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Production and Capital Cost Estimation                         69


            Calculation Procedures Using the Individual Factor Method

            Table 2.15  contains equations for calculating the depreciable capital cost using the
            individual factor  method. The  equations are similar to the  average  factor  method.
            Table  2.16  outlines the  calculation procedure.  Table  2.8  contains  direct-cost  fac-
            tors  for  several  pieces-of-equipment,  which  depends  on  the  material-of-
            construction. For indirect costs Guthrie  [13]  uses  1.34  for fluid processes and  1.29
            for  solids processes. He also uses  15% and 3% of the installation factor  for contin-
            gency  and  the  contractor's  fee.  Again, because  process  operating  conditions  and
            materials of construction do not affect  the cost of buildings and auxiliary facilities,
            we use the base installed costs to calculate these costs. For quick estimates Guthrie
            [36],  uses 2 to 6% of the  installed costs  for buildings  and  17 to  25%  for auxiliary
            facilities.  Use  averages of 4%  and  21% respectively for both costs. A calculation
            procedure for  the depreciable capital costs is outlined in Table 2.16.

            Table 2.15  Summary of Equations for Depreciable Capital Cost -
            Individual Factor Method (Based on Purchased Equipment Cost (FOB))

            The subscript i refers to a major piece-of-equipment.

                       roaV

            CpB2i  =  CpBii  I ——— I                                   (2.15.1)



            CPB i -  CpB2i  —                                          (2.15.2)
                       Iii

            CpAi  =  frifpifMifDiCpBi  —  for some equipment           (2.15.3)
                            f
            CPA i =  fr i (fp i + fo 0 M i Cp B ;  —  for heat exchangers
            fii = fuci  fici  foi  —  foci from  Table 2.8            (2.15.4)
               i =  1 .34 for a fluid  process or 1 .29 for a solids process
            f ic
            foi  =  1.18

                 I i
            C AI = f I i C P A i                                       (2.15.5)
                 Z
            C Bi = ifnCp B i                                           (2.15.6)
            CD =  CA, +  fAB CBI                                        (2.15.7)

            fAB  = auxiliary-facilities  factor + buildings factor = 0.04  + 0.21  = 0.25  (2.15.8)
            f^B  =  0 for a plant addition




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