Page 295 - Chemical engineering design
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                                                        CHEMICAL ENGINEERING
                           Fixed costs:
                              5. Maintenance, take as 5% of fixed capital D 445,000 ð 0.05 D  £22,250
                              6. Operating labour, allow one extra man on days. It is unlikely
                                 that one extra man per shift would be needed to operate
                                 this small plant, and one extra per shift would give
                                 a disproportionately high labour cost.
                                 Say, £30,000 per year, allowing for overheads D        £30,000
                              7. Supervision, no additional supervision would be needed
                              8. Plant overheads, take as 50% of operating labour D     £15,000
                              9. Laboratory, take as 30% of operating labour D           £ 9000
                             10. Capital charges, 6% of fixed capital (bank rate 4%)     £26,700
                             11. Insurance, 1% of fixed capital                           £ 4450
                             12. Local taxes                                            neglect
                             13. Royalties                                              not applicable
                                                                          Fixed cost D  £107,400
                                 Direct production costs D 17,396 C 107,400 D          £124,796

                             14. Sales expense                     not applicable
                             15. General overheads                 not applicable
                             16. Research and development          not applicable
                                          Annual operating cost, rounded D £125,000


                                      6.10. ECONOMIC EVALUATION OF PROJECTS
                           As the purpose of investing money in chemical plant is to earn money, some means of
                           comparing the economic performance of projects is needed.
                             For small projects, and for simple choices between alternative processing schemes and
                           equipment, the decisions can usually be made by comparing the capital and operating
                           costs. More sophisticated evaluation techniques and economic criteria are needed when
                           decisions have to be made between large, complex projects, particularly when the projects
                           differ widely in scope, time scale and type of product. Some of the more commonly used
                           techniques of economic evaluation and the criteria used to judge economic performance
                           are outlined in this section. For a full discussion of the subject one of the many specialist
                           texts that have been published should be consulted; Brennan (1998), Chauvel et al. (2003)
                           and Vale-Riestra (1983). The booklet published by the Institution of Chemical Engineers,
                           Allen (1991), is particularly recommended to students.
                             Making major investment decisions in the face of the uncertainties that will undoubtedly
                           exist about plant performance, costs, the market, government policy, and the world
                           economic situation, is a difficult and complex task (if not an impossible task) and in
                           a large design organisation the evaluation would be done by a specialist group.

                           6.10.1. Cash flow and cash-flow diagrams
                           The flow of cash is the life blood of any commercial organisation. The cash flows
                           in a manufacturing company can be likened to the material flows in a process plant.
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