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公开(公告)号:EP2133644A1
公开(公告)日:2009-12-16
申请号:EP08715068.6
申请日:2008-03-28
申请人: China Petroleum & Chemical Corporation , Beijing Research Institute of Chemical Industry, China Petroleum &Chemical Corporation
发明人: WANG, Guoqing , ZHANG, Lijun , DU, Zhiguo , CHEN, Shuo , ZHANG, Zhaobin , ZHOU, Cong , ZHOU, Xianfeng
CPC分类号: F28F13/12 , C10G2400/20 , F28D2021/0059 , F28F1/40 , F28F19/00 , Y10T29/4935
摘要: This invention relates to a tubular cracking furnace, especially an ethylene cracking furnace, which comprises a convection section and a or dual radiant section(s), at least one heat transfer intensifying member arranged in at least one pass each radiant tube in said radiant section, said at least one heat transfer intensifying member comprises a first heat transfer intensifying member, which is arranged at a location between 10D and 25D upstream of the extreme point of said at least one pass radiant tube metal temperature, wherein D is the inner diameter of the radiant tube having heat transfer intensifying members. The present invention could achieve the best enhanced heat transfer result with given number of heat transfer intensifying member, by optimizing the locations of heat transfer intensifying members in the radiant tube.
摘要翻译: 本发明涉及一种管状裂解炉,特别是乙烯裂解炉,其包括对流段和一个或两个辐射区,至少一个传热增强构件,其至少一个通路布置在所述辐射段内的每个辐射管 所述至少一个传热增强构件包括第一传热增强构件,其被布置在所述至少一个通过辐射管金属温度的极限点上游的10D和25D之间的位置,其中D是 辐射管具有传热增强构件。 通过优化辐射管中的传热增强构件的位置,本发明可以通过给定数量的传热增强构件实现最佳增强的传热结果。
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公开(公告)号:EP2172440B1
公开(公告)日:2015-08-19
申请号:EP08783535.1
申请日:2008-07-18
申请人: China Petroleum & Chemical Corporation , Beijing Research Institute of Chemical Industry, China Petroleum & Chemical Corporation
发明人: WANG, Guoqing , ZHANG, Zhaobin , CHEN, Shuo , ZHANG, Lijun
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公开(公告)号:EP2133644B1
公开(公告)日:2019-08-07
申请号:EP08715068.6
申请日:2008-03-28
申请人: China Petroleum & Chemical Corporation , Beijing Research Institute of Chemical Industry, China Petroleum &Chemical Corporation
发明人: WANG, Guoqing , ZHANG, Lijun , DU, Zhiguo , CHEN, Shuo , ZHANG, Zhaobin , ZHOU, Cong , ZHOU, Xianfeng
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公开(公告)号:EP2172440A1
公开(公告)日:2010-04-07
申请号:EP08783535.1
申请日:2008-07-18
申请人: China Petroleum & Chemical Corporation , Beijing Research Institute of Chemical Industry, China Petroleum & Chemical Corporation
发明人: WANG, Guoqing , ZHANG, Zhaobin , CHEN, Shuo , ZHANG, Lijun
摘要: The present invention discloses a process for producing olefins from petroleum saturated hydrocarbons. The process of the present invention comprises: contacting a preheated petroleum saturated hydrocarbons feedstock with a dehydrogenation catalyst in a dehydrogenation reaction zone of a reaction system to obtain a petroleum hydrocarbon stream containing unsaturated hydrocarbon compounds, in which the dehydrogenation reaction has a conversion rate of at least 20%; and contacting the obtained petroleum hydrocarbon stream containing the unsaturated hydrocarbon compounds with olefins cracking catalyst in an olefin cracking zone of the reaction system to obtain a product stream containing olefins with a reduced number of carbon atoms.
摘要翻译: 本发明公开了一种从石油饱和烃生产烯烃的方法。 本发明的方法包括:使预热的石油饱和烃原料与脱氢催化剂在反应体系的脱氢反应区中接触,以获得含有不饱和烃化合物的石油烃流,其中脱氢反应的转化率为 至少20%; 并将所得到的含有不饱和烃化合物的石油烃物流与烯烃裂解催化剂在反应体系的烯烃裂化区中接触,得到含有碳原子数减少的烯烃的产物流。
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