ZSM-5 zeolite membranes with boron substituted into the framework for silic
on were prepared on porous stainless-steel and cy-alumina tubular supports.
These membranes had higher n-C4H10/i-C4H10 separation selectivities, and e
ffectively separated these isomer mixtures to higher temperatures than memb
ranes with aluminum substituted into the framework. Membranes were prepared
with Si/B ratios as low as 12, and the best membranes were prepared from a
lkali-free gels. The highest n-C4H10/i-C4H10 permselectivity at 473 K was 6
0, and the highest at 527 K was 24. For most alkali-fr ee membranes, the n-
C4H10/i-C4H10 permselectivities and separation selectivities increased with
boron content, and membranes on alpha-alumina supports had both higher per
meances and separation selectivities. Membranes with the same permeances an
d selectivities can be reproducibly prepared, and they are stable at elevat
ed temperatures.