首页 | 本学科首页   官方微博 | 高级检索  
     

氧化镍改性的ZSM-5催化剂对甲苯和甲醇择形甲基化反应稳定性的影响
引用本文:谭伟,侯珂珂,刘民,李文慧,刘海鸥,宋春山,郭新闻.氧化镍改性的ZSM-5催化剂对甲苯和甲醇择形甲基化反应稳定性的影响[J].石油学报(石油加工),2015,31(2):503-522.
作者姓名:谭伟  侯珂珂  刘民  李文慧  刘海鸥  宋春山  郭新闻
作者单位:1. 大连理工大学 化工学院,精细化工国家重点实验室PSU-DUT联合能源研究中心,辽宁 大连 116024; 2. 宾夕法尼亚州立大学 能源与矿物工程学院PSU-DUT联合能源研究中心,美国 宾夕法尼亚州 16802
基金项目:教育部“新世纪优秀人才计划”项目(No.NCET-04-0268)资助
摘    要:在常压下,以N2为载气,采用固定床反应器考察了NiO改性的ZSM-5催化剂催化甲苯和甲醇择形烷基化反应的性能。采用Ar物理吸附、XRD、XRF、TEM、XPS、H2-TPR、NH3-TPD、Py-IR、UV-Vis、UV-Raman、TG、GC-MS等手段表征所制备的催化剂。结果表明,在ZSM-5催化剂上负载质量分数为3%或5%的Ni,催化剂的稳定性明显得到提高。在催化甲苯甲基化反应后,NiO改性ZSM-5催化剂上出现了金属Ni,这可能是由于在积炭过程中,伴随着氢转移过程或者是水消炭反应过程而产生的H2将NiO还原为金属Ni;而且,催化剂的积炭量明显降低,同时作为积炭前驱体的稠环芳烃的生成量也明显减少,推测可能是由于金属Ni的存在,抑制了烷基苯脱氢生成稠环芳烃积炭前驱体的反应,因而提高了催化剂的稳定性。

关 键 词:改性ZSM-5分子筛  Ni物种  催化稳定性  抑制脱氢  择形甲基化  
收稿时间:2014-12-03

Effect of NiO Modification on Stability of Nano-sized ZSM-5 Catalyst for the Para-Selective Methylation of Toluene with Methanol
TAN Wei,HOU Keke,LIU Min,LI Wenhui,LIU Haiou,SONG Chunshan,GUO Xinwen.Effect of NiO Modification on Stability of Nano-sized ZSM-5 Catalyst for the Para-Selective Methylation of Toluene with Methanol[J].Acta Petrolei Sinica (Petroleum Processing Section),2015,31(2):503-522.
Authors:TAN Wei  HOU Keke  LIU Min  LI Wenhui  LIU Haiou  SONG Chunshan  GUO Xinwen
Affiliation:1. State Key Laboratory of Fine Chemicals, PSU-DUT Joint Center for Energy Research, School of Chemical Engineering, Dalian University of Technology, Dalian 116024, China; 2. EMS Energy Institute, PSU-DUT Joint Center for Energy Research and Department of Energy & Mineral Engineering, Pennsylvania State University, University Park, PA 16802, USA
Abstract:Shape-selective methylation of toluene with methanol was carried out in a fixed-bed tubular reactor with a continuous down-flow over Ni doped ZSM-5 catalysts, with N2 as carrier gas under atmospheric pressure. All the catalysts were characterized by Ar-physisorption, XRD, XRF, TEM, XPS, H2-TPR, NH3-TPD, Py-IR, UV-Vis, UV-Raman, TG and GC-MS. The results showed that the catalytic stability of the ZSM-5 catalyst was significantly enhanced with Ni loading at 3% and 5%. The metal Ni is present on the spent catalysts, due to the hydrogen from hydrogen transfer reaction or the reaction between water and coke, which could reduce NiO to metal Ni within the coking process. The coke amounts were decreased by introducing Ni species, so were the highly condensed aromatics as coke precursors. The presence of metal Ni led to significant suppression of dehydrogenation and condensation, thus inhibition of the coking process, resulting in the improvement of catalyst stability.
Keywords:modified ZSM-5 zeolite  nickel species  catalytic stability  dehydrogenation inhibition  shape-selective methylation
本文献已被 CNKI 万方数据 等数据库收录!
点击此处可从《石油学报(石油加工)》浏览原始摘要信息
点击此处可从《石油学报(石油加工)》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