发明名称 HYDROCARBON BATCH CONVERSION PROCESS
摘要 FIELD: petrochemical processes. ^ SUBSTANCE: hydrocarbon batch comprising primary relatively heavy batch boiling above 350°C and secondary relatively light batch boiling approximately below 320°C. Primary batch, comprising at least 50% of the hydrocarbon batch, is subjected to cracking in fluidized-bed reactor in presence of cracking catalyst. Secondary batch, containing C4,5-olefin oligomers with at least 8 carbon atoms, is subjected to cracking with the same cracking catalyst, separately or in mixture with primary batch. Cracking products are fractioned to produce gasoline and propylene. ^ EFFECT: increased propylene yield. ^ 20 cl, 1 dwg, 1 tbl, 7 ex
申请公布号 RU2294916(C2) 申请公布日期 2007.03.10
申请号 RU20040130479 申请日期 2003.03.10
申请人 EHNSTITJU FRANSEH DJU PETROL' 发明人 DJUPLAN ZHAN-LJUK;LAKOMB SIL'VI;BEJL' ZHEROM;KUPAR VINSEN
分类号 C07C4/06;C07C11/06;C07B61/00;C10G11/05;C10G11/18;C10G35/04;C10G45/32;C10G50/00;C10G51/06;C10G57/02;C10G63/04;C10G69/04;C10G69/12 主分类号 C07C4/06
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