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Cooper, Jeffrey

Many people have eontributed their experienee and their wisdom to this workbook. Special thanks goes to Bernard Deppmeier, Andy Driessen, Tim Hume and Jeffrey Johnson at Wavefunction for their development of Spartan View, to Robert Topper (Cooper Union) and Jurgen Schnitker (Wavefunction) for their careful reading of the entire manuscript and to Patrick McDougal (Reed College) for suggesting several problems. As always, Pamela Ohsan is thanked for turning our sloppy manuscript into a finished book. [Pg.311]

The reaction is endothermic, and heat transfer to the reactor is required in order to accomplish the decomposition of the acetylated oil, to liberate acetic acid vapour. The example has been considered previously by Perona (1972), Smith (1972), Cooper and Jeffreys (1971) and Froment and Bischoff (1990), although their solution procedures differ from that here. Data values are based on those used by Froment and Bischoff. [Pg.294]

Cooper and Jeffreys (1971) Chemical Kinetics and Reactor Design, Chem Engr. Texts. [Pg.297]

Cooper, AR, GV Jeffreys, Chemical Kinetics and Reactor Design, Prentice-Hall, Englewood Cliffs, NJ, 1971. Espenson, JH, Chemical Kinetics and Reaction Mechanisms, McGraw-Hill, New York, NY, 1981. [Pg.8]

Cooper and Jeffreys (1971) Chemical Kinetics and Reactor Design, Chem Engr. Texts. Froment, G.F. and Bischoff, D.B. (1990) Chemical Reactor Analysis and Design. 2nd edition, Wiley. [Pg.247]

These topics are dealt with in greater detail in the books by Denbigh and Turner [1], Levenspiel [2], Cooper and Jeffreys [3] and Hill [4]. [Pg.47]

Cooper and Jeffreys [3] give a worked example in which an endothermic reaction carried out with various heating rates is considered in some detail. [Pg.58]

The simultaneous solution of eqns. (72) and (79) when h is not zero is generally achieved by a numerical method which considers small increments in reactor volume and then iterates the calculation of the resulting temperature and fractional conversion in a manner similar to that described for Sect. 2.5.3 for a batch reactor. Cooper and Jeffreys [3] give an illustrative example, together with a computer flow diagram, for calculating the reactor volume. [Pg.74]

Figure 14. After Jeffrey and Saenger s [81] idea to illustrate cooperative action Gulliver a giant, constrained by a multitude of weak bonds. Illustration by V. Kubasta in J. Swift, Gulliver Lilliputban, Artia, Praha. Figure 14. After Jeffrey and Saenger s [81] idea to illustrate cooperative action Gulliver a giant, constrained by a multitude of weak bonds. Illustration by V. Kubasta in J. Swift, Gulliver Lilliputban, Artia, Praha.
Jeffrey GA, Lewis L (1978) Cooperative aspects of hydrogen bonding in carbohydrates. Car-bohydr Res 60 179-182... [Pg.515]

Cooper and Jeffreys, Chemical netics and Reactor Design, Prentice-Hall, 1971. [Pg.508]

A. R. Cooper and G. V. Jeffreys, Chemical kinetics and reactor design, Prentice-Hall, Englewood Cliffs, 1971, ISBN 0131286781, Chapter 9. [Pg.388]

Calvin F. Roff, Amy M. Walz, Lisa B. Niehoff, David J. Sdano, Antoinette M. Bennaars, Jeffrey A. Cooper, Becky L. Senft, Anatoli A. Sorkin, Steven P. Stoesz, and Paul A. Saunders... [Pg.119]

Jeffrey A. Cooper R D Systems Inc., Minneapolis, MN Zbigniew Darzynkiewicz Brander Cancer Research Institute, New York Medical College, Valhalla, NY... [Pg.171]


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