Summary

Total Capital Cost [USD] 4625320

Total Operating Cost [USD/Year] 2834820
Total Raw Materials Cost [USD/Year] 0
Total Product Sales [USD/Year] 0
Total Utilities Cost [USD/Year] 1442080
Desired Rate of Return [Percent/'Year] 20
P.O.Period [Year] 0
Equipment Cost [USD] 779600
Total Installed Cost [USD] 1056600
 Utilities
Name Fluid Rate Rate Units Cost per Hour Cost Units
Electricity
Cooling Water Water 0.115057 MMGAL/H 13.80684 USD/H
Steam @165PSI Steam 14.57922 KLB/H 142.293187 USD/H
 Unit operation
Name Equipment Cost [USD] Installed Cost [USD]
E-101 16100 143200
E-100 29700 149300
RCY-1 0 0
P-100 17500 50000
MIX-100 0 0
E-102 9100 69900
CRV-100 779600 1056600
T-101 98000 383400
T-100 151700 621500
VLV-100 0 0
P-101 16300 43600
 Unit operation
Equipment Weight [LBS] Installed Weight [LBS] Utility Cost [USD/HR]
2600 13972 26.31888
6300 34384 0
0 0 0
1300 4574 0.57815
0 0 0
500 7909 1.23948
96700 127578 0
16340 52438 259.111899
28170 89441 182.121055
0 0 0
990 3466 0.0868
 Equip
Name Equipment Cost [USD]
E-101 16100
E-100 29700
RCY-1 0
P-100 17500
MIX-100 0
E-102 9100
CRV-100 779600
VLV-100 0
P-101 16300
Condenser_@T-101-reflux pump 4900
Condenser_@T-101-overhead split 0
Main Tower_@T-101 55700
Reboiler_@T-101-bottoms split 0
Reboiler_@T-101-reb 37400
Reboiler_@T-100-bottoms split 0
Reboiler_@T-100-reb 34000
Main Tower_@T-100 66700
Condenser_@T-100-cond 26000
Condenser_@T-100-cond acc 18400
Condenser_@T-100-overhead split 0
Condenser_@T-100-reflux pump 6600
 Equipment
Installed Cost [USD] Equipment Weight [LBS] Total Installed Weight [LBS] Sizing Errors
143200 2600 13972
149300 6300 34384
0 0 0
50000 1300 4574
0 0 0
69900 500 7909
1056600 96700 127578
0 0 0
43600 990 3466
34500 240 3225
0 0 0
219100 8400 27892
0 0 0
129800 7700 21321
0 0 0
119400 6800 18510
241300 11500 33032
121200 5500 22481
96200 3900 10750
0 0 0
43400 470 4668
Evaluation Errors
User tag number E-101
Remarks 1 Equipment mapped from 'E-101'.
Quoted cost per item [USD]
Currency unit for matl cost
Number of identical items 1
Installation option
Heat transfer area [m2] 30.634989517917
Number of shells
Front end TEMA symbol B
Shell TEMA symbol E
Rear end TEMA symbol M
Heat exchanger design option
Tube material
Tube design gauge pressure [kPag] 993.58774417
Tube design temperature [C] 390.352121666667
Tube operating temperature [C] 35
Tube outside diameter [m] 0.0254
Shell material
Shell design gauge pressure [kPag] 1541.04608315
Shell design temperature [C] 390.352121666667
Shell operating temperature [C] 362.574343888889
Tube side pipe material
Shell side pipe material
Number of tubes per shell
Tube length extended [m] 6.096
Tube gauge
Tube pitch [m] 0.03175
Shell diameter [m]
Shell wall thickness [m]
Shell corrosion allowance [m]
Expansion joint
Tube sheet material
Number of tube passes 1
Number of shell passes 1
Allow resize
 TEMA HEX
E-100 E-102
Equipment mapped from 'E-100'. Equipment mapped from 'E-102'.

1 1

97.3914089414526 1.9418359299678

B B
E E
M M

1621.0460791 573.587748195
343.333333333333 184.273645555556
250 35
0.0254 0.0254

1046.9210794 911.046078845
343.333333333333 184.273645555556
315.555555555556 156.495867777778

6.096 6.096

0.03175 0.03175

1 1
1 1
Condenser_@T-100-cond
Equipment mapped from 'Condenser_@T-100'.

90.6289908942006

B
E
M

700.254414195
121.111111111111
35
0.0254

1101.046077845
121.111111111111
47.3707611111111

6.096

0.03175

1
1
User tag number RCY-1
Remarks 1 Equipment mapped from 'RCY-1'.
Code of account 100
Icarus/User COA option
Material cost per unit 0
Currency unit for matl cost
Labor hours per unit [seconds]
Number of identical items
Installation option
Unit of measure
Quantity
Quantity adjustment option
Item classification
Item type
Material
Component weight [kg]
ID in bulk report
Allow resize
 Quoted equipme
MIX-100 VLV-100
Equipment mapped from 'MIX-100'. Equipment mapped from 'VLV-100'.
100 100

0 0
 Quoted equipment
Condenser_@T-101-overhead split Reboiler_@T-101-bottoms split
Equipment mapped from 'Condenser_@T-101'. Equipment mapped from 'Reboiler_@T-101'.
100 100

0 0
Reboiler_@T-100-bottoms split Condenser_@T-100-overhead split
Equipment mapped from 'Reboiler_@T-100'. Equipment mapped from 'Condenser_@T-100'.
100 100

0 0
User tag number P-100
Remarks 1 Equipment mapped from 'P-100'.
Quoted cost per item [USD]
Currency unit for matl cost
Number of identical items
Installation option
Casing material
Liquid flow rate [m3/h] 11.8297208234189
Fluid head [m] 188.8965221808
Speed [rpm]
Fluid specific gravity 0.783857
Driver power [kW]
Driver type
Seal type
Design gauge pressure [kPag] 1621.0460791
Design temperature [C] 121.111111111111
Fluid viscosity [cP] 0.534
Pump efficiency [%] 75
Allow resize
 Centrif pump
P-101 Condenser_@T-101-reflux pump
Equipment mapped from 'P-101'. Equipment mapped from 'Condenser_@T-101'.

2.93212239697839 2.343
124.5816211944 74.5444873344

0.672129 1

1621.0460791 801.04608269
154.115861666667 153.816395
0.172
75 70
Condenser_@T-100-reflux pump
Equipment mapped from 'Condenser_@T-100'.

34.1436587365741

0.572026

1101.046077845
121.111111111111
0.5
70
 Agitated reactor
User tag number
Remarks 1
Quoted cost per item [USD]
Currency unit for matl cost
Number of identical items
Installation option
Application
Shell material
Liquid volume [m3]
Vessel diameter [m]
Vessel tangent to tangent height [m]
Design gauge pressure [kPag]
Vacuum design gauge pressure [kPag]
Design temperature [C]
Operating temperature [C]
Jacket design gauge pressure [kPag]
Jacket type
Jacket material
Agitator power [kW]
Driver type
Cladding material
Skirt or leg height [m]
Base material thickness [m]
Corrosion allowance [m]
Cladding thickness [m]
Fluid depth [m]
Fluid density [kg/m3]
Fluid viscosity [cP]
Impeller type
Impeller diameter [m]
Number of impellers
Impeller speed [rpm]
Reynolds number
Power function
Allow resize
Agitated reactor
CRV-100
Equipment mapped from 'CRV-100'.

CONT
SS316

0.0299999908
 Multi-diameter tower
User tag number
Remarks 1
Quoted cost per item [USD]
Currency unit for matl cost
Number of identical items
Installation option
Application
Base material Bottom
Diameter Bottom section [m]
Bottom tangent to tangent height [m]
Design gauge pressure Bottom [kPag]
Design temperature Bottom [C]
Operating temperature Bottom [C]
Number of trays Bottom section
Bottom Tray type
Bottom Tray material
Bottom Tray spacing [m]
Bottom Packing material Section1
Packing height Bottom Section1 [m]
Bottom Packing material Section2
Packing height Bottom Section2 [m]
Cladding material Bottom
Cladding thickness Bottom [m]
Thickness Bottom section [m]
Corrosion allowance Bottom [m]
Base material Middle
Diameter Middle section [m]
Middle tangent to tangent height [m]
Design gauge pressure Middle [kPag]
Design temperature Middle [C]
Operating temperature Middle [C]
Number of trays Middle section
Middle Tray type
Middle Tray material
Middle Tray spacing [m]
Middle Packing material Section1
Packing height Middle Section1 [m]
Middle Packing material Section2
Packing height Middle Section2 [m]
Cladding material Middle
Cladding thickness Middle [m]
Thickness Middle section [m]
Corrosion allowance Middle [m]
Base material Top
Diameter Top section [m]
Top tangent to tangent height [m]
Design gauge pressure Top [kPag]
Design temperature Top [C]
Operating temperature Top [C]
Number of trays Top section
Top Tray type
Top Tray material
Top Tray spacing [m]
Top Packing material Section1
Packing height Top Section1 [m]
Top Packing material Section2
Packing height Top Section2 [m]
Cladding material Top
Cladding thickness Top [m]
Thickness Top section [m]
Corrosion allowance Top [m]
Skirt height [m]
Wind or seismic design
Fluid volume [%]
Vacuum design gauge pressure [kPag]
Transition height 1 [m]
Transition height 2 [m]
Molecular Wt Overhead Prod.
ASME design basis
Allow Resize
 Multi-diameter tower
Main Tower_@T-101
Equipment mapped from 'Main Tower_@T-101'.

0.9144
9.7536
831.046082895
191.447428888889
163.669651111111
10
SIEVE

0.6096
31.466809
Main Tower_@T-100
Equipment mapped from 'Main Tower_@T-100'.

1.0668
9.7536
1121.04608028
188.681227777778
160.90345
10
SIEVE

0.6096
45.986755
 U-tube reboiler
User tag number
Remarks 1
Quoted cost per item [USD]
Currency unit for matl cost
Number of identical items
Installation option
Heat transfer area [m2]
Number of shells
Heat exchanger design option
Tube material
Tube design gauge pressure [kPag]
Tube design temperature [C]
Tube operating temperature [C]
Tube outside diameter [m]
Shell material
Shell design gauge pressure [kPag]
Shell design temperature [C]
Shell operating temperature [C]
Tube side pipe material
Shell side pipe material
Number of tubes per shell
Tube length extended [m]
Tube gauge
Tube pitch [m]
Tube pitch symbol
Shell diameter [m]
Tube port diameter [m]
Shell wall thickness [m]
Shell corrosion allowance [m]
Tube sheet material
Number of tube passes
Duty [kJ/h]
Vaporization [%]
Specific gravity tower bottoms
Molecular weight Bottoms
Heat of vaporization [kJ/kgmole]
TEMA type
Allow resize
 U-tube reboiler
Reboiler_@T-101-reb Reboiler_@T-100-reb
Equipment mapped from 'Reboiler_@T-101'. Equipment mapped from 'Reboiler_@T-100'.

1 1

103.643339156703 90.5818772574756

1208.72108 1208.72108
212 212
184.222222222222 184.222222222222
0.0254 0.0254

831.046082895 1121.04608028
193.264700555556 193.253996666667
165.486922777778 165.476218888889

6.096 6.096

0.03175 0.03175
TRIANGULAR TRIANGULAR

2 2
8011785.0852 5190363.8532

BKU BKU
 Horizontal drum
User tag number
Remarks 1
Quoted cost per item [USD]
Currency unit for matl cost
Number of identical items
Installation option
Application
Shell material
Liquid volume [m3]
Vessel diameter [m]
Vessel tangent to tangent length [m]
Design gauge pressure [kPag]
Vacuum design gauge pressure [kPag]
Design temperature [C]
Operating temperature [C]
Cladding material
Diameter of drip leg [m]
Length of drip leg [m]
Base material thickness [m]
Corrosion allowance [m]
Cladding thickness [m]
Head type
Allow resize
Horizontal drum
Condenser_@T-100-cond acc
Equipment mapped from 'Condenser_@T-100'.

4.09218203997073
1.2192
3.5052
1101.046077845

121.111111111111
45.7936977777781