A method is reported for the synthesis of novel catalytic nanoporous carbon
membranes. Defect-free, nanoporous carbon films of 12.5- mum average thick
ness containing a dispersion of Pt-x were synthesized on macroporous stainl
ess-steel supports. Ideal gas selectivities for the catalytic membranes wer
e similar to those of inert nanoporous carbon membranes with He-N-2 = 58.6
and O-2-N-2 = 4.9. The selective hydrogenation of monoolefins (propylene, 1
-butene, isobutylene) was used to probe the shape-selective catalytic prope
rties and the transport selectivities of the membranes. The results were mo
deled using the linens regime of coupled adsorption, transport and reaction
in the membrane. Model regression yielded 14.9, 19.7, and 18.4 kJ/mol for
the activation energies of permeation for propylene, isobutylene, and 1-but
ene, respectively The system demonstrated selective reaction and transport
favoring propane production with selectivity? ratios of 28.9:3.2:1 for prop
ane:n-butane:isobutane at 125 degreesC.