A class of models is derived for studying the effects of chemical kine
tics on residue curve maps for reactive distillation. Activity-based r
ate and phase equilibrium expressions provide an accurate and thermody
namically consistent description of composition changes in nonideal, r
eacting vapor-liquid mixtures. For certain strategies of operation, wh
ich dictate the rate of product removal, the model equations are nonau
tonomous, leading to unusual dynamic behavior. However, for a certain
special product removal policy, the effects of kinetics can be describ
ed by a single parameter, the Damkohler number, which measures the rat
e of reaction relative to product removal. For small values of the Dam
kohler number, the nonreactive simple distillation residue curve map i
s recovered and the singular points are the pure components and azeotr
opes in the nonreactive mixture. A bifurcation analysis shows the defo
rmation and, in some cases, the disappearance of these singular points
as the Damkohler number is increased until the equilibrium reactive r
esidue curve map is recovered at large values. This bifurcation analys
is reveals the limitations of the equilibrium analysis. A model proble
m for the reactive distillation of methyl tert-butyl ether from isobut
ene and methanol is solved.