By Max Stone Peters, K. D. Timmerhaus
The contents of this ebook are for engineers whose professional could be plant layout and economics. The contents are: creation, strategy layout improvement, basic layout concerns, price Estimation, curiosity and funding expenditures, Taxes and assurance, Depreciation, Profitability, replacement, Investments and Replacements, optimal layout, price and Asset Accounting, fabrics and Fabrication choice, The layout record, fabrics move, dealing with and remedy Equipment--Design and price, warmth move Equipment--Design and value, Mass move Equipment--Design and price and Statistical research in layout. The Appendixes are: Notes and Linear programming, Notes on Dynamic Programming, laptop options for reactor layout, Auxiliary and software price information, layout difficulties and Tables of actual houses and Constants.
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Additional resources for Plant Design and Economics for Chemical Engineers (Chemical Engineering)
With the information from these two figures, prepare a quantitative energy balance for the process and size the equipment in sufficient detail for a preliminary cost estimate. 5. A search of the literature reveals many different processes for the production of acetylene. Select four different processes, prepare qualitative flow sheets for each, and discuss the essential differences between each process. When would one process be more desirable than the others? What are the main design problems which would TDetailed information on materials of construction is presented in Chap.
B) With cross reference to the qualitative flow sheet, list each piece of equipment and tabulate for each the information needed concerning chemicals and the process in order to design the equipment. 4. Figure 2-1 presents a qualitative flow diagram for the manufacture of nitric acid by the ammonia-oxidation process. Figure 2-2 presents a quantitative flow diagram for the same process. With the information from these two figures, prepare a quantitative energy balance for the process and size the equipment in sufficient detail for a preliminary cost estimate.
14. Make a material balance and a qualitative flow sheet for the synthesis gas process described in Prob. 13. 07 percent ash (all on a weight basis). The oxidant in this process will be oxygen having a purity of 95 percent. 2 m3/s. 15. Prepare an energy balance and a suitable flow sheet for the synthesis gas production requested in Prob. 14. 16. Size the equipment that is necessary for the synthesis gas production outlined in Probs. 13 and 14. 17. Estimate the required utilities for the synthesis gas plant described in the previous four problems.