期刊文献+

原料油中氮、硫体积分数及反应压力对加氢裂化催化剂积炭的影响 被引量:8

Effects of nitrogen or sulphide content and reaction pressure on coke deposited on hydrocracking catalyst
下载PDF
导出
摘要 在高压连续流动微型反应器上对加氢裂化催化剂进行催速老化实验,用元素分析、傅里叶变换红外光谱(FTIR)、X-光电子能谱(XPS)、热重 /微商热重(TG/DTG)等手段考察了不同体积分数的噻吩、吡啶和操作压力对催化剂积炭行为的影响。结果发现:原料中吡啶和噻吩体积分数分别高于 0. 1%和 0. 6%时,会导致催化剂积炭明显增加。含吡啶的原料在进行加氢裂化时生成的积炭,主要集中在微孔( <6nm)中,并会削弱催化剂的酸性中心,尤其是强酸中心。含噻吩原料加氢裂化生成的积炭,存在于不同孔径的孔中,在催化剂表面形成少量机械孔。原料中噻吩体积分数低于 0. 6%时,噻吩中的硫可以提高催化剂的硫化度使积炭减缓。相同体积分数的吡啶对催化剂积炭的贡献大于噻吩,催化剂比表面积降低更多。提高压力可以显著地降低催化剂的积炭量,减缓比表面的降低,减少酸中心数目的损失,导致微孔( <6nm)中积炭增多,积炭中石墨型积炭的相对比例增大。 The coke deposition of various contents of nitrogen (sulphide) in toluene under different reaction pressures on hydrocracking catalyst has been obtained using accelerated aging experiment. Coke type and amount, acid strength distribution, pore structure, and dispersion of active metal of catalyst were measured by elemental analysis, FTIR, physical adsorption, XPS, and TG/DTG. The results showed that the amount of coke increases significantly when the content of pyridine or thiophene is higher than 0.1% or 0.6% in toluene. The coke deposited due to pyridine accumulated mainly in small pores ( less than or equal 6 nm), and it decreased the amount of acid center especially strong acid center. The coke deposited due to thiophene impenetrated into all the pores and some of them could form mechanical pore on catalyst surface. When the content of thiophene was higher than 0.6% in toluene, thiophene could enhance the active-metal sulphidation and weaken the coke production. Higher reaction pressure could make coke deposited less abruptly, decrease the loss of acid center, but result in the ratio of pseudo-graphite structure coke increasing relatively.
出处 《燃料化学学报》 EI CAS CSCD 北大核心 2005年第1期101-106,共6页 Journal of Fuel Chemistry and Technology
关键词 加氢裂化催化剂 吡啶 噻吩 压力 积炭 hydrocracking catalyst pyridine thiophene reaction pressure coke deposite
  • 相关文献

参考文献10

二级参考文献24

  • 1朱泽霖,刘灵丽,李承烈.丝光沸石催化剂的结焦失活研究[J].催化学报,1996,17(1):40-44. 被引量:5
  • 2方向晨 谭汉森.-[J].石油学报:石油加工,1996,12(1):33-33.
  • 3方向晨 谭汉森.-[J].抚顺石油化工研究院院报,1991,4(4):31-31.
  • 4[1]Radwan A M, Kyotani T. Characterization of coke deposited from cracking of benzene over USY zeolite catalyst[J]. Appl Catal, 1999, 192(1):43-50.
  • 5[2]Wolf, E, Alfani, F. Catalyst deactivation by coking[J]. Catal Rev-Sci Eng, 1982, 24(3):3 29-371.
  • 6[6]Begon V, Warrington S B, Megaritis A, et al. Composition of carbanaceous deposits and catalyst deactivation in early stages of the hydrocr acking of a coal extract[J]. Fuel, 1999, 78: 681-688.
  • 7[10]Trim D L. Progress in Catalyst Deactivation[M]. Boston:Martinus Nijohoff,1982:32.
  • 8[11]Bhatia S,Beltramini J, Do D D. Deactivation of zeolite catalyst[J]. Cat Rev-Sci Eng, 1989-1990, 31 (4):431-480.
  • 9[14]Scherger J,Gruid A J. Hydrocracking Science and Technology[M]. New York:Marcel Dekker,Inc.1996.113.
  • 10柴章民,博士学位论文,1989年

共引文献68

同被引文献89

引证文献8

二级引证文献55

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部