首页 | 本学科首页   官方微博 | 高级检索  
     

DCR评价装置对重油催化裂化催化剂LDC-200的性能评价
引用本文:李荻,高永福,侯凯军,王智峰,汪毅.DCR评价装置对重油催化裂化催化剂LDC-200的性能评价[J].工业催化,2015,23(11):908-911.
作者姓名:李荻  高永福  侯凯军  王智峰  汪毅
作者单位:(中国石油石油化工研究院兰州化工研究中心,甘肃 兰州 730060 )
摘    要:采用DCR催化裂化评价装置,通过不同原料油及剂油比对重油催化裂化催化剂LDC-200的反应性能进行评价。结果表明,以中国石油天然气股份有限公司兰州石化公司3 Mt·a-1催化装置所用渣油为原料油,在剂油质量比大于8.4时,催化剂LDC-200裂化能力强,拥有良好的焦炭选择性,且异构化功能显著,明显提高汽油辛烷值。采用3 Mt·a-1催化装置所用渣油与蜡油质量分数各50%配成的原料油,在剂油质量比小于8.4时,能够在确保汽油收率的同时控制焦炭产率。

关 键 词:催化剂工程  DCR评价装置  催化裂化催化剂  重油  异构烷烃  辛烷值  

Performance evaluation of LDC-200 catalyst for heavy oil catalytic cracking in DCR evaluation device
Li Di,Gao Yongfu,Hou Kaijun,Wang Zhifeng,Wang Yi.Performance evaluation of LDC-200 catalyst for heavy oil catalytic cracking in DCR evaluation device[J].Industrial Catalysis,2015,23(11):908-911.
Authors:Li Di  Gao Yongfu  Hou Kaijun  Wang Zhifeng  Wang Yi
Affiliation:(Lanzhou Petrochemical Research Center, Research Institute of Petroleum and Petrochemicals of PetroChina, Lanzhou 730060, China)
Abstract:Under the condition of using different feedstock oil and different catalyst/oil ratios,the performance of LDC-200 catalyst for heavy oil catalytic cracking was investigated in DCR (Davison Circulating Riser,Model Ⅳ) evaluation device.The results showed that using residual oil in 3 Mt·a-1 FCC unit of PetroChina Lanzhou Petrochemical Company as the feedstock,LDC-200 catalyst possessed good catalytic cracking activity,coke selectivity,and remarkable isomerization function under catalyst/oil mass ratio of over 8.4,and the octane number of gasoline was significantly enhanced.When the mass ratio of catalyst to oil was less than 8.4 and feedstock oil mixed by 50wt% residual oil and 50wt% wax oil was used,the yield of gasoline was ensured,and the coke yield was controlled.
Keywords:catalyst engineering  DCR evaluation device  catalytic cracking catalyst  heavy oil  isoparaffin  octane number  
本文献已被 CNKI 万方数据 等数据库收录!
点击此处可从《工业催化》浏览原始摘要信息
点击此处可从《工业催化》下载全文
设为首页 | 免责声明 | 关于勤云 | 加入收藏

Copyright©北京勤云科技发展有限公司  京ICP备09084417号