By James R. Couper, W. Roy Penney, James R. Fair PhD

ISBN-10: 0123725062

ISBN-13: 9780123725066

A facility is simply as effective and ecocnomic because the gear that's in it. This hugely influential publication is a strong source for chemical, technique, or plant engineers who have to decide on, layout or configure plant effectively and profitably. Written by way of probably the most skilled and recognized chemical and procedure engineers within the this day, this information-packed quantity supplies the chemical or approach engineer or engineering scholar the entire instructions for the layout and choice of chemical technique apparatus. finished and functional, its scope and emphasis on real-world method layout and function of kit will end up precious for day by day challenge solving.The entire and influential consultant to the choice and layout of quite a lot of chemical technique apparatus, utilized by engineers globally . Copious examples of winning functions, with helping schematics and information to demonstrate the functioning and function of equipment Revised version, new fabric comprises up-to-date apparatus expense facts, liquid-solid and sturdy platforms, and the newest details on membrane separation technologyProvides gear score kinds and brands' facts, labored examples, beneficial shortcut equipment, principles of thumb, and gear score kinds to illustrate and help the layout processHeavily illustrated with many line drawings and schematics to help realizing, graphs and tables to demonstrate functionality facts

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Wiley, New York, 1999. Kirk-Othmer Encyclopedia of Chemical Technology, Wiley, New York, 1978–1984, 26 vols. , McGrawHill, New York, 1982. J. McKetta, Chemical Processing Handbook, Dekker, New York, 1992. J. McKetta and W. ), Encyclopedia of Chemical Processing and Design, Dekker, New York, 1976–date. G. Ullman, Encyclopedia of Chemical Technology, Verlag Chemie, Weinheim, FRG, English edition, 1994. C. Estimation of Properties B. General Data Collections AIChE Manual for Predicting Chemical Process Data, AIChE, New York, 1984–date.

Wiley, New York, 1998. P. Lechner, Designing for a Safe Process, Chem. , pp. 31–33 (December 20). P. , ButterworthHeinemann, Woburn, MA, 1996, 3 vols. J. , Van Nostrand Reinhold, New York, 1993. J. , Van Nostrand Reinhold, New York, 2000. P. Lieberman, Troubleshooting Refinery Processes, PennWell, Tulsa, OK, 1981. Process Safety Guidelines, Center for Chemical Process Safety, American Institute of Chemical Engineers, New York, 1992–date, 22 guidelines. C. ), Standard Handbook of Plant Engineering, McGraw-Hill, New York, 1983.

If the pumping rate of the agitator (Fa) is known, the deadtime (Td) of the real tank may be estimated by the following equation: Td = V/(F+Fa), where V is the volume of the tank and F is the flow through it. Process responses often consist of multiple lags in series. When these lags are non-interacting, the resulting response is predominantly deadtime, varying linearly with the number of lags in series. However when these lags are interacting, such as the trays on a distillation column, the resulting response remains predominantly a first-order lag with a time constant proportional to the number of lags squared.

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Chemical Process Equipment, Third Edition: Selection and Design by James R. Couper, W. Roy Penney, James R. Fair PhD


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