催化裂解多产丙烯新技术  

STATE-OF-THE-ART CATALYTIC CRACKING PROCESSES FOR MAXIMIZING PROPYLENE PRODUCTION

作　　者：徐占武[1] 

机构地区：[1]中国石油天然气股份有限公司大庆炼化分公司,黑龙江省大庆市163411

出　　处：《炼油技术与工程》2006年第8期4-8,共5页Petroleum Refinery Engineering

摘　　要：介绍了国内外利用蜡油或常压渣油等重质原料的增产丙烯技术CPP,ARGG+FDFCC和TSRMP;还介绍了利用富含烯烃的混合碳四和催化裂化汽油等轻质原料的增产丙烯技术OCP,Propylur,Superflex,OCT,Meta-4和BASF公司的丁烯歧化工艺技术。Here described are the catalytic cracking processes such as CPP, ARGG ＋ FDFCC, TSRMP for maximized propylene production from heavier oils like vacuum gas oil or atmospheric residue ere as well as OCP, Propylur, Superflex, OCT, Meta-4 and BASF$ butane disproportionation for maximized propylene yield from lighter feedstocks such as olefin-rich mixed C4s and cracked gasoline.

关 键 词：丙烯生产 催化裂解工艺 原料 重质烃 轻质烃 国内外 技术发展水平 

分 类 号：TQ221.212[化学工程—有机化工]