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Unit Number 100 CEPCI 500 User Added Equipment Total Bare Module Cost Add Equipment Edit Equipment Remove All Equipment

CAPCOST_2008

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cap cost. año 2008

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Capcost Beta

Equipment SummaryUnit Number100CEPCI500User Added EquipmentBlendersTypeVolume (cubic meters)# SparesPurchased Equipment CostBare Module CostCentrifugesTypeDiameter (meters)# SparesPurchased Equipment CostBare Module CostCompressorsCompressor TypePower (kilowatts)# SparesMOCPurchased Equipment CostBare Module CostConveyorsTypeArea (square meters)Purchased Equipment CostBare Module CostCrystallizersTypeVolume (cubic meters)Purchased Equipment CostBare Module CostDrivesDrive TypePower (kilowatts)# SparesPurchased Equipment CostBare Module CostDryersTypeArea (square meters)Purchased Equipment CostBare Module CostDust CollectorsTypeGas Flowrate (cubic meters/s)Purchased Equipment CostBare Module CostEvaporatorsTypeArea (square meters)Pressure (barg)MOCVolume (cubic meters)Purchased Equipment CostBare Module CostExchangersExchanger TypeShell Pressure (barg)Tube Pressure (barg)MOCArea (square meters)Purchased Equipment CostBare Module CostFans / BlowersTypeGas Flowrate (cubic meters/s)# SparesMOCPressure Rise Across Fan (barg)Purchased Equipment CostBare Module CostFiltersTypeArea (square meters)Purchased Equipment CostBare Module CostFired HeatersTypeHeat Duty (MJ/h)Steam Superheat (C)MOCPressure (barg)Purchased Equipment CostBare Module CostMixersTypePower (kilowatts)# SparesPurchased Equipment CostBare Module CostPumps (with drives)Pump TypePower (kilowatts)# SparesMOCDischarge Pressure (barg)Purchased Equipment CostBare Module CostReactorsTypeVolume (cubic meters)Purchased Equipment CostBare Module CostScreensTypeArea (square meters)# SparesPurchased Equipment CostBare Module CostStorage TanksTank TypeVolume (cubic meters)Purchased Equipment CostBare Module CostTowersTower DescriptionHeight (meters)Diameter (meters)Tower MOCDemister MOCPressure (barg)Purchased Equipment CostBare Module CostTurbinesTurbine TypePower (kilowatts)# SparesMOCPurchased Equipment CostBare Module CostVesselsOrientationLength/Height (meters)Diameter (meters)MOCDemister MOCPressure (barg)Purchased Equipment CostBare Module CostUser Added EquipmentDescriptionBMF0Actual BMFPurchased Equipment CostBare Module CostTotal Bare Module Cost0.0

Utilities SummaryNameTotal Module CostGrass Roots CostUtility UsedEfficiencyActual UsageAnnual Utility CostTotals0.00.00.0COUNTIF(costSummary:totals,"B-*")0000000COUNTIF(costSummary:totals,"K-*")0000COUNTIF(costSummary:totals,"M-*")COUNTIF(costSummary:totals,"P-*")00000COUNTIF(costSummary:totals,"V-*")000

COM SummaryMaterial NameClassificationPrice ($/kg)Flowrate (kg/h)Annual CostPropyleneRaw Material$0.321234.00$3,286,191endClassificationendMaterial0.0$3,286,1910.00.0Economic Options0.0Cost of Land$1,250,000Taxation Rate42%Annual Interest Rate10%Salvage Value0customWorking Capital$330,000functionFCIL0.0CSGRCTotal Module Factor1.18Grass Roots Factor0.50Economic Information Calculated From Given InformationRevenue From Sales0.0materialCRM (Raw Materials Costs)$3,286,191materialCUT (Cost of Utilities)0.0COMCWT (Waste Treatment Costs)0.0materialCOL (Cost of Operating Labor)0.0materialFactors Used in Calculation of Cost of Manufacturing (COMd)Comd = 0.18*FCIL + 2.76*COL + 1.23*(CUT + CWT + CRM)Multiplying factor for FCIL0.18Multiplying factor for COL2.76Facotrs for CUT, CWT, and CRM1.23COMd$4,042,015Factors Used in Calculation of Working CapitalWorking Capital = A*CRM + B*FCIL + C*COLA0.10B0.10C0.10Project Life (Years after Startup)10Construction period2Distribution of Fixed Capital Investment (must sum to one)End of year One60%End of year Two40%End of year ThreeEnd of year FourEnd of year Five

jweaver:Typo

Cash Flow AnalysisDiscounted Profitibility CriterionNon-Discounted Profitibility CriteriaNet Present Value (millions)(14.09)Cumulative Cash Position (millions)(23.44)Discounted Cash Flow Rate of Return10.00%Rate of Return on Investment0.00%Discounted Payback Period (years)UndefinedPayback Period (years)UndefinedYearInvestmentdkFCIL-SdkRCOMd(R-COMd-dk)*(1-t)+dkCash Flow (Non-discounted)Cash Flow (discounted)Cumulative Cash Flow (discounted)Cumulative Cash Flow (Non-discounted)01.250.00(1.25)(1.25)(1.25)(1.25)10.330.00(0.33)(0.30)(1.55)(1.58)2-0.004.04(2.34)(2.34)(1.94)(3.49)(3.92)3-0.004.04(2.34)(2.34)(1.76)(5.25)(6.27)4-0.004.04(2.34)(2.34)(1.60)(6.85)(8.61)5-0.004.04(2.34)(2.34)(1.46)(8.31)(10.96)6-0.004.04(2.34)(2.34)(1.32)(9.63)(13.30)7-0.004.04(2.34)(2.34)(1.20)(10.83)(15.65)8-0.004.04(2.34)(2.34)(1.09)(11.93)(17.99)9-0.004.04(2.34)(2.34)(0.99)(12.92)(20.33)10-0.004.04(2.34)(2.34)(0.90)(13.82)(22.68)11-0.004.04(2.34)(0.76)(0.27)(14.09)(23.44)

Cash Flow Analysis-1.25-3.540909087829.49550283459.528604540486.8314242365111.6521693812134.2164831185154.7294955792173.3776887190.3305915141205.7423213243221.0743467504

LProject Life (Years)Project Value (millions of dollars)Cash Flow Diagram

Monte Carlo SimulationProbable Variation of Key Parameters over Plant LifeLower LimitUpper LimitBase ValueFCIL-20%30%0.0Price of Product-10%10%0.0Working Capital-50%10%$330,000Income Tax Rate*-20%20%42%Interest Rate*-10%20%10%Raw Material Price-10%15%$3,286,191Salvage Value-80%20%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% uncertaintyNet Present Value DataLow NPV-172.9High NPV186.4BinsUpper Value# points/binCumulative0-172.9001-137.0552-101.022273-65.1741014-29.215625756.7232489642.7235724778.61568808114.5999799150.51999810186.421000Discounted Cash Flow Rate of Return DataLow DCFROR0.00High DCFROR0.27BinsUpper#/binCumulative00.000010.03636320.056813130.0812625740.1114039750.1316956660.1615972570.1910883380.216890190.2429930100.273933Discounted Payback Period DataLow DPBP2.8High DPBP30.7BinsUpper#/binCumulative02.80015.626326328.4321584311.2163747414.082829516.756885619.535920722.324944825.10944927.969501030.76956Cumulative Cash Position DataLow CCP-213.33High CCP533.67BinsUpper Value# points/binCumulativive0-213.33001-138.63442-63.932024310.775478485.471242025160.171953976234.872286257309.571737988384.271189169458.976998510533.67151000Rate of Return on Investment DataLow ROROI-14%High ROROI44%BinsUpper Value# points/binCumulative0-14%001-8%552-2%374234%100142410%193335515%228563621%210773727%130903833%65968939%279951044%51000Payback Period DataLow DPBP1.9High DPBP10.1BinsUpper#/binCumulative01.90012.721421423.631452834.415568345.210979256.07086266.93289477.71691088.53794799.3129591010.12961

Monte Carlo Simulation00000000000

Net Present Value (millions of dollars)Cumulative Number of Data Points

User Options00000000000

Cumulative Cash Position (millions of dollars)Cumulative Number of Data Points

Equipment Cost Data00000000000

ROROICumulative Number of Data Points

00000000000

DPBP (years)Cumulative Number of Data Points

00000000000

PBP (years)Cumulative Number of Data Points

00000000000

DCFRORCumulative Number of Data Points

Hours per Operting Year8322Cost ($/GJ)Power PreferenceCommon Utilitieskilowatts1kW / kWElectricity (110V - 440V)16.8Cooling Water (30C to 45C)0.354Pressure PreferenceRefrigerated Water (15C to 25C)4.43barg1barg / bargSteam from BoilersHeat Duty PreferenceLow Pressure (5 barg, 160C)13.28MJ/h3.6(MJ/h) / kWMedium Pressure (10 barg, 184C)14.19High Pressure (41 barg, 254C)17.7Length Preferencemeters1m / mFuelsFuel Oil (no. 2)14.2Area PreferenceNatural Gas11.1square meters1m^2 / m^2Coal (FOB mine mouth)1.72Volume PreferenceThermal Systemscubic meters1m^3/m^3Moderately High (up to 330C)12.33High (up to 400C)13Gas Flow PreferenceVery High (up to 600C)13.88cubic meters/s1m^3 / m^3RefrigerationCost PreferenceModerately Low (5C)4.43$/kg1kg / kgLow (-20C)7.89Very low (-50C)13.11Flowrate Preferencekg/h1kg / kgCost ($/tonne)Waste Disposal (solid and liquid)Energy Price PreferenceNon-Hazardous36$/Gigajoule1GJ / GJHazardous200Cost of Steam used in Steam DrivesCost ($/GJ)Steam used for steam-powered drives$9.83Equipment EffecienciesPump Efficiency70%Drive Efficiency90%Fan Efficiency70%Furnace Efficiency90%Turbine Efficiency65%Process EquipmentOperators per shift per equipmentCost of Labor (per operator/year)$52,900Miscellaneous NumebrsSolids Handling Coefficient1.00

Blender DataBlender TypeK1K2K3Vmin(m3)Vmax(m3)FBMKneader5.0141-0.41330.32240.1431.5Ribbon4.1366-0.49280.00700.70111.5Rotary4.1366-0.49280.00700.70111.5Centrifuge DataCentrifuge TypeK1K2K3Dmin(m)Dmax(m)FBMAuto Batch Seperator4.7681-0.02600.02400.501.701.5Centrifugal Seperator4.3612-0.1236-0.00490.501.001.5Oscillating Screen4.8600-0.66600.10630.501.101.5Solid Bowl w/o Motor4.96970.16890.00380.302.001.5Compressor Data (without electric motors)Compressor TypeK1K2K3FBMCSFBMSSFBMNiWmin(kW)Wmax(kW)Centrifugal2.28911.3604-0.10272.75.811.54503000Axial2.28911.3604-0.10273.88.015.94503000Rotary5.0355-1.80020.82532.45.09.918950Reciprocating2.28911.3604-0.10273.47.013.94503000Conveyor DataConveyor TypeK1K2K3Amin(m2)Amax(m2)FBMApron3.9255-0.49610.15061.0015.002Belt4.0637-0.74160.15500.50325.002Pneumatic4.6616-0.67950.06380.7565.002Screw3.6062-0.73410.19820.5030.002Crystallizer DataCrystallizer TypeK1K2K3Vmin(m3)Vmax(m3)FBMBatch4.5097-0.82690.13441.5030.001.5Drive DataElectric DrivesK1K2K3FBMWmin(kW)Wmax(kW)Explosion Proof2.46041.4191-0.17981.5752600Totally Enclosed1.9561.7142-0.22821.5752600Open/Drip Proof2.95081.0688-0.13151.5752600Non-Electric DrivesK1K2K3FBMWmin(kW)Wmax(kW)Gas Turbine-21.770213.2175-1.52793.5750023000Steam Turbine2.62591.4398-0.17763.5707500Internal Combustion2.76350.8574-0.00982.01010000Dryer DataDryer TypeK1K2K3Amin(m2)Amax(m2)FBMDrum4.5472-0.72690.13400.5050.001.5Rotary, Gas Fired3.56450.1118-0.07775.00100.001.5Tray3.6951-0.4558-0.12481.8020.001.5Dust Collectors DataCollector TypeK1K2K3Vmin(m3/s)Vmax(m3/s)FBMBaghouse4.5007-0.58180.08130.08350.001.5Cyclone Scrubbers3.6298-0.49910.04110.06200.001.5( Centrifugal, Gravity4.1520-0.52990.01710.1050.00Spray, Impingement,and Wet Dynamic)Electrostatic Precipitator3.6298-0.49910.04110.06200.001.5Venturi3.6298-0.49910.04110.06200.001.5Fan Data (include electric motors)Fan TypeK1K2K3FBMCSFBMfiberglassFBMSSFBMNiThresholdC1C2C3Vmin(m3/s)Vmax(m3/s)Pmax(barg)Centrifugal Radial Fan3.5391-0.35330.44772.75.05.811.50.010.000.209-0.03311000.16Centrifugal Backward curved fan3.3471-0.07340.30902.75.05.811.50.010.000.209-0.03311000.16Axial Tube Fan3.0414-0.33750.47222.75.05.811.50.040.000.209-0.03311000.16Axial Vane Fan3.1761-0.13730.34142.75.05.811.50.040.000.209-0.03311000.16Filter DataFilter TypeK1K2K3Amin(m2)Amax(m2)FBMBent5.1055-0.50010.00010.90115.001.5Cartridge3.2107-0.24030.002715.00200.001.5Disc and Drum4.8123-0.71420.04200.90300.001.5Gravity4.2756-0.64800.07140.5080.001.5Leaf3.8187-0.37650.01760.60235.001.5Pan4.8123-0.71420.04200.90300.001.5Plate and Frame4.2756-0.64800.07140.5080.001.5Table5.1055-0.50010.00010.90115.001.5Tube5.1055-0.50010.00010.90115.001.5Fired Heater DataBare Module FactorReactive HeatersK1K2K3Qmin(kW)Qmax(kW)Pmax(barg)C1C2C3CSAlloy SteelSSReformer Furnace3.0680.65970.019430001000002000.1405-0.26980.12932.132.512.81Pyrolysis Furnace2.38590.9721-0.020630001000002000.1017-0.19570.094032.132.512.81Bare Module FactorNon-reactive HeatersK1K2K3Qmin(kW)Qmax(kW)Pmax(barg)C1C2C3CSAlloy SteelSSProcess Heater7.3488-1.16660.202810001000002000.1347-0.23680.10212.132.512.81Steam Supreheat FactorThermal Fluid HeatersK1K2K3Qmin(kW)Qmax(kW)Pmax(barg)C1C2C3FbmFT1FT2FT3Hot Water2.08290.9074-0.024365010750200-0.01630.0569-0.00882.17Molten Salt, Mineral Oil,1.19791.4782-0.095865010750200-0.01630.0569-0.00882.17Diphenyl Based Oils2.26280.85810.000365010750200-0.01630.0569-0.00882.17Packaged Steam Boilers6.9617-1.480.316112009400402.5941-4.23481.72242.21.0000.001843.35E-06Evaporator DataEvaporator TypesK1K2K3Amin(m2)Amax(m2)Pmax(barg)C1C2C3Forced Circulation5.02380.34750.0703510001500.1578-0.29920.1413Falling Film3.91190.8627-0.0088505001500.1578-0.29920.1413Agitated (Scraped Wall)50.149-0.01340.551500.1578-0.29920.1413Short Tube5.2366-0.65720.35101001500.1578-0.29920.1413Long Tube4.6420.36980.0025100100001500.1578-0.29920.1413Heat Exchanger DataExchager TypeK1K2K3C1C2C3B1B2Amin(m2)Amax(m2)Pmax(barg)Double Pipe3.34440.2745-0.047213.1467-12.65743.07051.741.5511030040 barg < P < 100 barg0.6072-0.9120.3327P < 40 barg000Multiple Pipe2.76520.72820.078313.1467-12.65743.07051.741.551010030040 barg < P < 100 barg0.6072-0.9120.3327P < 40 barg000Fixed tube, sheet, or U tube4.3247-0.3030.16340.03881-0.112720.081831.631.6610.01000140tubes only > 5 barg-0.00164-0.006270.0123Floating Head4.8306-0.85090.31870.03881-0.112720.081831.631.6610.01000140tubes only > 5barg-0.00164-0.006270.0123Bayonet4.2768-0.04950.14310.03881-0.112720.081831.631.6610.01000140tubes only > 5 barg-0.00164-0.006270.0123Kettle Reboiler4.4646-0.52770.39550.03881-0.112720.081831.631.6610.0100140tubes only > 5 barg-0.00164-0.006270.0123Scraped Wall3.78030.85690.034913.1467-12.65743.07051.741.552.02030040 barg < P < 100 barg0.6072-0.9120.3327P < 40 barg000Teflon Tube3.80620.8924-0.16710001.631.661.01015Air Cooler4.03360.23410.0497-0.1250.15361-0.028610.961.211010000100Spiral Tube - shell and tube3.99120.06680.243-0.40450.185901.741.551100400tube only-0.21150.097170Spiral Plate4.6561-0.29470.22070000.961.21110019Flat Plate4.6656-0.15570.15470000.961.2110100019Materail Factors, FMShell - CSCSCuCSSSCSNiCSTiExchanger TypeTube - CSCuCuSSSSNiNiTiTiDouble Pipe1.001.351.691.812.732.683.734.6311.38Multiple Pipe1.001.351.691.812.732.683.734.6311.38Fixed tube, sheet, or U tube1.001.351.691.812.732.683.734.6311.38Floating Head1.001.351.691.812.732.683.734.6311.38Bayonet1.001.351.691.812.732.683.734.6311.38Kettle Reboiler1.001.351.691.812.732.683.734.6311.38Scraped Wall1.001.351.691.812.732.683.734.6311.38Spiral Tube1.001.351.691.812.732.683.734.6311.38Shell MaterailExchanger TypeCSCuSSNiTiTeflon Tube Exchanger1.001.201.301.403.30Material In Contact with Process FluidExchanger TypeCSCuSSNiTiSpiral Plate1.001.352.452.684.63Flat Plate1.001.352.452.684.63Tube MaterialExchanger TypeCSAlSSAir Cooler1.001.422.93Mixer DataMixer TypeK1K2K3Pmin(kW)Pmax(kW)FBMImpeller3.8511-0.2991-0.00035.00150.001.5Propeller4.3207-0.96410.13465.00500.001.5Turbine3.4092-0.51040.00305.00150.001.5Pump Data (including electric drives)Pump TypeK1K2K3C1C2C3B1B2FmCIFmCSFmCuFmSSFmNiFmTiPmax(barg)Wmin(kW)Wmax(kW)Centrifugal pump3.38920.05360.1538-0.39350.3957-0.002261.891.351.01.6NA2.34.4NA1001300Positive Displacement3.47710.13500.14380-0.2453820.259016-0.013631.891.351.01.41.32.74.710.71001100Reciprocating pump3.86960.31610.12200-0.24540.2590-0.01361.891.351.01.51.32.44.06.41000.1200Reactor DataReactor TypeK1K2K3Vmin(m3)Vmax(m3)FBMAutoclave4.5587-0.70140.00201.0015.001.5Fermenter4.1052-0.4680-0.00050.1035.001.5Inoculum Tank3.7957-0.54070.01600.071.001.5Jacketed Agitated4.1052-0.4680-0.00050.1035.001.5Jacketed Non-Agitated3.3496-0.27650.00255.0045.001.5Mixer/Settler4.7116-0.55210.00040.046.001.5Screen DataScreen TypeK1K2K3Amin(m2)Amax(m2)FBMDSM3.8050-0.41440.21200.306.001.5Rotary4.0485-0.88820.32600.3015.001.5Stationary3.82190.0368-0.60502.0011.001.5Vibrating4.0485-0.88820.32600.3015.001.5Tank DataTank TypeK1K2K3B1B2Vmin(m3/s)Vmax(m3/s)Fixed Roof4.8509-0.39730.14451.1009030000Floating Roof5.9567-0.75850.17491.100.00100040000Turbine DataTurbine TypeK1K2K3FBMCIFBMCSFBMCuFBMSSFBMNiFBMTiWmin(kW)Wmax(kW)Axial2.70511.4398-0.1776NA3.5NA6.111.7NA1004000Radial2.24761.4965-0.1618NA3.5NA6.111.7NA1001500Vaporizer TypesK1K2K3Vmin(m3)Vmax(m3)Pmax(barg)C1C2C3Jacketed Vessel3.87510.33280.190111003200.1578-0.29920.1413Internal Coil4.0380.091420.276611003200.1578-0.29920.1413Jacketed Vessel w/ Coil4.0380.091420.276611003200.1578-0.29920.1413Bare Module Factors, FBMEvaporator TypesCSCu AlloySSNi AlloyTiForced Circulation2.93.635.089.6614.5Falling Film2.252.813.947.4911.25Agitated (Scraped Wall)2.252.813.947.4911.25Short Tube2.93.635.089.6614.5Long Tube2.93.635.089.6614.5Bare Module Factors, FBMVaporizer TypesCSCuGL SS CoilsGlass Lined Ni CoilsSSSS CladNi AlloyNi Alloy CladTiTi CladJacketed Vessel2.73.44.74.94.83.89.15.913.79.5Internal Coil3.03.85.25.55.24.110.16.615.210.6Jacketed Vessel w/ Coil3.03.85.25.55.24.110.16.615.210.6Vessel Data (including data for distillation towers and packed columns)Vertical VesselsHorizontal VesselsK1K2K3VminVmaxK1K2K3VminVmaxPmax(barg)3.49740.44850.10740.35203.55650.37760.09050.1628400Vessel B-ValuesFBMVessel TypeB1B2MOCSieveValveDemisterHorizontal1.491.52CS1.01Vertical2.251.82SS1.81.831.0Fluorocarbon1.8FqNi-alloy5.65.585.6Tray TypeK1K2K3Amin(m2)Amax(m2)Sieve2.99490.44650.39610.0712.3Materials of ConstructionValve3.33220.48380.34340.710.5FM CS1.0Demister3.23530.48380.34340.710.5FM SS clad1.7FM SS3.1Tower PackingFM Ni clad3.6Materials of ConstructionK1K2K3Vmin(m3)Vmax(m3)FM Ni7.1Ceramic3.06640.97440.00550.03628FM Ti clad4.7304 SS3.29990.97440.00550.03628FM Ti9.4Plastic Saddle2.44930.97440.00550.03628