Add Equipment
Unit Number
100
CEPCI
568
Edit Equipment Remove All Equipment User Added Equipment Compressor s
Compressor Type
Power (kilowatts)
# Spares
MOC
Purchased Equipment Cost
Bare Module Cost
C-101
Centrifugal
318
1
Carbon Steel
$
$
Exchangers
Exchanger Type
Shell Pressure (barg)
Tube Pressure (barg)
MOC
E-101
Air Cooler
45
Aluminum
1900
$
310,000
$
896,000
E-102
Fixed, Sheet, or U-Tube
3
45
Stainless Steel / Stainless Steel
160
$
40,400
$
258,000
E-103
Fixed, Sheet, or U-Tube
3
3
Stainless Steel / Stainless Steel
820
$
127,000
$
785,000
Pumps (with drives)
Pump Type
Power (kilowatts)
# Spares
MOC
Discharge Pressure (barg)
P-101
Centrifugal
96
1
Stainless Steel
P-102
Centrifugal
6
1
Stainless Steel
429,000
Area Purchased (square meters) Equipment Cost
1,170,000
Bare Module Cost
Purchased Equipment Cost
Bare Module Cost
45
$
36,000
$
267,000
2
$
9,560
$
47,500
$
3,423,500
Total Bare Module Cost
Name
Total Module Cost
Grass Roots Cost
C-101 E-101 E-101 E-102 E-102 E-103 E-103 E-103 E-104 E-105 F-101 K-101 P-101 P-102
$ $ $ $ $ $ $ $ $ $ $ $ $ $
1,390,000 1,056,724 713,000 300,000 210,000 926,000 217,630 801,000 304,662 340,000 583,000 37,200,000 315,000 56,100
$ $ $ $ $ $ $ $ $ $ $ $ $ $
1,970,000 1,390,000 850,000 371,000 257,000 1,140,000 265,000 980,000 371,000 403,000 750,000 43,500,000 374,000 72,000
Totals
$
44,400,000
$
52,700,000
Utility Used NA Unspecified Unspecified Unspecified Unspecified Unspecified Unspecified Unspecified Unspecified Unspecified Electricity Unspecified Electricity Electricity
Efficiency
Actual Usage
Annual Utility Cost
0.7
1430 kilowatts
$
719,000
0.7 0.7
137 kilowatts 8.57 kilowatts
$ $
69,000 4,310
$
792,000
Add Materials Material Name
Classification
Price ($/kg)
Flowrate (kg/h)
Annual Cost
endClassification
endMaterial
Economic Options Cost of Land $
1,250,000
Taxation Rate
42%
Annual Interest Rate
10%
Salvage Value Working Capital $ FCIL $
0
custom 5,000,000
custom
10,000,000
custom
Total Module Factor
1.18
Grass Roots Factor
0.50
Economic Information Calculated From Given Information Revenue From Sales $ CRM (Raw Materials Costs) $ CUT (Cost of Utilities) $
75,000,000
custom
25,000,000
custom
10,000,000
CWT (Waste Treatment Costs) $ COL (Cost of Operating Labor) $
450,000
Factors Used in Calculation of Cost of Manufacturing (COM d) Comd = 0.18*FCIL + 2.76*COL + 1.23*(CUT + CWT + CRM) Multiplying factor for FCIL Multiplying factor for COL
0.18
Facotrs for CUT, CWT, and CRM
1.23
COMd $
2.76
46,092,000
Factors Used in Calculation of Working Capital Working Capital = A*CRM + B*FCIL + C*COL A
0.10
B
0.10
C
0.10
Project Life (Years after Startup)
10
Construction period
2
Distribution of Fixed Capital Investment (must sum to one) End of year One
60%
End of year Two
40%
End of year Three End of year Four End of year Five
custom material custom
$
-
$
-
$
-
$
-
$
-
P ro je c t V a lu e (m illio n s o f d o lla rs )
Cash Flow Diagram 200.00
150.00
100.00
50.00
0.00
(50.00) -1
0
1
2
3
4
5 6 7 Project Life (Years)
8
9
10
11
12
Generate CFD
Discounted Profitibility Criterion Net Present Value (millions)
75.68
Discounted Cash Flow Rate of Return
75.31%
Discounted Payback Period (years)
0.7
Non-Discounted Profitibility Criteria Cumulative Cash Position (millions) Rate of Return on Investment Payback Period (years)
161.87 161.87% 0.6
13
Year 0 0 1 2 2 3 4 5 6 7 8 9 10 11 12 12
Investment 0.00 1.25 6.00 4.00 5.00
dk
2.00 3.20 1.92 1.15 1.15 0.58
FCIL-Sdk
R
COMd
(R-COMd-dk)*(1-t)+dk
10.00 10.00 10.00 10.00 10.00 8.00 4.80 2.88 1.73 0.58 -
75.00 75.00 75.00 75.00 75.00 75.00 75.00 75.00 75.00 75.00
46.09 46.09 46.09 46.09 46.09 46.09 46.09 46.09 46.09 46.09
17.61 18.11 17.57 17.25 17.25 17.01 16.77 16.77 16.77 16.77
Cash Flow (Non-discounted) 0.00 (1.25) (6.00) (4.00) (5.00) 17.61 18.11 17.57 17.25 17.25 17.01 16.77 16.77 16.77 16.77 6.25
Cash Flow (discounted) 0.00 (1.25) (5.45) (3.31) (4.13) 13.23 12.37 10.91 9.74 8.85 7.94 7.11 6.46 5.88 5.34 1.99
Cumulative Cash Flow (discounted) 0.00 (1.25) (6.70) (10.01) (14.14) (0.91) 11.46 22.37 32.10 40.96 48.89 56.00 62.47 68.34 73.68 75.68
Cumulative Cash Flow (Non-discounted) 0.00 (1.25) (7.25) (11.25) (16.25) 1.36 19.47 37.04 54.29 71.54 88.55 105.32 122.08 138.85 155.62 161.87
Probable Variation of Key Parameters over Plant Life
FCIL Price of Product Working Capital Income Tax Rate* Interest Rate* Raw Material Price Salvage Value
Lower Limit -20% -10% -50% -20% -10% -10% -80%
Upper Limit 30% 10% 10% 20% 20% 15% 20%
Base Value 10,000,000 75,000,000 5,000,000 42% 10% $ 25,000,000 0 $ $ $
* Please note that variations for percentages are a percent of a percent. For example, a 10% variance on a 12% interst rate would imply a 1.2% uncertainty
Net Present Value Data Low NPV High NPV Bins 0 1 2 3 4 5 6 7 8 9 10
-172.9 186.4 Upper Value -172.9 -137.0 -101.0 -65.1 -29.2 6.7 42.7 78.6 114.5 150.5 186.4
# points/bin 0 5 22 74 156 232 235 156 99 19 2
Cumulative 0 5 27 101 257 489 724 880 979 998 1000
C u m u la t iv e N u m b e r o f D a t a P o in t s
Run Economic Analysis
1000
750
500
250
0 -200.0
-150.0
-100.0
-50.0
0.0
50.0
100.0
Net Present Value (millions of dollars)
150.0
200.0
250.0
C u m u la t iv e N u m b e r o f D a t a P o in t s
Discounted Cash Flow Rate of Return Data 0.00 0.27
Bins 0 1 2 3 4 5 6 7 8 9 10
Upper 0.00 0.03 0.05 0.08 0.11 0.13 0.16 0.19 0.21 0.24 0.27
#/bin 0 63 68 126 140 169 159 108 68 29 3
Cumulative 0 63 131 257 397 566 725 833 901 930 933
Discounted Payback Period Data Low DPBP High DPBP Bins 0 1 2 3 4 5 6 7 8 9 10
2.8 30.7 Upper 2.8 5.6 8.4 11.2 14.0 16.7 19.5 22.3 25.1 27.9 30.7
#/bin 0 263 321 163 82 56 35 24 0 6 6
Cumulative 0 263 584 747 829 885 920 944 944 950 956
1000
750
500
250
0 0.00
0.05
0.10
0.15
0.20
0.25
0.30
DCFROR
C u m u la t iv e N u m b e r o f D a t a P o in t s
Low DCFROR High DCFROR
1000
750
500
250
0 0.0
5.0
10.0
15.0
20.0
DPBP (years)
25.0
30.0
35.0
Bins 0 1 2 3 4 5 6 7 8 9 10
-213.33 533.67 Upper Value -213.33 -138.63 -63.93 10.77 85.47 160.17 234.87 309.57 384.27 458.97 533.67
# points/bin 0 4 20 54 124 195 228 173 118 69 15
Cumulativive 0 4 24 78 202 397 625 798 916 985 1000
Rate of Return on Investment Data Low ROROI High ROROI Bins 0 1 2 3 4 5 6 7 8 9 10
-14% 44% Upper Value -14% -8% -2% 4% 10% 15% 21% 27% 33% 39% 44%
# points/bin 0 5 37 100 193 228 210 130 65 27 5
Cumulative 0 5 42 142 335 563 773 903 968 995 1000
C u m u la t iv e N u m b e r o f D a t a P o in t s
Low CCP High CCP
1000
750
500
250
0 -300.00
-200.00
-100.00
0.00
100.00
200.00
300.00
400.00
500.00
600.00
Cumulative Cash Position (millions of dollars)
C u m u la t iv e N u m b e r o f D a t a P o in t s
Cumulative Cash Position Data
1000
750
500
250
0 -20%
-10%
0%
10%
20%
ROROI
30%
40%
50%
Low DPBP High DPBP Bins 0 1 2 3 4 5 6 7 8 9 10
1.9 10.1 Upper 1.9 2.7 3.6 4.4 5.2 6.0 6.9 7.7 8.5 9.3 10.1
#/bin 0 214 314 155 109 70 32 16 37 12 2
Cumulative 0 214 528 683 792 862 894 910 947 959 961
C u m u la t iv e N u m b e r o f D a t a P o in t s
Payback Period Data
1000
750
500
250
0 1.0
2.0
3.0
4.0
5.0
6.0
PBP (years)
7.0
8.0
9.0
10.0
11.0
Hours per Operting Year
Update Preferences
8322 Cost ($/GJ)
Common Utilities Electricity (110V - 440V) Cooling Water (30°C to 45°C) Refrigerated Water (15°C to 25°C)
16.8 0.354 4.43
Steam from Boilers Low Pressure (5 barg, 160°C) Medium Pressure (10 barg, 184°C) High Pressure (41 barg, 254°C)
13.28 14.19 17.7
Fuels Fuel Oil (no. 2) Natural Gas Coal (FOB mine mouth)
14.2 11.1 1.72
Thermal Systems Moderately High (up to 330°C) High (up to 400°C) Very High (up to 600°C)
12.33 13 13.88
Refrigeration Moderately Low (5°C) Low (-20°C) Very low (-50°C)
4.43 7.89 13.11
Power Preference kilowatts
1 kW / kW
Pressure Preference barg
1 barg / barg
Heat Duty Preference MJ/h
3.6 (MJ/h) / kW
Length Preference meters
1 m/m
Area Preference square meters
1 m^2 / m^2
Volume Preference cubic meters
1 m^3/m^3
Gas Flow Preference cubic meters/s
1 m^3 / m^3
Cost Preference $/kg
1 kg / kg
Flowrate Preference kg/h
1 kg / kg
Energy Price Preference $/Gigajoule
1 GJ / GJ
Cost ($/tonne) Waste Disposal (solid and liquid) Non-Hazardous Hazardous
36 200
Cost of Steam used in Steam Drives Steam used for steam-powered drives $
Cost ($/GJ) 9.83
Equipment Effeciencies Pump Efficiency Drive Efficiency Fan Efficiency Furnace Efficiency Turbine Efficiency
70% 90% 70% 90% 65%
Process Equipment Operators per shift per equipment Cost of Labor (per operator/year) $
52,900
Miscellaneous Numebrs Solids Handling Coefficient
1.00
Blender Data Blender Type Kneader Ribbon Rotary
K1
K2
K3
Vmin(m3)
Vmax(m3)
5.0141 4.1366 4.1366
-0.4133 -0.4928 -0.4928
0.3224 0.0070 0.0070
0.14 0.70 0.70
3 11 11
FBM 1.5 1.5 1.5
Centrifuge Data K1
K2
K3
Dmin(m)
Dmax(m)
4.7681 4.3612 4.8600 4.9697
-0.0260 -0.1236 -0.6660 0.1689
0.0240 -0.0049 0.1063 0.0038
0.50 0.50 0.50 0.30
1.70 1.00 1.10 2.00
Compressor Data (without electric motors) K1 K2 Compressor Type Centrifugal 2.2891 1.3604 Axial 2.2891 1.3604 Rotary 5.0355 -1.8002 Reciprocating 2.2891 1.3604
K3 -0.1027 -0.1027 0.8253 -0.1027
FBMCS 2.7 3.8 2.4 3.4
FBMSS 5.8 8.0 5.0 7.0
FBMNi 11.5 15.9 9.9 13.9
K3 0.1506 0.1550 0.0638 0.1982
Amin(m2) 1.00 0.50 0.75 0.50
Amax(m2) 15.00 325.00 65.00 30.00
FBM
FBM
Centrifuge Type Auto Batch Seperator Centrifugal Seperator Oscillating Screen Solid Bowl w/o Motor
FBM 1.5 1.5 1.5 1.5
Wmin(kW) 450 450 18 450
Wmax(kW) 3000 3000 950 3000
FBMNi 11.5 11.5 11.5 11.5
Threshold 0.01 0.01 0.04 0.04
C1 0.00 0.00 0.00 0.00
Conveyor Data Conveyor Type Apron Belt Pneumatic Screw
K1 3.9255 4.0637 4.6616 3.6062
K2 -0.4961 -0.7416 -0.6795 -0.7341
2 2 2 2
Crystallizer Data Crystallizer Type Batch
K1
K2
K3
Vmin(m3)
Vmax(m3)
4.5097
-0.8269
0.1344
1.50
30.00
1.5
Drive Data Electric Drives Explosion Proof Totally Enclosed Open/Drip Proof Non-Electric Drives Gas Turbine Steam Turbine Internal Combustion
K1
K2
K3
FBM
Wmin(kW)
Wmax(kW)
2.4604 1.956 2.9508
1.4191 1.7142 1.0688
-0.1798 -0.2282 -0.1315
1.5 1.5 1.5
75 75 75
2600 2600 2600
K1 -21.7702 2.6259 2.7635
K2 13.2175 1.4398 0.8574
K3 -1.5279 -0.1776 -0.0098
FBM 3.5 3.5 2.0
Wmin(kW) 7500 70 10
Wmax(kW) 23000 7500 10000
K1 4.5472 3.5645 3.6951
K2 -0.7269 0.1118 -0.4558
K3 0.1340 -0.0777 -0.1248
Amin(m2) 0.50 5.00 1.80
Amax(m2) 50.00 100.00 20.00
FBM
Dryer Data Dryer Type Drum Rotary, Gas Fired Tray
1.5 1.5 1.5
Dust Collectors Data Collector Type Baghouse Cyclone Scrubbers ( Centrifugal, Gravity Spray, Impingement, and Wet Dynamic) Electrostatic Precipitator Venturi
K1
K2
K3
4.5007 3.6298 4.1520
-0.5818 -0.4991 -0.5299
0.0813 0.0411 0.0171
0.08 0.06 0.10
350.00 200.00 50.00
1.5 1.5
3.6298 3.6298
-0.4991 -0.4991
0.0411 0.0411
0.06 0.06
200.00 200.00
1.5 1.5
K2 -0.3533 -0.0734 -0.3375 -0.1373
K3 0.4477 0.3090 0.4722 0.3414
FBMCS 2.7 2.7 2.7 2.7
FBMfiberglass 5.0 5.0 5.0 5.0
FBMSS 5.8 5.8 5.8 5.8
FBM
Fan Data (include electric motors) K1 Fan Type Centrifugal Radial Fan 3.5391 Centrifugal Backward curv 3.3471 Axial Tube Fan 3.0414 Axial Vane Fan 3.1761
Vmin(m3/s) Vmax(m3/s)
FBM
C2 0.209 0.209 0.209 0.209
C3 -0.033 -0.033 -0.033 -0.033
Vmin(m3/s) 1 1 1 1
Vmax(m3/s) 100 100 100 100
Filter Data K1
K2
K3
Amin(m2)
Amax(m2)
5.1055 3.2107 4.8123 4.2756 3.8187 4.8123 4.2756 5.1055 5.1055
-0.5001 -0.2403 -0.7142 -0.6480 -0.3765 -0.7142 -0.6480 -0.5001 -0.5001
0.0001 0.0027 0.0420 0.0714 0.0176 0.0420 0.0714 0.0001 0.0001
0.90 15.00 0.90 0.50 0.60 0.90 0.50 0.90 0.90
115.00 200.00 300.00 80.00 235.00 300.00 80.00 115.00 115.00
Reactive Heaters Reformer Furnace Pyrolysis Furnace
K1 3.068 2.3859
K2 0.6597 0.9721
K3 0.0194 -0.0206
Qmin(kW) 3000 3000
Qmax(kW) Pmax(barg) 100000 200 100000 200
C1 0.1405 0.1017
C2 -0.2698 -0.1957
C3 0.1293 0.09403
Non-reactive Heaters Process Heater
K1 7.3488
K2 -1.1666
K3 0.2028
Qmin(kW) 1000
Qmax(kW) Pmax(barg) 100000 200
C1 0.1347
C2 -0.2368
C3 0.1021
CS 2.13
Thermal Fluid Heaters Hot Water Molten Salt, Mineral Oil, Diphenyl Based Oils
K1
K2
K3
Qmin(kW)
Qmax(kW) Pmax(barg)
C1
C2
C3
2.0829 1.1979 2.2628
0.9074 1.4782 0.8581
-0.0243 -0.0958 0.0003
650 650 650
-0.0163 -0.0163 -0.0163
0.0569 0.0569 0.0569
-0.0088 -0.0088 -0.0088
Fbm 2.17 2.17 2.17
Filter Type Bent Cartridge Disc and Drum Gravity Leaf Pan Plate and Frame Table Tube
1.5 1.5 1.5 1.5 1.5 1.5 1.5 1.5 1.5
Fired Heater Data Bare Module Factor CS 2.13 2.13
Alloy Steel 2.51 2.51
SS 2.81 2.81
Bare Module Factor
10750 10750 10750
200 200 200
Alloy Steel 2.51
SS 2.81
Steam Supreheat Factor FT1 FT2
FT3
Pmax(barg) 0.16 0.16 0.16 0.16
Packaged Steam Boilers
6.9617
-1.48
0.3161
1200
9400
40
2.5941
-4.2348
1.7224
K1 5.0238 3.9119 5 5.2366 4.642
K2 0.3475 0.8627 0.149 -0.6572 0.3698
K3 0.0703 -0.0088 -0.0134 0.35 0.0025
Amin(m2) 5 50 0.5 10 100
Amax(m2) 1000 500 5 100 10000
Pmax(barg) 150 150 150 150 150
C1 0.1578 0.1578 0.1578 0.1578 0.1578
C2 -0.2992 -0.2992 -0.2992 -0.2992 -0.2992
C3 0.1413 0.1413 0.1413 0.1413 0.1413
2.2
1.000
Evaporator Data Evaporator Types Forced Circulation Falling Film Agitated (Scraped Wall) Short Tube Long Tube
Heat Exchanger Data Exchager Type Double Pipe 40 barg < P < 100 barg P < 40 barg Multiple Pipe 40 barg < P < 100 barg P < 40 barg Fixed tube, sheet, or U tu tubes only > 5 barg Floating Head tubes only > 5barg Bayonet tubes only > 5 barg Kettle Reboiler tubes only > 5 barg Scraped Wall 40 barg < P < 100 barg P < 40 barg Teflon Tube Air Cooler Spiral Tube - shell and tub tube only Spiral Plate Flat Plate
K1
K2
K3
C1
C2
C3
B1
B2
Amin(m2)
Amax(m2)
Pmax(barg)
3.3444
0.2745
-0.0472
1
10
300
0.0783
1.74
1.55
10
100
300
4.3247
-0.303
0.1634
1.63
1.66
10.0
1000
140
4.8306
-0.8509
0.3187
1.63
1.66
10.0
1000
140
4.2768
-0.0495
0.1431
1.63
1.66
10.0
1000
140
4.4646
-0.5277
0.3955
1.63
1.66
10.0
100
140
3.7803
0.8569
0.0349
1.74
1.55
2.0
20
300
3.8062 4.0336 3.9912
0.8924 0.2341 0.0668
-0.1671 0.0497 0.243
1.63 0.96 1.74
1.66 1.21 1.55
1.0 10 1
10 10000 100
15 100 400
4.6561 4.6656
-0.2947 -0.1557
0.2207 0.1547
3.0705 0.3327 0 3.0705 0.3327 0 0.08183 0.0123 0.08183 0.0123 0.08183 0.0123 0.08183 0.0123 3.0705 0.3327 0 0 -0.02861 0 0 0 0
1.55
0.7282
-12.6574 -0.912 0 -12.6574 -0.912 0 -0.11272 -0.00627 -0.11272 -0.00627 -0.11272 -0.00627 -0.11272 -0.00627 -12.6574 -0.912 0 0 0.15361 0.1859 0.09717 0 0
1.74
2.7652
13.1467 0.6072 0 13.1467 0.6072 0 0.03881 -0.00164 0.03881 -0.00164 0.03881 -0.00164 0.03881 -0.00164 13.1467 0.6072 0 0 -0.125 -0.4045 -0.2115 0 0
0.96 0.96
1.21 1.21
1 10
100 1000
19 19
0.00184
3.35E-06
Materail Factors, FM Shell - CS Exchanger Type Tube - CS Double Pipe 1.00 Multiple Pipe 1.00 Fixed tube, sheet, or U tu 1.00 Floating Head 1.00 Bayonet 1.00 Kettle Reboiler 1.00 Scraped Wall 1.00 Spiral Tube 1.00
CS Cu 1.35 1.35 1.35 1.35 1.35 1.35 1.35 1.35
Cu Cu 1.69 1.69 1.69 1.69 1.69 1.69 1.69 1.69
CS SS 1.81 1.81 1.81 1.81 1.81 1.81 1.81 1.81
SS SS 2.73 2.73 2.73 2.73 2.73 2.73 2.73 2.73
Exchanger Type Teflon Tube Exchanger
Shell Materail CS Cu 1.00 1.20
SS 1.30
Ni 1.40
Ti 3.30
Exchanger Type Spiral Plate Flat Plate
Material In Contact with Process Fluid CS Cu SS Ni 1.00 1.35 2.45 2.68 1.00 1.35 2.45 2.68
Ti 4.63 4.63
Exchanger Type Air Cooler
Tube Material CS Al 1.00 1.42
CS Ni 2.68 2.68 2.68 2.68 2.68 2.68 2.68 2.68
Ni Ni 3.73 3.73 3.73 3.73 3.73 3.73 3.73 3.73
CS Ti 4.63 4.63 4.63 4.63 4.63 4.63 4.63 4.63
Ti Ti 11.38 11.38 11.38 11.38 11.38 11.38 11.38 11.38
B1 1.89 1.89 1.89
B2 1.35 1.35 1.35
FmCI 1.0 1.0 1.0
FmCS 1.6 1.4 1.5
FmCu NA 1.3 1.3
Wmin(kW) 100 100
Wmax(kW) 4000 1500
SS 2.93
Mixer Data K2 -0.2991 -0.9641 -0.5104
K3 -0.0003 0.1346 0.0030
Pump Data (including electric drives) K1 K2 Pump Type Centrifugal pump 3.3892 0.0536 Positive Displacement 3.4771 0.1350 Reciprocating pump 3.8696 0.3161
K3 0.1538 0.14380 0.12200
Mixer Type Impeller Propeller Turbine
K1 3.8511 4.3207 3.4092
Pmin(kW) 5.00 5.00 5.00
Pmax(kW) 150.00 500.00 150.00
C1 C2 -0.3935 0.3957 -0.245382 0.259016 -0.2454 0.2590
FBM 1.5 1.5 1.5
C3 -0.00226 -0.01363 -0.0136
Reactor Data K1 4.5587 4.1052 3.7957 4.1052 3.3496 4.7116
K2 -0.7014 -0.4680 -0.5407 -0.4680 -0.2765 -0.5521
K3 0.0020 -0.0005 0.0160 -0.0005 0.0025 0.0004
Vmin(m3) 1.00 0.10 0.07 0.10 5.00 0.04
Vmax(m3) 15.00 35.00 1.00 35.00 45.00 6.00
FBM
K1 3.8050 4.0485 3.8219 4.0485
K2 -0.4144 -0.8882 0.0368 -0.8882
K3 0.2120 0.3260 -0.6050 0.3260
Amin(m2) 0.30 0.30 2.00 0.30
Amax(m2) 6.00 15.00 11.00 15.00
FBM
K1 4.8509 5.9567
K2 -0.3973 -0.7585
K3 0.1445 0.1749
B1 1.10 1.10
B2 0 0.00
Vmin(m3/s) 90 1000
Vmax(m3/s) 30000 40000
Axial Radial
K1 2.7051 2.2476
K2 1.4398 1.4965
K3 -0.1776 -0.1618
FBMCI NA NA
FBMCS 3.5 3.5
FBMCu NA NA
FBMSS 6.1 6.1
FBMNi 11.7 11.7
FBMTi NA NA
Vaporizer Types Jacketed Vessel Internal Coil Jacketed Vessel w/ Coil
K1 3.8751 4.038 4.038
K2 0.3328 0.09142 0.09142
K3 0.1901 0.2766 0.2766
Vmin(m3) 1 1 1
Vmax(m3) 100 100 100
Pmax(barg) 320 320 320
C1 0.1578 0.1578 0.1578
C2 -0.2992 -0.2992 -0.2992
C3 0.1413 0.1413 0.1413
Evaporator Types Forced Circulation Falling Film Agitated (Scraped Wall) Short Tube Long Tube
CS 2.9 2.25 2.25 2.9 2.9
Bare Module Factors, FBM Cu Alloy SS Ni Alloy 3.63 5.08 9.66 2.81 3.94 7.49 2.81 3.94 7.49 3.63 5.08 9.66 3.63 5.08 9.66
Ti 14.5 11.25 11.25 14.5 14.5
Vaporizer Types Jacketed Vessel Internal Coil Jacketed Vessel w/ Coil
CS 2.7 3.0 3.0
SS Clad 3.8 4.1 4.1
Ni Alloy Ni Alloy Clad 9.1 5.9 10.1 6.6 10.1 6.6
Ti 13.7 15.2 15.2
Ti Clad 9.5 10.6 10.6
K3 0.0905
Vmax 628
Pmax(barg) 400
Sieve 1.0 1.8
Valve 1 1.83
Demister
5.6
5.58
5.6
Reactor Type Autoclave Fermenter Inoculum Tank Jacketed Agitated Jacketed Non-Agitated Mixer/Settler
1.5 1.5 1.5 1.5 1.5 1.5
Screen Data Screen Type DSM Rotary Stationary Vibrating
1.5 1.5 1.5 1.5
Tank Data Tank Type Fixed Roof Floating Roof
Turbine Data Turbine Type
Bare Module Factors, FBM Cu 3.4 3.8 3.8
GL SS Coils Glass Lined Ni CoilsSS 4.7 4.9 4.8 5.2 5.5 5.2 5.2 5.5 5.2
Vessel Data (including data for distillation towers and packed columns) Vertical Vessels Horizontal Vessels K1 K2 K3 Vmin Vmax K1 K2 3.4974 0.4485 0.1074 0.3 520 3.5565 0.3776 Vessel B-Values Vessel Type Horizontal Vertical
B1 1.49 2.25
B2 1.52 1.82
K1
K2
FBM MOC CS SS Fluorocarbon
Fq
Ni-alloy Tray Type
K3
Amin(m2)
Amax(m2)
Vmin 0.1
1.0 1.8
FmSS 2.3 2.7 2.4
FmNi 4.4 4.7 4.0
FmTi NA 10.7 6.4
Pmax(barg) 100 100 100
Wmin(kW) 1 1 0.1
Wmax(kW) 300 100 200
Sieve
2.9949
0.4465
0.3961
0.07
12.3
Valve
3.3322
0.4838
0.3434
0.7
10.5
Materials of Construction FM CS 1.0
Demister
3.2353
0.4838
0.3434
0.7
10.5
FM SS clad
1.7
FM SS
3.1
FM Ni clad
3.6
FM Ni
7.1 4.7 9.4
Tower Packing Materials of Construction
K1
K2
K3
Vmin(m3)
Vmax(m3)
Ceramic
3.0664
0.9744
0.0055
0.03
628
FM Ti clad
304 SS Plastic Saddle
3.2999 2.4493
0.9744 0.9744
0.0055 0.0055
0.03 0.03
628 628
FM Ti
