equipment data sheet (2)

DATE BY CHECKED02/22/15 GOH JPA03/01/15 GOH JPA

ITEM: D-6503 SERVICE: FIRST STAGE HDS HOT SEPARATORNote DESIGN CONDITIONS

PRESSURE: kPag TEMPERATURE: deg C

Note OPERATING CONDITIONSPRESSURE: kPag TEMPERATURE: deg C

TYPE OF HEADS EllipsoidalINSULATION Heat Conservation

Note MATERIALSSHELL Carbon Steel

Note MATERIAL FOR INTERNALSFIXED Carbon SteelREMOVABLE

CONNECTIONS NOMENCLATURENote Item Qty. Size Service

A1 1 10" FEED INLETB1 1 2" LIQUID OUTLETB2 1 10" VAPOR OUTLETM 1 24" MANWAYV 1 2" VENTS 1 2" STEAMOUT CONNECTIONL 2 2" LEVEL CONNECTION

josephthedaydreamer:Company Name and Logo

josephthedaydreamer:Include in the drawing all the nozzles connected to the vessel + manways. Critical dimensions should be expressed in terms of mm (no need to put mm). Label the nozzles

josephthedaydreamer:Type of Material

A2

josephthedaydreamer: Company Name and Logo

A7

josephthedaydreamer: Include in the drawing all the nozzles connected to the vessel + manways. Critical dimensions should be expressed in terms of mm (no need to put mm). Label the nozzles

I17

josephthedaydreamer: Type of Material

REV.0A

FIRST STAGE HDS HOT SEPARATORDESIGN CONDITIONS

OPERATING CONDITIONS

EllipsoidalHeat Conservation

CORR ALLOW2 mm

CORR ALLOW2 mm

CONNECTIONS NOMENCLATUREService

FEED INLETLIQUID OUTLETVAPOR OUTLETMANWAYVENTSTEAMOUT CONNECTIONLEVEL CONNECTION



josephthedaydreamer:If no insulation, place No


josephthedaydreamer:Place all nozzles attached on the vessel

I15

josephthedaydreamer: If no insulation, place No

F21

josephthedaydreamer: Place all nozzles attached on the vessel


ITEM: D-6510 SERVICE: HEAVY NAPHTHA SPLITTER REFLUX DRUMNote DESIGN CONDITIONS



TYPE OF HEADS EllipsoidalINSULATION Personnel Protection


Note MATERIAL FOR INTERNALSFIXED Carbon SteelREMOVABLE Carbon Steel


A1 1 8" FEED INLETA2 1 10" BYPASS T-6505B1 1 8" HC LIQUID OUTLETB2 1 2" VAPOR OUTLETM 1 24" MANWAYV 1 2" VENTS 1 2" STEAMOUT CONNECTION

PSV 1 6" PRESSURE SAFETY VALVEL 2 2" LEVEL CONNECTION




A2


A7


I17


REV.0A

HEAVY NAPHTHA SPLITTER REFLUX DRUMDESIGN CONDITIONS


EllipsoidalPersonnel Protection

CORR ALLOW2 mm

CORR ALLOW2 mm2 mm


FEED INLETBYPASS T-6505HC LIQUID OUTLETVAPOR OUTLETMANWAYVENTSTEAMOUT CONNECTIONPRESSURE SAFETY VALVELEVEL CONNECTION






I15


F21



ITEM: T-6505 SERVICE: HEAVY NAPHTHA SPLITTERNote DESIGN CONDITIONS



NB OF TRAYS 25TYPE OF HEADS EllipsoidalINSULATION Heat Conservation


Note MATERIAL FOR INTERNALSFIXED SS 304REMOVABLE SS 304TRAYS 11/13 Cr


A1 1 10" FEED INLETA2 1 4" REFLUX INLETA3 1 20" REBOILER RETURNB1 1 18" VAPOR OUTLETB2 1 6" LIQUID OUTLETB3 1 12" PRODUCT DRAWOFFM 5 24" MANWAYV 1 2" VENTS 1 2" STEAMOUT CONNECTIONT 1 2" TEMPERATURE CONNECTIONP 1 2" PRESSURE CONNECTIONL 2 2" LEVEL CONNECTION

PSV 1 12" PRESSURE SAFETY VALVE




A2


A7


I18


REV.0A

HEAVY NAPHTHA SPLITTERDESIGN CONDITIONS


25Ellipsoidal

Heat ConservationCORR ALLOW

2 mmCORR ALLOW


FEED INLETREFLUX INLETREBOILER RETURNVAPOR OUTLETLIQUID OUTLETPRODUCT DRAWOFFMANWAYVENTSTEAMOUT CONNECTIONTEMPERATURE CONNECTIONPRESSURE CONNECTIONLEVEL CONNECTIONPRESSURE SAFETY VALVE






I16


F23



ITEM: T-6201 SERVICE: LPG AMINE ABSORBERNote DESIGN CONDITIONS



NB OF PACKING 3TYPE OF HEADS EllipsoidalINSULATION No

Note MATERIALSSHELL CS HIC Resistant

Note MATERIAL FOR INTERNALSFIXED SS TP 316 LREMOVABLE SS TP 316 LPACKING SS TP 316 L


A1 1 8" LPG FEED INLETA2 1 4" LEAN AMINE INLETB1 1 8" LPG OUTLETB2 1 6" RICH AMINE OUTLETV 1 2" VENTM 5 24" MANWAYS 1 2" STEAMOUT CONNECTION

PSV 1 10" PRESSURE SAFETY VALVEL 2 2" LEVEL CONNECTION




A2


A7


I18


REV.0A

LPG AMINE ABSORBERDESIGN CONDITIONS


3Ellipsoidal

NoCORR ALLOW

2 mmCORR ALLOW


LPG FEED INLETLEAN AMINE INLETLPG OUTLETRICH AMINE OUTLETVENTMANWAYSTEAMOUT CONNECTIONPRESSURE SAFETY VALVELEVEL CONNECTION






I16


F23



ITEM: R-6501 SERVICE: SHU REACTORNote DESIGN CONDITIONS



REACTOR TYPE Fixed BedTYPE OF HEADS EllipsoidalINSULATION Heat Conservation


Note MATERIAL FOR INTERNALSFIXED Carbon SteelREMOVABLE Carbon Steel


A1 1 10" INLETB1 1 10" OUTLETH 2 8" CATALYST UNLOADING NOZZLEM 1 24" MANWAYT 9 2" TEMPERATURE CONNECTION




A2


A7


I18


REV.0A

SHU REACTORDESIGN CONDITIONS


Fixed BedEllipsoidal

Heat ConservationCORR ALLOW

2 mmCORR ALLOW

2 mm2 mm


INLETOUTLETCATALYST UNLOADING NOZZLEMANWAYTEMPERATURE CONNECTION






I16


F22


DATE BY02/22/15 GOH03/01/15 GOH

ITEM: E-6502 SERVICE: SHU REACTOR FEED / EFFLUENT EXCHANGER

CHARACTERISTICS

Shell / Unit Surf. / Shell m² Type

PERFORMANCE OF ONE UNIT

Shell Side Tube Side

Fluid name

Fluid quantity, total kg/h

Vapor (in/out) kg/h

Liquid (in/out) kg/h

Steam (in/out) kg/h

Free water (in/out) kg/h

Temperature (in/out) °C

Density kg/m3

Viscosity cP

Vapor Molecular weight kg/kmol

Specific heat kJ/kg.°C

Thermal cond. W/m.°C

Density kg/m3

Liquid Viscosity cP

Specific heat kJ/kg.°C

Thermal cond. W/m.°C

Latent heat kJ/kg

Inlet pressure kPa g

Velocity m/s

Pressure drop kPa Allow. Calc. Allow.

Fouling resistance m².°C/W

Heat exchanged MW LMTD (corrected)

Transfer rate W/m².°C

GENERAL DESIGN INFORMATION

Note Design conditions Shell Side Tube Side

Pressure kPa g

Temperature °C

MATERIAL AND CORROSION ALLOWANCE

Note Materials Corr. Allow. mm

Non condensable(mole fraction on total inlet fluid)

CONNECTIONS NOMENCLATURE

Note Shell Side Tube Side

Line size (in/out)

Material induced by Shell Side fluid characteristics

Material induced by Tube Side fluid characteristics

CHECKED REV.JPA 0JPA A

SHU REACTOR FEED / EFFLUENT EXCHANGER

Tube Side

Calc.

°C

Tube Side

Corr. Allow. mm

Tube Side

DATE BY02/22/15 GOH03/01/15 GOH

ITEM: SERVICE:

CHARACTERISTICSTube surface m² m² Total developed surface

Tube Side Inlet Outlet

Fluid nameFluid quantity, total kg/h

Vapor kg/hLiquid kg/hSteam kg/hWater kg/h

Temperature °CDensity (PT) kg/m3Viscosity cP

Vapor Molecular weight kg/kmolSpecific heat kJ/kg.°CThermal cond. W/m.°CDensity (PT) kg/m3

Liquid Viscosity cPSpecific heat kJ/kg.°CThermal cond. W/m.°C

Latent heat kJ/kgInlet pressure kPa gPressure drop kPa Allow. Calc.Fouling resistance m².°C/W

Air Side

Temperature (in) °CAltitude m

Heat exchanged MWTransfer rate W/m².°CMean temperature difference °C

GENERAL DESIGN INFORMATIONNote Design conditions

Design pressure kPa gTemperature °C

MATERIAL AND CORROSION ALLOWANCENote Materials Corr. Allow. mm

Non condensable(mole fraction on total inlet

CONNECTIONS NOMENCLATURENote

Line size (in/out) in

Material induced by fluid characteristics

CHECKED REV.JPA 0JPA A

m²

Outlet

Corr. Allow. mm

DATE02/22/1503/01/15

ITEM: SERVICE:

CHARACTERISTICSMax average radiant heat flux allowable kW/m²

OPERATING CONDITIONSInlet Outlet

Fluid nameFluid quantity, total kg/h

Vapor kg/hLiquid kg/hSteam kg/hFree Water kg/h

Vaporized weight %Temperature °C

Density (PT) kg/m3Viscosity cP

Vapor Molecular weight kg/kmolSpecific heat kJ/kg.°CThermal cond. W/m.°CDensity (PT) kg/m3

Liquid Viscosity cPSpecific heat kJ/kg.°CThermal cond. W/m.°C

Inlet pressure kPa gPressure drop kPaAbsorbed heat MW

CONSTRUCTIONDesign pressure kPa gTube material (process side)Corrosion allowance mmFuel

Non condensable(mole fraction on total inlet fluid)

BY CHECKED REV.GOH JPA 0GOH JPA A

Outlet

DATE02/22/1503/01/15

ITEM: SERVICE:

FLUID HANDLEDOperating caseFluid circulatedCorrosive/erosive agentsPumping temperature °CViscosity (PT) cPVapor pressure kPa absDensity (60°F/15°C) kg/m3Density (PT) kg/m3

OPERATING CONDITIONSNormal flow m3/hDesign flow m3/hSuction pressure kPa gDischarge pressure kPa gDifferential pressure kPaDifferential head mNPSH available mNormal hydraulic power MW

PUMPNumber and type 2 (1 operating + 1 spare) / CentrifugalAssumed efficiencyNormal shaft power (estimated) MWMaterial

DRIVERType operating Electrical

spare ElectricalNominal power (estimated) MWConsumption (estimated) MW

DATE BY CHECKED REV.02/22/15 GOH JPA 003/01/15 GOH JPA A

2 (1 operating + 1 spare) / Centrifugal

ElectricalElectrical

DATE02/22/1503/01/15

ITEM: SERVICE:

GAS HANDLEDStageGas analysis mol %

Molecular weight kg/kmolMass rate kg/hStandard Volume rate (15°C - 1 atm) Sm3/h

SUCTION CONDITIONSPressure kPa absTemperature °CCp/CvCompressibility factor ZInlet volume m3/h

DISCHARGE CONDITIONSPressure kPa absTemperature (estimated) °CCp/CvCompressibility factor Z

COMPRESSORNumber and typeCompression ratioAssumed polytropic efficiencyAssumed polytropic head mHydraulic power MWShaft power @ Normal flowrate MWShaft power @ Design flowrate MW

DRIVERType operating

spareNominal power MWConsumption @ Normal flowrate MWConsumption @ Design flowrate MW

C2- 0.01PROPENE 99.72 PROPANE 0.27 H2O 0.00

OTHERS 0.00 ------ TOTAL 100.00


C2- 0.01PROPENE 99.72 PROPANE 0.27 H2O 0.00

OTHERS 0.00 ------ TOTAL 100.00

DATE02/22/1503/01/15

ITEM: SERVICE:

GAS HANDLEDStageGas analysis mol %

Molecular weight kg/kmolMass rate kg/hStandard Volume rate (15°C - 1 atm) Sm3/h

SUCTION CONDITIONSPressure kPa absTemperature °CCp/CvCompressibility factor ZInlet volume m3/h

DISCHARGE CONDITIONSPressure kPa absTemperature (estimated) °CCp/CvCompressibility factor Z

COMPRESSORNumber and typeCompression ratioAssumed adiabatic efficiencyAssumed adiabatic head mHydraulic power MWShaft power @ Normal flowrate MWShaft power @ Design flowrate MW

DRIVERType operating

spareNominal power MWConsumption @ Normal flowrate MWConsumption @ Design flowrate MW

equipment data sheet (2)

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