plant cost estimate

7/30/2019 Plant Cost Estimate

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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


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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


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No. Tower Item Number Dia. [m]

Cp: Purchase CostAssuming CarbonSteel Construction.[$/Tray]

Number of Trays Case 1


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Case 10


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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


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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


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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


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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


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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


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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


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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


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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


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No Item Number TypeWs Min[kW]

Ws Max[kW]

ShaftPower[kW]


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


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Reactive ProcessHeater (ReformerFurnace)

10

Reactive ProcessHeater (PyrolysisFurnace)

50

Non-ReactiveProcess Heater

100

200

No Item Number TypeQ Min[kW]

Q Max[kW]

HeatDuty [kW]


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


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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


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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


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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


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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


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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


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C3 B1 B2

0.056 1.8 1.510.4841 1.8 1.51


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Cast Iron Cast Steel SS Ni_alloyReciprocating 1 1.4 1.9 3.5Centrifugal 1 1.8 2.4 5


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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


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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


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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

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