This paper considers the application of inorganic membranes in conjunc
tion with catalysis and discusses attempts which have been made to aff
ect changes in the yields and product distributions in a number of cat
alytic reactions with a number of different conformations of catalyst
and membrane. Various possible reactor conformations are first conside
red and then some results obtained for catalytically-active perm-selec
tive membranes are presented to illustrate some of the problems encoun
tered with such membranes. The use of non-perm-selective wall-and-tube
reactors is then considered. Finally, the results of model calculatio
ns are presented which show that the most promising confirmation for t
he use of perm-selective membranes is one in which the membrane and ca
talyst are in separate units and external recirculation of reactants a
nd products is carried out.