By James R. Couper, W. Roy Penney, James R. Fair, Stanley M. Walas
Chemical approach gear is a consultant to the choice and layout of a variety of chemical method apparatus. Emphasis is put on particular details about the procedure layout and function of apparatus. To this finish, awareness is given to examples of winning purposes, and a beneficiant variety of line sketches exhibiting the functioning of apparatus is integrated with many graphs and tables giving their real functionality. For coherence, short stories of perininent idea, together with numerical examples to demonstrate the extra concerned strategies, are supplied in key chapters. Professor Walas, drawing up on his a long time of expertise in and academia, offers a wealth of helpful shortcut tools, principles of thumb, and layout by way of analogy purposes. References to assets of extra exact layout systems are brought up every time they're to be had. to demonstrate the knowledge necessary to strategy layout, a considerable variety of apparatus ranking types and brands' questionnaires were amassed. simply because judgements usually has to be in accordance with monetary grounds, a brief bankruptcy on charges of kit rounds out the e-book. Serves as a advisor for choosing and designing chemical technique equipment.Provides various examples with many graphs and tables.Includes a bankruptcy on gear rate to handle vital financial issues.
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Extra info for Chemical Process Equipment, Selection and Design (Butterworth's Series in Chemical Engineering)
4. Reid, Prausnitz, and Poling, The Properties of Gases and Liquids, McGraw-Hill, New York, 1987. 5. Sterbacek, Biskup, and Tausk, Calculation of Properties Using Corresponding States Methods, Elsevier, New York, 1979. 6. M. Walas, Phase Equilibria in Chemical Engineering, Buttenvorths, Stoneham, MA, 1984. D. Equipment 1. Chemical Engineering Catalog, Penton/Reinhold, New York, annual. 2. Chemical Engineering Equipment Buyers' Guide, McGraw-Hill, New York, annual. 3. Kieser, Handbuch der chemisch-technischen Apparate, Spamer-Springer, Berlin, 1934-1939.
Bodman, The Industrial Practice of Chemical Process Engineering, MIT Press, Cambridge, MA, 1968. 6. Branan, Process Engineers Pocket Book, Gulf, Houston, 1976, 1983, 2 vols. 7. Burklin, The Process Plant Designers Pocket Handbook of Codes and Standards, Gulf, Houston, 1979; also, Design codes standards and recommended practices, Encycl. Chem. Process. Des. 14, 416-431, Dekker, New York, 1982. 8. Cremer and Watkins, Chemical Engineering Practice, Butterworths, London, 1956-1965, 12 vols. 9. , Chemical Plant Simulation, Prentice-Hall, Englewood Cliffs, NJ, 1971.
50,332 (1954)l. only to a certain accuracy. AT may be uncertain because of possible fluctuations in regulated steam and tower pressures. the bottom of the column. Accordingly, anticipated ranges of operating conditions. In addition, the design of equipment and plant must minimize potential harm to personnel and the public in case of accidents, of which the main causes are a. T) +A+- AT ’ that is, the fractional uncertainty of q is the sum of the fractional uncertainties of the quantities on which it is dependent.
Chemical Process Equipment, Selection and Design (Butterworth's Series in Chemical Engineering) by James R. Couper, W. Roy Penney, James R. Fair, Stanley M. Walas