP



REV

1. Conventional : Up to 10% back pressure. Balanced Bellows : Up to 50% back pressure (Vendor to confirm). Pilot operated : Up to 100% back pressure (Internal pick-up with non flowing type). 2. 10% for blocked discharged , 21% for fire. 3. Required heat treament of carbon steel casting.


Page 131 of 154

DATA SHEET-Sheet 69 INSTRUMENT DATA SHEETS FOR PRESSURE SAFETY VALVES 1. Tag No. 2. Service 3. Line No./Vessel No. GENERAL

CONNECTION

MATERIALS

OPTIONS

BASIS

FLUID DATA



REV

DATE

BY

0

13/11/00

D.G.L.

T.S.K.

S.K.K.

1

15/01/01

K.B.M.

T.S.K.

S.K.K.

2

16/08/01

K.B.M.

T.S.K.

S.K.K.

UNIT 310/320

310 / 320-PSV-18 (Note3) BLANKET GAS TO L.P FLARE HEADER

310 / 320-PSV-20 PROCESS GAS TO H.P FLARE HEADER

310 / 320-PSV-23 RICH AMINE TO L.P FLARE HEADER

4"-A17-BG-31023 / 3"-A9-F-31033

10"-A11-G-31044 / 12"-A11-F-31058

3"-A10-RA-31162 / 4"-A9-F-31065

4"-A17-BG-32023 / 3"-A9-F-32033

10"-A11-G-32044 / 12"-A11-F-32058

3"-A10-RA-32162 / 4"-A9-F-32065

PP-17-7-C2-0134 / 0234 Full Safety Balanced Bellows (Note 1) Closed 1 1/2" 3" 150# 150# RF RF ASME SA216 WCC 316SS 316SS ALLOY STEEL INCONEL Screwed No -

PP-17-7-C2-0119 / 0219 Full Safety Balanced Bellows (Note 1) Closed 6" 10" 300# 150# RF RF ASME SA351 CF8M 316SS 316SS ALLOY STEEL INCONEL Screwed No -

PP-17-7-C2-0121 / 0221 Full Safety Balanced Bellows (Note 1) Closed 2" 3" 150# 150# RF RF ASME SA351 CF8M 316SS 316SS ALLOY STEEL INCONEL Screwed No -

API RP 520,526,527 Yes No Amine+Steam / Vapor 2593 (lb/h) 20 50 140 312 0 ~ 15 0 ~ 15 21% 0.97 1.3 0.014 0.19 0.6236 0.785 H Dresser (Consolidated)

API RP 520,526,527 Gas Blow-by Yes Hydro Carbon / Vapor 174352 (lb/h) 22.9 157.5 153 99 0 ~ 30 0 ~ 30 10% 0.96 1.23 0.012 0.71 13.5464 16 R Dresser (Consolidated)

API RP 520,526,527 Yes Yes Amine+Steam / Vapor 3558 (lb/h) 20 50 196 312 0 ~ 15 0 ~ 15 21% 0.97 1.3 0.43 0.19 0.8557 1.287 J Dresser (Consolidated)

1905-30HC-1-CC-MS-31-RF-GS-HP

1910-30RC-2-CC-*-MS-31-RF-GS-HP

1905-30JC-2-CC-*-MS-31-RF-GS-HP

1. Conventional : Up to 10% back pressure. Balanced Bellows : Up to 50% back pressure (Vendor to confirm). Pilot operated : Up to 100% back pressure (Internal pick-up with non flowing type). 2. 10% for blocked discharged , 21% for fire. 3. Required heat treament of carbon steel casting.


CHK'D APP'D

Page 132 of 154

B. INSTRUMENT SUMMARY Instrument Summary for Hydrocarbon Drain System-Sheet 1 UNIT NO.

TAG NO. TAG 3 TAG 4

TYPE

PID NO.

LOCATION

REMARKS

TYPE

P&ID NO

LOCATION

REMARKS

UNIT

TAG 2

910

LT

01

E

0189

L

910

LI

01

S

0189

DCS

910

LSH

01

E

0189

L

910

LAH

01

S

0189

DCS

910

LSHH

01

E

0189

L

910

LAHH

01

S

0189

DCS

910

LSL

01

E

0189

L

910

LAL

01

S

0189

DCS

910

LSLL

01

E

0189

L

910

LALL

01

S

0189

DCS

910

XA

01

A

S

0189

DCS

P-9101A, FAULT

910

XI

01

A/1

S

0189

DCS

P-9101A, RUNNING

910

XI

01

A/3

E

0189

L

P-9101A, RUNNING

910

XI

01

A/2

S

0189

DCS

P-9101A, STOPPED

910

XI

01

A/4

E

0189

L

P-9101A, STOPPED

910

PB

01

A/1

S

0189

DCS

P-9101A, STOP

910

PB

01

A/2

E

0189

L

P-9101A, START

910

PB

01

A/3

E

0189

L

P-9101A, STOP

910

PB

01

A/4

S

0189

ESD

P-9102A, ESD TRIP

910

XA

01

B

S

0189

DCS

P-9101B, FAULT

910

XI

01

B/1

S

0189

DCS

P-9101B, RUNNING

910

XI

01

B/3

E

0189

L

P-9101B, RUNNING

910

XI

01

B/2

S

0189

DCS

P-9101B, STOPPED

910

XI

01

B/4

E

0189

L

P-9101B, STOPPED

910

PB

01

B/1

S

0189

DCS

P-9101B, STOP

910

PB

01

B/2

E

0189

L

P-9101B, START

910

PB

01

B/3

E

0189

L

P-9101B, STOP

910

PB

01

B/4

S

0189

ESD

P-9102B, ESD TRIP

910

PI

01

D

0189

L

910

PI

02

D

0189

L


A

Page 133 of 154

LAHHH REQUIRED

910

TI

01

D

0189

L

910

TW

01

-

0189

L

910

LG

01

D

0189

L

910

RO

01

A

-

0189

L

910

RO

01

B

-

0189

L

920

LT

01

E

0289

L

920

LI

01

S

0289

DCS

920

LSH

01

E

0289

L

920

LAH

01

S

0289

DCS

920

LSHH

01

E

0289

L

920

LAHH

01

S

0289

DCS

LAHHH REQUIRED

Instrument Summary for Hydrocarbon Drain System-Sheet 2 UNIT NO.

TAG NO. TAG 3 TAG 4

TYPE

PID NO.

LOCATION

REMARKS

TYPE

P&ID NO

LOCATION

REMARKS

UNIT

TAG 2

920

LSL

01

E

0289

L

920

LAL

01

S

0289

DCS

920

LSLL

01

E

0289

L

920

LALL

01

S

0289

DCS

920

XA

01

A

S

0289

DCS

P-9201A, FAULT

920

XI

01

A/1

S

0289

DCS

P-9201A, RUNNING

920

XI

01

A/3

E

0289

L

P-9201A, RUNNING

920

XI

01

A/2

S

0289

DCS

P-9201A, STOPPED

920

XI

01

A/4

E

0289

L

P-9201A, STOPPED

920

PB

01

A/1

S

0289

DCS

P-9201A, STOP

920

PB

01

A/2

E

0289

L

P-9201A, START

920

PB

01

A/3

E

0289

L

P-9201A, STOP

920

PB

01

A/4

S

0289

ESD

P-9202A, ESD TRIP

920

XA

01

B

S

0289

DCS

P-9201B, FAULT

920

XI

01

B/1

S

0289

DCS

P-9201B, RUNNING

920

XI

01

B/3

E

0289

L

P-9201B, RUNNING

920

XI

01

B/2

S

0289

DCS

P-9201B, STOPPED

920

XI

01

B/4

E

0289

L

P-9201B, STOPPED

920

PB

01

B/1

S

0289

DCS

P-9201B, STOP

920

PB

01

B/2

E

0289

L

P-9201B, START

920

PB

01

B/3

E

0289

L

P-9201B, STOP


Page 134 of 154

920

PB

01

920

PI

01

920

PI

02

920

TI

920

B/4

S

0289

ESD

D

0289

L

D

0289

L

01

D

0289

L

TW

01

-

0289

L

920

LG

01

D

0289

L

920

RO

01

A

-

0289

L

920

RO

01

B

-

0289

L

A

P-9202B, ESD TRIP

Instrument Summary for Amine Drain System-Sheet 1 UNIT NO.

TAG NO. TAG 3 TAG 4

TYPE

PID NO.

LOCATION

REMARKS

TYPE

P&ID NO

LOCATION

REMARKS

UNIT

TAG 2

310

FI

14

D

0134

L

310

PT

03

E

0134

L

310

PIC

03

/1

S

0134

DCS

PAL REQUIRED

310

PIC

03

/2

S

0134

DCS

PAH REQUIRED

310

LT

13

E

0134

L

310

LI

13

E

0134

L

310

LI

13

S

0134

DCS

310

PDI

09

D

0134

L

310

FE

16

-

0134

L

310

FI

16

D

0134

L

310

PI

42

D

0134

L

310

PI

43

D

0134

L


/1

A

Page 135 of 154

LAHH REQUIRED

310

PI

43

B

D

0134

L

310

PI

44

/1

D

0134

L

310

PI

44

/2

D

0134

L

310

PI

58

D

0134

L

310

TI

72

D

0134

L

310

TW

72

-

0134

L

310

RO

04

A

-

0134

L

310

RO

04

B

-

0134

L

310

PI

115

A

D

0134

L

310

PI

115

B

D

0134

L

310

LSLL

13

E

0134

L

310

LALL

13

S

0134

DCS

310

LSL

13

E

0134

L

310

LAL

13

S

0134

DCS

310

LSHH

14

E

0134

L

310

LAHH

14

S

0134

DCS

310

XA

04

A

S

0134

DCS

FAULT (P-3104A)

310

XI

04

A/1

S

0134

DCS

RUNNING (P-3104A)

310

XI

04

A/3

E

0134

L

RUNNING (P-3104A)

310

XI

04

A/2

S

0134

DCS

STOPPED (P-3104A)

310

XI

04

A/4

E

0134

L

STOPPED (P-3104A)

310

PB

04

A/1

S

0134

DCS

STOP (P-3104A)

310

PB

04

A/2

E

0134

L

START (P-3104A)

310

PB

04

A/3

E

0134

L

STOP (P-3104A)

310

PB

04

A/4

S

0134

ESD

ESD TRIP (P-3104A)

310

XA

04

A

S

0134

DCS

FAULT (P-3104B

310

XI

04

A/1

S

0134

DCS

RUNNING (P-3104B)

310

XI

04

A/3

E

0134

L

RUNNING (P-3104B)

310

XI

04

A/2

S

0134

DCS

STOPPED (P-3104B)

310

XI

04

A/4

E

0134

L

STOPPED (P-3104B)


TAG NO. TAG 3 TAG 4

TYPE

PID NO.

LOCATION

REMARKS

TYPE

P&ID NO

LOCATION

REMARKS

UNIT

TAG 2

310

PB

04

A/1

S

0134

DCS

STOP (P-3104B)

310

PB

04

A/2

E

0134

L

START (P-3104B)


Page 136 of 154

310

PB

04

A/3

E

0134

L

STOP (P-3104B)

310

PB

04

A/4

S

0134

ESD

ESD TRIP (P-3104B)

320

FI

14

D

0234

L

320

PT

03

E

0234

L

320

PIC

03

/1

S

0234

DCS

PAL REQUIRED

320

PIC

03

/2

S

0234

DCS

PAH REQUIRED

320

LT

13

E

0234

L

320

LI

13

E

0234

L

320

LI

13

S

0234

DCS

320

PDI

09

D

0234

L

320

FE

16

-

0234

L

320

FI

16

D

0234

L

320

PI

42

D

0234

L

320

PI

43

A

D

0234

L

320

PI

43

B

D

0234

L

320

PI

44

/1

D

0234

L

320

PI

44

/2

D

0234

L

320

PI

58

D

0234

L

320

TI

72

D

0234

L

320

TW

72

-

0234

L

320

RO

04

A

-

0234

L

320

RO

04

B

-

0234

L

320

PI

115

A

D

0234

L

320

PI

115

B

D

0234

L

320

LSLL

13

E

0234

L

320

LALL

13

S

0234

DCS

320

LSL

13

E

0234

L

320

LAL

13

S

0234

DCS

320

LSHH

14

E

0234

L

320

LAHH

14

S

0234

DCS

320

XA

04

A

S

0234

DCS

FAULT (P-3204A)

320

XI

04

A/1

S

0234

DCS

RUNNING (P-3204A)

320

XI

04

A/3

E

0234

L

RUNNING (P-3204A)

320

XI

04

A/2

S

0234

DCS

STOPPED (P-3204A)

320

XI

04

A/4

E

0234

L

STOPPED (P-3204A)

320

PB

04

A/1

S

0234

DCS

STOP (P-3204A)

320

PB

04

A/2

E

0234

L

START (P-3204A)

320

PB

04

A/3

E

0234

L

STOP (P-3204A)


/1

Page 137 of 154

LAHH REQUIRED

320

PB

04

A/4

S

0234

ESD

ESD TRIP (P-3204A)

320

XA

04

A

S

0234

DCS

FAULT (P-3204B

320

XI

04

A/1

S

0234

DCS

RUNNING (P-3204B)

320

XI

04

A/3

E

0234

L

RUNNING (P-3204B)


TAG NO. TAG 3 TAG 4

TYPE

PID NO.

LOCATION

REMARKS

TYPE

P&ID NO

LOCATION

REMARKS

UNIT

TAG 2

320

XI

04

A/2

S

0234

DCS

STOPPED (P-3204B)

320

XI

04

A/4

E

0234

L

STOPPED (P-3204B)

320

PB

04

A/1

S

0234

DCS

STOP (P-3204B)

320

PB

04

A/2

E

0234

L

START (P-3204B)

320

PB

04

A/3

E

0234

L

STOP (P-3204B)

320

PB

04

A/4

S

0234

ESD

ESD TRIP (P-3204B)

Instrument Summary for Heating Medium Drain System-Sheet1 UNIT NO.

TAG NO. TAG 3 TAG 4

TYPE

PID NO.

LOCATION

REMARKS

TYPE

P&ID NO

LOCATION

REMARKS

UNIT

TAG 2

300

PDI

01

D

0144

L

300

LT

02

E

0144

L

300

LI

02

E

0144

L

300

LI

02

S

0144

DCS

300

FE

03

-

0144

L

300

FI

03

D

0144

L

300

PT

04

E

0144

L

300

PIC

04

/1

S

0144

DCS

PAH AND PAL REQUIRED

300

PIC

04

/2

S

0144

DCS

PAH AND PAL REQUIRED

300

PI

11

D

0144

L

300

PI

12

A

D

0144

L

300

PI

12

B

D

0144

L

300

PI

18

/1

D

0144

L

300

PI

18

/2

D

0144

L


/1

Page 138 of 154

LAHHH REQUIRED

300

PI

29

D

0144

L

300

RO

05

A

-

0144

L

300

RO

05

B

-

0144

L

300

TI

16

D

0144

L

300

TW

16

-

0144

L

300

TI

17

D

0144

L

300

TW

17

-

0144

L

300

LSLL

13

E

0144

L

300

LALL

13

S

0144

DCS

300

LSL

13

E

0144

L

300

LAL

13

S

0144

DCS

300

LSHH/ H

03

E

0144

L

300

LAHH

03

S

0144

DCS

Instrument Summary for Heating Medium Drain System-Sheet2 UNIT NO.

TAG NO. TAG 3 TAG 4

TYPE

PID NO.

LOCATION

REMARKS

TYPE

P&ID NO

LOCATION

REMARKS

S

0144

DCS

UNIT

TAG 2

300

LAH

03

300

XA

23

A

S

0144

DCS

FAULT (P-3003A)

300

XI

23

A/1

S

0144

DCS

RUNNING (P-3003A)

300

XI

23

A/3

E

0144

L

RUNNING (P-3003A)

300

XI

23

A/2

S

0144

DCS

STOPPED (P-3003A)

300

XI

23

A/4

E

0144

L

STOPPED (P-3003A)

300

PB

23

A/1

S

0144

DCS

STOP (P-3003A)

300

PB

23

A/2

E

0144

L

SRART (P-3003A)

300

PB

23

A/3

E

0144

L

STOP (P-3003A)

300

PB

23

A/4

S

0144

ESD

ESD TRIP (P-3003A)

300

XA

23

B

S

0144

DCS

FAULT (P-3003B)

300

XI

23

B/1

S

0144

DCS

RUNNING (P-3003B)

300

XI

23

B/3

E

0144

L

RUNNING (P-3003B)

300

XI

23

B/2

S

0144

DCS

STOPPED (P-3003B)

300

XI

23

B/4

E

0144

L

STOPPED (P-3003B)

300

PB

23

B/1

S

0144

DCS

STOP (P-3003B)

300

PB

23

B/2

E

0144

L

START (P-3003B)

300

PB

23

B/3

E

0144

L

STOP (P-3003B)

300

PB

23

B/4

S

0144

ESD

ESD TRIP (P-3003B)


Page 139 of 154

300

PI

112

A

D

0144

L

300

PI

112

B

D

0144

L

300

TI

111

D

0144

L

300

TW

111

-

0144

L

Instrument Summary for Produced Water Drain System No Instruments are in this system.

9.

DRAWINGS……………………………………………….…………132


Page 140 of 154

Annex 1- Process Flow Diagrams Annex 2- Process and Instrumentation Diagrams Annex 3- Materials of Construction Diagram Annex 4- Plot Plan of the Plant

9. DRAWINGS In annexes are presented: Annex 1- Process Flow Diagrams for Closed Drain System Annex 2- Process and Instrumentation Diagrams for Closed Drain System Annex 3- Materials of Construction Diagram for Closed Drain System Annex 4- Plot Plan of the Plant


Page 141 of 154

10.


SAFETY

Page 142 of 154

A. B. C. D.

GENERAL…………………………………………………………………………….134 GOOD HOUSE KEEPING……………………………………………………………135 MAINTENANCE OF EQUIPMENT………………………………………………….135 USE OF SAFETY ITEMS……………………………………………………………. 136

10. SAFETY A. GENERAL There are some general safety rules for operating areas: Obtain approval before entering any operating area or doing any work on equipment or installation in these areas. Know and understand emergency procedures, both for the area you are working and for the plant as a whole. Be alert for any changes in conditions that may make it unsafe to proceed with your work. Notify your supervisor or responsible operating personnel. Take extra precautions before proceeding with work in areas designated as “Restricted” by the “Custodian”. You must have the proper permit and follow the instructions you have been given for all work. Extra precautions must be observed when doing hazardous work such as confined space jobs, excavation, electrical work, “Hot Work” etc. Never enter an area having a noticeable concentration of gas until you have evaluated the hazard involved.


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-

Label all containers holding toxic, flammable or harmful substances. Make sure that the contents and the hazard(s) indicated on the container are correct.

Before start the unit there are some checks that are must be done: Check Fire fighting Equipment Truck and its Fire Pump are available with supplies for fire fighting, hose, electric cable, floodlights and tools, are ready in the truck and in good condition. Check first aid supplies available. Check the Fire Equipment Cabinets in the area. extinguishers are in place, (including any 125 lb. trailer mounted units) and are at pressure or dated correctly with pins in place. Check burn blankets are in place. Operate reel hoses for a short time. Operate all monitors for a short time, and fire fighting pumps start automatically and firewater tank is full. Establish availability and condition of fire rescue suits and proximity suits. Check safety showers and eyes washes operate and portable eye wash units available. Establish sets of 30 minute SC breathing apparatus and 5 minute escape sets are in good condition and their air cylinders are at pressure. Inspect gas masks. Have available calibrated test apparatus to analyse for combustibles and oxygen. Check all installed field detectors for hydrocarbons are functioning. Check sirens, audible alarms sound and the PA functions. Check out radio and telephone communications and portable loud speakers. Have available low range pressure gauges for use during purging operations. Unit to be free of any debris, scaffolding, mobile equipment, gas cylinders etc. Plant to be taped off with notices posted barring entry except to authorised personnel. Inform utility plant operators of the intention to use plant air, instrument air, and water, power and blanket gas.

B. GOOD HOUSE KEEPING In order to prevent any accident or fire is indicated to maintain all equipment and instruments in proper operating conditions. Also after each intervention in unit or all remaining materials must be evacuates. All road and access way must be keep free for any kind of material in order to not hinder the access in unit. All equipments must be cleaned properly of all debris, sand and oil losses must be eliminated before start up and every time is need.


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C. MAINTENANCE OF EQUIPMENT Equipment Preparation Effective cleaning and gas freeing are required on process equipment, which is to be worked on, or when personnel have to enter the equipment for inspection or repair. It is essential to remove all substances capable of forming mixtures with air, as well as any toxic or corrosive chemicals. Specific methods and procedures will vary depending on the particular vessel and system (size, configuration, contents, piping etc.) but shall be specified in writing prior to actual work or entry. The first requirement is effective isolation of vessel, either by blinding or disconnecting. Included in this process are all auxiliary piping and equipments which could either provide entry paths for contaminants or could provide space for entrapment of such contaminants. When isolated, the vessel system should be emptied of as much product as possible, utilizing any combination of transfer pumping and gravity drainage but all the time taking care to control drainage to a safe area. Where products are toxic and/ or corrosive personnel exposure must be controlled. When purging equipment that contained untreated gas, nitrogen shall be used prior to any washing or venting. Such inert-gas-purging should be continued to a point where flammable gas testing indicates less that 2 % combustible by volume. Acids and caustic are best removed by draining and rapid dilution. The decision as to when all acid or caustic has been washed out of the vessel or system may be made by testing with pH-indicator paper. A gas check must be done before any work can be started. An oxygen check must also be done before any worker allowed into a vessel.

D. USE OF SAFETY ITEMS Work clothing – must be suitable for protection against common hazards expected in industrial area. Must be used all the times. Work clothing should be kept as clean as possible. Head protection – an approved hard hat consists of a hard impact shell and an adjustable inside cradle and distributed over the head surface area. Hand protection – must use leather palm gloves for work with sharp or rough objects – cuts or abrasion. This is recommendation for working with piping, handling etc. To minimize the risk of foot injury, steel-toed shoes or boots must be provided for all employees whose work requires them to be worn.


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Eye protection – is required in situations where exposure to flying particles (sand, dust etc.) may exists. Can be ordinary safety glasses, these have plain, proof glass inside safety frames and must also have attached side shields or goggles, spectacles with side shields, plastic eye shields. Excessive noise – in situations where it is not possible or practical to reduce the noise level (up 90 dBA) is necessary to minimize the possibility of hearing damage through the use of hearing protection devices. There are two type of hearing protection devices used muff protectors and plastic foam plugs. Respiratory protection equipment – fall into air purifying, self-contained breathing air systems, supplied air systems. Minimum 19.5% oxygen is needed for working without supplied air breathing. Air Purifying – Cartridge/ filter type respirators. These types of respiratory protection devices filter air contaminants trough a medium and allow free air to be breathed by workers. Purifying types of respirators do not provide protection in locations where contamination concentration is high or immediately dangerous to life (oxygen deficiency etc.). When the cartridge or canister is used up it should be removed and replaced by a fresh one. Self-contained breathing apparatus is used primarily for emergency work and rescues because of its mobility. The apparatus consists of a pressurized cylinder, which is worn on the person’s back, an air pressure reducer, a full-face mask and a carrying harness.

11.


APPENDIX

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A. B. C. D.

CONVERSION TABLE…………………………………………………………. 138 GENERAL PRE START-UP PROCEDURES……………………………………140 OPERATIONAL PROBLEMS-POSIBLE CAUSES AND REMEDIES…………146 MISCELLANEOUS……………………………………………………………….149

11. APPENDIX A. CONVERSION TABLE UNITS OF LENGTH Unit Symbol

Name of unit

Relationship

1 in = 1”

Inch

25.4 mm

1ft = 1’

Foot

12 in = 0.3048 m

1 yd

Yard

36 in = 3 ft = 0.914398 m

1 mile

Mile

1760 yd = 1 609 m

1 mm

Milimeter

0.03937 in = 0.00328 ft

1 cm

Centimeter

0.3937 in = 0.03281 ft

1m

Meter

39.37 in = 3.28084 ft

1 km

Kilometer

39 370 in = 3280.84 ft = 1093.62 yd

UNITS OF AREA


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Unit Symbol

Name of unit

Relationship

1 sq in

Square inch

6.4516 cm2 = 645.16 mm2

1 sq ft

Square foot

0.0929 m2 = 929.03 cm2

1 sq yd

Square yard

0.83612 m2 = 8361.24 cm2

1a

Acre

4840 sq yd = 4046.24 m2

1 sq mile

Square mile

640 acres = 2.58999 km2

1 cm2

Square centimeter

0.155 sq in

1 m2

Square meter

1550sq in = 10.7639sq ft = 1.19599 sq yd

1 km2

Square kilometer

0.3861 sq mile

UNITS OF VOLUME Unit Symbol

Name of unit

Relationship

1 cu in

Cubic inch

16.3870 cm3

1 cu ft

Cubic foot

0.02832 m3

1 cu yd

Cubic yard

0.7646 m3

1 gal (USA)

Gallon

3.78543 l

1 fl oz (USA)

Fluid ounce

28.413 cm3

1 bus (USA)

Bushel

35.24 l = 0.3524 hl

1 bl (USA)

Barrel

119.24 l = 1.1924 hl

1 cm3

Cubic centimeter

0.06102 cu in

1 dm3 = 1 l

Cubic decimeter = liter

61.0237 cu in = 0.03531 cu ft

1 m3

Cubic meter

35.315 cu ft

Unit Symbol

Name of unit

Relationship

1 gal (USA)

Gallon

8 pints = 4 quarts = 3.7853 l

1qt (USA)

Quart

¼ gallon = 2 pints = 0.9463 l

1 pt (USA)

Pint

1/8 gallon = 0.4732 l

UNITS OF CAPACITY

UNITS OF MASS Unit Symbol

Name of unit

Relationship

1 oz

Ounce

1/16 lb = 28.3495 g

1 lb

Pound

16 oz = 0.453592 Kg

1 sh cwt (USA)

Short hundredweight

100 lb = 45.3592 Kg

1 sh tn (USA)

Short ton

2000 lb = 907.185 Kg

1g

Gram

0.03527 oz = 0.0022 lb


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1 Kg

Kilogram

2.20462 lb = 35.274 oz

1t

Ton

2204.62 lb = 35 274 oz

Unit Symbol

Name of unit

Relationship

K

Kelvin

C

Degree Celsius

F

Degree Fahrenheit

UNTS OF TEMPERATURE

0 C = 32 F 100 C = 212 F 0 K = - 273.15 C = - 459.67 F

(F – 32) X 5 / 9 = C K – 273.15 = C

UNITS OF PRESSURE Unit Symbol

Name of unit

Relationship

1 lbf / sq in (psi)

Pound-force per square inch

0.070307 kgf/cm2 (at)

1 lbf / sq in (psi)

Pound-force per square inch

6894.76 N/m2 (Pa)

1 kgf/cm2 (at)

Kilogram-force per square centimeter

14.2233335 lbf/sq in

1 N/m2 (Pa)

Newton per square meter

0.0000145 lbf/sq in

UNITS OF ENERGY, HEAT AND POWER Unit Symbol

Name of unit

Relationship

1 cal

Calorie

4.1868 J

1J

Joule

0.23884 cal

1 Btu

British Thermal Unit

1055.06 J

1J

Joule

0.000948 Btu

1 Btu


0.2520 kcal

1 kcal

Kilocalorie

3.968254 Btu

1 hp

Horse power

0.74570 kW

1 kW

Kilowatt

1.341022 hp

1 Btu/h


0.293071 W

1W

Watt

3.41242 Btu/h

1 Btu/lb

British Thermal Unit per pound

2.326 kJ/kg

1 kJ/Kg

Kilojoule per kilogram

0.42992 Btu/lb

SPECIFIC GRAVITY


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Degrees Baume:

Be = 145 – (145 / sp gr) Be = (140 / sp gr) – 130

for products heavier than H2O for products lighter than H2O

Degrees Twaddell:Tw = (sp gr 60/60F – 1) / 0.005 Degrees API:

API = (141.5 / sp gr) – 131.5

sp gr = [ gr / dm3]

B. GENERAL PRE START UP PROCEDURES

1.

Air Blowing Procedure

Purpose The purpose of air blowing is to remove loose foreign matter from the inside of line (welding rods, sand, nuts, bolts, tools, etc). Applications The following systems are generally air blow in accordance with Job Specifications Piping System Pressure Testing JS-MP-6045 and Piping Erection And Testing JS-MP-6044: Some process lines of the facilities eg.: vapor lines, airlines, and inert gas lines. Low operating temperature systems (eg. Propane Refrigeration). Hydraulic piping. Lube Oil systems are air blown before lube oil circulation via filters. Flare lines. METHODOLOGY Usage During the cleaning operations, the air velocity can be up to 60 m/s. Two main methods will be used: Continuous Air Blowing. Air is continuously supplied from a source through the lines to carry away the loose material, normally used for small diameter piping.


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Quick Decompression This method is to have SOC approval for use in each case. A pipe network is charged with air up to the release pressure of a plastic film fitted on an open pipe end. When the film is perforated, the pressure inside the network drops quickly providing high velocities and requires minimum air use for these velocities and effectiveness. The rupture devices are planned to be made using polyethylene film. The film will be perforated, at the required release pressure, by a mechanically linked arm. If it mal functions then the air can be released manually. The rupture device will be installed at the one open flange using a temporary holder. Temporary bolts, nuts and gaskets can be used for the device. Alternatively, a network is filled with compressed air up to the required pressure and a valve is open quickly at the end of the system. The pressure in the pipes could be raised up to 90 psig if needed, but design pressure of the system must not be exceeded (Eg.30 to 40 psig for 50 psig design). PREPARATIONS Items that can be damaged or impede air blowing will be removed from the pipe before flushing. These are: Control valves, check valves and relief valves. Orifice plates. Flowmeters: Venturies, Pitot tubes, Rotameters. Nozzles, coupons, probes etc. Traps Butterfly valves. Expansion bellows. Internals of filters and strainers. Thermowells. Impulse lines for instruments and sample lines shall be disconnected. Block valves fully opened and not to be used to control air flow. Pipe restraints, clamps, s will be fitted as required. Equipment to be isolated to avoid dirty air entry. In case of need tarpaulin cover motors, insulation, and instruments near the air outlet. Install a baffle sheet perpendicularly to the flow, in order to break the flow. Temporary s may have to be used, when the lines are disconnected as specified by engineering. Spring s, spring hangers to be ”locked” for air blowing.

Other Preparations


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Precommissioning test sheet “Pipework Flushing Form” , will be prepared, ready for use. The P&ID, ISOS etc. will be used to define the extent of air blowing. The following colors will be used: -Blue for the lines to be flushed -Green for the items to be removed. -Red for the flanges to be disconnected (opened). -Orange for the items to be isolated. Safety High forces can be generated at the air outlet. Therefore, specific safety procedures must be closely adhered to. The following precautions shall be taken for blowing operations: Select time to avoid interference with other activities in the area. Restricted access from the outlet points by roping off and install “no-entry” signs. Work Permits will be issued if needed. Personnel must be equipped with: ear protection, gloves, coveralls, goggles, safety shoes, and safety hat. Air shall never impinge on any equipment Cleanliness Principal checks are: “Colour” of the air at the exit point. This will indicate whether rust and dirt remain inside of the piping. This is usually sufficient for the majority of process and utility piping. Use of a target plate (Eg. for compressor suction lines; GT oil system and FG lines). If the exhaust air appears to be clean install, the target plate and air blow the line. If the plate has became eroded and pitted or distorted, continue the air blowing. When the target plate remains clear the pipe is clean. Ensure that no dirt is re-introduced into the piping during re-assembly following the air blowing. Reestablish pipe condition as per design settings and install all instruments, valves, orifice plates, etc. Once all these activities are concluded sign off PCMT-05 for the System. If pipe system cleaned, was in more that one System put original in System Dossier where maximum piping was and put copies in other System Dossiers as applicable.

2.

Water Flushing Procedure


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1.0 Water Flushing 1.1 Purpose The purpose of water flushing is to clean pipe free of foreign matter such as: loose rust, sand, nuts, bolts, tools, etc light enough to be moved. 2.0 Applications 2.1 Usage Process lines, water and chemical solution lines will normally be flushed with water. Lines, which will be chemically or solvent cleaned can be water flushed first if deemed required. 2.2 Exclusions The following will not normally be water flushed: Air lines, inert gas lines, gas lines, vapor lines should be only air blown. Large diameter lines for which the exercise is redundant, i.e. velocities too low or weight too much as for a vapor line. Low operating temperature systems (eg. Propane refrigeration). Hydraulic pipes. Lube Oil systems. 3.0

Methodology

3.1 Water Rates During flushing, the water velocity target is up to 3m/s. These velocities can be assisted by air injection at the water entry point.

3.2 Flushing with Continuous Water Flow. This type of flushing involves taking a section of piping and flushing it from “start point “ to an open end. Filtered water to be pumped long enough and at target velocity to achieve the required cleanliness. Flushing water will be from the utility or fire water systems or using temporary water tank and imported water. This latter method will be applied for stainless steel and duplex lines, with water as per


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specifications for chloride content as per Job Specification: Piping System Pressure Testing JS-MP6045. 3.3 Fill and Dump Flushing. Fill and dump flushing is used cleaning lines from drums, towers, filters etc. Where continuous flow is impractical, the vented vessel and lines are filled with water to the desired level and then the water is dumped to grade or a safe location (break tank or plastic reservoir). The water dislodges loose debris, rust etc and carries it out of the equipment. 4.0 Preparations 4.1 Piping Preparations The water preparation will be done as per Job Specification JS-MP-6045 and Piping Erection And Testing Job Specification JS-MP-6044. Items that can be damaged or impede cleaning will be removed from the pipe before flushing. These are: Control valves check valves and relief valves. Orifice plates. Flowmeters: Venturies, Pitot tubes, Rotameters. Nozzles, coupons, probes etc. Traps Butterfly valves. Expansion bellows. Internals of filters and strainers. Thermowells. Impulse lines for instruments and sample lines shall be disconnected. Block valves fully opened and not to be used to control water flow. Pipe restraints, clamps, s will be fitted as required. Water discharge will be routed to a “break tank” and drained slowly. Equipment to be isolated to avoid dirty water entry. In case of need tarpaulin cover motors, insulation, and instruments near the flow outlet. Install a baffle sheet perpendicularly to the flow, in order to break the flow into the “break tank”. Temporary s may have to be used, when the lines is disconnected as specified by engineering. Spring s, spring hangers to be ”locked” for flushing.

4.2 Other Preparations


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Precommissioning test sheet “Piperwork Flushing Form” PCMT-05 (See attached), will be prepared, ready for use. The P&ID, ISOS etc. will be used to define the extent of cleaning. The following colours will be used: Blue for the lines to be flushed Green for the items to be removed. Red for the flanges to be disconnected (opened). Orange for the items to be isolated. 5.0 Safety 5.1 Precautions The following precautions shall be taken for water flushing operations: Select time to avoid interference with other activities in the area. Restricted access from the outlet points by roping off and install “no-entry” signs. Work Permits will be issued if needed. -

Personnel must be equipped with: ear protection, gloves, coveralls, goggles, safety shoes, and safety hat.

6.0 cleanliness The “color” of the water at the exit point and other drains and vents will indicate whether rust and dirt remain inside of the piping. The Commissioning representative together with SOC representative will decide that the desired cleanliness has been reached by comparing samples in clean glasses bottles taken at intervals from the water outlets. Inspect end of pipe for accumulation of rubble and remove it. Ensure that no dirt is re-introduced into the piping during re-assembly following the water flushing. Reestablish pipe condition as per design settings and install all instruments, valves, orifice plates, etc. Once all these activities are concluded sign off PCMT-05 for the System. If pipe system cleaned was in more that one System put original in System Dossier where maximum piping was and put copies in other System Dossiers as applicable.

3.

Pressure Testing Procedures


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Planning and Scheduling of Test Drawings and piping shall be reviewed to ensure that adequate temporary s, vents, drains and spades (as necessary to allow testing) are provided to test the facility. All high points in the piping shall be provided with a vent and all low points with a drain, regardless of whether or not they are specifically shown on the drawings. Each Pressure Test Procedure must include the following items:  

     

Mark-ups of piping and instrument diagrams (P&ID’s) showing the limits of piping and equipment to be included in each test. Test diagrams shall show all temporary spools, test blinds, internals, which have been removed to perform the test. All temporarily installed items shall be adequately marked using paint or tag for easy identification. Test medium to be used. Location of all isolation blinds, high point vents, low-point drains, and temporary piping s. Procedures for flushing lines including fill points and equipment to be removed for flushing. Procedures for filling lines including addition of water chemicals in proper quantities. Procedures for pressurization of the system, including the location of the injection points and specified test pressures. The forms that shall be used to record hydrostatic test data.

The test operation shall be conducted carefully, thoroughly, and in a safe manner, in accordance with accepted piping testing practices. Test Method Hydrostatic Method Hydrostatic testing shall be used wherever possible and is preferable to any other testing method. Hydrostatic testing shall be performed using water as the testing medium, unless water is prohibited from process piping or due to other special considerations.

Test Water


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The test water shall be clean and free from suspended matter. Suspended matter in the fill water shall be removed before injection into the piping by a filter, capable of removing 99 per cent of all particles 92 microns in diameter and larger, or equivalent to using a 100 X 100 wire mesh screen. If foreign material is pumped into the piping because of faulty equipment or carelessness, the line shall be again flush with clean water. Only potable water shall be used in piping systems containing stainless steel components. pH of test water shall be between 6 and 8. Conditions requiring the use of corrosion inhibitor, oxygen scavenger and bacteria control, depend on how long the test media shall remain in the system. If potable water is used for hydrostatic testing, corrosion inhibition, oxygen removal and bacteria control shall be required as follows:  

Treatment rate - 150 ppm Treatment Chemical – Visco Uni-treat 3900 or equal

If test water with a maximum of 500ppm chlorides is used for hydrotesting, the following steps shall be taken:  

Isolation of austenitic piping and connected equipment from with the test water Complete removal of test water from the system after testing.

Corrosion inhibition, oxygen removal and bacteria control treatment shall be as follows:  

Treatment rate - 150 ppm Treatment Chemical – Visco Uni-treat 3900 or equal

Water used to test piping or vessels fabricated from or containing parts of austenitic stainless steel, which cannot be isolated, shall not contain more than 30ppm chloride content.

Test Procedure The normal location for the pressure test gauge is at grade near the pressure test pump. Readings may be made at higher points providing static head between grade and point of measurement is subtracted from the specified pressure. During testing, care must be taken not to exceed the specified test pressure.


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When conditions require that a pressure test be maintained for a period of time during which the testing medium in the system would be subject to thermal expansion, and pressure increase (solar heating, heat source vicinity) provision shall be made to relieve of excess of pressure. Piping systems shall be filled from a low point. Vents or high point connections shall be opened to eliminate air from the lines. All air shall be removed from the piping system by venting before hydrostatic test pressure is applied. Hydrostatic test pressure shall not be applied until the pipe and the medium are at approximately the same temperature. Pressure test shall not be conducted when the liquid and/or metal temperature is below 5 degrees C. Test pressure shall be gradually increased. A facility for continuous checking of the test pressure shall be provided. Pressurize the piping system to the specified test pressure and hold for a sufficient length of time to allow the piping to equalize strains. Pressure test shall be recorded on a pressure recorder with a range suitable for recording the test pressure. At the start of each test, the pressure recorder and test gauge shall be verified by a dead weight tester. All hydrostatic tests shall be a minimum of two (2) hours duration. Readings shall be taken from the test gauge at fifteen-minute intervals during the test, and recorded. Test pumps shall be isolated from the system before the pipe inspection. Pressure tests are satisfactory if:  

There are no leaks There are no cracks nor deformation detected during tests.

Leak Testing Procedure Leak testing is most efficiently done with a conveniently sized grouping of vessels/equipment and performed in the order of the process flow sequence. Leak testing is performed with air by raising the piping and equipment pressures with the air to 130 psig. Temporary 150 psig pressure gauges are needed for regulation and monitoring. Tape all flanges in the facility from the block valves between Unit 200 manifolds and headers to the valves on gas inlet to the Inlet Filter Separators FIL-3101A/B and FIL-3201A/B, on the condensate outlet to Unit 510/520, on the produced water outlet to the produced water header. Leaks are indicated by decreasing test system pressure and may be audible. Pressure reduction


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may also be due to a valve leak to another section. The pressure in downstream equipment should be monitored frequently. A search is made methodically for leaks at all flanges, valve packing followers and threaded fittings by applying detergent solution from plastic spray bottles or with a brush to the top hole in the tape at packing or where threads . Any bubbling of the solution indicates a leak. Mark and note the leak locations for corrective actions. After testing and repairs are complete perforate the tape low points, small size hole, so any liquid shall be able to drain. If leaks cannot be tightened up, for example when a gasket replacement is required, check the remainder of the system before depressuring. Then all repairs can be attended to together. There may however be convenient valves to isolate the leak, at a control valve for example. Leak testing is most efficiently done by dividing the system into sections with conveniently sized grouping of vessels / equipment and doing these in the order of the process flow sequence. For example, air in Units 200, whether a leak is found or not, can be ed in part onto the Units 210/220. Ways, like this, of re-using air or nitrogen are managed to optimise gas use and time.

C. OPERATIONAL PROBLEMS – POSSIBLE CAUSES AND REMEDIES Vertical Centrifugal Pumps:

Symptom 1. Pump does not deliver product

Possible cause of failure          


Pump not primed Pump or suction pipe not completely filled with liquid Suction lift too high Insufficient margin between suction pressure and vapor pressure Air or vapor pocket in suction line Inlet of suction pipe insufficiently submerged Speed to low Total head of system higher than head of pump Parallel operation of pumps unsuitable for such operation Foreign matter in impeller

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Symptom 2. Insufficient capacity delivered

Possible cause of failure                  

3. Insufficient pressure developed

       

4. Pump loses prime after starting


    

Pump or suction pipe not completely filled with liquid Suction lift too high Insufficient margin between suction pressure and vapor pressure Excessive amount of air or gas in liquid Air or vapor pocket in suction line Air leaks into suction line Air leaks into pump through sleeve ts, casing ts or pipe plugs Foot valve too small Foot valve partially clogged Inlet of suction pipe insufficiently submerged Speed too low Wrong direction of rotation Total head of system higher than head of pump Viscosity of liquid differs from designed viscosity Parallel operation of pumps unsuitable for such operation Foreign matter in impeller Bearing ring surfaces worn Impeller damaged or eroded Excessive amount of air or gas in liquid Speed too low Wrong direction of rotation Total head of system higher than head of pump Viscosity of liquid differs from designed viscosity Parallel operation of pumps unsuitable for such operation Wearing ring surfaces worn Impeller damaged or eroded

Pump or suction pipe not completely filled with liquid Suction lift too high Excessive amount of air or gas in liquid Air or vapor pocket in suction line Air leaks into suction pump through sleeve ts, casing ts or pipe plugs

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

Symptom 5. Pump requires excessive power

Possible cause of failure             


Inlet of suction pipe insufficiently submerged

Speed too high Wrong direction of rotation Total head of system lower than pump design head Specific gravity of liquid different from design Viscosity of liquid differs from designed viscosity Foreign matter in impeller Misalignment due to pipe strain Shaft bent Rotating part rubbing on stationary part internally Wearing ring surfaces worn Mechanical seal improperly installed Incorrect type of mechanical seal for operating conditions Abrasive solids in liquid pumped

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6. Mechanical seal leaks excessively

            

Symptom 7. Mechanical seal has short life


Misalignment due to pipe strain Shaft bent Bearings worn Leakage under sleeve due to t failure Shaft sleeve worn or scored or running off center Mechanical seal improperly installed Incorrect type of mechanical seal for operating conditions Shaft running off center because of worn bearings or misalignment Impeller out of balance resulting in vibration Abrasive solids in liquid pumped Internal misalignment of parts preventing seal ring and seat from mating properly Mechanical seal was run dry Internal misalignment due to improper repairs causing impeller to rub

Possible cause of failure      

Misalignment due to pipe strain Shaft bend Bearings worn Shaft sleeve worn or scored or running off center Mechanical seal improperly installed Incorrect type of mechanical seal for operating

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     

8. Pump vibrates or is noisy

                  

 


conditions Shaft running off center because of worn bearings or misalignment Impeller out of balance resulting in vibration Abrasive solids in liquid pumped Internal misalignment of parts preventing seal ring and seat from mating properly Mechanical seal was run dry Internal misalignment due to improper repairs causing impeller to rub

Pump or suction pipe not completely filled with liquid Suction lift too high Insufficient margin between suction pressure and vapor Foot valve too small Foot valve partially clogged Inlet of suction pipe insufficiently submerged Operation at very low capacity Foreign matter in impeller Misalignment due to pipe strain Improperly designed foundation Shaft bent Rotating part rubbing on stationary part internally Bearings worn Impeller damaged or eroded Shaft running off center because of worn bearings or misalignment Impeller out of balance resulting in vibration Excessive thrust caused by mechanical failure inside the pump Lack of lubrication for bearings Improper installation of bearings (damage during assembly), incorrect assembly, wrong type of bearings,etc. Dirt getting into bearings Rusting of bearings due to water getting into housing around liquid thrower

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Symptom 9. Bearings have short life

Possible cause of failure         

 

10. Pump overheats and seizes

         

Misalignment due to pipe strain Shaft bent Rotating part rubbing on stationary part internally Bearings worn Shaft running off center because of worn bearings or misalignment Impeller out of balance resulting in vibration Excessive thrust caused by a mechanical failure inside the pump Lack of lubrication of bearings Improper installation of bearings (damage during assembly), incorrect assembly, wrong type of bearings etc Dirt getting into bearings Rusting of bearings due to water getting into housing around liquid thrower Pump not primed Insufficient margin between suction pressure and vapor pressure Operation at very low capacity Parallel operation of pumps unsuitable for such operation Misalignment due to pipe strain Rotating part rubbing on stationary part internally Bearings worn Shaft running off center because of worn bearings or misalignment Impeller out of balance resulting in vibration Excessive thrust caused by a mechanical failure inside the pump

D. MISCELLANEOUS Operating Instruction for Sample Connections


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The Heating Medium Drain Drum Filter is provided with Sample Connection Type 6. The Amine Drain Drum Filters are provided with Sample Connections Type 5. Refer to Appendix 1 and 2 They are use to take samples for products testing. For safe operation of the Sample Connections proceed as follows:

a) For Sample Connection type 5.     

     

that block valve for pressure indicators are open (Valve 8 and 9). that valve 4 and 5 are closed and connect the bottle. Open outlet valve from sample connection to flare / process (Valve 6). Open by- valve of bottle (Valve 7) Open slowly inlets valve in Sample connection (Valve 3) for purge Sample Connection Lines and monitor the temperature by the temperature indicator on outlet from Sample Cooler. Open valves 4 and 5, and also isolating valve of the bottle (NV1 and NV2). Close by- valve (Valve 7) After three minutes, close isolating valves NV2 and NV1 (starting with NV2). Close the inlet valve into Sample connection (Valve 3) Open the by- valve (Valve 7) to de-pressurize the Sample Connection. Close the outlet valve from Sample Connection (Valve 6), close valve 4 and 5, and remove the bottle from connections.

b) For Sample Connection type 6.        

 

whether the Sample Cooler is full with water. If not, if ¾”drain valve of cooler is closed (Valve 1). Open ¾”valve on demineralised water and fill Sample Cooler (Valve 2). that the block valves for the pressure indicators are open (Valve 8 and 9). that valve 4 and 5 are closed and connect the bottle. Open the outlet valve from the sample connection to flare / process (Valve 6). Open the by- valve of the bottle (Valve 7) Open slowly the inlets valve on the Sample connection (Valve 3) for purge Sample Connection Lines and monitor the temperature seen at the temperature indicator on the outlet from the Sample Cooler. Open valves 4 and 5, and also isolating valve of the bottle (NV1 and NV2). Close the by- valve (Valve 7)


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   

After three minutes, close the isolating valves NV2 and NV1 (starting with NV2). Close the inlet valve into the Sample connection (Valve 3) Open the by- valve (Valve 7) to de-pressurize the Sample Connection. Close the outlet valve from Sample Connection (Valve 6), close valve 4 and 5, and remove the bottle from the connections.


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