发明名称 Process for joint production of propylene and catalytic cracking of mixture of heavy and light hydrocarbon charges, the light charge comprising oligomers formed from C4/5 olefins
摘要 Conversion of a charge comprising a main heavy fraction of boiling point more than 350degreesC and a secondary fraction of boiling point less than 320degreesC by catalytic cracking in a fluidized bed, to obtain good yields of both propylene and petrol. Process for conversion of a charge made up of a main heavy hydrocarbon fraction of boiling point more than 350degreesC and a secondary light fraction of which the boiling point less than 320degreesC, in which: (a) The main charge (at least 50% wt. of the total charge) is cracked in a fluidized bed reactor in the presence of a catalyst; (b) The secondary charge is cracked in a fluidized bed with the same catalyst, separately or with the main charge; the secondary charge comprises 8C+ olefins obtained by oligomerization of 4 and/or 5C olefins; and (c) The effluents obtained are fractionated in a common fractionation zone and the catalysts are regenerated in a common regeneration zone.
申请公布号 FR2837213(A1) 申请公布日期 2003.09.19
申请号 FR20020003212 申请日期 2002.03.15
申请人 INSTITUT FRANCAIS DU PETROLE 发明人 DUPLAN JEAN LUC;LACOMBE SYLVIE;BAYLE JEROME;COUPARD VINCENT
分类号 C07C4/06;C07B61/00;C07C11/06;C10G11/05;C10G11/18;C10G35/04;C10G45/32;C10G50/00;C10G51/06;C10G57/02;C10G63/04;C10G69/04;C10G69/12;(IPC1-7):C10G65/12 主分类号 C07C4/06
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