化工进展 ›› 2020, Vol. 39 ›› Issue (11): 4488-4496.DOI: 10.16085/j.issn.1000-6613.2020-0145

• 工业催化 • 上一篇    下一篇

甲醇制对二甲苯联产低碳烯烃改性ZSM-5催化剂在流化床中的反应性能

刘丹(), 陈星月, 时一鸣, 代成义, 马晓迅()   

  1. 西北大学化工学院,国家碳氢资源清洁利用国际科技合作基地,陕北能源先进化工利用技术教育部工程研究 中心,陕西省洁净煤转化工程技术研究中心,陕北能源化工产业发展协同创新中心,陕西 西安 710069
  • 出版日期:2020-11-05 发布日期:2020-11-06
  • 通讯作者: 马晓迅
  • 作者简介:刘丹(1994—),女,硕士研究生,研究方向为甲醇催化转化。E-mail:237561087@qq.com
  • 基金资助:
    国家重点研发计划(2018YFB0604901);国家自然科学基金(21536009)

Performance of modified ZSM-5 zeolite in fluidized bed for co-production of low-carbon olefins and p-xylene from methanol

Dan LIU(), Xingyue CHEN, Yiming SHI, Chengyi DAI, Xiaoxun MA()   

  1. School of Chemical Engineering, Northwest University, International Science and Technology Cooperation Base of MOST for Clean Utilization of Hydrocarbon Resources, Chemical Engineering Research Center of the Ministry of Education for Advanced Use Technology of Shanbei Energy, Shaanxi Research Center of Engineering Technology for Clean Coal Conversion, Collaborative Innovation Center for Shanbei Energy and Chemical Industry Development, Xi’an 710069, Shaanxi, China
  • Online:2020-11-05 Published:2020-11-06
  • Contact: Xiaoxun MA

摘要:

在流化床反应器中,对Zn、Si和P改性的ZSM-5催化剂的甲醇制对二甲苯联产低碳烯烃的反应性能进行了研究。采用X射线衍射(XRD)、BET比表面积、扫描电镜(SEM)、NH3-程序升温脱附(NH3-TPD)等手段进行表征分析。结果表明,Zn改性使得催化剂酸强度降低,中强酸酸量增加,对二甲苯和低碳烯烃选择性都随之提高;一定量的硅沉积改性在降低催化剂外表面酸量的同时缩小孔口,浸渍适量P能够调变分子筛的酸中心强度和酸量,这都能够提高对二甲苯选择性。在流化床反应器中甲醇制对二甲苯联产低碳烯烃反应结果表明,3Zn-3Si-3P/ZSM-5催化剂在温度425℃、常压、反应时间40min、空速1h-1的条件下,对二甲苯在二甲苯中的选择性为76.0%,C2~C4低碳烯烃选择性为24.4%,特别是芳烃和C2~C4低碳烯烃的总选择性高达92.2%。

关键词: 流化床, 煤基甲醇, 对二甲苯, 低碳烯烃, 分子筛, 催化作用

Abstract:

In a fluidized bed reactor, the reaction performance of Zn, Si and P-modified ZSM-5 catalysts for conversion of methanol to p-xylene and co-production of lower olefins was studied. XRD, BET, SEM, and NH3-TPD etc. were used for the characterization analysis. The results showed that the modification by Zn decreased the acid strength of the catalyst, increased the amounts of medium and strong acids, and increased the selectivities of both p-xylene and lower olefins. The modification by deposition of silicon reduced the pore size as well as the amount of acid on the outer surface of the catalyst. Immersion of an appropriate amount of phosphorus can modulate the strength of the acid center of the zeolite and the amount of acid. The reaction results of converting methanol to p-xylene in the fluidized bed reactor to produce low-carbon olefins showed that at the temperature of 425 ℃, normal pressure, reaction time of 40min, and space velocity of 1h-1, the 3Zn-3Si-3P/ZSM-5 catalyst gave the selectivities of p-xylene in xylene and C2—C4 lower olefins were 76% and 24.4%, respectively. In particular, the total selectivity of aromatics and C2—C4 lower olefins was as high as 92.2%.

Key words: fluidized bed, coal-based methanol, p-xylene, low-carbon olefins, molecular sieve, catalysis

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