Isomerization Reaction of n-Pentane over WC Catalyst
DAI Quan-bing~1,DAI Yong-chuan~2,JIANG Hong-bo~3(1.Plastic Plant of Daqing Petrochemical Company,Daqing 163714,Heilongjiang Province,China;2.College of Petrochemical Technology,Liaoning University of Petroleum & Chemical Technology,Fushun 113001,Liaoning Province,China;3.Daqing Xuelong Packaging Co.,Ltd.,Daqing 163714,Heilongjiang Province,China)
(1.Plastic Plant of Daqing Petrochemical Company,Daqing 163714,Heilongjiang Province,China;2.College of Petrochemical Technology,Liaoning University of Petroleum & Chemical Technology,Fushun 113001,Liaoning Province,China;3.Daqing Xuelong Packaging Co.,Ltd.,Daqing 163714,Heilongjiang Province,China
Abstract��
WC catalyst was prepared by temperature-programmed reduction and was oxygen-modified on surface to do line evaluation.Results indicate that under the condition of ��=287 ��,p=2.0 MPa,SV=1.0 h~(-1),n(H_2)/n(n-C_5)=4.0(molar ratio), conversion rate of n-pentane is 64.31%,yield of i-pentane is 61.92%,selectivety of i-pentane is 96.29% and liquid product yield is 97.64%.The catalytic activity of WC is close to that of loaded Pt,and the selectivity of WC is equivalent to that of loaded Pt catalyst.
DAI Quan-bing~1,DAI Yong-chuan~2,JIANG Hong-bo~3.Isomerization Reaction of n-Pentane over WC Catalyst[J]. Chemcial Industry and Engineering, 2007,24(2): 154-157
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