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Equipment CategoryBare Module Cost (EquipmentDirect and Indirect Cost:CEPCI=382)
Process Vessels $0Trays $0Heat Exchangers $0Pump with Electric Driver $0Compressor $0Compressor Driver $0Furnace $0
Total Bare Module Cost $0Plant Construction CostIncluding 18% contingency
$0
Chemical Engineering PlantCost Index (CEPCI) in 2009
521.90
Plant Construction Cost in2009
$0
7/30/2019 Plant Cost Estimate
2/29
No Item Number Type Diameter[m]MinimumLength[m]
MaximumLength[m]
VesselLength[m]
Cp: Purchase CostAssuming AmbientOperating Pressureand Carbon SteelConstruction. [$]
0 Example Vertical 1 2.5 30 20 $46,9411 0.3 0 0 1 $12 0.3 0 0 1 $13 0.3 0 0 1 $14 0.3 0 0 1 $15 0.3 0 0 1 $16 0.3 0 0 1 $17 0.3 0 0 1 $18 0.3 0 0 1 $19 0.3 0 0 1 $1
10 0.3 0 0 1 $111 0.3 0 0 1 $112 0.3 0 0 1 $113 0.3 0 0 1 $114 0.3 0 0 1 $115 0.3 0 0 1 $116 0.3 0 0 1 $117 0.3 0 0 1 $118 0.3 0 0 1 $119 0.3 0 0 1 $1
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OperatingPressure[barg]
FP:PressureFactor
MaterialFM:MaterialFactor
Bare ModuleCost [$]
10 1.5209 CS 1 $240,1471 1 CS 1 $01 1 CS 1 $01 1 CS 1 $01 1 CS 1 $01 1 CS 1 $01 1 CS 1 $01 1 CS 1 $01 1 CS 1 $01 1 CS 1 $01 1 CS 1 $01 1 CS 1 $01 1 CS 1 $01 1 CS 1 $01 1 CS 1 $01 1 CS 1 $01 1 CS 1 $01 1 CS 1 $01 1 CS 1 $01 1 CS 1 $0
$0
7/30/2019 Plant Cost Estimate
4/29
No. Tower Item Number Dia. [m]
Cp: Purchase CostAssuming CarbonSteel Construction.[$/Tray]
Number of Trays Case 1
7/30/2019 Plant Cost Estimate
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Case 10
7/30/2019 Plant Cost Estimate
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SS case NI Alloy caseFM:MaterialFactor
Bare ModuleCost [$]
0 1 5.5 $101,179
0 0 0 $00 0 0 $00 0 0 $00 0 0 $00 0 0 $00 0 0 $00 0 0 $00 0 0 $00 0 0 $0
$0
7/30/2019 Plant Cost Estimate
7/29
No Item Number
HeatTransferArea
(m2)
Heat ExchangerType
Cp: Purchase CostAssuming AmbientOperating Pressure andCarbon SteelConstruction. [$]
ShellOperatingPressure
[bar(g)]
0 Example 170 Floating Head $19,629 61 1 $0 12 1 $0 13 1 $0 14 1 $0 15 1 $0 16 1 $0 17 1 $0 18 1 $0 19 1 $0 1
10 1 $0 111 1 $0 112 1 $0 113 1 $0 114 1 $0 115 1 $0 116 1 $0 117 1 $0 118 1 $0 119 1 $0 120 1 $0 121 1 $0 1
22 1 $0 123 1 $0 124 1 $0 125 1 $0 126 1 $0 127 1 $0 128 1 $0 129 1 $0 130 1 $0 131 1 $0 132 1 $0 133 1 $0 134 1 $0 135 1 $0 136 1 $0 137 1 $0 138 1 $0 139 1 $0 140 1 $0 141 1 $0 142 1 $0 1
7/30/2019 Plant Cost Estimate
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43 1 $0 144 1 $0 145 1 $0 146 1 $0 147 1 $0 148 1 $0 1
49 1 $0 1
7/30/2019 Plant Cost Estimate
9/29
TubeOperatingPressure
[bar(g)]
Fp: PressureFactor
ShellMaterial
TubeMaterial
FM:MaterialFactor
Bare ModuleCost [$]
6 1 CS CS 1 $64,7751 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $0
1 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $0
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1 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $01 1 CS CS 1 $0
1 1 CS CS 1 $0$0
7/30/2019 Plant Cost Estimate
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No. Item Number Pump TypeShaftPower[KW]
Numberof Pumps
Cp: Purchase CostAssuming 10[barg]Suction Pressureand Cast Iron. [$]
SuctionPressure[barg]
0 Example Centrifugal 5 2 $13,137 15
1 5 0 $0 12 5 0 $0 13 5 0 $0 14 5 0 $0 15 5 0 $0 16 5 0 $0 17 5 0 $0 18 5 0 $0 19 5 0 $0 1
10 5 0 $0 111 5 0 $0 112 5 0 $0 113 5 0 $0 114 5 0 $0 115 5 0 $0 116 5 0 $0 117 5 0 $0 118 5 0 $0 119 5 0 $0 1
7/30/2019 Plant Cost Estimate
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FP:PressureFactor
MaterialFM:MaterialFactor
BareModuleCost [$]
1.245906 CastIron 1 $48,360
0 0 $00 0 $00 0 $00 0 $00 0 $00 0 $00 0 $00 0 $00 0 $00 0 $00 0 $00 0 $00 0 $00 0 $00 0 $00 0 $00 0 $00 0 $00 0 $0
$0
7/30/2019 Plant Cost Estimate
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Centrifugal CSReciprocating SS
Ni_alloy
No. Item Number Compressor Type Wfmin Wfmax Material CS SS
0 Example Centrifugal 50 8000 CS 1 01 0 0 0 02 0 0 0 03 0 0 0 04 0 0 0 05 0 0 0 06 0 0 0 07 0 0 0 08 0 0 0 09 0 0 0 0
10 0 0 0 011 0 0 0 012 0 0 0 013 0 0 0 014 0 0 0 015 0 0 0 016 0 0 0 017 0 0 0 018 0 0 0 0
19 0 0 0 0
7/30/2019 Plant Cost Estimate
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F_BMFluidPower[kW]
PurchaseBaseCost [$]
Bare ModuleCost [$]
0 2.5 1000 $719,615 $1,799,0370 0 1 $1 $00 0 1 $1 $00 0 1 $1 $00 0 1 $1 $00 0 1 $1 $00 0 1 $1 $00 0 1 $1 $00 0 1 $1 $00 0 1 $1 $00 0 1 $1 $00 0 1 $1 $00 0 1 $1 $00 0 1 $1 $00 0 1 $1 $00 0 1 $1 $00 0 1 $1 $00 0 1 $1 $00 0 1 $1 $0
0 0 1 $1 $0$0
7/30/2019 Plant Cost Estimate
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No Item Number TypeWs Min[kW]
Ws Max[kW]
ShaftPower[kW]
PurchaseBaseCost [$]
BareModuleCosr [$]
0 Example Electric 3 6000 1000 $46,806 $70,2091 1 $1 $0
2 1 $1 $03 1 $1 $04 1 $1 $05 1 $1 $06 1 $1 $07 1 $1 $08 1 $1 $09 1 $1 $0
10 1 $1 $011 1 $1 $012 1 $1 $013 1 $1 $014 1 $1 $015 1 $1 $016 1 $1 $017 1 $1 $018 1 $1 $019 1 $1 $0
$0
7/30/2019 Plant Cost Estimate
16/29
Reactive ProcessHeater (ReformerFurnace)
10
Reactive ProcessHeater (PyrolysisFurnace)
50
Non-ReactiveProcess Heater
100
200
No Item Number TypeQ Min[kW]
Q Max[kW]
HeatDuty [kW]
PurchaseBaseCost [$]
Order ofPressure[barg]
0 ExampleReactive ProcessHeater (ReformerFurnace)
3000 150000 10000 $811,895 200
1 0 0 1 $12 0 0 1 $13 0 0 1 $14 0 0 1 $15 0 0 1 $16 0 0 1 $17 0 0 1 $18 0 0 1 $19 0 0 1 $1
10 0 0 1 $111 0 0 1 $1
12 0 0 1 $113 0 0 1 $114 0 0 1 $115 0 0 1 $116 0 0 1 $117 0 0 1 $118 0 0 1 $119 0 0 1 $1
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CS
Alloy
SS
PressureFactor
TubeMaterial
MaterialFactor
Bare ModuleCost [$]
1.3 SS 2.7 $2,849,752
0 0 $00 0 $00 0 $00 0 $00 0 $00 0 $00 0 $00 0 $00 0 $00 0 $00 0 $0
0 0 $00 0 $00 0 $00 0 $00 0 $00 0 $00 0 $00 0 $0
$0
7/30/2019 Plant Cost Estimate
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Dia (m) k1 k2 k3 Lmin (m) Lmax (m) B1 B2 k1 k20.3 3.3392 0.5538 0.2851 1.2 16 2.9202 0.50560.5 3.4746 0.5893 0.2053 1.5 20 3.1032 0.5782
1 3.6237 0.5262 0.2146 2.5 30 3.3592 0.59051.5 3.7559 0.6361 0.1069 3 41 3.4204 0.8141
2 3.9484 0.4623 0.1717 4 45 3.7599 0.36832.5 4.0547 0.462 0.1558 5 50 3.678 0.712
3 4.111 0.6094 0.049 6 50 3.7718 0.71594 4.3919 0.2859 0.1842 7 50 4.1551 0.2238
Vertical Orientation
2.5 1.72
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H and Vk3 Lmin Lmax B1 B2 Pmax [barg]
0.1261 1 20 4000.0632 1.5 25 4000.1106 2.2 30 400
-0.0046 3.5 36 400
0.1954 4.5 40 4000.043 5.5 42 4000.047 6.5 50 400
0.2499 8 52 400
Horizontal Orientation
1.62 1.47
7/30/2019 Plant Cost Estimate
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K1 K2 K3 C1 C2 C3
Fixed Tube Sheet or U-Tube 3.2138 0.2688 0.07961Floating Head 3.4338 0.1445 0.1079Kettle Reboiler 3.5638 0.1906 0.1107
-0.06499 0.05025 0.01474
7/30/2019 Plant Cost Estimate
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C1(onlytube>11bar)
C2(onlytube>11bar)
C3(onlyTube>11bar)
B1 B2 Amin Amax Pmax
4 900 14010 900 14010 100 140
1.8 1.5-0.04139 0.04139 0
7/30/2019 Plant Cost Estimate
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Shell CS CS SS CS Ni_alloyTube CS SS SS Ni_alloy Ni_alloy
Fixed Tube Sheet or U-TubeFloating HeadKettle Reboiler
3.81 1.7 3 2.8
7/30/2019 Plant Cost Estimate
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k1 k2 k3Ws mini[KW]
Ws max[KW]
Pmax[barg]
C1 C2
Reciprocating 3.9412 0.417 0.09141 0.01 280 1200 0.312 0.632Centrifugal 3.5793 0.3208 0.0285 0.01 250 350 0.1682 0.347
7/30/2019 Plant Cost Estimate
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C3 B1 B2
0.056 1.8 1.510.4841 1.8 1.51
7/30/2019 Plant Cost Estimate
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Cast Iron Cast Steel SS Ni_alloyReciprocating 1 1.4 1.9 3.5Centrifugal 1 1.8 2.4 5
7/30/2019 Plant Cost Estimate
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K1 K2 K3 Wfmin Wfmax CS SS Ni_alloyCentrifugal 2.9945 0.9542 0 50 8000 2.5 6.3 13Reciprocating 2.9945 0.9542 0 50 8000 2.9 7.3 15
7/30/2019 Plant Cost Estimate
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k1 k2 k3Ws mini[kW]
Ws Max[kW]
F_BM
Electric 2.3006 1.0947 -0.1016 3 6000 1.5Gas Turbine 3.4171 0.6112 0 10 15000 3.5Steam Turbine 3.7222 0.4401 0 100 15000 3.5
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K1 K2 K3Q Min[kW]
Q Max[kW]
P Max[barg]
Fp P=10[barg]
Reactive Process Heater(Reformer Furnace)
2.6379 0.8179 0 3000 150000 200 1
Reactive Process Heater(Pyrolysis Furnace)
2.5689 0.8067 0 3000 150000 200 1
Non-Reactive ProcessHeater
2.5526 0.7962 0 3000 150000 200 1
7/30/2019 Plant Cost Estimate
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Fp P=50[barg]
Fp P=100[barg]
Fp P=200[barg]
F_BM CSF_BMAlloy
F_BM SS
1.05 1.15 1.3 2.1 2.5 2.7
1.05 1.15 1.3 2.1 2.5 2.7
1.1 1.235 1.4 2.1 2.5 2.7