Porous Vycor membrane tubes were used in shell-and-tube type membrane
reactors to study the effect on the oxidative coupling of methane of m
etering the oxygen into the catalyst bed. Experimental studies showed
that under conditions of complete oxygen conversion, Vycor membrane re
actors packed with Sm2O3 catalyst exhibited enhanced hydrocarbon (C-2)
selectivity. C-2 yields were comparable to those of the conventional
co-feed packed bed reactors operated under the same conditions. The hi
gher C-2 selectivity in the membrane reactors indicated that, for meth
ane coupling, regulating the supply of oxygen along the length of the
packed bed may be beneficial to C-2 formation.