Pressure swing adsorption (PSA) processes are commonly used to produce pure
hydrogen from the steam-methane reformer (SMR) off-gas. The typical hydrog
en recoveries for PSA processes producing 99.999 + % hydrogen are in the ra
nge 70-85%. The nanoporous selective surface flow (SSF) carbon membrane can
be used to extract hydrogen from the low pressure waste gases of the PSA p
rocesses and the enriched hydrogen stream can be recycled as feed gas to th
e PSA process after recompression. The net result of this integration betwe
en the PSA process and the SSF membrane is increased hydrogen recovery from
the SMR off-gas.
The separation performance of the SSF membrane in producing a hydrogen-enri
ched gas from the PSA waste gas was experimentally evaluated and two differ
ent schemes to integrate the membrane with a specific PSA process for hydro
gen purification were studied. The performance of the PSA process was simul
ated using a software package called SIMPAC. It is demonstrated that the in
tegrated process can increase the net hydrogen recovery to 84-85% from a hy
drogen recovery value of 77-78% by the base PSA process. (C) 1999 Published
by Elsevier Science B.V. All rights reserved.