In our original paper the subscript i was lost in eq 3, and consequently we used the rate expression given below (4) Clearly, the effect of dropping the subscript i in eq 3 is to use the current polymer concentration, instead of the initial polymer concentration, as the driving force for the reverse reaction, and, since C, < Cpi, our earlier analysis should have predicted values for the polymer concentration and degree of polymerization that are too large. Warner (1981) had, in fact, pointed out to us some time ago the incorrectness of eq 4 and on the basis of his comments we then computed solutions to the revised equations. Indeed, our revised computations yielded values for the degree of polymerization at the exit of the reactor which were smaller than the ones we reported earlier. However, i n all cases the qualitative trends were found t o be identical.
r(C,C,) = kC,2 -(k/K)C,CWe are unable to comment on the quantitative result for the degree of polymerization at the reactor exit, E, , = 52.7, given by Gupta et al., since the Gupta model incorporates an additional dimensionless parameter and is philosophically different from our model. The Gupta model takes the wiped film to be of finite thickness, whereas our model considers the film thickness to be infinite in relation to the penetration depth for mass transfer.
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