A TUNGSTEN OXIDE ON SILICA CATALYST FOR PHILLIPS TRIOLEFIN PROCESS

被引：69
作者：
HECKELSBERG, LF
BANKS, RL
BAILEY, GC
机构：
[1] Phillips Petroleum Co., Bartlesville, Okla.
来源：
INDUSTRIAL & ENGINEERING CHEMISTRY PRODUCT RESEARCH AND DEVELOPMENT | 1968年 / 7卷 / 01期
关键词：
D O I：
10.1021/i360025a007
中图分类号：
TQ [化学工业];
学科分类号：
0817 ;
摘要：
A catalyst consisting of tungsten oxide on silica that disproportionates olefins at relatively high temperatures will disproportionate propylene with equilibrium conversions (45%) and high efficiencies to ethylene and butenes at 600° F. or higher, 450-p.s.i.g. pressure, and space rates of 20 to 60 WHSV. No special pretreatments are required and the catalyst shows considerable resistance to common poisons such as air and water. © 1968, American Chemical Society. All rights reserved.
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页码：29 / +
页数：1
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JOURNAL OF CATALYSIS, 1967, 7 (03) :269-&
[6]  
HECKELSBERG LF, 1965, Patent No. 689882
[7]  
HECKELSBERG LF, 1963, Patent No. 1006049
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