A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND … · Figure 1-12b Process flow diagram ... 778 A...
Transcript of A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND … · Figure 1-12b Process flow diagram ... 778 A...
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Appendix A
A LIST OF ENGINEERING PROCESS FLOW DIAGRAMSAND PROCESS DATA SHEETS
A-1 PROCESS FLOW DIAGRAMS USING VISIO 2002SOFTWARE
Figure 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 CO2 removal.
Figure 1-15 Piping and instrumentation diagram: Ammoniasynthesis and refrigeration unit (2).
A-2 PROCESS DATA SHEETS
1. Air cooled heat exchanger process data sheet2. Centrifugal pump schedule: driver3. Centrifugal pump schedule: pump4. Centrifugal pump summary5. Column schedule6. Deaerator process data sheet: Deaerated water storage tank7. Deaerator process data sheet: Deaerator head8. Drum process data sheet9. Effluent schedule
10. Equilibrium flash calculation11. Fabricated equipment schedule12. Fan/Compressor process duty specification13. Fractionator calculation summary14. General services and utilities checklist15. Hazardous chemical and conditions schedule16. Heat and mass balances
17. Heat exchanger rating sheet18. Hydrocarbon dew point calculation19. Line list schedule20. Line schedule21. Line schedule sheet22. Line summary table23. Mass balance24. Mechanical equipment schedule25. Pipe line list26. Pipe list27. Piping process conditions summary28. Plate heat exchanger data sheet29. Calculation of pressure drop in fixed catalyst beds30. Process engineering job analysis summary31. Pump calculation sheet32. Pump schedule33. Relief device philosophy sheet34. Tank and vessel agitator data sheet35. Tank process data sheet36. Tank schedule37. Tie-in-schedule38. Tower process data sheet39. Tray loading summary40. Trip schedule41. Utility summary sheet42. Vessel and tank schedule43. Vessel and tank summary: driver44. Vessel schedule45. Water analysis sheet
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772 A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND PROCESS DATA SHEETS
A.K.C.TECHNOLOGY
Document No.
Sheet of Rev.
Job Item No.(s)Item Name No. Working Total No. Off
Unless otherwise stated, fluid properties are for mean fluid temperature. For lines 30-36 this is mean from dewpoint to outlet temperatures.
1 TUBE SIDE DATA2 Fluid Circulated Tubes3 Total Fluid Entering (Normal) kg/h lb/h Fins
4 Flow Margin % % Header Boxes
5 Temperature: In/Out °C °F Tubesheets
6 Max. Pressure Drop at Line 4 bar psi Stress Relief Yes/as Codes
7 Inlet Pressure: Operat./Design barg psig Radiography Yes/as Codes
8 Normal Heat Load kW Btu/h Sour Service Yes/No
9 Heat Load Margin % %
10 Design Temperature °C °F11 Corrosion Allowance mm in.
12 Fouling Resistance m2 °C/W °Fft2h/Btu13 Line N.B.: In/Out mm. in.
14 GAS (AND VAPOR) PROCESS CONTROL REQUIREMENTS
15 Flow of Vapor & Gas at Inlet kg/h lb/h Local / Remote Set
16 Molecular Weight: In/Out Hand / Automatic
17 Thermal Conductivity: In/Out W/m °C Btu/h.ft. °F Adjustable Pitch Fans
18 Specific Heat kJ/kg °C Btu/lb. °F Variable Speed Motor
19 Compressibility Factor Louvres20 Viscosity In / Out cP lb/ft.h Air Recirculation
21 LIQUID IN
22 Total Flow of Liquid at Inlet kg/h lb/h
23 Thermal Conductivity: In/Out W/m °C Btu/h.ft. °F24 Specific Heat kJ/kg °C Btu/lb. °F25 Density kg/m3 lb/ft3
26 Viscosity cP lb/ft.h
27 CONDENSATION
28 Fluid Condensed kg/h lb/h
29 Molecular Weight
30 Thermal Conductivity W/m °C Btu/h.ft. °F31 Specific Heat kJ/kg °C Btu/lb. °F32 Density kg/m3 lb/ft3
33 Viscosity cP lb/ft.h
34 Latent Heat kJ/kg Btu/lb
35 %Condensate Forming Film % %36 Temps. for Phase Change: In/Out °C °F37 COOLING CURVE DATA
38 %Heat Load
39 Condensing Fluid Temp. °C40
41 AIR SIDE DATA
42 Design Inlet Temp. Max/Min °C °F43 No. of Fans Assumed44 Estimated Power per Fan kW
45 SITE DATA
46 Altitude
47 Plot Size Limitations Length: Width:
48 Noise Limits
49 Atmospheric Contamination50
51 NOTES
52
53
54
55
1 Date 2 Date 3 Date 4 Date 5 DateDescription
Made/Revised by
Checked by
Approved ProcessApproved by
AIR COOLED HEAT EXCHANGERPROCESS DATA SHEET
MATERIALSUNITS
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APPENDIX A 777
Document No.Sheet of Rev.
Job Item No.(s)
Item Name DEAERATED WATER STORAGE TANK No. Working Total No. Off
NOTE: ∗ indicates delete as necessary: ∗∗ indicates for other than code reason.
123456789
1011121314151617181920212223242526 Shell Diameter (O.D.) Shell Length: (T.L. - T.L.) No. Required27 Center Line: ∗Horizontal28 Pressure: Temperature: Nozzles Mark No. Size In Qty29 psig bar g °F °C Inlet C-1 130 Operating 3.0 0.237 223 106 Steam In C-2 1 NOTE 431 Design 10.0 0.73 241 116 Vapour Out C-3 132 emergency Vacuum Design: ∗Yes Sample Point C-4 133 Liquid Out C-5 134 Shell 1/16" (1.6mm) Cond. Out C-6 1 NOTE 435 Heads36 Liner Vent C-37 Type of Heads Drain C-7 138 Code: Steam Out C-39 Stress Relieve∗∗: Yes Pressure Relief C-8 140 Radiography∗∗: No Spill Back C-9 141 joint Efficiency: Start Up C-10 1 NOTE 342 Weight Empty: Weight Full:43 Is vessel subject to mechanical vibration? NOTE 244 Insulation: Conservation45 ∗Yes46 NOTES47 1) Corrosion Allowance on Tank Only Manhole A-1 1
48 2) Water Hammer Only49 3) Sparge Pipe To Have Delavan Type BB Nozzles Thermocouple R-1 150 and Terminate 1000mm Before Baffle. Pressure Gauge R-2 151 4) Allow for Temp of Desuperheating Steam Gauge Glass R-3 252 or condensate at Inlet Nozzles. Level Control R-4 2 Incl.LAHL/LL53 5) Normally at 0.67 Dia. Above Base.5455 Min. Base Elevation: Skirt Length:
56 Material:1 Date 2 Date 3 Date 4 Date 5 Date
DescriptionMade/Revised byChecked byApproved ProcessApproved by
CS 1/16" (1.6MM)
DEAERATOR PROCESS DATA SHEET
by In
st. G
p.
Material Corr. AllowanceCS
R-3
R-4
R-3
BAFFLE WALLCROSS SECTION
VORTEX BREAKER
MANWAY
R-4R-2
MANWAY
NOTE 5NWL
C-4
C-1
C-3
C-2C-6C-8C-9
FOR DETAILS AND MATERIALSOF DEAERATOR HEAD
SEE SHEET 2.
C-7
C-10
R-1
C-5
A-1
A.K.C.TECHNOLOGY
TANKSIZE O.D. LENGTH O.D. LENGTH2 m3
5 m3 1600 310010 m3 1800 500015 m3 2000 600020 m3 7′–0″
6′–9″6′–0″5′–3″
21′–0″18′–6″15′–0″10′–3″
2200 6600
VERTICAL TANK ONLY
ENGLISH METRICSTANDARD TANK DIMENSIONS
NOTE1
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778 A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND PROCESS DATA SHEETS
Document No.Sheet of Rev.
Job Item No.(s)
Item Name DEAERATOR HEAD No. Working Total No. Off
1. DESIGN FOR FULL VACUUM. OPERATING TEMPERATURE _______________ OPERATING PRESSURE __________________
2. TRAYS TO BE SEALED TO SHELL WITH STEAM QUALITY RUBBER GASKETS.
3. C4 TO BE CAPPED FOR SITE INSTALLATION OF STANDARD SAMPLING EQUIPMENT.
4. HEAD TO BE IN S.S OR COATED M.S. BELOW 120°C MAX. EPOXY RESIN BELOW 180°C MAX. STOVED PHENOLIC RESIN (SAKAPHEN). PROCESS TO ADVICE ON SPECIFICATION & APPLICATION.
5. TRAYS TO BE IN 18/8 S/S. TRIANGULAR PERFORATION. PATTERN TO BE N.GREENING'S___ OR EQUAL.
6. SPRAY NOZZLE TO BE IN 18/8 S/S. SIMILAR TO DELAVAN WATSON S. _______________ AND WITHDRAWABLE THROUGH C-1.
NOTE: Bubbling Area Is Any Part Of Tray Within 4" Distance Of A Hole
MARK SIZE QTYC-1C-3C-4 STD 1 Water Feed 1
Water Feed 2Water Feed 3Heating SteamStart-Up SteamVent SteamDeaerated Feed Water
∗ No. Of Hole Is More Important Than Pitch1 Date 2 Date 3 Date 4 Date 5 Date
Water InletVentSample PointPerf. Area/TrayBubbling Area/TrayNo. Of TraysTray ThicknessHole DiameterPitch. Approx.No. of Holes/Tray
DescriptionMade/Revised byChecked byApproved ProcessApproved by
DESIGNFLOWS (kg/hr)
DEAERATOR PROCESS DATA SHEET
NORMAL
NOZZLES
A.K.C.TECHNOLOGY
C4
C3
NOTE 6
MIN C1
PERFORATED AREA
GASKET
½" S.S.PIPE
1" S.S. FLANGE
1" N.B.S.S.PAD
11/4"(30 mm)
SEAL PAN
DETAILS OF C4
(12 mm)
1/2"
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APPENDIX A 779
Doc. No:
Item No.
Job: Sheet of
Distribution: Item Name:
NOTE: ∗indicates delete as necessary; ∗∗indicates for other than Code reason
5
10
15
20
2526 Shell Diameter (O.D. / I.D.): Shell Length: No. Required:27 Center+C71 Line: ∗Horizontal / Vertical28 Pressure: g Temperature: °F /°C Nozzles Mark No. Size Number29 Item Number Inlet C-30 Operating31 Design Vapor Out C-32 Emergency Vacuum Design: ∗ Yes / No33 Liquid Out: C-34 Shell35 Heads36 Liner Thermocouple R-37 Type of Heads Pressure Gauge R-38 Code: Gauge Glass R-39 Stress Relieve∗∗: Radiography∗∗: Level Control R-40 Joint Efficiency: Safety Valve R-41 Density of Contents: at ∗°F / °C42 Weight Empty: Weight Full:
43 Is vessel subject to mechanical vibration? ∗Yes / No Vent C-44 insulation: Type: ∗Frost and Personnel Protection / Cold Drain C-45 ∗Yes / No / Anticondensation / Heat Conservation Steam Out C-46 REMARKS:47 Manhole A-484950515253 min. Base Elev'n:54 Material:
Issue No. 1 Date 2 Date 3 Date 4 DateMade/Revised byChecked byApproved - ProcessApproved by
Material Corr. Allowanceby
Inst
. Op.
DRUM PROCESS DATA SHEETA.K.C.TECHNOLOGY
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APPENDIX A 781
Job No.
Item No.
Job: Sheet of
Temperature: °FPressure: psiaPg: psia
Assumed
m K
H2
COCH4
CO2
C2H6
C3H8
C2H4
C3H6
C6H6
i-C4H10
n-C4H10
Issue No. 1 Date 2 Date 3 Date 4 Date 5 DateMade/Revised byChecked byApproved - ProcessApproved by
EQUILIBRIUM FLASH CALCULATION (Form 1 of 2)
PROCESS DATA SHEETA.K.C.
TECHNOLOGY
m
LV
K +1
m
LV
K +1
m
LV
K +1
m
LV
K +1
m
LV
K +1LV
K +1LV
K +1 LV
K +1LV
K +1LV
K +1
=LV
Calculated =LV
m
LV
K +1
=∑
LVCalculated −1= 1
m
K LV +1∑
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782 A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND PROCESS DATA SHEETS
Job No.
Item No.
Job: Sheet of
Temperature: °FPressure: psiaPg: psia
Vy = m − Lx
Issue No. 1 Date 2 Date 3 Date 4 Date 5 DateMade/Revised byChecked byApproved - ProcessApproved by
EQUILIBRIUM FLASH CALCULATION (Form 2 of 2)
PROCESS DATA SHEET
Feedm
LiquidLx
GasVy
Liquidx
Gasy
MOLES MOL. FRACTION
L xm
K LV + 1
=
H2
COCH4
CO2
C2H6
C3H8
C2H4
C3H6
C6H6
i-C4H10
n-C4H10
A.K.C.TECHNOLOGY
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784 A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND PROCESS DATA SHEETS
Document No.Sheet of Rev.
Job Item No.(s)\Item Name No. Working Total No. Off
12 Operating Case3 Mass Flowrate kg/h lb/h
4 Standard Volumetric Flowrate nm3/h std ft3/h5 Volume at Suction m3/h6
7 Pressure bara psia8 Temperature °C °F9 Molecular Weight
10 Cp/Cv11 Compressibility
12 DISCHARGE CONDITIONS13 Pressure bara psia14 Temperature oC oF15 Cp/Cv16 Compressibility
17
18 Mol % Mol %19202122232425262728293031 Entrained Liquids/Solids32
33 Compression Ratio34 Estimated Efficiency % %
35 Estimated Absorbed Power kW hp36 Recommended Driver Power kW hp
37 MECHANICAL ARRANGEMENT38 Compressor/Fan Type39 Number of Stages40 Gas to be kept Oil Free Yes / No4142 Driver Type4344 Casing Design Pressure45 Design Pressure46
47 Material - Casting
48 - Impeller49
50 Sour Service Yes / No
51 NOTES52 1. Cooling medium available:-535455
1 Date 2 Date 3 Date 4 Date 5 DateDescriptionMade/Revised byChecked byApproved ProcessApproved by
PERFORMANCE
UNITS
OPERATING CONDITIONS PER UNIT
FAN/COMPRESSOR PROCESS DUTY SPECIFICATION
INLET CONDITIONS
GAS ANALYSIS
A.K.C.TECHNOLOGY
SKETCH
ft3/h
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APPENDIX A 785
Job No:Item No:Sheet ____ of _____
Job:Item Name:
1 Operate at psig Units: Metric / British (delete one)
Distribution 2 Fractionation: Reflux Ratio & No. of Plates:
3 Ovhd Prod: C < Reflux Ratio: Actual: ; Use
4 Bottoms: C < Rectifying Plates: Theoretical: ; Use
5 Stripping Plates: Theoretical: ; Use
6
7 Vapour
8 Pressure
9 1
10 2
11 3
12 4
13 5
14 6
15 7
16 8
17 9
18 10
19
20 Ext. Rflx.
21
22
23 1
24 2
25 3
26 4
27 5
28 6
29 7
30 8
31 9
32 10
33
34 Thermal Conditions of Feed: Reboiler Vapour Quantity:
35
36
37
38
39
40
41 Sp.Gr.
42 at 15oC
43 at 60oF
44 Feed
45 Net Bottoms
46 Net Overheads
47 Gross Overheads
48 Gross Bottoms
49 Reboiler Vapour
50
51
52
53 REMARKS
54
55
56 Issue No. 1 Date 2 Date 3 Date
57 Made/Revised by
58 Checked by
59 Approved - Process
60 Approved by
Kg/hr lb/hr
cu. m/kg
cu. Ft/lb
Mol % K
Sp. Vol. At T
o
Mols/hr Mol. Wt.Stream oAPI Temp.Sp.Gr. at
To
KX or Mols MolsComponent Mols Mol % K
KX Pat
Net Overheads Gross Overheads
FRACTIONATOR CALCULATIONSUMMARY
Feed Net Bottoms
Component Mols Mol % Mols Mol % K
A.K.C.TECHNOLOGY
F
Co
o
Fpsia
CKscao
o
Fpsia
CKscao
o
Fpsia
CKscao
o
K
Y
K
Y
Co
Fo
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786 A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND PROCESS DATA SHEETS
GENERAL SERVICES AND UTILITIES CHECKLIST
Job No.: PREPARED BY:Job Name:Document No. DATE:Project No.ClientLocationPlant
SERVICE QUANTITY OPERATING PRESSURE AND REMARKSSUSTAINED PEAK UNIT TEMPERATURE
ELECTRICAL 13.8 KV *KVA
ELECTRICAL 2300 V *KVA
ELECTRICAL 440 V *KVA
MISC. LIGHTING, ST. ETC., (110 V) *KVA
WELL WATER (CITY) gpm
SEA WATER gpm
RIVER WATER – PROCESS gpm
RIVER WATER – FIRE PROT. gpm
FUEL GAS SCFMODORIZED GAS SCFM
COMPRESSED AIR SCFM
STEAM lb/h(400 OR 475) Psig lb/h235 Psig lb/h150 Psig lb/h30 Psig lb/hCONDENSATE RETURN lb/hCONDENSATE USAGE lb/hPROCESS TRANSFER AND RAW MATERIALSCAUSTIC (–%) lb/hBRINE (–%) lb/hLPG lb/h
SITE DEV. (AREA FILL)
RAIL ROADS
BLOCK ACCESS ROADS
SANITARY SEWERS gpmgpm
WASTE WATER
* ASSUME 1 HORSE POWER = 1 KVA
NOTE: ONE COPY OF THIS LIST TO BE GIVEN TO SERVICE AND UTILITY SECTION.
A.K.C.TECHNOLOGY
Sheet of
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HA
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No.
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A.K
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TE
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787
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H
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1 2 3 4 5 6 7 8 9 10 11 12 13 14 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
↓
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A.K
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TE
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788
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APPENDIX A 789
Document No.
HEAT EXCHANGER RATING SHEET
Sheet of Rev.PART 1 - TO BE FILLED IN COMPLETELY Items No. (s)
1 Exchanger Name: *
2 Job: * * * Arrangement: Horiz = 0; Vert = 1
3 Type of Unit: F.T.S.=0; FLTG.HEAD=1; U-TUBE=2; FOR KETTLES ADD 3 Units: S.I. 0; Engineering = 14 Hot Side: Either=0; Shell=1; Tubes=2
5 Units
6 Fluid Circulated - -
7 Total Fluid Entering (Normal) kg/hr lb/hr
8 Flow Margin % %
9 Temperature In/Out °C °F
10 Max Pressure Drop at line 8 bar psi
11 Inlet Pressure Operating/Design barA psia
12 Normal Heat Load kW Btu/hr
13 Heat Load Margin % %
14 Design Temperature °C °F
15 Corrosion Allowance mm ins
16 Fouling Resistance °Cm2/Wl °F hr ft2/Btu
17 Line N.B. In/Out mm ins
18 Part 2
19 GAS (AD VAPOR) IN - -
20 Flow of Vapor and Gas at Inlet kg/hr lb/hr
21 Code Number - -
22 Molecular Weight - -
23 Thermal Conductivity W/m °C Btu/hr ft °F
24 Specific Heat kJ/kg °C Btu/lb °F
25 Compressibility Factor - -
26 Viscosity cP lb/ft hr
27 LIQUID IN - -
28 Total Flow of Liquid at Inlet kg/hr lb/hr
29 Code Number - -
30 Thermal Conductivity W/m °C Btu/hr ft °F
31 Specific Heat kJ/kg °C Btu/lb °F
32 Density kg/m3 lb/ft3
33 Viscosity cP lb/ft hr
34 Viscosity at Ave. Temp. other side cP lb/ft hr
35 CONDENSATION AND VAPORIZATION - -
36 Fluid Condensed or Vaporized kg/hr lb/hr
37 Code Number - -
38 Molecular Weight - -
39 Thermal Conductivity W/m °C Btu/hr ft °F
40 Specific Heat kJ/kg °C Btu/lb °F
41 Density (Hot Fluid) kg/m3 lb/ft3
42 Compressibility Factor (Cold Fluid) - -
43 Viscosity cP lb/ft hr
44 Latent Heat kJ/kg Btu/lb
45 Surface Tension N/m lb/ft
46 Expansion Coefficient 1/ °C 1/ °F
47 % Condensate Forming Film % %
48 Thermal Conductivity W/m °C Btu/hr ft °F
49 Density kg/m3 lb/ft3
50 Viscosity cP lb/ft hr
51 Temps for Phase Change Start/Finish °C °F
52 LMTD weighting Factor 'F' - -
53 PART 3
54 Number of Points in Table Below
55 % Heat Load % % 1 2 3 4 5 6 7 8 9 10
56 Hot Fluid Temperature °C °F
57 Cold Fluid Temperature °C °F
58 PART 4 - CODE NUMBERS TO BE FILLED IN COMPLETELY
59 Material for Description Code No. O.D. Thickness Length Passes Number Contents Lethal?
60 Tubes
61 Shell
62 Floating Head Tube Pitch = mm/in. o Δ �
63 Channel
64 Tube Sheets
NOTES
Issue No. 1 Date 2 Date 3 Date 4 Date 5 Date
Made/Revised by
Checked by
Approved- ProcessApproved by
Yes/No
Yes/No
Location:
S.I. Engineering HOT FLUID COLD FLUID
A.K.C.
TECHNOLOGY
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790 A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND PROCESS DATA SHEETS
Job No:Item No.
Job: Page of
Pressure: psia
Heaviest Compound: PROPANE Convergence Pressure: psia
oFFeL TbFeL FeH TbFeH K y/K K y/K K y/K K y/K x
H2 67 1.000 67.000N2 130 0.0229 2.972 0.105CO 172 0.0046 0.797 0.180CH4 201 0.0019 0.383 0.244C2H4 305 0.548CO2 330 0.638C2H6 332 0.646C2H2 340 0.676C3H6 406 0.954C3H8 416 1.000
13.6131.0049.02167.0210.6214.3229.9387.3416.0
1.000 Σ y/K 1.000
x for H2
Σ (yFeL/K)Σ (yFeH/K)E.B.PLE.B.PHPg
Estimate of Dewpoint: oFat Estimate Pg of: psia
Issue No. 1 Date 2 Date 3Made/Revised byChecked byApproved - ProcessApproved by
HYDROCARBON DEWPOINTCALCULATION
TbyASSUMED TEMPERATUREoF oF oF
Date
HEAVYCOMPONENT
LIGHTCOMPONENT oF
A.K.C.TECHNOLOGY
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793
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794
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MA
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30 31 32 33 34 35 36 37 38 39 40 41 42N
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A.K
.C.
TE
CH
NO
LO
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795
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ME
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G/M
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APA
CIT
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UR
E(k
g/cm
2 g) IN
LE
TT
EM
P. (
° C)
NPS
HA
TY
PEM
AT
ER
IAL
SA
BSO
LU
TE
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(R
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RE
MA
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h)IN
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ote
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ipm
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A =
Axi
al;
C =
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trif
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= M
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ing;
R =
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g; S
= S
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ll dr
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A.K
.C.
TE
CH
NO
LO
GY
796
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PIP
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ft/s
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A.K
.C.
TE
CH
NO
LO
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TE
MP
ER
AT
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797
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PIPE
LIS
TT
ITL
E:
Job
No.
:Sh
eet
of
Issu
e N
o.:
1D
ate
2D
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= ac
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= lb
/h
A.K
.C.
TE
CH
NO
LO
GY
798
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PIPI
NG
PR
OC
ESS
CO
ND
ITIO
NS
SU
MM
AR
Y
Job
No.
:Sh
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ofIs
sue
No.
:1
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e2
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e3
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b N
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A.K
.C.
TE
CH
NO
LO
GY
799
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800 A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND PROCESS DATA SHEETS
Document No.
Sheet of Rev.
Job Item No.(s)
Item Name No. Working Total No. Off
1 FLUID 1 FLUID 2 FLUID 32 Fluid Circulated - -3 Total Fluid Entering (Normal) kg/h lb/h
4 Flow Margin % %5 Inlet Vapor and Gas (&MW) kg/h lb/h6 Inlet Liquid kg/h lb/h7 Fluid Vaporized/Condensed (&MW) kg/h lb/h8 Temperature In/Out oC
oF9 Max. Pressure Drop bar psi
10 Inlet Pressure (Operating) bar g psig
11 Normal Heat Load kW Btu/h12 Heat Load Margin % %13 Fouling Resistance m2 ο 2 ο
C/W ft Fh/Btu14 FLUID PROPERTIES15 Specific Heat kJ/kg C Btu/lb F
16 Thermal Conductivity W/m C Btu/hr ft F17 Density kg/m3 lb/f t3
18 Viscosity cP lb/hr.ft19 Liquid Viscosity (at Temp.) cP lb/hr.ft20 Latent Heat kJ/kg Btu/lb
21 ENGINEERING DESIGN22 Process Design Pressure bar g psig23 Process Design Temperature C F24 Corrosion Allowance (Header) mm in.25 Line N.B. In/Out in in.26 Minimum Flow Passage mm in.27 Plate Material28 Frame Material29 Gasket Material30 Desgin Code31 NOTES3233 1. Unless otherwise stated fluid properties are for mean fluid temperatures.34 2. Sour Service Yes / No3536373839404142434445464748495051525354
1 Date 2 Date 3 DateDescriptionMade/Revised byChecked byApproved ProcessApproved by
UNITSPROCESS DESIGN
PLATE HEAT EXCHANGER DATA SHEET
A.K.C.
TECHNOLOGY
ο
ο
ο ο
ο
ο
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APPENDIX A 801
MadeJob No.
Checked
Item No.Date
Job Sheet of
REQUIRED DATAVESSEL NO:SERVICE:CATALYST: VOLUME REQUIRED V ft3
MANUFACTURER & NO.DIMENSIONSEQUIV. PARTICLE DIA. Dp ft.SHAPE/SIZE FACTOR Sf
GAS DATA: FLOW RATE W lb/hW2 (lb/h)2
MIN. MOLECULAR WEIGHTBED OUTLET PRESSURE P psiaMAX. BED TEMPERATURE CABS. TEMPERATURE (ο ο
ο
K = C + 273) T K
CALCULATION
=
SYMBOLS UNITS CALCULATION CASE 1 CASE 2 CASE 3 CASE 4BED DIAMETER D ftBED C.S.A. A ft2 0.7854D2
BED DEPTH L ft. V/ASUPERFICIAL MASS FLOW G lb/h.ft2 W/AMASS FLOW FACTOR Gf -DpG -
REYNOLDS NO. FACTOR Ref -
k2k2 - k1Ref
CLEAN PRESSURE DROP/UNIT DEPTH ΔPc psi/ft. k2Gf
CLEAN OVERALL PRESSURE DROP ΔPc psi LΔPc
SAFETY/FOULING FACTOR f - 1.25/ FLOW SHEET PRESSURE DROP ΔP psi fΔPc
* IF VALUE OF DpG > 200 (750 FOR RING CATALYSTS) PUT Ref = 1.0IF VALUE OF DpG < 200 (750 FOR RING CATALYSTS) CALCULATE Re = DpG/μ(WHERE μ = DYNAMIC VISCOSITY OF GAS, lb/ft.hr)
1 2 3 4 5 6DescriptionMade/Revised byChecked byApproved ProcessApproved by
CALCULATION OF PRESSURE DROP IN FIXED CATALYST BEDS
PROCESS DATA SHEET
( )( )( )( ) ==
PM
STk f
1
A.K.C.
TECHNOLOGY
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802 A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND PROCESS DATA SHEETS
PROCESS ENGINEERING JOB ANALYSIS SUMMARY
Job Title
Job No. Charge No. Date
Based Upon Cost Estimated Dated or Actual Construction Cost
Summary Prepared By Information Dated
Production Basis (lb/day, tonnes/day, lb/month)
SERVICE REQUIREMENTS: UNIT RATE UNIT RATE/PRODUCTION BASIS
1 Steam (30 lb) lb/h
2 Steam (150 lb) lb/h
3 Steam (400 lb) lb/h
4 Steam ( lb) lb/h
5 Treated R.W. gpm
6 Untreated R.W. gpm
7 Fresh Water gpm
8 Sea Water gpm
9 Fuel Gas ( psi) cfm (60° F and 1atm)
cfm (60° F and 1atm)10 Air ( psi)
11 Power ( )
12 Horsepower
13 Condensate lb/h
14
RAW MATERIALS UNIT RATE
1 Chlorine
2 Hydrogen ( %)
3 Caustic ( %)
4 Salt
5 Sat. Brine
6 Natural Gas
7 Air
8 Ethylene
9
10
11
PRODUCTS AND BY- PRODUCTS UNIT RATE
1 Chlorine
2 HCl ( %)
3 Salt ( %)
4 Caustic ( %)
5 Ammonia ( %)
6 H2SO4 ( %)
7 Gas ( )
8
9
10
11
A.K.C.
TECHNOLOGY
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APPENDIX A 803
PUMP CALCULATION SHEET Document No.Sheet of Rev.
Job Item No. (s)Item Name. No. Working Total No. off
UNITS CASE I CASE II SKETCH OF PUMP HOOK-UP12 Liquid Pumped3 Corrosion/Erosion4 Due To
5 Operating Temp. (T ) ° C ° F
6 Specific Gravity at T7 Viscosity cP cP8 Vapor Pressure at T bara psia9 Normal mass Flowrate kg/h lb/h
10 Normal Vol. Flowrate m3/h gpm
11 Min. Vol. Flowrate
12 Design Vol. Flowrate m3/h gpm13 SUCTION CONDITION14 Pressure at Equipment barg psig + +15 Static Head bar psi + / –16 Total – Lines 14 + 15 bar psi + +17 Suction Line bar psi – –18 Filter/Strainer bar psi – –1920 Total Suction Pressure barg psig + +21 DISCHARGE CONDITION22 Pressure at Equipment barg psig + +23 Static Head bar psi + / – + / –2425 Exchanger bar psi + +2627 Furnace bar psi + +28 Orifice bar psi + +29 Control Valve bar psi + +3031 Line bar psi + +3233 Total Discharge Press. barg psig + +34 Differential Pressure bar psi35 Differential Head bar psi36 NPSH NOTES
37 Total Suction Pressure bara psia 1. Pump shut-off head not to exceed………38 Vapor Pressure bara psia39 NPSH – Lines 37 – 38 bara psia 2. Relief valve on pump discharge to be set at ……………40 = m ft41 Safety Margin m ft 3. Pump case design pressure…………42 NPSH – Lines 40–41 m ft design temperature……..43 Hydraulic Power kW Hp44 Estimated Efficiency % % 4. Sealing/flushing fluid available:45 Estimated Abs. Power kW Hp46 Type of Pump 5. Cooling medium available:47 Drive48 6. Insulation required: 49 Material – Casing50 – Impeller 7. Start-up/commissioning fluid SG.51 – Shaft5253 Sour Service Yes/No
54 HEAD m = 10.2 × bar/SG m = 10 × kg/cm2/SG ft = 2.31 × psi/SG
55 VOLUME m3/h × SG × 1000 = kg/h igpm × SG × 600 = lb/h
56 POWER kW = m3/h × bar/36.0 kW = m3/h × kg/cm2/36.71 Hp = igpm × psi/142757 1 Date 2 Date 3 Date 4 Date 5 Date58 Description
59 Made/Revised by
60 Checked by61 Approved Process62 Approved
ΔP
ΔP
ΔP
ΔP
ΔP
ΔP
ΔP
A.K.C.
TECHNOLOGY
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PU
MP
SC
HE
DU
LE
Job
No.
:Sh
eet o
fIs
sue
No.
:1
Dat
e2
Dat
e3
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b N
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2It
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3N
umbe
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o. R
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otal
Ins
talle
d4
Pref
erre
d T
ype
Uni
ts5
Liq
uid
Pum
ped
6O
pera
ting
- T
empe
ratu
reο
οC
F7
Spec
ific
Gra
vity
at O
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tiong
Tem
pera
ture
8
Vis
cosi
ty a
t Ope
ratin
g T
empe
ratu
recP
lb/f
t.h9
Vap
or P
ress
ure
at O
pera
ting
Tem
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ture
bara
psia
10D
esig
n C
apac
ity (
per
pum
p)m
3 /hft
3 /h
11N
orm
al C
apac
ity (
per
pum
p)m
3 /hft
3 /h12
Dis
char
ge P
ress
ure
bar
gps
ig13
Suct
ion
Pres
sure
bar
gps
ig14
Dif
fere
ntia
l Hea
dba
r /m
psi/f
t15
Min
imum
NPS
H A
vaila
ble
/ Req
uire
dm
ft.
16H
ydra
ulic
Pow
er (
per
pum
p)kW
hp
17R
.P.M
--
18E
stim
ated
Pum
p E
ffic
ieny
--
19E
stim
ated
Sha
ft P
ower
( p
er p
ump)
kWhp
20T
ype
of D
rive
r-
-
21D
river
Rat
ed P
ower
( p
er p
ump)
kWhp
22D
esig
n P
ower
Con
sum
ptio
n (
per
pum
p)kW
hp23
Nor
mal
Pow
er C
onsu
mpt
ion
(per
pum
p)kW
hp24
Max
. Shu
t-O
ff H
ead
bar
psi
25
26M
ater
ial:
Cas
ing
27Im
pelle
r28
Shaf
t29
Sour
Ser
vice
30Pa
ckin
g T
ype
/ Mec
hani
cal S
eal T
ype
31
32Se
rvic
es /
Util
ities
33C
oolin
g W
ater
34Se
al /
Flus
h Fl
uid
m3 /h
ft3 /h
35Q
uenc
hm
3 /hft
3 /h
36N
otes
37 38 39 40 41 42 43 44 45
A.K
.C.
TE
CH
NO
LO
GY
804
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APPENDIX A 805
A.K.C.TECHNOLOGY
RELIEF DEVICE PHILOSOPHY SHEET DOCUMENT / ITEM REFERENCE
EQUIPMENT No.:
DATE: SHEET No.: OF
CHECKED BY: MADE BY: 1
2
DESIGN CODES: VESSELS EXCHANGERS LINES 3
4
OTHER REQUIREMENTS 5
6
BASIS FOR CALCULATION: 7
8
SET PRESSURE, PSIG: MAX. BACK PRESSURE: (a) BEFORE RELIEVING (b) WHILE RELIEVING 9
NORMAL CONDITIONS UNDER RELIEF DEVICE: Calculated 10
STATE: TEMPERATURE, °F: PRESSURE, PSIG: POSSIBLE FLUID
RELIEVED
RELIEF
RATE, lb/h
ORIFICE
AREA, in2.
11
CAUSE? 12
HAZARDS CONSIDERED 13
1. Outlets blocked 14
2. Control Valve malfunction 15
3. Machine trip/ overspeed/density change 16
4. Exchanger tube rupture 17
5. Power failure/ Voltage dip 18
6. Instrument air failure 19
7. Cooling failure 20
8. Reflux failure 21
9. Abnormal entry of volatile liquid 22
10 . Loss of liquid level 23
11. Abnormal chemical reaction24
12. Boxed in thermal expansion25
13. External fire26
14. (specify)27
15. (specify)28
16. (specifty)29
SELECTED DESIGN CASE: 30
31
RELIEVED FLUID: STATE DENSITY / MW: TEMPERATURE: Cp/Cv: 32
COMPOSITION: FLASHING: 33
RELIEF RATE REQUIRED, lb/h: ORIFICE SELECTED: AREA, in2: TYPE: 34
ACTUAL CAPACITY, lb/h 35
REMARKS/SKETCH 36
37
38
39
40
41
42
43
44
45
Issue No: 1 Date 2 Date 3 Date 46
Description 47
Made/Revised by 48
Checked by 49
Approved- Process 50
Approved 51
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806 A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND PROCESS DATA SHEETS
Drawing No:Project Name: Project No.:
sheet …….. Of ……..
No. Off: Associated Vessel/Tank* Item No:1. Largest and smallest charge:2. Components added during mixing:3. Agitator operating while vessel is being filled or product withdrawn? Yes/No* 4. If continuous, throughput per hour:5. Process duty: Mixing liquids/Dissolving/Suspensions/Emulsions/Gas absorption/Homogenisation*6. Mixing effect: Violent/Medium/Moderate* Time available for mixing:7. Working Pressure: Design Pressure:8. Working Temperature: Design Temperature:
2
9. Special Remarks:
Dat
e 10. Components % by weight:
11. Temperature during mixing:12. Specific gravity of components:13. Viscosity of mixing at mixing temperature:14. Specific gravity of product at mixing temperature:15. Size of solid particles:16. Special Remarks:
17. Type of impeller:18. Number of impellers on shaft:19. Position of impellers:20. Distance between shaft end & vessel: Bottom bearing:21. Preferred impeller speed: Shaft diameter:22. Type of drive: Direct/Vee belt/Fluid*23. Type of seal: Vapor/Packed gland/Mechanical/Easy replacement*24. Method of installation: Assembled in/Assembled out* of vessel25. Entry position:26. Materials of construction:
27. Absorbed HP/KW*: Installed HP/KW*:28. Other information:
29. Dimensions: Capacity:30. Coils, baffles, etc.:31. Fixing agitator (beams, flanges, etc.):32. If at atmospheric pressure: Closed/Open* Can stuffing box be greased? Yes/No*33. Headroom available above agitator:34. Other information:
35. Agitator installed: Indoors/Outdoors Motor enclosure:36. Electrical specification:37. Any other electrical information:
38. Motor to be included: Yes/No*39. Motor Will/Will not* be sent to manufacturer for assembly and alignment.40. Threads: Unified /*41. All rotating parts must be strictly guarded to BS 1649/ASME42. Fixing bolts supplied by:43. Net weight including motor:
44. Witnessed run in air:45. General notes:
NOTE: * Indicates delete as necessary.
TANK AND VESSEL AGITATOR DATA SHEET
Equipment No:
DE
SIG
N D
EPT
. IN
FO
RM
AT
ION
IMPE
LL
ER
TA
NK
OR
VE
SSE
LE
LE
CT
.
Dat
e
MIX
ING
3D
ate
1
PRO
CE
SS
PRO
CE
SS D
EPT
. IN
FOR
MA
TIO
N
App
rove
d
Des
crip
tion
Mad
e/R
evis
ed b
y
Che
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by
App
rove
d Pr
oces
s
GE
NE
RA
L
A.K.C.TECHNOLOGY
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APPENDIX A 807
Doc. No:Item No.
Job: Sheet of
Item Name:
NOTE: * indicates delete as necessary; ** indicates for other than Code reason
5
10
15
20
2526 Shell Diameter (O.D. / I.D.): Shell Length: No. Required:
27 Center Line: *Horizontal / Vertical28 Pressure: g Temperature: F / C Nozzles Mark No. Size Number29 Item Number Inlet C-30 Operating31 Design Vapor Out C-32 Emergency Vacuum Design: * Yes / No33 Liquid Out: C-34 Shell35 Heads36 Liner Thermocouple R-37 Type of Heads Pressure Gauge R-38 Code: Gauge Glass R-39 Stress Relieve**: Radiography**: Level Control R-40 Joint Efficiency: Safety Valve R-41 Density of Contents: at * °
° °
°F / C
42 Weight Empty: Weight Full:
43 Is vessel subject to mechanical vibration? *Yes / No Vent C-44 insulation: Type: *Frost and Personnel Protection / Cold Drain C-45 *Yes / No Anticondensation / Heat Conservation Steam Out C-
46 REMARKS:
47 Manhole A-
484950515253 min. Base Elev'n: k-Skirt Length
54 Material:
Issue No. 1 Date 2 Date 3 Date 4 DateMade/Revised byChecked byApproved - ProcessApproved by
Material Corr. Allowance
by In
st. O
p.
TANK PROCESS DATA SHEETA.K.C.
TECHNOLOGY
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808 A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND PROCESS DATA SHEETS
TA
NK
SC
HE
DU
LE
Job
No.
:Sh
eet
of
Is
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No.
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A.K
.C.
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810 A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND PROCESS DATA SHEETS
Made by: Document No.
Date:Job Item No:(s)
Checked by: Item NameSheet of
Tower Name:
NOTE: * indicates delete as necessary; ** indicates for other than code reason1 Top Bottom2 Shell Diameters O.D. - I.D.3 No. of Trays4 Pressure Operating5 *psig Design6 Temperature Operating7 *oF / oC Design8 Material Shell9 Trays10 Caps11 Liner or Clad12 Corrosion - Shell13 Allowance Heads14 Trays15 Tray Spacing16 Type of Liquid Flow17 Type of Trays18 Joint Efficiency19 Code Emergency Vac. Design *Yes / No20 Stress Relieved **Yes / No Radiography **Yes / No21 Is vessel subject to mechanical vibration *Yes / No22 Insulation Type: *Frost and Personnel Protection / Cold /23 *Yes / No /anticondensation / Heat Conservation /24 Min. Base Elevation: Skirt length:25 Weight Empty: Full:26 Nozzles Mark No. Size Number27 Feed C-2829 Overhead Vpr. C-30 Reflux In C-3132 Bottoms C-33 Reboiler Vpr C-34 Reboiler liq C-353637 Thermocouple R-38 Level Glass R-39 Press Gauge R-40 Level Control R-41 Safety Valve R-424344 Vent C-45 Drain C-46 Steam Out C-47 Manholes A-48 Handholes A-49 Cap Type: Tray Layout Ref:50 NOTES5152535455 1 Date 2 Date 3 Date 4 Date56 Description57 Made/Revised by58 Checked by59 Approved Process60 Approved by
.pG.tsni
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TOWER PROCESS DATA SHEETA.K.C.TECHNOLOGY
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APPENDIX A 811
Job No.item No.
Job: Sheet of
Tower Name: Type of Tray1 Manufacturer Mfr. Ref:2 Pressure at top of Tower barg psia3 Max. ΔP over Tower bar psi units Used: METRIC/BRITISH (delete one)4 No. of Trays Aboved Feed Below Feed5 Tray location6 Tray Number*7 Tray Spacing mm in.8 Tower Internal Diameter I.D. mm in.9 Vapor to Tray
10 Temperature oC oF11 Compressibility12 Density kg/m3 lb/ft3
13 Molecular Weight14 Rate kg/h lb/h1516 Liquid from Tray17 Temperature °C °F18 Surface Tension dynes/cm lb/ft19 Viscosity cps lb ft/hr20 Density kg/m3 lb/ft3
21 Rate kg/h lb/h22 Foaming Tendency **23 Number of Passes24 Minimum Hole Diameter *** mm in.25 Minimum DC Residence Time*** secs s26 Maximum Rate as % Design27 Minimum Rate as % Design28 Design Rate % Flood Rate***2930 Tray Material31 Valve or Cap Material32 Corrosion Allowance mm in.33 Tray Thickness*** mm in.3435363738 NOTES: * Trays are numbered from the bottom of the tower upwardstop of the tower downwards39 ** Indicate whether 'non', 'moderate', 'high' or 'severe'40 ∗ ∗ ∗ Data to be supplied by tray manufacturer unless special Process/Client requirement entered here.41 REMARKS:4243444546474849505152535455 1 Date 2 Date 3 Date56 Description57 Made/Revised by58 Checked by59 Approve - Process60 Approved by
TRAY LOADING SUMMARYA.K.C.
TECHNOLOGY
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A.K
.C.
TE
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NO
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816
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APPENDIX A 817
WATER Submitted by:ANALYSIS Address: Location:SHEET
Date:Analysis No.
Date:pH ValueSuspended Solids mg/lTotal Dissolved Solids mg/l at 110° CTotal Dissolved Solids mg/l at 180° CAlkalinity to Pp as mg/l CaCO3
Alkalinity to MO as mg/l CaCO3
Sulphate as mg/l SO4
Chloride as mg/l ClNitrate as mg/l NO3
Silica as mg/l SiO2
Phosphate as mg/l PO4
Total Anions as mg/l CaCO3
Total Hardness as mg/l CaCO3
Calcium as mg/l CaMagnesium as mg/l MgSodium* as mg/l NaPotassium* as mg/l KIron as mg/l FeManganese as mg/l MnFree and Saline Ammonia as mg/l NH3
Total Cations as mg/l CaCO3
Free Dissolved CO2 as mg/l CO2
Dissolved O2 as mg/l OColor Hazaen UnitsTurbidity Formazin Units+ FTU APHALead as mg/l PbCopper as mg/l CuResidual ChlorineFlouride as mg/l FSulfite as mg/l SO3
NOTES: 1. Please state if units other than milligrams per liter, or different conditions of test, are used.2. * If Na and/or K form an appreciable amount of total cations, please state Alkalinity to
Phenolphthalein (p), Alkalinity to Methyl Orange (MO), and Carbonate Hardness.3. + DO NOT use Formazin Units as defined by British Standard BS. 2690 Pt. 9.4. ** Tick if item definitely to be included in analysis.
5. 100 mg/L CaCO3 = 2 milliequivalents/(m val/L).
**
A.K.C.
TECHNOLOGY