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Appendix A
A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS
AND PROCESS DATA SHEETS
A-1 PROCESS FLOW DIAGRAMS USING VISIO 2002
SOFTWARE
Figure 1-12b Process flow diagram (Feed and fuel desulfurization
section).
Figure 1-12c Typical process flow diagram for the production
of Methyl Tertiary Butyl Ether (MTBE).
Figure 1-14 Piping and instrumentation diagram for Ammonia
plant CO2 removal.
Figure 1-15 Piping and instrumentation diagram: Ammonia
synthesis and refrigeration unit (2).
A-2
1.
2.
3.
4.
5.
6.
7.
8.
9.
10.
11.
12.
13.
14.
15.
16.
PROCESS DATA SHEETS
Air cooled heat exchanger process data sheet
Centrifugal pump schedule: driver
Centrifugal pump schedule: pump
Centrifugal pump summary
Column schedule
Deaerator process data sheet: Deaerated water storage tank
Deaerator process data sheet: Deaerator head
Drum process data sheet
Effluent schedule
Equilibrium flash calculation
Fabricated equipment schedule
Fan/Compressor process duty specification
Fractionator calculation summary
General services and utilities checklist
Hazardous chemical and conditions schedule
Heat and mass balances
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.
Heat exchanger rating sheet
Hydrocarbon dew point calculation
Line list schedule
Line schedule
Line schedule sheet
Line summary table
Mass balance
Mechanical equipment schedule
Pipe line list
Pipe list
Piping process conditions summary
Plate heat exchanger data sheet
Calculation of pressure drop in fixed catalyst beds
Process engineering job analysis summary
Pump calculation sheet
Pump schedule
Relief device philosophy sheet
Tank and vessel agitator data sheet
Tank process data sheet
Tank schedule
Tie-in-schedule
Tower process data sheet
Tray loading summary
Trip schedule
Utility summary sheet
Vessel and tank schedule
Vessel and tank summary: driver
Vessel schedule
Water analysis sheet
771
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772 A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND PROCESS DATA SHEETS
AIR COOLED HEAT EXCHANGER
PROCESS DATA SHEET
A.K.C.
TECHNOLOGY
Document No.
Sheet
of
Item No.(s)
No. Working
Job
Item Name
Rev.
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.
UNITS
1
2
3
4
5
6
7
8
9
10
11
12
13
TUBE SIDE DATA
Fluid Circulated
14
15
16
17
18
19
20
GAS (AND VAPOR)
21
LIQUID IN
22
23
24
25
26
Total Flow of Liquid at Inlet
Thermal Conductivity: In/Out
Specific Heat
Density
Viscosity
27
CONDENSATION
28
29
30
31
32
33
34
35
36
Fluid Condensed
Molecular Weight
Thermal Conductivity
Specific Heat
Density
Viscosity
Latent Heat
%Condensate Forming Film
Temps. for Phase Change: In/Out
37
COOLING CURVE DATA
38
39
40
%Heat Load
Condensing Fluid Temp. °C
41
AIR SIDE DATA
42
43
44
Design Inlet Temp. Max/Min
No. of Fans Assumed
Estimated Power per Fan
45
SITE DATA
46
47
48
49
50
Altitude
Plot Size Limitations
Noise Limits
Atmospheric Contamination
51
52
53
54
55
NOTES
MATERIALS
Total Fluid Entering (Normal)
Flow Margin
Temperature: In/Out
kg/h
%
°C
Max. Pressure Drop at Line 4
bar
psi
Inlet Pressure: Operat./Design
barg
psig
Normal Heat Load
Heat Load Margin
Design Temperature
Corrosion Allowance
Fouling Resistance
Line N.B.: In/Out
kW
%
°C
mm
Btu/h
%
°F
in.
Tubes
Fins
Header Boxes
Tubesheets
Stress Relief Yes/as Codes
Radiography Yes/as Codes
Sour Service Yes/No
lb/h
%
°F
°Fft2h/Btu
in.
m2 °C/W
mm.
PROCESS CONTROL REQUIREMENTS
Flow of Vapor & Gas at Inlet
Molecular Weight: In/Out
kg/h
Thermal Conductivity: In/Out
Specific Heat
Compressibility Factor
Viscosity
W/m °C
kJ/kg °C
1
In / Out
Local / Remote Set
Hand / Automatic
Adjustable Pitch Fans
Variable Speed Motor
Louvres
Air Recirculation
lb/h
Btu/h.ft. °F
Btu/lb. °F
cP
lb/ft.h
kg/h
W/m °C
kJ/kg °C
lb/h
Btu/h.ft. °F
Btu/lb. °F
kg/m3
cP
lb/ft3
lb/ft.h
kg/h
lb/h
W/m °C
kJ/kg °C
Btu/h.ft. °F
Btu/lb. °F
lb/ft3
lb/ft.h
Btu/lb
%
°F
kg/m3
cP
kJ/kg
%
°C
°C
°F
kW
Length:
Date
2
Width:
Date
3
Date
4
Date
5
Date
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TECHNOLOGY
TYPE
HP
RPM
ROTATION
CW-CCW
CENTRIFUGAL PUMP SCHEDULE:
DRIVER
ELECTRICAL
CHARACTERISTICS
Sheet of
NEMA
FRAME
Issue No.:
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Approved
STEAM CONDITIONS
psig
TEMP, ° F
1
MAKE
Date
MODEL
2
STEAM
RATE
Date
WEIGHT
3
P.O.
No.
Date
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MAKE
CENTRIFUGAL PUMP SCHEDULE: PUMP
MODEL
PUMP
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TYPE
SIZE CONNECTION
SUCTION
DISCHARGE
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REFERENCE
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PURCHASE
ORDER No.
2
SEAL
TYPE
Date
TYPE
COUPLING
3
FILE
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Date
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LIQUID
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°F
OPERATING
TEMPERATURE
CENTRIFUGAL PUMP SUMMARY
SpGr
OPER. TEMP.
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OPER. TEMP.
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NPSHA
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DISCHARGE
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SPEED
RPM
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PUMP
2
HP
DRIVER
Date
DRIVER TYPE
3
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mm
°C
barg
mm/m3
kg/m3
Top
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Chapter:0capaappA
17 Other Internals
18
19
20
21 Operating – Pressure
– Temperature
22
Design – Pressure
23
– Temperature
24
25 Vacuum Design
26 Material: Shell
Liner
27
Internals
28
29
30 Shell Corrosion Allowance
31 Sour Service
32 Stress Relieved for Process Reasons
33 Insulation
34
35
36 Notes
37
38
39
40
41
42
43
44
45
– Density
mm
Units
mm
mm
mm
mm
COLUMN SCHEDULE
Job Code:CAPA
16
Job No.:
Job Name:
Document No.
Project No.
Client
Location
Plant
1 Item Number
2 Item Name
3 Number Required
4
5 Shell Diameter (ID/OD)
6 Shell Length (T.L. - T.L.)
7 Overall Shell Length - (T.L. - T.L.)
8 Base Elevation
9 Trays – Type
– Number
10
– Spacing
11
– Liquid Flow
12
Packing
– Type
13
– Number of Beds
14
– Bed Height/Volume
15
TECHNOLOGY
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APPENDIX A
A.K.C.
TECHNOLOGY
Document No.
Sheet of
DEAERATOR PROCESS DATA SHEET
Job
Item Name
777
Rev.
Item No.(s)
DEAERATED WATER STORAGE TANK
No. Working
Total No. Off
NOTE: ∗ indicates delete as necessary: ∗∗ indicates for other than code reason.
48
49
50
51
52
53
54
55
STANDARD TANK DIMENSIONS
ENGLISH
METRIC
LENGTH
O.D.
LENGTH
VERTICAL TANK ONLY
10′–3″
1600
3100
5′–3″
15′–0″
1800
5000
6′–0″
18′–6″
2000
6000
6′–9″
21′–0″
2200
6600
7′–0″
TANK
SIZE
2 m3
5 m3
10 m3
15 m3
20 m3
C-3
C-1
FOR DETAILS AND MATERIALS
OF DEAERATOR HEAD
SEE SHEET 2.
O.D.
BAFFLE WALL
CROSS SECTION
C-4
C-9
C-8
C-6
R-2
C-2
NWL
A-1
MANWAY
R-4
R-3
NOTE 5
MANWAY
R-1
R-4
C-10
C-7
R-3
C-5
VORTEX BREAKER
Shell Diameter (O.D.)
Center Line: ∗Horizontal
Pressure:
psig
Shell Length: (T.L. - T.L.)
bar g
Operating
3.0
0.237
Design
10.0
0.73
emergency Vacuum Design: ∗Yes
Material
Shell
CS
Heads
CS
Liner
Type of Heads
Code:
Stress Relieve∗∗: Yes
Radiography∗∗: No
joint Efficiency:
Weight Empty:
Is vessel subject to mechanical vibration?
Insulation:
Conservation
∗Yes
NOTES
1) Corrosion Allowance on Tank Only
Temperature:
°F
223
241
°C
106
116
Corr. Allowance
1/16" (1.6mm) NOTE
1/16" (1.6MM)
1
No. Required
Nozzles
Inlet
Steam In
Vapour Out
Mark No.
C-1
C-2
C-3
Size In
Sample Point
Liquid Out
Cond. Out
C-4
C-5
C-6
1
1
1
Vent
Drain
Steam Out
CC-7
C-
1
Pressure Relief
Spill Back
Start Up
C-8
C-9
C-10
1
1
1
Manhole
A-1
1
Thermocouple
Pressure Gauge
Gauge Glass
Level Control
R-1
R-2
R-3
R-4
1
1
2
2
Min. Base Elevation:
56
Date
NOTE 4
NOTE 4
NOTE 3
NOTE 2
2) Water Hammer Only
3) Sparge Pipe To Have Delavan Type BB Nozzles
and Terminate 1000mm Before Baffle.
4) Allow for Temp of Desuperheating Steam
or condensate at Inlet Nozzles.
5) Normally at 0.67 Dia. Above Base.
1
Qty
1
1
1
Weight Full:
by Inst. Gp.
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
2
Date
Material:
3
Date
Incl.LAHL/LL
Skirt Length:
4
Date
5
Date
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778 A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND PROCESS DATA SHEETS
A.K.C.
TECHNOLOGY
DEAERATOR PROCESS DATA SHEET
Job
Item Name
DEAERATOR HEAD
Document No.
Sheet
of
Item No.(s)
No. Working
Rev.
Total No. Off
C3
MIN
PERFORATED AREA
NOTE 6
C1
1/2"
SEAL PAN
DETAILS OF C4
(12 mm)
1" N.B.S.S.
PAD
1" S.S.
FLANGE
11/4"
(30 mm)
½" S.S.
PIPE
C4
GASKET
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.
NOTE: Bubbling Area Is Any Part Of
Tray Within 4" Distance Of A Hole
NOZZLES
MARK
SIZE
C-1
Water Inlet
C-3
Vent
C-4
STD
Sample Point
Perf. Area/Tray
Bubbling Area/Tray
No. Of Trays
Tray Thickness
Hole Diameter
Pitch. Approx.
No. of Holes/Tray
1
Date
Description
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6. SPRAY NOZZLE TO BE IN 18/8 S/S. SIMILAR TO
DELAVAN WATSON S. _______________
AND WITHDRAWABLE THROUGH C-1.
QTY
FLOWS (kg/hr)
NORMAL
1
2
Margins:Top:3p6
Water Feed 1
Water Feed 2
Water Feed 3
Heating Steam
Start-Up Steam
Vent Steam
Deaerated Feed Water
∗ No. Of Hole Is More Important Than Pitch
Date
3
Date
4
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Date
DESIGN
5
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APPENDIX A
Doc. No:
DRUM PROCESS DATA SHEET
A.K.C.
TECHNOLOGY
Item No.
Job:
Distribution:
779
Sheet
of
Item Name:
NOTE: ∗indicates delete as necessary;
∗∗indicates for other than Code reason
5
10
15
20
Shell Diameter (O.D. / I.D.):
Center+C71 Line: ∗Horizontal / Vertical
°F /°C
g
Pressure:
Temperature:
Item Number
Operating
Design
Emergency Vacuum Design: ∗ Yes / No
Material
Corr. Allowance
Shell
Heads
Liner
Type of Heads
Code:
Stress Relieve∗∗:
Radiography∗∗:
Shell Length:
Nozzles
Inlet
Mark No.
C-
Vapor Out
C-
Liquid Out:
C-
Thermocouple
Pressure Gauge
Gauge Glass
Level Control
Safety Valve
RRRRR-
Joint Efficiency:
∗°F / °C
Density of Contents:
at
Weight Empty:
Weight Full:
Is vessel subject to mechanical vibration? ∗Yes / No
Vent
Type: ∗Frost and Personnel Protection / Cold
insulation:
Drain
∗Yes / No
Steam Out
/ Anticondensation / Heat Conservation
REMARKS:
Manhole
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33
34
35
36
37
38
39
40
41
42
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46
47
48
49
50
51
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53
54
CCCA-
min. Base Elev'n:
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Date
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3
Date
4
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EFFLUENT SOURCE
EFFLUENT SCHEDULE
of
FLUID
Sheet
TOTAL FLOWRATE
tonne/h.
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MAIN CONTAMINANTS
CONTAMINANT
kg/h.
QUANTITY
1 Date
CONTAMINANT
CONCENTRATION
STREAM
TEMP.
°C.
2 Date
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9
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22
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40
41
42 Notes:
43
44
45
46
47
48
STREAM NUMBER
Job No.:
Job Name:
Document No.
Project No.
Client
Location
Plant
A.K.C.
TECHNOLOGY
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APPENDIX A
PROCESS DATA SHEET
A.K.C.
TECHNOLOGY
781
Job No.
Item No.
Sheet of
Job:
EQUILIBRIUM FLASH CALCULATION (Form 1 of 2)
°F
psia
psia
Temperature:
Pressure:
Pg:
V
=
L
Assumed
m
K
K
V
+1
L
K
m
V
+1
L
m
V
K L +1
K
V
+1
L
K
m
V
+1
L
K
3
Date
V
+1
L
K
m
V
+1
L
K
4
Date
V
+1
L
K
m
V
+1
L
K
5
Date
V
+1
L
H2
CO
CH4
CO2
C2H6
C3H8
i-C4H10
n-C4H10
C2H4
C3H6
C6H6
∑ K V +1 =
m
L
Calculated
V
=
L
Calculated
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V
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782 A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND PROCESS DATA SHEETS
Job No.
PROCESS DATA SHEET
A.K.C.
TECHNOLOGY
Item No.
Job:
Sheet of
EQUILIBRIUM FLASH CALCULATION (Form 2 of 2)
°F
psia
psia
Temperature:
Pressure:
Pg:
MOLES
MOL. FRACTION
Gas
Vy
Liquid
Lx
Feed
m
Liquid
x
Gas
y
H2
CO
CH4
CO2
C2H6
C3H8
i-C4H10
n-C4H10
C2H4
C3H6
C6H6
Lx =
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m
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K V +1
L
1
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Date
4
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Date
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Date
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A.K.C.
No.
OFF
DESCRIPTION
DIAMETER
(m)
FABRICATED EQUIPMENT SCHEDULE
LENGTH
(m)
Sheet of
SURFACE
(m2/SHELL)
(tonne/SHELL)
WEIGHT
S = Shell
T
S
T
S
T
S
T
S
T
S
T
S
T
S
T
S
T
S
T
S
T
S
T
S
T
S
T
S
T
S
T
S
T
S
T
S
T
S
T
S
T
S
T
S
T
S
T
S
(See Note 1)
MATERIAL
FLUID
T = Tube
Date
1
H.E. TYPE
INTERNALS/
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Description
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Approved
PRESSURE
(kg/cm2.g)
DESIGN
2
TEMPERATURE
(°C)
CONDITIONS
Date
REMARKS
3
Date
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Notes: 1. H.E. Type Coding - A.C. = Air Cooler; K = Kettle; U.B. = U - Tube Bundle; F.H. = Floating Head; F.T.S. = Fixed Tube Sheet
Job No.:
Job Name:
Document No.
Project No.
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Location
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ITEM No.
TECHNOLOGY
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784 A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND PROCESS DATA SHEETS
FAN/COMPRESSOR PROCESS DUTY
SPECIFICATION
A.K.C.
TECHNOLOGY
Document No.
Sheet
of
Item No.(s)\
No. Working
Job
Item Name
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
48
49
50
51
52
53
54
55
Rev.
Total No. Off
OPERATING CONDITIONS PER UNIT
UNITS
Operating Case
Mass Flowrate
Standard Volumetric Flowrate
Volume at Suction
kg/h
nm3/h
m3/h
lb/h
std ft3/h
ft3/h
INLET CONDITIONS
bara
psia
°F
°C
Pressure
Temperature
Molecular Weight
Cp/Cv
Compressibility
DISCHARGE CONDITIONS
bara
psia
o
o
C
F
Pressure
Temperature
Cp/Cv
Compressibility
GAS ANALYSIS
Mol %
Mol %
Entrained Liquids/Solids
PERFORMANCE
Compression Ratio
Estimated Efficiency
Estimated Absorbed Power
Recommended Driver Power
%
%
kW
hp
kW
hp
MECHANICAL ARRANGEMENT
Compressor/Fan Type
Number of Stages
Gas to be kept Oil Free
SKETCH
Yes / No
Driver Type
Casing Design Pressure
Design Pressure
Material - Casting
- Impeller
Yes / No
Sour Service
NOTES
1. Cooling medium available:-
1
Date
2
Date
3
Date
4
Date
5
Date
Description
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APPENDIX A
Job No:
Item No:
Sheet ____ of _____
FRACTIONATOR CALCULATION
SUMMARY
A.K.C.
TECHNOLOGY
785
Job:
Item Name:
Distribution
1
Operate at
2
Fractionation:
psig
3
Ovhd Prod:
C
<
Reflux Ratio:
Actual:
; Use
4
Bottoms:
C
<
Rectifying Plates:
Theoretical:
; Use
Stripping Plates:
Theoretical:
; Use
Reflux Ratio & No. of Plates:
5
Feed
6
7
8
Units: Metric / British (delete one)
Net Bottoms
Ksca o C
Component
9
1
10
2
11
3
12
4
13
5
14
6
15
7
16
8
17
9
18
10
Mols
Mol %
Mols
Mol %
K
KX
psia o F
Vapour
o
Pat oC
F
Pressure
19
Net Overheads
20
21
Component
22
23
1
24
2
25
3
26
4
27
5
28
6
29
7
30
8
31
9
32
10
Mols
Mol %
K
Gross Overheads
Ext. Rflx.
Ksca o C
psia o F
KX or
Y
K
Mols
Mols
Mol %
K
Ksca o C
psia o F
Y
K
33
34
Thermal Conditions of Feed:
Reboiler Vapour Quantity:
35
36
37
38
39
40
41
Stream
42
o
API
Sp.Gr.
at 15oC
o
Temp.
at 60oF
43
44
Feed
45
Net Bottoms
46
Net Overheads
47
Gross Overheads
48
Gross Bottoms
49
Reboiler Vapour
o
C
F
Sp.Gr. at
To
Sp. Vol. At T
o
cu. m/kg
Mols/hr
Mol. Wt.
Kg/hr
lb/hr
Date
3
Date
cu. Ft/lb
50
51
52
53
REMARKS
54
55
56
Issue No.
57
Made/Revised by
58
Checked by
59
Approved - Process
60
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786 A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND PROCESS DATA SHEETS
A.K.C.
TECHNOLOGY
GENERAL SERVICES AND UTILITIES CHECKLIST
Job No.:
Job Name:
Document No.
Project No.
Client
Location
Plant
PREPARED BY:
Sheet of
DATE:
SERVICE
SUSTAINED
QUANTITY
PEAK
UNIT
ELECTRICAL 13.8 KV
*
KVA
ELECTRICAL 2300 V
*
KVA
ELECTRICAL 440 V
*
KVA
MISC. LIGHTING, ST. ETC., (110 V)
WELL WATER (CITY)
SEA WATER
RIVER WATER – PROCESS
RIVER WATER – FIRE PROT.
*
FUEL GAS
ODORIZED GAS
SCFM
SCFM
COMPRESSED AIR
SCFM
STEAM
(400 OR 475) Psig
235 Psig
150 Psig
30 Psig
CONDENSATE RETURN
CONDENSATE USAGE
PROCESS TRANSFER AND RAW MATERIALS
CAUSTIC (–%)
BRINE (–%)
LPG
lb/h
lb/h
lb/h
lb/h
lb/h
lb/h
lb/h
OPERATING PRESSURE AND
TEMPERATURE
REMARKS
KVA
gpm
gpm
gpm
gpm
lb/h
lb/h
lb/h
SITE DEV. (AREA FILL)
RAIL ROADS
BLOCK ACCESS ROADS
gpm
gpm
SANITARY SEWERS
WASTE WATER
* ASSUME 1 HORSE POWER = 1 KVA
NOTE: ONE COPY OF THIS LIST TO BE GIVEN TO SERVICE AND UTILITY SECTION.
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2
Chemical
Symbol
3
Phase
4
Location in Plant
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4. Column 11
Open Cup
(Note 3)
7
6
Flash Point ° C
Closed Cup
5
Issue No.:
Description
Made/Revised by
Checked by
Approved Process
Approved
Toxicity
Sheet of
HAZARDOUS CHEMICAL AND CONDITIONS SCHEDULE
Lower
A – Water
E – Foam
B – Powered Talc F – See Remarks
C – CO2
D – Dry Chemical
Upper
8
9
Fire Hazard
Explosive Limits % by Volume in Air
1
12
Date
Equipment
Protective
B.A. – Breathing Apparatus
F.C. – Full Clothing
F.W. – Footware
G.O. – Goggles
Extinguishing Agents
Temp ° C
5. Column 12
Suitable
1
2
Autoignition
10
Date
13
G.V. – Gloves
X – See Remarks.
Remarks
Job Code:CAPA
Note:
1. This Schedule is given without any Legal responsibility on the part of AKC Technology.
2. Column 3: Vapor – V, Liquid – L, Solid – S
3. Toxicity: Denotes Threshold Limit (T.L.) under which it is believed nearly all workers
may be exposed day after day without adverse effect. The figures relate
to average concentration for a normal working day.
1
Chemical Hazard
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32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
Stream
HEAT AND MASS BALANCES
Units
→?
Job Name:
Job No.:
°API
K
of
M.W.
Sheet
SpGr
FLOWING
*barg
psig
*° F
°C
?
Issue No.:
Made/Revised by
Checked by
Approved Process
Approved by
B.P.S.D.
at 60° F
1
GPM
FLOWING
Date
Mol %
2
Mol/h
Date
lb/h
*kg/h
3
?
Btu/lb
*kcal/kg
Date
?
106 Btu/h
*106 kcal/h
Job Code:CAPA
↓
* delete unit as necessary
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TECHNOLOGY
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APPENDIX A
789
Document No.
A.K.C.
TECHNOLOGY
HEAT EXCHANGER RATING SHEET
Sheet of
Items No. (s)
PART 1 - TO BE FILLED IN COMPLETELY
1 Exchanger Name:
2 Job:
*
Location: *
*
Arrangement: Horiz = 0; Vert = 1
3 Type of Unit: F.T.S.=0; FLTG.HEAD=1; U-TUBE=2; FOR KETTLES ADD 3
4 Hot Side: Either=0; Shell=1; Tubes=2
5
Units
Units: S.I. 0; Engineering = 1
S.I.
Engineering
6 Fluid Circulated
-
-
7 Total Fluid Entering (Normal)
kg/hr
lb/hr
8 Flow Margin
%
%
9 Temperature In/Out
°C
°F
bar
psi
11 Inlet Pressure Operating/Design
barA
psia
12 Normal Heat Load
kW
13 Heat Load Margin
%
%
14 Design Temperature
°C
°F
10 Max Pressure Drop at line 8
Rev.
*
HOT FLUID
COLD FLUID
Btu/hr
15 Corrosion Allowance
mm
ins
16 Fouling Resistance
°Cm2/Wl
°F hr ft2/Btu
17 Line N.B. In/Out
mm
ins
19 GAS (AD VAPOR) IN
-
-
20 Flow of Vapor and Gas at Inlet
kg/hr
lb/hr
21 Code Number
-
-
18 Part 2
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
-
-
W/m °C
39 Thermal Conductivity
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
3
3
49 Density
kg/m
lb/ft
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
%
%
56 Hot Fluid Temperature
°C
°F
57 Cold Fluid Temperature
°C
°F
1
2
3
4
5
6
7
8
9
10
58 PART 4 - CODE NUMBERS TO BE FILLED IN COMPLETELY
59 Material for
Description
Code No.
O.D.
Thickness
Length
Passes
Number
Contents Lethal?
Δ
Yes/No
60 Tubes
Yes/No
61 Shell
62 Floating Head
Tube Pitch = mm/in.
o
63 Channel
64 Tube Sheets
NOTES
Issue No.
1 Date
2 Date
3 Date
4 Date
5 Date
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790 A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND PROCESS DATA SHEETS
HYDROCARBON DEWPOINT
CALCULATION
A.K.C.
TECHNOLOGY
Job No:
Item No.
Job:
Heaviest Compound:
y
H2
N2
CO
CH4
C2H4
CO2
C2H6
C2H2
C3H6
C3H8
Tb
67
130
172
201
305
330
332
340
406
416
Page
PROPANE
LIGHT
COMPONENT
TbFeL
FeL
67.000
1.000
2.972
0.0229
0.797
0.0046
0.383
0.0019
HEAVY
COMPONENT
FeH
TbFeH
0.105
0.180
0.244
0.548
0.638
0.646
0.676
0.954
1.000
Pressure:
psia
Convergence Pressure:
psia
o
ASSUMED TEMPERATURE
o
o
F
F
F
K
y/K
K
y/K
K
y/K
o
F
K
of
y/K
F
x
13.61
31.00
49.02
167.0
210.6
214.3
229.9
387.3
416.0
Σ y/K
1.000
o
1.000
x for H2
Σ (yFeL/K)
Σ (yFeH/K)
E.B.PL
E.B.PH
Pg
Estimate of Dewpoint:
at Estimate Pg of:
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psia
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TECHNOLOGY
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PRESSURE:
barg
SIZE
psig
kg/cm2 g
3
4
5
NOM. PIPING FLUID
PIPE SPEC. DENSITY PHASE
6
Issue No.:
Description
Made/Revised by
Checked by
Approved Process
Approved
°C
°F
TEMP.
1
Date
2
mm
10
INSULATION
CLASS
NOM. THICK
NOMINAL PIPE SIZE in.
7
8
9
ROUTING
PLANT
OPERATING
DESIGN
TO
CONDITION PRESS.
TEMP. PRESS.
TEMPERATURE:
LINE
FROM
Sheet of
11
CLASS
TEST
Date
PRESS.
TEST
Date
Insulation Thickness
CLASS
FIELD
3
in.
CLASS
4
FIELD
TEST
5
12
mm
Date
6
Date
13
14 14a
CHEMICAL REMARKS STRESS
CLEANING
CATEGORY
PRESS. LIMITED BY
Date
No.
15
16
ELD
ISO. DRG.
DRG.
No.
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DATA
CHANGES
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1
ISS
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COLUMN
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NUMBER
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SIZE
in.
FROM
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TITLE:
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CLASS OR CODE
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PRESSURE, psig
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SPECIAL
REMARKS
1
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2
Date
3
Date
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LINE
FLOW
NUMBER
MEDIUM
A.K.C.
TECHNOLOGY
QUANTITY QUANTITY
FLOW, gpm
FLOW
or SCFH
lb/h
FLUID
TEMP.
°F
Sheet of
LINE SCHEDULE SHEET
DENSITY
lb/ft3
DENSITY
lb/gal
SpGr
at 60° F
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Date
SpGr
EXPANSION
AT FLOW
COEFFICIENT
TEMPERATURE
1
Date
3
Date
CHEMICAL MOL. MW LINE SIZE
PRESS.
FORMULA
DROP/100 ft
2
EST. LINE
LENGTH
4
LINE
PRESS
DROP
Date
Date
LINE
LINE
ORIGIN TERMINATION
5
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NUMBER MATERIAL
A.K.C.
TECHNOLOGY
FROM
TO
LINE SUMMARY TABLE
TITLE:
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LINE SIZE OPERATING OPERATING
TEMP.
PRESS.
°F
psig
Sheet
TEST
PRESS.
psig
lb/h
1
GPM at 60° F
QUANTITY
Date
GPM
(HOT)
2
CFS
(HOT)
Date
VEL.
fps
3
PRESSURE DROP
PER 100 ft
TOTAL
psi
psi
Date
REMARKS
NO.
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22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42 Notes:
43
44
45
46
47
48
kg mol/h
BALANCE
MOL WT
MASS
Mol %
kg mol/h
of
Mol %
Sheet
kg mol/h
Mol %
Issue No.:
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Approved
kg mol/h
Mol %
1
kg mol/h
Date
Mol %
2
kg mol/h
Date
Mol %
3
kg mol/h
Date
Mol %
Job Code:CAPA
STREAM NAME
PHASE
TEMPERATURE (° C)
COMPONENT
Water
Hydrogen
Nitrogen
Carbon monoxide
Carbon dioxide
Methane
Acetylene
Ethylene
Ethane
Propyne
Propadiene
Propylene
Propane
Isobutane
Isobutene
n -Butane
1-Butene
1,3-Butadiene
1-Pentene
neo-Pentane
Isopentane
n -Pentane
Toluene
m -Xylene
Methanol
MTBE
TBA
DIISO
TOTAL (kg mol/h)
STREAM NUMBER
Job No.:
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CAPACITY
PRESSURE
(m3/h) (Turbine - Te/h)
IN
OUT
(kg/cm2g)
Issue No.:
Description
Made/ Revised by
Checked by
Approved Process
Approved
INLET
TEMP. (° C)
1
NPSHA
(m)
Date
TYPE
(see Note 1)
2
MATERIALS
Date
Date
ABSOLUTE SPEED (RPM)/ REMARKS
POWER (kW)
3
Job Code:CAPA
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Notes: 1. Rotary Equipment Type Coding: A = Axial; C = Centrifugal; M = Metering; R = Reciprocating; S = Screw
2. All drives electric motor unless specified otherwise.
FLUID
S.G/M.W
OFF
SERVICE DESCRIPTION
ITEM No.
No.
Sheet of
MECHANICAL EQUIPMENT SCHEDULE
Job No.:
Job Name:
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TECHNOLOGY
FROM
PIPE LINE LIST
TITLE:
TO
TEMPERATURE (° F)
OPERATING DESIGN
Sheet
of
PRESSURE (psig)
OPERATING DESIGN
VELOCITY
ft/s
Issue No.:
Description
Made/ Revised by
Checked by
Approved Process
Approved
PRESSURE/100 ft
PD/100 ft
1
FLOW 1
Date
P&ID
NUMBER
2
Date
3
Date
Job Code:CAPA
Fonts used:Times & Universal 55 family
Note: 1. Flow Units: G = gpm; C = acfm; P = lb/h
Job No.:
Job Name:
Document No.
Project No.
Client
Location
Plant
LINE
NUMBER
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FROM
PIPE LIST
TITLE:
TO
Fonts used:Times & Universal 55 family
TEMPERATURE (° F)
OPERATING DESIGN
Sheet
of
PRESSURE (psig)
OPERATING DESIGN
VELOCITY
ft/s
Issue No.:
Description
Made/Revised by
Checked by
Approved Process
Approved
PRESSURE/100 ft
PD/100 ft
1
FLOW1
Date
P&ID
NUMBER
2
Date
3
Date
Job Code:CAPA
NOTE: 1. FLOW UNITS: G = gpm; C = acfm; P = lb/h
Job No.:
Job Name:
Document No.
Project No.
Client
Location
Plant
LINE
NUMBER
A.K.C.
TECHNOLOGY
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of
FLUID
SYMBOL
Sheet
Issue No.:
Description
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Approved
1
Date
2
Date
HAZARDOUS
FLUID
MAXIMUM
CONTINUOUS
PIPE
NOTES
MAXIMUM
SPECIFICATION
PIPE SIZE
MATERIAL
STATE
RANGE
OPERATING
in.
CLASSIFICATION LIQUID/GAS
TEMPERATURE, ° F PRESSURE, psia
PIPING PROCESS CONDITIONS SUMMARY
Job No.:
Job Name:
Document No.
Project No.
Client
Location
Plant
INDEX
MATERIAL AND COMPOSITION
NUMBER
A.K.C.
TECHNOLOGY
3
Date
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Page:800
800 A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND PROCESS DATA SHEETS
PLATE HEAT EXCHANGER
DATA SHEET
A.K.C.
TECHNOLOGY
Job
Item Name
PROCESS DESIGN
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
48
49
50
51
52
53
54
UNITS
Fluid Circulated
Total Fluid Entering (Normal)
Flow Margin
Inlet Vapor and Gas (&MW)
Inlet Liquid
Fluid Vaporized/Condensed (&MW)
Temperature In/Out
Max. Pressure Drop
Inlet Pressure (Operating)
Normal Heat Load
Heat Load Margin
Fouling Resistance
FLUID PROPERTIES
Specific Heat
Thermal Conductivity
-
kg/h
%
kg/h
kg/h
kg/h
o
C
bar
bar g
kW
%
m2 ο C/W
lb/h
%
lb/h
lb/h
lb/h
o
F
psi
psig
Btu/h
%
ft 2 ο Fh/Btu
kJ/kgοC
cP
cP
kJ/kg
Btu/lb οF
ο
Btu/hr ft F
t3
lb/f
lb/hr.ft
lb/hr.ft
Btu/lb
bar g
ο
C
mm
in
mm
psig
ο
F
in.
in.
in.
W/m C
kg/m3
Density
Viscosity
Liquid Viscosity (at Temp.)
Latent Heat
ENGINEERING DESIGN
Process Design Pressure
Process Design Temperature
Corrosion Allowance (Header)
Line N.B. In/Out
Minimum Flow Passage
Plate Material
Frame Material
Gasket Material
Desgin Code
FLUID 1
-
ο
Document No.
Sheet
of
Item No.(s)
No. Working
Rev.
Total No. Off
FLUID 2
FLUID 3
3
Date
NOTES
1. Unless otherwise stated fluid properties are for mean fluid temperatures.
2. Sour Service
Yes / No
1
Date
2
Date
Description
Made/Revised by
Checked by
Approved Process
Approved by
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Page:801
801
APPENDIX A
Made
Job No.
Checked
PROCESS DATA SHEET
A.K.C.
TECHNOLOGY
Item No.
Date
Job
Sheet
of
CALCULATION OF PRESSURE DROP IN FIXED CATALYST BEDS
REQUIRED DATA
VESSEL NO:
SERVICE:
CATALYST:
GAS DATA:
VOLUME REQUIRED
MANUFACTURER & NO.
DIMENSIONS
EQUIV. PARTICLE DIA.
SHAPE/SIZE FACTOR
FLOW RATE
MIN. MOLECULAR WEIGHT
BED OUTLET PRESSURE
MAX. BED TEMPERATURE
ο
ο
ABS. TEMPERATURE ( K = C + 273)
CALCULATION
k1 =
BED DIAMETER
BED C.S.A.
BED DEPTH
SUPERFICIAL MASS FLOW
MASS FLOW FACTOR
DpG
REYNOLDS NO. FACTOR
k2
CLEAN PRESSURE DROP/UNIT DEPTH
CLEAN OVERALL PRESSURE DROP
SAFETY/FOULING FACTOR
FLOW SHEET PRESSURE DROP
SYMBOLS
D
A
L
G
Gf
Ref
k2
ΔPc
ΔPc
f
ΔP
V
ft3
Dp
Sf
ft.
W
W2
lb/h
(lb/h)2
P
psia
ο
C
K
T
(T )(Sf ) =
(M )(P )
UNITS
ft
2
ft
ft.
2
lb/h.ft
psi/ft.
psi
psi
=
CALCULATION
0.7854D
V/A
W/A
CASE 1
CASE 2
CASE 3
5
6
CASE 4
2
k1Ref
k2Gf
LΔPc
1.25/
fΔPc
* IF VALUE OF DpG > 200 (750 FOR RING CATALYSTS) PUT Ref = 1.0
IF 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
Description
Made/Revised by
Checked by
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802 A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND PROCESS DATA SHEETS
PROCESS ENGINEERING JOB ANALYSIS SUMMARY
A.K.C.
TECHNOLOGY
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
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)
10
Air ( psi)
cfm (60° F and 1atm)
11
Power (
12
Horsepower
13
Condensate
lb/h
RAW MATERIALS
UNIT RATE
UNIT RATE/
PRODUCTION BASIS
)
14
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
1
Chlorine
2
HCl ( %)
3
Salt ( %)
4
Caustic ( %)
5
Ammonia ( %)
6
H2SO4 ( %)
7
Gas (
UNIT RATE
)
8
9
10
11
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APPENDIX A
PUMP CALCULATION SHEET
A.K.C.
TECHNOLOGY
Document No.
Sheet
of
Item No. (s)
No. Working
Job
Item Name.
UNITS
CASE I
CASE II
+
803
Rev.
Total No. off
SKETCH OF PUMP HOOK-UP
1
2 Liquid Pumped
3 Corrosion/Erosion
4 Due To
5
6
7
8
9
Operating Temp. (T )
Specific Gravity at T
Viscosity
Vapor Pressure at T
Normal mass Flowrate
°C
°F
cP
bara
kg/h
cP
psia
lb/h
gpm
3
10 Normal Vol. Flowrate
11 Min. Vol. Flowrate
m /h
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
Design Vol. Flowrate
m3/h
SUCTION CONDITION
Pressure at Equipment
barg
Static Head
bar
Total – Lines 14 + 15
bar
Suction Line
bar
ΔP
ΔP
Filter/Strainer
bar
gpm
psig
psi
psi
psi
psi
+
+/–
+
–
–
+
–
–
Total Suction Pressure
barg
DISCHARGE CONDITION
Pressure at Equipment
barg
Static Head
bar
psig
+
+
psig
psi
+
+/–
+
+/–
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
Exchanger
ΔP
bar
psi
+
+
Furnace
Orifice
Control Valve
ΔP
ΔP
bar
bar
bar
psi
psi
psi
+
+
+
+
+
+
Line
ΔP
bar
psi
+
+
Total Discharge Press.
Differential Pressure
Differential Head
NPSH
barg
bar
bar
psig
psi
psi
+
+
Total Suction Pressure
Vapor Pressure
NPSH – Lines 37 – 38
=
Safety Margin
NPSH – Lines 40–41
Hydraulic Power
Estimated Efficiency
Estimated Abs. Power
Type of Pump
Drive
bara
bara
bara
m
m
m
kW
%
kW
psia
psia
psia
ft
ft
ft
Hp
%
Hp
NOTES
1. Pump shut-off head not to exceed………
2. Relief valve on pump discharge to be set at ……………
3. Pump case design pressure…………
design temperature……..
4. Sealing/flushing fluid available:
5. Cooling medium available:
6. Insulation required:
Material – Casing
– Impeller
– Shaft
7. Start-up/commissioning fluid SG.
Sour Service
54 HEAD
55 VOLUME
56
57
58
59
60
61
62
ΔP
Yes/No
m = 10 × kg/cm 2/SG
m = 10.2 × bar/SG
3
m /h × SG × 1000 = kg/h
POWER
3
ft = 2.31 × psi/SG
igpm × SG × 600 = lb/h
kW = m /h × bar/36.0
1 Date
3
2
kW = m /h × kg/cm /36.71
2 Date
Hp = igpm × psi/1427
3 Date
4 Date
5 Date
Description
Made/Revised by
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A.K.C.
Fonts used:Times & Universal 55 family
ft3/h
psig
psig
psi/ft
ft.
hp
-
m3/h
bar g
bar g
bar /m
m
kW
-
11
12
13
14
15
16
Margins:Top:3p6
Gutter:4p6
34 Seal / Flush Fluid
35 Quench
36 Notes
37
38
39
40
41
42
43
44
45
Services / Utilities
Cooling Water
Material: Casing
Impeller
Shaft
Sour Service
Packing Type / Mechanical Seal Type
hp
ft3/h
ft3/h
hp
hp
hp
psi
-
Issue No.:
Description
Made/Revised by
Checked by
Approved- Process
Approved
1
Date
2
Date
3
Date
22-12-2006
m3/h
m3/h
kW
kW
kW
bar
20
21
22
23
24
25
26
27
28
29
30
31
32
33
Type of Driver
Driver Rated Power ( per pump)
Design Power Consumption ( per pump)
Normal Power Consumption (per pump)
Max. Shut-Off Head
kW
18 Estimated Pump Efficieny
19 Estimated Shaft Power ( per pump)
17 R.P.M
Sheet of
Chapter:0capaappA
-
ft3/h
m3/h
10 Design Capacity (per pump)
Normal Capacity (per pump)
Discharge Pressure
Suction Pressure
Differential Head
Minimum NPSH Available / Required
Hydraulic Power (per pump)
F
ο
lb/ft.h
psia
Units
cP
bara
6
7
8
9
ο
PUMP SCHEDULE
Job Code:CAPA
C
Operating - Temperature
Specific Gravity at Operationg Temperature
Viscosity at Operating Temperature
Vapor Pressure at Operating Temperature
1
2
3
4
5
TECHNOLOGY
Job No.:
Job Name:
Document No.
Project No.
Client
Location
Plant
Item Number.
Item Name
Number Off: No. Running /Total Installed
Preferred Type
Liquid Pumped
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Page:805
APPENDIX A
DOCUMENT / ITEM REFERENCE
RELIEF DEVICE PHILOSOPHY SHEET
A.K.C.
TECHNOLOGY
805
EQUIPMENT No.:
SHEET No.:
DATE:
CHECKED BY:
OF
1
MADE BY:
2
DESIGN CODES:
VESSELS
LINES
EXCHANGERS
3
4
OTHER REQUIREMENTS
5
6
BASIS FOR CALCULATION:
7
8
SET PRESSURE, PSIG:
(a) BEFORE RELIEVING
MAX. BACK PRESSURE:
(b) WHILE RELIEVING
9
Calculated
10
NORMAL CONDITIONS UNDER RELIEF DEVICE:
STATE:
TEMPERATURE, °F:
PRESSURE, PSIG:
POSSIBLE
FLUID
RELIEF
ORIFICE
CAUSE?
RELIEVED
RATE, lb/h
AREA, in2.
11
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 reaction
24
12. Boxed in thermal expansion
25
13. External fire
26
14. (specify)
27
15. (specify)
28
16. (specifty)
29
SELECTED DESIGN CASE:
30
31
RELIEVED FLUID: STATE
DENSITY / MW:
TEMPERATURE:
COMPOSITION:
RELIEF RATE REQUIRED, lb/h:
AREA, in2:
ORIFICE SELECTED:
Cp/Cv:
32
FLASHING:
33
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
TANK AND VESSEL AGITATOR DATA SHEET
Project Name:
PROCESS
MIXING
IMPELLER
TANK OR VESSEL
GENERAL
ELEC T.
DESI GN DEPT . INFORMATION
Drawing No:
Project No.:
sheet …….. Of ……..
Associated Vessel/Tank* Item No:
Equipment No:
No. Off:
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:
9. Special Remarks:
10. Components % by weight:
Approved
Approved Process
Checked by
Made/Revised by
Description
1
Da te
2
Da te
PROCESS DEPT. INFORMATION
3
Da te
A.K.C.
TECHNOLOGY
11.
12.
13.
14.
15.
16.
Temperature during mixing:
Specific gravity of components:
Viscosity of mixing at mixing temperature:
Specific gravity of product at mixing temperature:
Size of solid particles:
Special Remarks:
17.
18.
19.
20.
21.
22.
23.
24.
25.
26.
Type of impeller:
Number of impellers on shaft:
Position of impellers:
Distance between shaft end & vessel:
Preferred impeller speed:
Type of drive: Direct/Vee belt/Fluid*
Type of seal: Vapor/Packed gland/Mechanical/Easy replacement*
Method of installation: Assembled in/Assembled out* of vessel
Entry position:
Materials of construction:
Bottom bearing:
Shaft diameter:
27. Absorbed HP/KW*:
28. Other information:
Installed HP/KW*:
29.
30.
31.
32.
33.
34.
Capacity:
Dimensions:
Coils, baffles, etc.:
Fixing agitator (beams, flanges, etc.):
If at atmospheric pressure: Closed/Open*
Headroom available above agitator:
Other information:
Can stuffing box be greased? Yes/No*
Motor enclosure:
35. Agitator installed: Indoors/Outdoors
36. Electrical specification:
37. Any other electrical information:
38.
39.
40.
41.
42.
43.
44.
45.
Motor to be included: Yes/No*
Motor Will/Will not* be sent to manufacturer for assembly and alignment.
Threads: Unified /*
All rotating parts must be strictly guarded to BS 1649/ASME
Fixing bolts supplied by:
Net weight including motor:
Witnessed run in air:
General notes:
NOTE: * Indicates delete as necessary.
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Page:807
APPENDIX A
TANK PROCESS DATA SHEET
A.K.C.
TECHNOLOGY
Job:
807
Doc. No:
Item No.
Sheet of
Item Name:
NOTE: * indicates delete as necessary;
** indicates for other than Code reason
5
10
15
20
Issue No.
Made/Revised by
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Margins:Top:3p6
Date
Gutter:4p6
2
Shell Length:
No. Required:
Nozzles
Inlet
Mark No.
C-
Vapor Out
C-
Liquid Out:
C-
Thermocouple
Pressure Gauge
Gauge Glass
Level Control
Safety Valve
RRRRR-
Vent
Drain
Steam Out
CCC-
Manhole
A-
min. Base Elev'n:
Material:
Date
Size
Number
by Inst. Op.
25
26 Shell Diameter (O.D. / I.D.):
27 Center Line: *Horizontal / Vertical
28
Pressure:
g
Temperature: °F / °C
29 Item Number
30 Operating
31 Design
32 Emergency Vacuum Design: * Yes / No
Material
Corr. Allowance
33
34 Shell
35 Heads
36 Liner
37 Type of Heads
38 Code:
39 Stress Relieve**:
Radiography**:
40 Joint Efficiency:
* °F / °C
at
41 Density of Contents:
Weight Full:
42 Weight Empty:
43 Is vessel subject to mechanical vibration? *Yes / No
Type: *Frost and Personnel Protection / Cold
44 insulation:
Anticondensation / Heat Conservation
45 *Yes / No
46 REMARKS:
47
48
49
50
51
52
53
54
k-Skirt Length
3
Font Size:9/10 pt
Date
4
Text Width:41p6
Date
Depth:65 Lines
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
Fonts used:Times & Universal 55 family
in.
ft 3
ft 3
mm
m3
m3
Total Volume
Working Capacity
Internals / Fittings
Margins:Top:3p6
Gutter:4p6
in.
Issue No.:
Description
Made/Revised by
Checked by
Approved- Process
Approved
1
Date
2
Date
3
Date
22-12-2006
Notes
Shell Corrosion Allowance
Sour Service
Stress Relieved for Process Reasons
Insulation
mm
°F
psig
°F
°C
bar g
°C
Operating Temperature
Design Pressure +/ -
of
Chapter:0capaappA
Design Temperature
Vacuum Design
Material: Shell
Liner
Internals
psig
bar g
Operating Pressure
in.
in.
Sheet
Job Code:CAPA
mm
mm
Units
TANK SCHEDULE
Job No.:
Job Name:
Document No.
Project No.
Client
Location
Plant
Item Number.
Item Name
Number Required
Type
Length x Width
Height
Diameter
Minimum Base Elevation
A.K.C.
TECHNOLOGY
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808 A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND PROCESS DATA SHEETS
Depth:65 Lines
A.K.C.
TECHNOLOGY
SERVICE
DESCRIPTION
TIE-IN-SCHEDULE
EXISTING LINE
NUMBER
of
NEW LINE
NUMBER
Sheet
EXISTING
ELD*
NUMBER
NEW
ELD*
NUMBER
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Approved
1
REMARKS
Date
2
Date
3
TIE-IN
NUMBER
Date
Job Code:CAPA
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* ELD = ENGINEERING LINE DRAWING
TIE-IN
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810 A LIST OF ENGINEERING PROCESS FLOW DIAGRAMS AND PROCESS DATA SHEETS
Made by:
Document No.
TOWER PROCESS DATA SHEET
A.K.C.
TECHNOLOGY
Date:
Job
Checked by:
Item No:(s)
Item Name
Sheet
of
Tower Name:
NOTE: * indicates delete as necessary; ** indicates for other than code reason
Top
Bottom
Shell Diameters O.D. - I.D.
No. of Trays
Pressure
Operating
*psig
Design
Temperature
Operating
Design
*oF / oC
Material
Shell
Trays
Caps
Liner or Clad
Corrosion Shell
Allowance
Heads
Trays
Tray Spacing
Type of Liquid Flow
Type of Trays
Joint Efficiency
Code
Emergency Vac. Design *Yes / No
Stress Relieved **Yes / No
Radiography **Yes / No
Is vessel subject to mechanical vibration *Yes / No
Insulation
Type: *Frost and Personnel Protection / Cold /
*Yes / No
/anticondensation / Heat Conservation /
Min. Base Elevation:
Skirt length:
Weight Empty:
Full:
Nozzles
Mark No.
Size
Number
Feed
COverhead Vpr. CReflux In
CBottoms
Reboiler Vpr
Reboiler liq
CCC-
Thermocouple
Level Glass
Press Gauge
Level Control
Safety Valve
RRRRR-
Vent
Drain
Steam Out
Manholes
Handholes
Cap Type:
NOTES
CCCAA-
by inst. Gp.
1
2
3
4
5
6
7
8
9
10
11
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14
15
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41
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46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
Tray Layout Ref:
1
Date
2
Date
3
Date
4
Date
Description
Made/Revised by
Checked by
Approved Process
Approved by
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APPENDIX A
TRAY LOADING SUMMARY
A.K.C.
TECHNOLOGY
Job:
Tower Name:
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
48
49
50
51
52
53
54
55
56
57
58
59
60
Job No.
item No.
Sheet of
Type of Tray
Manufacturer
Pressure at top of Tower
Max. ΔP over Tower
No. of Trays
Tray location
Tray Number*
Tray Spacing
Tower Internal Diameter I.D.
Vapor to Tray
Temperature
Compressibility
Density
Molecular Weight
Rate
Liquid from Tray
Temperature
Surface Tension
Viscosity
Density
Rate
Foaming Tendency **
Number of Passes
Minimum Hole Diameter ***
Minimum DC Residence Time***
Maximum Rate as % Design
Minimum Rate as % Design
Design Rate % Flood Rate***
Tray Material
Valve or Cap Material
Corrosion Allowance
Tray Thickness***
NOTES:
811
Mfr. Ref:
barg
bar
psia
psi
Aboved Feed
mm
mm
in.
in.
o
o
C
kg/m
units Used: METRIC/BRITISH (delete one)
Below Feed
F
3
lb/ft
3
kg/h
lb/h
°C
dynes/cm
cps
kg/m3
kg/h
°F
lb/ft
lb ft/hr
lb/ft3
lb/h
mm
secs
in.
s
mm
mm
in.
in.
* Trays are numbered from the bottom of the tower upwardstop of the tower downwards
** Indicate whether 'non', 'moderate', 'high' or 'severe'
∗ ∗ ∗ Data to be supplied by tray manufacturer unless special Process/Client requirement entered here.
REMARKS:
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1
Date
2
Date
3
Date
Description
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1
INITIATING VARIABLE
Job No.:
Job Name:
Document No.
Project No.
Client
Location
Plant
TECHNOLOGY
2
BASIC
INST. No.
3
4
PRE- ALARM
INST. No.
SETTING
TRIP SCHEDULE
of
5
6
CUT OUT
INST. No.
SETTING
Sheet
7
FIRST FAULT
INDICATION
Issue No.
Decription
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Approved
8
INHIBIT
SWITCH
1
9
TRIP LINKAGE
Date
10
ITEM
ACTUATED
2
11
PRIMARY
PROCESS
EFFECT
Date
12
REMARKS
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A.K.C.
TECHNOLOGY
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Source I is:
NUMBER OFF
Inst/d Work'g
%
Motor
Efficiency
UTILITY SUMMARY SHEET
kW
kW
Electrical
kW
HT
kW
LT
Total Consumption
Electrical
Issue No.:
Description
Made/Revised by
Checked by
Approved- Process
Approved by
Date
2
kg/h=
T=
kg/h=
T=
kg/h=
T=
STEAM/ CONDENSATE/ BOILER
See Note 1
P=
P=
P=
1
kg/h=
Condensate
FEEDWATER
Date
kg/h=
BFW
3
Flow
m3/h
Source
Date
kW
ΔT
°C
Flow
m3/h
ΔT
°C
FUEL
Date
Absorbed
5
II
Date
COOLING WATER
See Note 2
I
Source
4
kW
Fired
6
See Note 1
nm3/h
P=
COMPRESSED
AIR
Date
REMARKS AND OTHER SERVICES
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T is
Source II is
Electrical
Shaft
kW
ELECTRICITY
Per Machine
Consumption
Installed
Sheet of
Job Code:CAPA
Note 1: State units - P is
Note 2: Cooling water
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Item Name
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Location
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ITEM No.
No.
UNITS
A.K.C.
TECHNOLOGY
SERVICE DESCRIPTION
VERTICAL OR
HORIZONTAL
VESSEL AND TANK SCHEDULE
DIAMETER LENGTH
Sheet of
THICKNESS
HEAD
SHELL
Issue No.:
Description
Made/Revised by
Checked by
Approved Process
Approved
LINING
1
INSULATION
CODE
Date
Date
WEIGHT
2
TEST
PRESSURE, psig
REFERENCE
DRAWING
3
PURCHASE
ORDER TO
Date
P.O.
Number
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TECHNOLOGY
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O.D.
HEIGHT GALLONS
or LENGTH.
CAPACITY
AND TANK SUMMARY
Driver
Vessel and tank summary
TYPE
VESSEL
Issue No.:
Description
Made/Revised by
Checked by
Approved- Process
Approved
1
Date
THICKNESS, INCHES
CORROSION MATERIAL
SADDLE
SHELL
HEAD SADDLE ALLOWANCE SHELL
SKIRT
SKIRT
& HEADS
INCHES
SUPPORT
SUPPORT
Sheet of
OPER'N
2
3
PRESSURE, PSIG
DESIGN
TEST
Date
4
TEMP., °F
OPER'N DESIGN
Date
CODE
Date
Date
STAMP REFERENCE
DRAWING
No.
5
NOTES
Job Code:CAPA
Figure 1-38
ITEM No. EQUIPMENT
Job No.:
Job Name:
Document No.
Project No.
Client
Location
Plant
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°F
psig
°F
°C
bar g
°C
17
18
19
20
21
22
23
24
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26
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Date
2
Date
3
Date
22-12-2006
Notes
Shell Corrosion Allowance
Sour Service
Stress Relieved for Process Reasons
Insulation
in.
psig
bar g
15 Operating Temperature
16 Design Pressure
Issue No.:
Description
Made/Revised by
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Approved
Chapter:0capaappA
mm
in.
in.
mm
mm
Sheet of
Job Code:CAPA
Design Temperature
Vacuum Design
Material: Shell
Liner
Internals
in.
in.
Units
mm
mm
VESSEL SCHEDULE
Job No.:
Job Name:
Document No.
Project No.
Client
Location
Plant
1 Item Number.
2 Item Name
3 Number Required
4
5 Shell Diameter (O.D/I.D.)
6 Shell Length
7 Center Line (H/V)
8 Boot Size
9 Base Elevation
10 Internals
11
12
13
14 Operating Pressure
A.K.C.
TECHNOLOGY
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APPENDIX A
WATE R
ANALYSIS
SHEET
A.K.C.
TECHNOLOGY
Submitted by:
Address:
817
Location:
Date:
**
Analysis
No.
Date:
pH Value
Suspended Solids
Total Dissolved Solids
Total Dissolved Solids
Alkalinity to Pp
mg/l
mg/l at 110° C
mg/l at 180° C
as mg/l CaCO3
Alkalinity to MO
as mg/l CaCO3
Sulphate
Chloride
Nitrate
as mg/l SO4
as mg/l Cl
as mg/l NO3
Silica
as mg/l SiO2
Phosphate
as mg/l PO4
Total Anions
as mg/l CaCO3
Total Hardness
Calcium
Magnesium
Sodium*
Potassium*
Iron
Manganese
Free and Saline Ammonia
as mg/l CaCO3
as mg/l Ca
as mg/l Mg
as mg/l Na
as mg/l K
as mg/l Fe
as mg/l Mn
as mg/l NH3
Total Cations
Free Dissolved CO2
as mg/l CO2
Dissolved O2
Color Hazaen Units
Turbidity Formazin Units+
Lead
Copper
Residual Chlorine
Flouride
Sulfite
as mg/l CaCO3
as mg/l O
FTU APHA
as mg/l Pb
as mg/l Cu
as mg/l F
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).
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