|
Abstract
This paper deals with the development of membranes to be used in membrane reactors in which either natural gas or a coal gasification product is converted to CO
2 and H
2, while these two components are separated from each other simultaneously. In this way, a pure hydrogen stream is produced for combustion in a fuel cell or gas turbine for electricity production as well as a pure CO
2 stream for storage in e.g. an empty gas field. Two cases are described: one for the development of H
2 and one for CO
2 selective membranes. The H
2 selective membrane is a porous one, where the pore size has been tuned by Atomic Layer Deposition (ALD) to the kinetic diameter of hydrogen. The separation is thus based upon molecular sieving. The CO
2 selective membranes are also porous but here the transport mechanism is based upon affinity separation. Performances of both kinds of membranes are presented. They are promising, although both the membrane support and the synthesis of the separating layer need improvement.