重油催化裂解制低碳烯烃工艺技术研究进展  

Research progress in heavy oil catalytic pyrolysis technology for light olefins

作　　者：侯凯军 高金森[1] 马安[1,3] 王刚 王智峰[2] 高永福 刘超伟 HOU Kai-jun;GAO Jin-sen;MA An;WANG Gang;WANG Zhi-feng;GAO Yong-fu;LIU Chao-wei(College of Chemical Engineering and Environment,China University of Petroleum(Beijing),Beijing 102249,China;Lanzhou Petrochemical Research Center,Petrochemical Research Institute,PetroChina,Lanzhou 730060,China;PetroChina Planning&Engineering Institute,Beijing 100083,China)

机构地区：[1]中国石油大学(北京)化学工程与环境学院,北京102249 [2]中国石油石油化工研究院兰州化工研究中心,甘肃兰州730060 [3]中国石油规划总院,北京100083

出　　处：《应用化工》2022年第11期3278-3284,共7页Applied Chemical Industry

基　　金：国家自然科学基金面上项目(22178385)。

摘　　要：综述了国内外重油催化裂解工艺技术的研究进展,总结了重油催化裂解工艺技术的特点,指出现有技术存在的主要问题是:重油提升管、密相流化床或快速床的反应温度和反应时间无法独立控制,采用同一种催化剂很难满足重油裂化和汽油柴油二次裂化的需要,适用于提升管反应的多产乙烯催化剂还未有明显的突破性进展。展望了未来的研究方向。Heavy oil catalytic pyrolysis process technology at home and abroad was reviewed.The characteristics of heavy oil catalytic pyrolysis technology were summarized.This paper points out that the main problems existing in the existing technology are:the reaction temperature and reaction time of heavy oil riser,dense phase fluidized bed or fast bed cannot be controlled independently;it is difficult to use the same catalyst to meet the needs of heavy oil cracking and gasoline and diesel cracking;the productive ethylene catalyst suitable for riser reaction has not been broken through obviously.The future research directions are prospected.

关 键 词：重油 催化裂解 低碳烯烃 丙烯 工艺 进展 

分 类 号：TQ221.21[化学工程—有机化工] TQ203.2TQ426.1