欢迎登录材料期刊网

材料期刊网

高级检索

采用等体积分步浸渍法制备了费托合成用Co/ZrO2/SiO2催化剂,并用XRD,TPR和N2-吸附等手段对催化剂进行了表征.考察了催化剂在费托反应过程中的结构变化和失活行为.结果表明,反应过程中硅酸钴物种的生成是催化剂失活的主要原因,且硅酸钴的生成与产物水的分压有关;晶粒长大也可能是催化剂失活的原因之一.

参考文献

[1] Zhang J L;Chen J G;Li Y W;Sun Y H .[J].Journal of Natural Gas Chemistry,2002,11(3/4):99.
[2] Espinoza R L;Steynberg A P;Jager B;Vosloo A C .[J].Applied Catalysis A:General,1999,186(1/2):13.
[3] Agrawal P K;Katzer J R;Manogue W H .[J].Journal of Catalysis,1981,69(02):327.
[4] Schanke D;Hilmen A M;Bergene E;Kinnari K, Rytter E, Adnanes E, Holmen A .[J].Catalysis Letters,1995,34(3/4):269.
[5] Hilmen A M;Schanke D;Hanssen K F;Holmen A .[J].Applied Catalysis A:General,1999,186(1/2):169.
[6] van Berge P J;van de Loosdrecht J;Barradas S;van der Kraan A M .[J].Catalysis Today,2000,58(04):321.
[7] Jacobs G;Patterson P M;Zhang Y Q;Das T,Li J L,Davis B H .[J].Applied Catalysis A:General,2002,233(1/2):215.
[8] Hilmen A-M;Lindvag O A;Bergene E;Schanke D, Eri S, Holmen A .[J].Studies in Surface Science and Catalysis,2001,136:295.
[9] Chen J G;Wang X Z;Xiang H W;Sun Y H .[J].Studies in Surface Science and Catalysis,2001,136:525.
[10] Chen J G;Xiang H W;Gao H Y;Sun Y H .[J].Reaction Kinetics and Catalysis Letters,2001,73(01):169.
[11] Kiss G.;Kliewer CE.;DeMartin GJ.;Culross CC.;Baumgartner JE. .Hydrothermial deactivation of silica-supported cobalt catalysts in Fischer-Tropsch synthesis[J].Journal of Catalysis,2003(1):127-140.
[12] Agrawal P K;Katzer J R;Manogue W H .[J].Journal of Catalysis,1981,69(02):312.
[13] Das T K;Jacobs G;Patterson P M;Conner W A, Li J L, Davis B H .[J].FUEL,2003,82(07):805.
[14] Vansteen E.;Makhothe RA.;Micklethwaite C.;Manstein H. Delange M.;Oconnor CT.;Sewell GS. .TPR STUDY ON THE PREPARATION OF IMPREGNATED CO/SIO2 CATALYSTS[J].Journal of Catalysis,1996(2):220-229.
[15] 陈建刚,相宏伟,李永旺,孙予罕.费托法合成液体燃料关键技术研究进展[J].化工学报,2003(04):516-523.
[16] 高海燕,陈建刚,相宏伟,杨继礼,李永旺,孙予罕.Co/SiO2催化剂合成重质烃的反应性能[J].催化学报,2001(02):133-137.
[17] 陈建刚,相宏伟,孙予罕.硅胶来源对费-托合成用Co/SiO2催化剂性能的影响[J].催化学报,2000(02):169-171.
[18] 陈建刚,相宏伟,王秀芝,孙予罕,刘涛,胡天斗,谢亚宁.锆助剂含量对钴基费-托合成催化剂的影响[J].催化学报,2000(04):359-362.
[19] Ali S;Chen B;Goodwin J G .[J].Journal of Catalysis,1995,157(01):35.
[20] Vaddad G J;Chen B;Goodwin J G .[J].Journal of Catalysis,1996,161(01):274.
[21] Viswanathan B;Gopalakrishnan R .[J].Journal of Catalysis,1986,99(02):342.
[22] [S].ES 8 604 428,1986.
[23] [S].Post M F M.ES 8 601 726,1985.
[24] Sie S T .[P].US 4579986,1986.
[25] Jacobs G;Das T K;Zhang Y Q;Li J L,Racoillet G,Davis B H .[J].Applied Catalysis A:General,2002,233(1/2):263.
[26] 刘维桥;孙桂大.固体催化剂实用研究方法[M].北京:中国石化出版社,2000:38.
[27] Iglesia E;Soled S L;Fiato R A .[J].Journal of Catalysis,1992,137(01):212.
[28] Jablonski JM.;Krajczyk L.;Wolcyrz M. .On cobalt silicate formation during high-temperature calcination of impregnated cobalt/silica catalysts[J].Journal of Catalysis,1998(2):530-534.
[29] Rodrigues E L;Bueno J M C .[J].Applied Catalysis A:General,2002,232(1/2):147.
[30] Самахов A A;Зайпман Н М;Чижик М Ц;Буянов Р А. 陆常德.催化剂在使用过程中活性的变化[M].北京:化学工业出版社,1981:30.
[31] Riva R.;Vitali R.;Del Piero G.;Miessner H. .Metal-support interaction in Co/SiO2 and Co/TiO2[J].Applied Catalysis, A. General: An International Journal Devoted to Catalytic Science and Its Applications,2000(1):111-123.
[32] 周广林,杨颜伟,张献军,冯兵,周红军.合成气脱羰基铁、镍技术及吸附剂的研究开发[J].天然气化工,2001(05):35-38,44.
上一张 下一张
上一张 下一张
计量
  • 下载量()
  • 访问量()
文章评分
  • 您的评分:
  • 1
    0%
  • 2
    0%
  • 3
    0%
  • 4
    0%
  • 5
    0%