Page 66 - Chemical process engineering design and economics
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Production and Capital Cost Estimation                         51




                                          UtflMn
                             Gas       Air     Refrigeration  Electricity





            r-
                    Storage, Receiving >nd Shipping   ProtMj Are* (Butter; Unit)

                   Q                                QUO


            L_


                                           Servtew

                                                 Shops    Laboratories



            Figure 2.5  The process area and auxiliary facilities of a chemical plant.







            plant design involves all the common branches of engineering -  mechanical, civil
            and  electrical  engineering.  Engineering  and  construction  costs  are  indirect  costs
            and are part of the depreciable capital cost.
                 Next,  two  methods  for  calculating  the  costs  listed  in  Figure  2.4  are  dis-
            cussed. One method is the  average  factor  method,  and the other method is the in-
            dividual factor  method. The accuracy of a cost estimate should be considered. Ta-
            ble 2.5 contains the accuracy of various methods and their cost. Although the costs
            are out-of-date, they do show that as a process becomes well-defined  the estimates
            become more costly. In the early stages, when a project  is ill-defined,  an accurate
            cost estimate is not warranted. The factor methods are study estimates and are less
            accurate than the detailed estimate.










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