PREPARATION AND CATALYTIC PERFORMANCE OF SUPPORTED Cs2.5H0.5PW12O40 ETHERIFICATION CATALYST
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PREPARATION AND CATALYTIC PERFORMANCE OF SUPPORTED Cs2.5H0.5PW12O40 ETHERIFICATION CATALYST
CIESC JournalIssue 10, Pages: 1374-1377(2003)
作者机构:
辽宁石油化工大学石油化工系,辽宁,抚顺,113001
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Online First:25 October 2003,
Published:25 October 2003
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WANG Haiyan, CHEN Wenyi, WEI Min. PREPARATION AND CATALYTIC PERFORMANCE OF SUPPORTED Cs2.5H0.5PW12O40 ETHERIFICATION CATALYST[J]. CIESC Journal, 2003, (10): 1374-1377.
DOI:
WANG Haiyan, CHEN Wenyi, WEI Min. PREPARATION AND CATALYTIC PERFORMANCE OF SUPPORTED Cs2.5H0.5PW12O40 ETHERIFICATION CATALYST[J]. CIESC Journal, 2003, (10): 1374-1377.DOI:
PREPARATION AND CATALYTIC PERFORMANCE OF SUPPORTED Cs2.5H0.5PW12O40 ETHERIFICATION CATALYST
Some supported cesium salts of 12-tungstophoric acid (Cs2.5H0.5PW12O40) were prepared. The effects of support category
support properties
preparation methods and preparation conditions on the performance of supported Cs2.5H0.5PW12O40 catalysts were investigated. The catalysts prepared were characterized by XRD and Hammett indicator method. The results showed that silica gel is the preferred support
among Al2O3
silica gel
active carbon
MCM-41 and Si MCM-41. With decreasing sodium content of silica gel support
the activity of prepared catalyst increased. The catalysts prepared by both one-step method and two-step method showed strong acidity
high activity and excellent stability. XRD revealed that CsCO3 completely reacted with H3PW12O40 and formed Cs2.5 H0.5PW12O40 on the surface of silica gel support. Hammett constant(H0)of the catalyst was lower than -13.61. The Cs2.5H0.5PW12O40/SiO2 catalyst (loading of Cs2.5H0.5PW12O40 40%) showed the highest catalytic activity for the etherification of FCC light gasoline
and the etherification conversion of tertiary carbonic olefins was up to 56.54%
which could replace liquid acids and ion exchange resin and become a environmentally friendly solid acid catalyst.
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