English
新闻公告
More
化学进展 2010, Vol. 22 Issue (10): 1911-1920 前一篇   后一篇

• 综述与评论 •

用于选择性合成清洁液体燃料的钴基F-T合成催化剂*

邵燕  姚楠  卢春山  吕德义  刘化章  李小年**   

  1. (浙江工业大学工业催化研究所,绿色化学合成技术国家重点实验室培育基地,杭州,310032)
  • 收稿日期:2010-01-25 修回日期:2010-03-25 出版日期:2010-10-24 发布日期:2010-10-20
  • 通讯作者: 邵燕 E-mail:yanzi.shao@yahoo.com.cn
  • 基金资助:

    国家自然科学基金;浙江省自然科学基金

Cobalt-based Catalyst for Selective Synthesis of Clean Liquid Fuel via Fischer-Tropsch Synthesis

Shao Yan  Yao Nan  Lu Chunshan   Lv Deyi   Liu Huazhang   Li Xiaonian**   

  1. (Institute of Industrial Catalysis, College of Chemical Engineering and Materials Science, State Key Laboratory Breeding Base of Green Chemistry-Synthesis Technology, Zhejiang University of Technology, Hangzhou, 310032, China)
  • Received:2010-01-25 Revised:2010-03-25 Online:2010-10-24 Published:2010-10-20
  • Contact: Shao Yan E-mail:yanzi.shao@yahoo.com.cn

在传统F-T合成(Fischer-Tropsch synthesis)中,烃类产物受到Anderson-Schulz-Flory (ASF)方程的控制,这使得烃类产物分布宽,不具有选择性。因此,如何突破ASF产物分布控制,实现以合成气为原料,高选择性合成特定碳数范围内的烃类产品是F-T合成研究领域中的前沿和热点之一。本文以钴基负载型催化剂的活性中心和载体孔结构与F-T合成产物分布之间的关联为探讨重点,综述了这一领域的最新研究成果。

The hydrocarbon products distribution of traditional Fischer-Tropsch synthesis (FTS) is controlled by Anderson-Schulz-Flory (ASF) kinetics. This leads to extensive carbon number distribution and nonselective products. How to break Anderson-Schulz-Flory kinetics is one of the front and hot topics in the research field of selective synthesis hydrocarbon via FTS. In this paper, we review the recent progress of the above area by discussing the relationship between the cobalt-based catalyst’s active sites and pore structure and product distribution.

Contents
1 Introduction
2 Controlling the hydrocarbon products distribution of F-T Synthesis by designing the catalyst’s active sites
2.1 Physical mixed bi-functional catalyst
2.2 Zeolite loaded bi-functional catalyst
2.3 Bi-functional catalyst with core-shell structure
3 Controlling the hydrocarbon products distribution of F-T Synthesis by changing supports’ pore structure
4 Conclusions and outlook

()

[1 ] Khodakov A Y,Chu W,Fongarland P. Chem. Rev. ,2007,
107: 1692—1744
[2 ] Anderson R B. The Fischer-Tropsch Synthesis. Orlando:
Academic Press Inc. ,1984
[3 ] Schulz H. Appl. Catal. A: General,1999,186: 3—12
[4 ] Batholomew C H. AIChE Spring Meeting,New Orleans,LA,
2003,paper 83b
[5 ] Gloria H S,Duncan S. UK0199475,1989
[6 ] Patzlaff J,Liu Y,Graffmann C,Gaube J. Appl. Catal. ,1999,
186: 109—119
[7 ] Friedel R A,Anderson R B. J. Am. Chem. Soc. ,1950,72:
1212—1215
[8 ] Flory P J. J. Am. Chem. Soc. ,1936,58: 1877—1885
[9 ] Dry M E. The Fischer-Tropsch Synthesis in Catalysis: Sci. and
Tech. ,Ⅰ ( eds. Anderson J R,Boudart M) . Springer-Verlag,1981
[10] Dupain X,Krul R A,Makkee M,Moulijn J A. Catal. Today,
2005,106: 288—292
[11] Borodko Y,Somorjai G A. Appl. Catal. A: Gen. ,1999,186:
355—362
[12] The Sasol Story: A half-century of technological innovation.
[2009-09-20]. http: / / sasol. investoreports. com / sasol _mm_
2006 / index. php
[13] 南非SASOL 公司网. [2009-09-20]http: / /www. Sasol. Com
[14] Bromfield T C,Vosloo A C. Macromol. Symp. ,2003,193:
29—34
[15] Hoek A,Kersten L B J M. Stud. Surf. Sci. ,Catal. ,2004,
147: 25—30
[16] Raoa V U S,Stiegela G J. Fuel Process Technology,1992,30:
83—107
[17] Espinoza R L,Steynberg A P,Jager B,Vosloo A C. Applied
Catalysis A: General,1999,186: 13—26
[18] Khodakov A Y,Chu W,Fongarland P. Chem. Rev. ,2007,
107: 1692—1744
[19] Song C S. Catal. Today,2006,115: 2—32
[20] DOE /NETL, Carbon Sequestration. Technology Roadmap and
Program Plan 2005. US Department of Energy,National Energy
Technology Laboratory,May 2005. [2009-09-20]. http: / / fossil.
energy. gov / sequestration / publications / programplans /2005 /
sequestrationroadmap2005. pdf
[21] Rajagopalan K,Young G W. Fluid Catalytic Cracking. NY:
American Chemical Society,1988. 34—48
[22] Schulz H,Niederberger H L,Kneip M,Weil F. Stud. Surf.
Sci. Catal. ,1991,61: 313—324
[23] Nam I,Chuo K M,Seo J G,Hwang S,Jun K W,Song I K.
Catal. Lett. ,2009,130: 192—197
[24] Ngamcharussrivichai C,Liu X,Li X,Vitidsant T,Fujimoto K.
Fuel,2007,86: 50—59
[25] Li X H,Asami K,Luo M F,Michiki K,Tsubaki N,Fujimoto
K. Catalysis Today,2003,84: 59—65
[26] Jothimurugesan K, Gangwal S K. Ind. Eng. Chem. Res. ,
1998,37: 1181—1188
[27] 李宇萍( Li Y P) ,王铁军(Wang T J) ,吴创之(Wu C Z) ,吕
永兴( Lv Y X) ,李海滨( Li H B) . 石油化工( Petro Chemical
Technology) ,2008,37(5) : 445—449
[28] Li X H,Yang J N,Liu Z W,Asami K,Fujimoto K. Journal of
the Japan Petroleum Institute,2006,49: 86—90
[29] Thomson R T,Wolf E E. Applied Catalysis,1988,41: 65—80
[30] 刘雪暖( Liu X N) ,邹钢( Zou G) ,李玉秋( Li Y Q) . 石油化
工高等学校学报( Journal of Petrochemical Unirersity) ,2000,
13(3) : 9—12
[31] Murata K,Okabe K,Takahara I,Inaba H. JP 2010001241,
2010
[32] Yoneyama Y,Sun X Y,Zhao T S,Wang T J,Iwai T,Ozaki K,
Tsubaki N. Catalysis Today,2010,149: 105—110
[33] Liu Z W,Li X H,Fujimoto K. Energy & Fuels,2005,19:
1790—1794
[34] Liu Z W,Li X H,Fujimoto K. Fuel Processing Technology,
2007,88: 165—170
[35] Liu Z W,Asami K,Fujimoto K. Catalysis Communications,
2005,6: 503—506
[36] Li X H,Liu X,Liu Z W,Asami K,Fujimoto K. Catalysis
Today,2005,106: 154—160
[37] Liu Z W,Li X H,Asami K,Fujimoto K. Appl. Catal. A:
General,2006,300: 162—169
[38] Liu Z W,Li X H,Asami K,Fujimoto K. Catalysis Today,
2005,104: 41—47
[39] Li X H,Feng X L,Ge Q,Fujimoto K. Fuel,2008,87: 534—
538
[40] Yoneyama Y,San X G,Iwai T,Tsubaki N. Energy & Fuels,
2008,22: 2873—2876
[41] Guczi L, Kiricsi I. Appl. Catal. A: General,1999,186:
375—394
[42] Jong S J,Cheng S. Appl. Catal. A: General,1995,126: 51—
66
[43] Rossin J A,Davis M E. Division of Fuel Chemistry,1986,31:
71—74
[44] Altwasser S, Glser R, Weitkamp J. Microporous and
Mesoporous Materials,2007,104: 281—288
[45] Shamsi A,Rao V U S,Gormley R J,Obermyer R T,Schehl R
R,Stencel J M. Ind. Eng. Chem. Prod. Res. Dev. ,1984,
23: 513—519
[46] Sun S,Fujimoto K,Yoneyama Y,Tsubaki N. Fuel,2002,81:
1583—1591
[47] Wang W J,Lin H Y,Chen Y W. Journal of Porous Materials,
2005,12: 5—12
[48] Bessell S. Appl. Catal. A: General,1993,96: 253—268
[49] Calleja G,de Lucas A,van Grieken R. Appl. Catal. ,1991,
68: 11—29
[50] Li Y P,Wang T J,Wu C Z,Qin X X,Tsubaki N. Catalysis
Communication,2009,10: 1868—1874
[51] Tang Q H,Wang Y,Zhang Q H,Wan H L. Catal. Commun. ,
2003,4: 253—258
[52] Yang G H,Tan Y S,Han Y Z,Qiu J S,Tsubaki N. Catalysis
Communication,2008,9: 2520—2524
[53] Yang G H,He J J,Yoneyama Y,Tan Y S,Han Y Z,Tsubaki
N. Res. Chem. Intermed. ,2008,34: 771—779
[54] He J,Yoneyama Y,Xu B,Nishiyama N,Tsubaki N. Langmuir,
2005,21: 1699—1702
[55] He J J,Liu Z L,Yoneyama Y,Nishiyama N, Tsubaki N.
Chem. Eur. J. ,2006,12: 8296—8304
[56] Li X G,He J J,Meng M,Yoneyama Y,Tsubaki N. Journal of
Catalysis,2009,265: 26—34
[57] Yang G H,He J J,Zhang Y,Yoneyama Y,Tan Y S,Han Y Z,
Vitidsant T,Tsubaki N. Energy & Fuel,2008,22: 1463—1468
[58] Iglesia E. Appl. Catal. A: Gen. ,1997,161: 59—78
[59] Soled S L,Iglesia E,Fiato R A,Baumgartner J E,Vroman H,
Miseo S. Topics in Catalysis,2003,26: 101—109
[60] Martinez A,Rollan J,Arribas M A,Cerqueira H S,Costa A F,Falabella E. J. Catal. ,2007,249: 162—173
[61] Pour A N,Shahri S M K,Zamani Y,Irani M,Tehrani S.
Journal of Natural Gas Chemistry,2008,17: 242—248
[62] Liu Y C,Fang K G,Chen J G,Sun Y H. Green Chem. ,2007,
9: 611—615
[63] Van der Laan G P,Beenackers A A C M. Catal. Rev. Sci.
Eng. ,1999,41: 255—264
[64] Li Y P,Wang T J,Wu C Z,Lv Y X,Tsubaki N. Energy &
Fuels,2008,22: 1897—1901
[65] 李宇萍( Li Y P) ,王铁军(Wang T J) ,吴创之(Wu C Z) ,李
新军( Li X J) ,吕永兴( Lv Y X) . 现代化工(Modern Chemical
Industy) ,2008,28(2) : 43—46
[66] Zhao D Y,Feng J L,Huo Q S,Melosh N,Fredrickson G H,
Chmelka B F,Stucky G D. Science,1998,279: 548—552
[67] Khodakov A Y,Bechara R,Griboval-Constant A. Appl. Catal.
A,2003,254: 273—288
[68] Cai Q,Li J. Catal. Commun. ,2008,9: 2003—2006
[69] Xiong H F,Zhang Y H,Liew K Y,Li J L. Journal of Molecular
Catalysis A: Chemical,2008,295: 68—76
[70] Hong J P,Chernavskii P A,Khodakov A Y,Chu W. Catalysis
Today,2009,140: 135—141
[71] Xiong H F,Zhang Y H,Liew K Y,Li J L. Fule Process
Technol. ,2009,90: 237—246
[72] Martínez A,Prieto G. Top. Catal. ,2009,52: 75—90
[73] Sun Y,Jia L,Li D,Mu S. CN101224425,2008
[74] Gonzalo P,Agustin M,Raul M,Maria A A. Applied Catalysis
A: General,2009,367: 146—156
[75] 银董红(Yin D H) ,李文怀( Li W H) ,钟炳( Zhong B) ,彭少
逸( Peng S Y ) . 催化学报( Chinese Journal of Catalysis ) ,
2000,21(3) : 221—224
[76] 银董红(Yin D H) ,李文怀( Li W H) ,钟炳( Zhong B) ,彭少
逸( Peng S Y ) . 催化学报( Chinese Journal of Catalysis ) ,
2002,23(2) : 118—120
[77] González O,Pérez H,Navarro P,Almeida L C,Pacheco J G,
Montes M. Catalysis Today,2009,148: 140—147
[78] Khodakov A Y,Griboval-Constant A,Bechara R,Zholobenko V
L. Journal of Catalysis,2002,206: 230—241
[79] Christensen C H,Johannsen K,Trnqvist E,Schmidt I,Topse
H,Christensen C H. Catalysis Today,2007,128: 117—122
[80] 杨文书(Yang W S) ,房鼎业( Fang D Y) ,相宏伟( Xiang H
W) . 催化学报( Chinese Journal of Catalysis) ,2005,26 ( 4 ) :
329—334
[81] Lira E,Lopez C M,Oropeza F. J. Mol. Catal. A: Chem. ,
2008,281: 146—153
[82] 杨文书(Yang W S) ,高海燕( Gao H Y) ,相宏伟( Xiang H
W) ,银董红(Yin D H) ,杨勇(Yang Y) ,徐元源( Xu Y Y) ,
钟炳( Zhong B) ,李永旺( Li Y W) . 高等学校化学学报
( Chemical Journal of Chinese Universities ) ,2002,23 ( 9 ) :
1748—1752

[1] 杨林颜, 郭宇鹏, 李正甲, 岑洁, 姚楠, 李小年. 钴基费托合成催化剂的表界面性质调控[J]. 化学进展, 2022, 34(10): 2254-2266.
[2] 石玉梅 姚楠 卢春山 范洋波 刘化章 李小年. 用于费-托合成的高分散型钴基催化剂*[J]. 化学进展, 2009, 21(10): 2044-2052.
[3] 张辉,储伟. 贵金属助剂对费-托合成用钴基催化剂的促进作用*[J]. 化学进展, 2009, 21(04): 622-628.
[4] 周玮,房克功,陈建刚,孙予罕. 水对钴基Fischer-Tropsch合成的影响[J]. 化学进展, 2006, 18(01): 45-50.