capital and manufacturing cost estimation.ppt
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Capital and ManufacturingCost Estimation
Jim Frederick
CHBE4505A
Summer, 2005
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Capital Cost Estimation
Purchased vs. installed cost, etc.
Use simple estimation methods Cost vs. capacity power law scale-up
Cost factors or equations from equipmentvendors
Cost charts from plant design textbooks, etc.
Cost estimates from web sites
Inflation factors
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Cost Estimation Terminology
Cp= Purchased cost This is what you pay the vendor for the equipment
CBM= Bare module cost Cost of the equipment plus installation
CTM= Total module cost Cost of addition of equipment or minor expansion
Includes contingency and costs and other fees
CGR= total grass-roots cost Cost of a new mill or major mill expansion
Includes a site development, auxiliary buildings, etc.
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Cost vs. Capacity Power LawScale-up
Power law equation:
Cp,2/Cp,1= (Capacity2/Capacity1)n
For process equipment, nis equipmentspecific, range from 0.41 (heat exchangers) to 1.15
(jaw crushers) For an entire plant, use n= 0.6
CGR,2/CGR,1= (Capacity2/Capacity1)0.6
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MaterialsSelection
Factors:
Temperature
ChemicalEnvironment
Pressure
Stress-temperature relationships for important metals and alloys. (Source:Ulrich, 1984)
Temperature, oC
Allowablete
nsilestress,
bar
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Cost Factors or Equations FromEquipment Vendors
Cost factors (apply for a narrow size range)
Installed cost for black liquor evaporators:
$60/ft2heat transfer area Installed cost for kraft recovery boilers: $11 to
$13 per lb BL solids/day
Cost equations (apply over a wider size range)
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Example of a Cost Equation (1/2)
A. Cost equations:
For effects in a multiple-effect evaporator operating with black
liquor above 30% solids content and/or at pressures above 1atm,
CBM= $1,770 A0.55
For evaporator effects operating with black liquor at or below
30% solids content and/or at pressures at or below 1 atm,
CBM= $830 A0.55
Note: in both correlations, where A = heat transfer area, ft2
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Example of a Cost Equation (2/2)
B. Size limitations:
The largest dimple plate, falling film evaporator unit in the
world: evaporates 2.2x106pounds of water per hour,
contains 628,000 ft2of heat transfer area (~147,000 ft2
per effect for the 6-effect train)
The 6theffect is 34 ft in diameter
Be aware of min and max equipment sizes in normaldesign practice
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Cost Estimation Charts
Based on data from many plants
Procedure
estimate Cp,csfor equipment constructed fromcarbon steel, and to operate at or only slightlyabove one bar
Determine the factors for materials other than
carbon steel, pressure, etc.
Calculate CBM from Cp,csand these factors
Each chart has a specific equation for CBM= f(Cp,cs)
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Max
size
Min
size
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From Cpto CTM
1. Account for inflation
Use the ratio of the Chemical Engineering Plan CostIndex (CE Index) for the year of purchase and the yearon which the purchased cost estimation is based, i.e.
CBM,2006= CBM,1978(CE Index2006/CE Index1978)
Account for cost of installation, etc.
Add contingency + fee = 0.18 FBM
Simplest: use Lang factor: fLang= CTM/Cp
fLang= 4.5 for chemical plants, 3.2 for solids processing
plants, and 2.5 for P&P mills