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化学工业与工程
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��ѧ��ҵ�빤�� 2007, Vol. 24 Issue (2) :154-157    DOI:
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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

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ժҪ ���ó������»�ԭ���Ʊ���WC�߻���,�����˱��������κ���������ԭλ���ۡ����۽������,�ڦ�=287�桢p=2.0 MPa������Ϊ1.0 h-1��n(H2)/n(n-C5)=4.0��������,������ת���ʴﵽ64.31%,���ʴﵽ61.92%,ѡ���ʴﵽ96.29%,Һ���ʴﵽ97.64%,��߻�����ʮ�ֽӽ������͹�����߻���,��ѡ��������븺���͵�Pt�߻�����������
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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.
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Received 2007-03-15; published 2007-03-15
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��ȫ��;��ӽ��;���鲨;.̼���ٴ߻������������칹����Ӧ[J].  ��ѧ��ҵ�빤��, 2007,24(2): 154-157
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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