摘要
采用浸渍法制备Ni改性的HZSM-5催化剂,采用BET,XRD,Py-FTIR,NH3-TPD等分析手段对催化剂进行表征。以纯甲醇为原料,在固定床微反装置上,考察不同Ni负载量改性HZSM-5催化剂对甲醇芳构化(MTA)反应性能的影响。实验结果表明:Ni的引入使催化剂产生了比较稳定的新L酸位;随着Ni负载量的增加,Ni/HZSM-5催化剂的总酸量增加,尤其是弱酸酸量;MTA反应的芳烃总收率随着Ni负载量的增加呈现先减少后增加然后又减少的趋势;Ni的引入可能改变了HZSM-5催化剂上MTA反应的路径,由氢转移芳构化向脱氢芳构化转变;生成的芳烃主要以C7-C9芳烃为主,C6和C10+芳烃相对较少;副产物甲烷和COx收率则随Ni负载量的增加而增加,这可能与Ni促进了甲醇的甲烷化反应有关。
The performance of modified HZSM-5 catalysts with different loadings of nickel on the aromatization of methanol was investigated in a continuous fixed bed microreactor using pure methanol as raw material.The catalysts were characterized by BET,XRD,Py-FTIR,and NH3-TPD techniques.Results show that the introduction of nickel species results in the formation of new Lewis acid sites.Furthermore,the total acid amount of the HZSM-5catalyst increases gradually,especially the weak acid,with increasing amount of nickel.The total aromatic yield decreases first and then increases,followed by decrease again with the Ni loading.The introduction of nickel species may change the path from the hydrogen transfer aromatization to the dehydrogenation aromatization.In addition,aromatic hydrocarbons generated are mainly C7—C9aromatics,while C6 and C10+aromatics are relatively few.Meanwhile,by-products such as methane and COxincrease gradually with the increase of nickel loading,which is probably in correlation with the enhancement of methylation of methanol caused by nickel species.
出处
《石油炼制与化工》
CAS
CSCD
北大核心
2015年第2期58-63,共6页
Petroleum Processing and Petrochemicals
基金
青岛民生计划项目(No.13-1-3-126-nsh)
关键词
甲醇
甲醇芳构化
镍
脱氢
HZSM-5
methanol
methanol aromatization
nickel
dehydrogenation
HZSM-5