全部 标题 作者
关键词 摘要

OALib Journal期刊
ISSN: 2333-9721
费用:99美元

查看量下载量

相关文章

更多...
催化学报  2012 

助剂促进的Rh-Fe/Al2O3催化剂上CO加氢制乙醇反应性能

DOI: 10.3724/SP.J.1088.2012.11215, PP. 1007-1013

Keywords: ,,氧化铝,负载型催化剂,一氧化碳,加氢,乙醇

Full-Text   Cite this paper   Add to My Lib

Abstract:

?考察了Fe,Rh载量以及助剂对Rh-Fe/Al2O3催化剂上合成气制乙醇反应性能的影响.结果表明,随着Fe载量的增加,甲醇选择性持续上升伴随着甲烷选择性的持续下降,而乙醇选择性有最优值.助剂的添加或多或少促进了甲醇耦合、CO插入和解离的活性,或抑制了催化剂加氢能力,使得乙醇选择性有所上升,甲醇选择性有所下降,而烃类选择性变化不大.随着CO加氢反应的进行,Rh-Fe/Al2O3催化剂上烃类选择性逐渐下降,但甲醇的生成活性逐渐上升,而乙醇选择性和生成活性逐渐下降;然而,助剂的添加并未提高催化剂的稳定性.这可能是由于在反应过程中Fe物种逐渐被合成气还原使得乙醇生成活性位数量逐渐减少所致.

References

[1]  陈明英, 翁维正, 华卫琦, 伊晓东, 万惠霖. 催化学报 (Chen M Y, Weng W Zh, Hua W Q, Yi X D, Wan H L. Chin J Catal), 2011, 32: 672
[2]  Chen G, Guo C, Zhang X, Huang Z, Yuan G. Fuel Process Technol, 2011, 92: 456
[3]  Fan Z, Chen W, Pan X, Bao X. Catal Today, 2009, 147: 86
[4]  Pan X L, Fan Z L, Chen W, Ding Y J, Luo H Y, Bao X H. Nat Mater, 2007, 6: 507
[5]  黄利宏, 储伟, 洪景萍, 罗仕忠. 催化学报 (Huang L H, Chu W, Hong J P, Luo Sh Zh. Chin J Catal), 2006, 27: 596
[6]  Ngo H, Liu Y, Murata K. React Kinet Mech Catal, 2011, 102: 425
[7]  Wang K, Cook R A. US 200710 004 588. 2007
[8]  Haider M A, Gogate M R, Davis R J. J Catal, 2009, 261: 9
[9]  Gogate M R, Davis R J. Catal Commun, 2010, 11: 901
[10]  Gogate M R, Davis R J. ChemCatChem, 2009, 1: 295
[11]  Egbebi A, Schwartz V, Overbury S H, Spivey J J. Catal Today, 2010, 149: 91
[12]  Schwartz V, Campos A, Egbebi A, Spivey J J, Overburg S H. ACS Catal, 2011, 1: 1298
[13]  Liu Y, Murata K, Inaba M, Takahara I, Okabe K. Catal Today, 2011, 164: 308
[14]  Burch R, Hayes M J. J Catal, 1997, 165: 249
[15]  Ojeda M, Granados M L, Rojas S, Terreros P, Garcia-Garcia J L G, Fierro J L G. Appl Catal A, 2004, 261: 47
[16]  Zakumbaeva G D, Beketaeva L A, Uvaliev T Yu, Khlystov A S, Litvyakova E N. React Kinet Catal Lett, 1985, 28: 425
[17]  李经伟, 丁云杰, 林荣和, 龚磊峰, 宋宪根, 陈维苗, 王涛, 罗洪原. 催化学报 (Li J W, Ding Y J, Lin R H, Gong L F, Song X G, Chen W M, Wang T, Luo H Y. Chin J Catal), 2010, 31: 365
[18]  Chen W M, Ding Y J, Song X G, Wang T, Luo H Y. Appl Catal A, 2011, 407: 231
[19]  Niemantsverdriet J W, van der Kraan A M, Delgass W N. J Catal, 1984, 89: 138
[20]  Ichikawa M, Fukushima T, Shikakura K. (Proceedings of 8th International Congress on Catalysis, II.
[21]  Fukuoka A, Ichikawa M, Hriljac J A, Shriver D F. Inorg Chem, 1987, 26: 3643
[22]  Bowker M. Catal Today, 1992, 15: 77
[23]  Ichikawa M, Fukushima T. J Chem Soc, Chem Commun, 1985: 321
[24]  Egbebi A, Spivey J J. Catal Commun, 2008, 9: 2308
[25]  Zhang X, Li Z, Guo Q, Zheng Y, Xie K. Fuel Process Technol, 2010, 91: 379
[26]  Hargis D C, Dubeck M. US 4 309 314. 1982
[27]  Hargis D C, Dubeck M. US 4 370 507. 1983
[28]  Xu M, Iglesia E. J Catal, 1999, 188: 125
[29]  Khodakov A, Chu W, Fongarland P. Chem Rev, 2007, 107: 1692
[30]  Hayashi H, Chen L Z, Tago T, Kishida M, Wakabayashi K. Appl Catal A, 2002, 231: 81
[31]  Subramani V, Gangwal S K. Energy Fuels, 2008, 22: 814
[32]  Subramanian N D, Gao J, Mo X, Goodwin J G, Rorres W, Spivey J J. J Catal, 2010, 272: 204
[33]  Gao J, Mo X, Chien A C-Y, Torres W, Goodwin J G Jr. J Catal, 2009, 262: 119
[34]  Wang J, Zhang Q, Wang Y. Catal Today, 2011, 171: 257
[35]  Chen G, Guo C, Huang Z, Yuan G. Chem Eng Res Des, 2011, 89: 249

Full-Text

Contact Us

service@oalib.com

QQ:3279437679

WhatsApp +8615387084133