A process for carrying out simultaneous reaction and separation of des
ired products in a single unit operation is described It uses a fixed
packed column of an admixture of a catalyst and a sorbent that selecti
vely removes a reaction by-product from the reaction zone. The sorbent
is periodically regenerated by using the principles of pressure-swing
adsorption. The process steps allow direct production of the desired
product at high purity and at the reaction pressure. High conversion o
f the reactants to products in an endothermic, equilibrium-controlled
reaction can be achieved while operating the reaction at a substantial
ly lower temperature than would be necessary by a plug-flow reactor pa
cked with the catalyst alone. The equilibrium-controlled reverse water
-gas shift reaction for the production of carbon monoxide is experimen
tally evaluated as a proof of the concept.