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Production and Capital Cost Estimation                           47

                 According to Table  2.1,  the  fixed  capital  cost  equals the  sum of the  depre-
            ciable capital cost, land cost, and land development cost. Land cost is 0.015  times
            the depreciable capital cost and land  development is 0.0211 times the depreciable
            capital cost for a fluid processing plant. Thus,

            C F = C D + 0.015  C D + 0.0211 C D =0.103 $/kg  (0.0467 c/kg)
                 Solving for C D, we obtain

               = 0.0994 $/kg  (0.0451 $/lb)
            C D
                 After,  calculating the  operating  labor  cost  and  depreciable  capital  cost, use
            the procedure  outlined in Table  2.1 to calculate  all  other  costs,  except  for the  ad-
            ministrative,  marketing,  and  research  and  development  costs.  First,  calculate  the
            production cost by summing up all the costs given in Table 2.1.1. These  costs are
            the  direct  cost,  indirect  cost,  administrative  cost,  marketing  cost,  financing  cost,
            and  the  research  and  development  cost.  Thus,  the  production  or  manufacturing
            cost is,

            CM = 86.4  +  11.9  + 0.045 C M + 0.135  C M +  1.24 + 0.0575 C M

                 Solving for C M, we obtain

            C M =  131 c/kg  (59.4  c/lb)
                 We  can now  complete  Table  2.1.1  for those  items  that  depend  on the  pro-
            duction  cost.  The production  cost  for this process, reported by  Kohn  [12],  is  119
            c/kg  (54.0  c/lb). Because  the  estimation  of N  in  the  operating  labor  cost requires
            judgment, we should expect that process engineers will differ  in their estimates. If
            we  estimate N  to  be  8  instead  of  7,  the production  cost  is  132  c/kg  (59.9  c/lb),
            which is not significant.




            CAPITAL COST ESTIMATION
            Calculating the production cost requires estimating the depreciable capital cost and
            fixed  capital cost. Before  estimating the depreciable capital cost, the process engi-
            neer must first  calculate mass and energy flow rates to size process equipment. He
            can then estimate  the  cost  of  all  equipment  and  finally  the  depreciable  and  fixed
            capital costs.  Besides sizing equipment he must also calculate utility requirements
            from  the  mass  and  energy  flow  rates.  Two  methods  for  estimating  capital  costs
            will be discussed: one is the  average  factor  method  and the  second is the  individ-
            ual  factor  method. At the  early  stages of developing  a process,  you  can use  these



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