NaX and NaY zeolite membranes were grown hydrothermally on the surface of a
porous cylindrical support. The molar compositions of the starting gel of
NaX and NaY zeolite membranes were SiO2/Al2O3 = 3.6-5.3 (X), 25 (Y), Na2O/S
iO2 = 1.2-1.4 (X), 0.88 (Y), H2O/Na2O = 30-50. X-ray diffraction (XRD) patt
erns of membranes consist of peaks corresponding to the support and NaX or
NaY zeolite. The Si/Al ratio of these NaX and NaY zeolites determined by at
omic absorption spectrophotometry was 1.3 and 2.1, respectively. The outer-
surface of the porous support was completely covered with randomly oriented
, intergrown NaX or NaY zeolite crystals and the thickness of the membrane
was about 20-30 mum, judging from the scanning electron microscopy (SEM) ob
servation. Pervaporation and vapor permeation of organic mixtures through N
aY and NaX zeolite membranes was investigated. The zeolite membranes showed
high alcohol selectivity for several feed mixtures with methanol or ethano
l. Furthermore, high benzene selectivity was observed for benzene/cyclohexa
ne and benzene/n-hexane separation. High perm-selectivity of the zeolite me
mbrane can be attributed to the selective sorption into the membrane. (C) 2
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