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Chem. Process Des. DeveJ.. 8, 385 (1969). + Chemical Reaction Models 37 Wei. , and C. D. Prater, The structure and analysis of complex reaction systems. Adv. , 13, 203-392 (1962). , and J. C. W.

Macromol. , C8, 1-56 (1972). Ray, W. , Current problems in polymerization reaction engineering, ACS Symp. , 226, 101-133 (1983). , and R. L. Laurence, Polymerization reaction engineering, in Chemical Reactor Theory: A Review, L. Lapidus and N. R. , PrenticeHall, Englewood Cliffs, NJ (1977), 532-582. Razbn, L. , and R. A . Schmitz, Multiplicities and instabilities in chemically reacting systems - a review, Chem. Eng. , 42, 1005-1047 (1987). Rideal, E. : A note on a simple molecular mechanism for heterogeneous catalytic react,ions, Proc.

1. 5 mole rnP3 s-'. The feed stream was free of C2H40. and the residence time in the reactor wa5 short enough that the secondary reaction of combustion of C 2 H 4 0 could be neglected. C Reaction Rate Near Equilibrium Show that Eqs. 3-14) lead to the following expressions for the derivatives in Eq. 5-1). (2. T*) = R,,(b*. T*) is the magnitude of each right-hand term in Eq. 4-5) at the particular equilibrium point ( b * ,T * ) . 2 to include reversibility of all the reactions. Reduce your expression for R H Bby ~ use of a common denominator.

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Answer to Prof. Stormers Remark by Epstein P. S.

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