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A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND …

Elsevier USJob Code:CAPAC hapter:0capaappA22-12-20065 :771 11inFonts used:Times & Universal 55 familyMargins:Top:3p6 Gutter:4p6 Font Size:9/10ptText Width:41p6 Depth:65 LinesAppendix AA LIST OF ENGINEERING PROCESS FLOW DIAGRAMSAND PROCESS DATA SHEETSA-1 PROCESS FLOW DIAGRAMS USING VISIO 2002 SOFTWAREF igure 1-12b PROCESS flow diagram (Feed and fuel desulfurizationsection).Figure 1-12c Typical PROCESS flow diagram for the productionof Methyl Tertiary Butyl Ether (MTBE).Figure 1-14 Piping and instrumentation diagram for Ammoniaplant 1-15 Piping and instrumentation diagram: Ammoniasynthesis and refrigeration unit (2).A-2 PROCESS DATA cooled heat exchanger PROCESS data pump schedule: pump schedule: pump PROCESS data sheet: Deaerated water storage PROCESS data sheet: Deaerator PROCESS data flash equipment PROCESS duty calculation services and utilities chemical and conditions and mass exchanger rating dew point list schedule summary equipment line PROCESS conditions heat exchanger data of pressure drop in fixed catalyst ENGINEERING job analysis calculation device philosophy and vessel agitator data PROCESS data PROCESS data loading summary and tank and tank summary: analysis sheet771 Elsevier US

A-2 PROCESS DATA SHEETS 1. Air cooled heat exchanger process data sheet 2. Centrifugal pump schedule: driver 3. Centrifugal pump schedule: pump 4. Centrifugal pump summary 5. Column schedule 6. Deaerator process data sheet: Deaerated water storage tank 7. Deaerator process data sheet: Deaerator head 8. Drum process data sheet 9. Effluent ...

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Transcription of A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND …

1 Elsevier USJob Code:CAPAC hapter:0capaappA22-12-20065 :771 11inFonts used:Times & Universal 55 familyMargins:Top:3p6 Gutter:4p6 Font Size:9/10ptText Width:41p6 Depth:65 LinesAppendix AA LIST OF ENGINEERING PROCESS FLOW DIAGRAMSAND PROCESS DATA SHEETSA-1 PROCESS FLOW DIAGRAMS USING VISIO 2002 SOFTWAREF igure 1-12b PROCESS flow diagram (Feed and fuel desulfurizationsection).Figure 1-12c Typical PROCESS flow diagram for the productionof Methyl Tertiary Butyl Ether (MTBE).Figure 1-14 Piping and instrumentation diagram for Ammoniaplant 1-15 Piping and instrumentation diagram: Ammoniasynthesis and refrigeration unit (2).A-2 PROCESS DATA cooled heat exchanger PROCESS data pump schedule: pump schedule: pump PROCESS data sheet: Deaerated water storage PROCESS data sheet: Deaerator PROCESS data flash equipment PROCESS duty calculation services and utilities chemical and conditions and mass exchanger rating dew point list schedule summary equipment line PROCESS conditions heat exchanger data of pressure drop in fixed catalyst ENGINEERING job analysis calculation device philosophy and vessel agitator data PROCESS data PROCESS data loading summary and tank and tank summary: analysis sheet771 Elsevier USJob Code:CAPAC hapter:0capaappA22-12-20065 :772 11inFonts used:Times & Universal 55 familyMargins:Top:3p6 Gutter:4p6 Font Size:9/10ptText Width:41p6 Depth.

2 65 Lines772A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND PROCESS DATA of No.(s)Item NameNo. WorkingTotal No. OffUnless otherwise stated, fluid properties are for mean fluid temperature. For lines 30-36 this is mean from dewpoint to outlet SIDE DATA2 Fluid CirculatedTubes3 Total Fluid Entering (Normal)kg/hlb/hFins4 Flow Margin%%Header Boxes5 Temperature: In/Out C FTubesheets6 Max. Pressure Drop at Line 4barpsiStress Relief Yes/as Codes7 Inlet Pressure: Yes/as Codes8 Normal heat LoadkWBtu/hSour Service Yes/No9 heat Load Margin%%10 Design Temperature C F11 Corrosion Resistancem2 C/W Fft2h/Btu13 Line : (AND VAPOR) PROCESS CONTROL REQUIREMENTS15 Flow of Vapor & Gas at Inletkg/hlb/hLocal / Remote Set16 Molecular Weight: In/OutHand / Automatic17 Thermal Conductivity: In/OutW/m FAdjustable Pitch Fans18 Specific HeatkJ/kg CBtu/lb. FVariable Speed Motor19 Compressibility FactorLouvres20 ViscosityIn / Recirculation21 LIQUID IN22 Total Flow of Liquid at Inletkg/hlb/h23 Thermal Conductivity: In/OutW/m F24 Specific HeatkJ/kg CBtu/lb.

3 F25 Densitykg/m3lb/ft326 Condensed kg/hlb/h29 Molecular Weight30 Thermal ConductivityW/m F31 Specific HeatkJ/kg CBtu/lb. F32 Densitykg/m3lb/ft333 HeatkJ/kg Btu/lb35%Condensate Forming Film%%36 Temps. for Phase Change: In/Out C F37 COOLING CURVE DATA38% heat Load39 Condensing Fluid Temp. C4041 AIR SIDE DATA42 Design Inlet Temp. Max/Min C F43No. of Fans Assumed44 Estimated Power per FankW45 SITE DATA46 Altitude47 Plot Size LimitationsLength:Width:48 Noise Limits49 Atmospheric Contamination5051 NOTES525354551 Date2 Date3 Date4 Date5 DateDescriptionMade/Revised byChecked byApproved ProcessApproved byAIR cooled heat EXCHANGERPROCESS DATA SHEETMATERIALSUNITSE lsevier USJob Code:CAPAC hapter:0capaappA22-12-20065 :773 11inFonts used:Times & Universal 55 familyMargins:Top:3p6 Gutter:4p6 Font Size:9/10ptText Width:41p6 Depth:65 LinesCENTRIFUGAL PUMP SCHEDULE:DRIVERJob No.

4 :Sheet ofIssue No.:1 Date2 Date3 DateJob Name:DescriptionDocument byProject byClientApproved ProcessLocationApproved PlantITEM CW-CCWCHARACTERISTICSFRAME psigTEMP, F RATE No. USJob Code:CAPAC hapter:0capaappA22-12-20065 :774 11inFonts used:Times & Universal 55 familyMargins:Top:3p6 Gutter:4p6 Font Size:9/10ptText Width:41p6 Depth:65 LinesCENTRIFUGAL PUMP SCHEDULE: PUMPJob No.:Sheet ofIssue No.:1 Date2 Date3 DateJob Name:DescriptionDocument byProject byClientApproved ProcessLocationApproved PlantITEM No. No. OF UNITSSERVICEMAKEMODELTYPESIZE CONNECTIONWEIGHTREFERENCEPURCHASESEALTYP EFILESUCTIONDISCHARGEDRAWINGSORDER USJob Code:CAPAC hapter:0capaappA22-12-20065 :775 11inFonts used:Times & Universal 55 familyMargins:Top:3p6 Gutter:4p6 Font Size:9/10ptText Width:41p6 Depth:65 LinesCENTRIFUGAL PUMP SUMMARYJob No.

5 :Sheet ofIssue No.:1 Date2 Date3 DateJob Name:DescriptionDocument byProject byClientApproved ProcessLocationApproved PlantITEM No. No. OF UNITSSERVICELIQUIDOPERATINGSpGrGPMDISCHA RGESPEEDBHPHPDRIVER TYPEFILE TEMPERATUREOPER. FNPSHA USJob Code:CAPAC hapter:0capaappA22-12-20065 :776 11inFonts used:Times & Universal 55 familyMargins:Top:3p6 Gutter:4p6 Font Size:9/10ptText Width:41p6 Depth:65 LinesCOLUMN SCHEDULEJob No.:Sheet ofIssue No.:1 Date2 Date3 DateJob Name:DescriptionDocument byProject byClientApproved ProcessLocationApprovedPlant1 Item Number2 Item Name3 Number Required4 UnitsTopBottomTopBottomTopBottomTopBotto mTopBottomTopBottom5 Shell Diameter (ID/OD)mm6 Shell Length ( - )mm7 Overall Shell Length - ( - )mm8 Base Elevationmm9 Trays Type 10 Number 11 Spacingmm12 Liquid Flow13 Packing Type14 Number of Beds 15 Bed Height/Volumemm/m316 Densitykg/m317 Other Internals18192021 Operating Pressure22 Temperature23 Design Pressurebarg24 Temperature C25 Vacuum Design26 Material: Shell27 Liner28 Internals2930 Shell Corrosion Allowancemm31 Sour Service32 Stress Relieved for PROCESS USJob Code:CAPAC hapter:0capaappA22-12-20065 :777 11inFonts used:Times & Universal 55 familyMargins:Top:3p6 Gutter:4p6 Font Size:9/10ptText Width:41p6 Depth.

6 65 LinesAPPENDIX A777 Document No.(s)Item NameDEAERATED WATER STORAGE TANKNo. WorkingTotal No. OffNOTE: indicates delete as necessary: indicates for other than code Diameter ( )Shell Length: ( - )No. Required27 Center Line: Horizontal28 Pressure:Temperature:NozzlesMark InQty29psigbar g F InC-21 NOTE OutC-3132emergency Vacuum Design: YesSample PointC-4133 Liquid OutC-5134 Shell1/16" ( )Cond. OutC-61 NOTE 435 Heads36 LinerVentC-37 Type of HeadsDrainC-7138 Code:Steam OutC-39 Stress Relieve : YesPressure ReliefC-8140 Radiography : NoSpill BackC-9141joint Efficiency:Start UpC-101 NOTE 342 Weight Empty:Weight Full:43Is vessel subject to mechanical vibration?NOTE 244 Insulation:Conservation45 Yes46 NOTES471) Corrosion Allowance on Tank OnlyManholeA-11482) Water Hammer Only493) Sparge Pipe To Have Delavan Type BB NozzlesThermocoupleR-1150 and Terminate 1000mm Before GaugeR-21514) Allow for Temp of Desuperheating SteamGauge GlassR-3252 or condensate at Inlet 5) Normally at Dia.

7 Above Base Elevation:Skirt Length:56 Material:1 Date2 Date3 Date4 Date5 DateDescriptionMade/Revised byChecked byApproved ProcessApproved byCS1/16" ( )DEAERATOR PROCESS DATA SHEETby Inst. AllowanceCSR-3R-4R-3 BAFFLE WALLCROSS SECTIONVORTEX BREAKERMANWAYR-4R-2 MANWAYNOTE 5 NWLC-4C-1C-3C-2C-6C-8C-9 FOR DETAILS AND MATERIALSOF DEAERATOR HEADSEE SHEET m35 m31600310010 m31800500015 m32000600020 m37 0 6 9 6 0 5 3 21 0 18 6 15 0 10 3 22006600 VERTICAL TANK ONLYENGLISHMETRICSTANDARD TANK DIMENSIONSNOTE1 Elsevier USJob Code:CAPAC hapter:0capaappA22-12-20065 :778 11inFonts used:Times & Universal 55 familyMargins:Top:3p6 Gutter:4p6 Font Size:9/10ptText Width:41p6 Depth:65 Lines778A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND PROCESS DATA SHEETSD ocument of No.(s)Item NameDEAERATOR HEADNo. WorkingTotal No. Off1. DESIGN FOR FULL VACUUM.

8 OPERATING TEMPERATURE _____ OPERATING PRESSURE _____2. TRAYS TO BE SEALED TO SHELL WITH STEAM QUALITY RUBBER C4 TO BE CAPPED FOR SITE INSTALLATION OF STANDARD SAMPLING HEAD TO BE IN OR COATED BELOW 120 C MAX. EPOXY RESIN BELOW 180 C MAX. STOVED PHENOLIC RESIN (SAKAPHEN). PROCESS TO ADVICE ON SPECIFICATION & TRAYS TO BE IN 18/8 S/S. TRIANGULAR PERFORATION. PATTERN TO BE 'S___ OR SPRAY NOZZLE TO BE IN 18/8 S/S. SIMILAR TO DELAVAN WATSON S. _____ AND WITHDRAWABLE THROUGH : Bubbling Area Is Any Part Of Tray Within 4" Distance Of A HoleMARKSIZEQTYC-1C-3C-4 STD1 Water Feed 1 Water Feed 2 Water Feed 3 Heating SteamStart-Up SteamVent SteamDeaerated Feed Water No. Of Hole Is More Important Than Pitch1 Date2 Date3 Date4 Date5 DateWater InletVentSample PointPerf. Area/TrayBubbling Area/TrayNo.

9 Of TraysTray ThicknessHole DiameterPitch. of Holes/TrayDescriptionMade/Revised byChecked byApproved ProcessApproved byDESIGNFLOWS (kg/hr)DEAERATOR PROCESS DATA 6 MINC1 PERFORATED AREAGASKET " " FLANGE1" "(30 mm)SEAL PANDETAILS OF C4(12 mm) 1/2"Elsevier USJob Code:CAPAC hapter:0capaappA22-12-20065 :779 11inFonts used:Times & Universal 55 familyMargins:Top:3p6 Gutter:4p6 Font Size:9/10ptText Width:41p6 Depth:65 LinesAPPENDIX A779 Doc. No:Item :Sheet of Distribution:Item Name:NOTE: indicates delete as necessary; indicates for other than Code reason51015202526 Shell Diameter ( / ):Shell Length:No. Required:27 Center+C71 Line: Horizontal / Vertical28 Pressure:gTemperature: F / CNozzlesMark NumberInletC-30 Operating31 DesignVapor OutC-32 Emergency Vacuum Design: Yes / No33 Liquid Out:C-34 Shell35 Heads36 LinerThermocoupleR-37 Type of HeadsPressure GaugeR-38 Code:Gauge GlassR-39 Stress Relieve :Radiography :Level Control R-40 Joint Efficiency:Safety ValveR-41 Density of Contents:at F / C42 Weight Empty:Weight Full:43Is vessel subject to mechanical vibration?

10 Yes / NoVentC-44 insulation:Type: Frost and Personnel Protection / ColdDrainC-45 Yes / No/ Anticondensation / heat ConservationSteam OutC-46 REMARKS:47 ManholeA-484950515253min. Base Elev'n:54 Material:Issue byChecked byApproved - ProcessApproved byMaterialCorr. Allowanceby Inst. PROCESS DATA USJob Code:CAPAC hapter:0capaappA22-12-20065 :780 11inFonts used:Times & Universal 55 familyMargins:Top:3p6 Gutter:4p6 Font Size:9/10ptText Width:41p6 Depth:65 LinesEFFLUENT SCHEDULEJob No.:Sheet of Issue No.:1 Date2 DateJob Name:DescriptionDocument byProject byClientApproved- ProcessLocationApprovedPlantSTREAM NUMBEREFFLUENT SOURCEFLUIDTOTAL USJob Code:CAPAC hapter:0capaappA22-12-20065 :781 11inFonts used:Times & Universal 55 familyMargins:Top:3p6 Gutter:4p6 Font Size:9/10ptText Width:41p6 Depth:65 LinesAPPENDIX A781 Job :Sheet ofTemperature: FPressure:psiaPg:psiaAssumedmKH2 COCH4CO2C2H6C3H8C2H4C3H6C6H6i-C4H10n-C4H 10 Issue byChecked byApproved - ProcessApproved byEQUILIBRIUM FLASH CALCULATION (Form 1 of 2) PROCESS DATA +1mLVK+1mLVK+1mLVK+1mLVK+1 LVK+1 LVK+1 LVK+1 LVK+1 LVK+1=LVCalculated=LVmLVK+1= LVCalculated 1=1mKLV+1 Elsevier USJob Code:CAPAC hapter:0capaappA22-12-20065 :782 11inFonts used:Times & Universal 55 familyMargins:Top:3p6 Gutter:4p6 Font Size:9/10ptText Width:41p6 Depth.


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