The removal of heavy hydrocarbons from natural gas becomes necessary to fac
ilitate its pipeline transport and distribution, and for applications in co
nventional gas burners and co-generation engines. This work presents the us
e of silicalite membranes for this separation process. It was found that n-
butane permeates preferentially over methane, due to its strong adsorption
on the membrane, which hinders methane permeation. The influence of the ope
rating conditions (temperature, sweep gas flow, gas composition, etc.) was
studied experimentally. Several membranes prepared by different methods are
compared. The best separations are obtained with the same pressure at both
sides of the membrane and with the use of a sweep gas. Pretreatment of the
support before the zeolite synthesis improves the separation performance.
(C) 2001 Elsevier Science B.V. All rights reserved.