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��ѧ��ҵ�빤�� 2003, Vol. 20 Issue (6) :425-428    DOI:
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Catalytic Behavior of Fluidized-Bed Catalystfor Oxidation of n-Butane to Maleic Anhydride
WEN Yu-long,XU Wen(School of Chemical Engineering,Tianjin University,Tianjin 300072,China)
(School of Chemical Engineering,Tianjin University,Tianjin 300072,China

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ժҪ ������ǰ�����Ʊ����������Ậ���Դ߻������ܵ�Ӱ�졣�ɽϸߺ����ƵõĴ߻���,��(VO)2P2O7�ຬ���϶�,������ת���ʽϸߡ�������Ũ�ȵļ�С,��-VOPO4��ĺ���������,������ת������֮����;��˳��ѡ���Կ�ʼʱ����,�ﵽ���ֵ���𽥽��͡�������������Ϊ95 0%ʱ�Ʊ��Ĵ߻������,�ڶ����������Ϊ4 0%������Ϊ500h-1�ķ�Ӧ������,˳�����ʿɴ�45 49%��
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Abstract�� The effects of orthophosphoric acid concentration in precursor preparation on the catalyst behavior have been studied.For the catalysts prepared at higher concentrations of acid,the quantity of V~(4+) phase (VO)_2P_2O_7 is quite large,and the n-butane conversions are all considerably high.With decreasing the acid concentration in precursor preparation,the relative amount of V~(5+) phase ��-VOPO_4 and the n-butane conversion increase continuously,whereas the selectivity to MA increases at beginning and then decreases after it reaches a maximum value.The catalyst prepared at the acid concentration of 95.0% gave the maximum yield of MA of 45.49% at an inlet n-butane concentration of 4.0% and a space velocity of 500h~(-1).
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Received 2003-11-15; published 2003-11-15
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������,����.������������˳���������߻���������[J].  ��ѧ��ҵ�빤��, 2003,20(6): 425-428
WEN Yu-long,XU Wen.Catalytic Behavior of Fluidized-Bed Catalystfor Oxidation of n-Butane to Maleic Anhydride[J].  Chemcial Industry and Engineering, 2003,20(6): 425-428
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