发明名称 Catalytic cracking of petroleum hydrocarbons comprises use of double tube reactor, producing reaction streams for separation into lighter products
摘要 The cracking process takes place in four stages commencing with the introduction of catalyst and charge in the inner tube and the concentric space between the inner and outer walls of the reactor, and terminating with the separation of the catalyst for regeneration and the separation of the hydrocarbon products obtained. The process comprises: (i) supplying catalyst to an inner reactor tube and the concentric space between the inner and outer tubes in ascending mode by the action of a pre-lifting medium; (ii) supplying a hydrocarbon charge to the inner and outer spaces to contact with the catalyst to form an oil/catalyst mixture, so that a reaction occurs in cracking conditions to form an ascending reaction stream; (iii) propagating the reaction streams from the inner tube and the concentric space together to the entry of the confluence tube and to a separation unit where the hydrocarbon products are separated from the catalyst; and (iv) separating the hydrocarbons into different products including petrol, diesel oil and liquefied petroleum gas, re-generation of used catalyst and recycling of the latter.
申请公布号 FR2829143(A1) 申请公布日期 2003.03.07
申请号 FR20020010720 申请日期 2002.08.29
申请人 CHINA PETROLEUM AND CHEMICAL CORPORATION 发明人 ZHANG RUICHI;ZHONG XIAOXIANG;ZHANG JIUSHUN;XU KEJIA;ZHANG ZHIGANG;HOU SHUANDI;CHANG XUELIANG;WU ZHIGUO
分类号 B01J8/00;B01J8/18;B01J8/24;B01J8/26;B01J8/30;B01J8/32;B01J8/34;B01J19/26;C10G11/18;(IPC1-7):C10G11/16 主分类号 B01J8/00
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