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化学工业与工程
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��ѧ��ҵ�빤�� 2004, Vol. 21 Issue (5) :379-382    DOI:
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Process Optimization of Residual Catalytic Cracking Reactor-Regenerator System
CHANG He-ying~1,HAN Jin-yu~1,WANG Hua~1,HE Xiu-yun~2 (1.School of Chemical Engineering,Tianjin University,Tianjin 300072,China; 2.Oil Refinery of the Daqing Oilfield Chemical Plant,Heilongjiang Daqing 163411,China)
(1.School of Chemical Engineering,Tianjin University,Tianjin 300072,China; 2.Oil Refinery of the Daqing Oilfield Chemical Plant,Heilongjiang Daqing 163411,China

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Abstract�� By using of thirteen lumped kinetic models,the simulation calculation for fluidized catalytic cracking unit with capacity of residual 6��10~5 (t/a) in Daqing Oilfield Chemical Plant was carried out.The effect of feedstocks ratio,reaction temperature,dispersion steam quantity and fast cooling oil quantity on product distribution have been investigated and the process is optimized.The results of simulation were very comparable with the actual operational data.
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Received 2004-09-15; published 2004-09-15
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����Ӣ,������,����,������.���ʹ߻��ѻ���Ӧ����ϵͳ�����Ż�[J].  ��ѧ��ҵ�빤��, 2004,21(5): 379-382
CHANG He-ying~1,HAN Jin-yu~1,WANG Hua~1,HE Xiu-yun~2 .Process Optimization of Residual Catalytic Cracking Reactor-Regenerator System[J].  Chemcial Industry and Engineering, 2004,21(5): 379-382
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