期刊文献+

硅对铁基费-托合成催化剂的影响 被引量:7

Effect of Silica Promoter on Iron-Based Catalyst for Fischer-Tropsch Synthesis
下载PDF
导出
摘要 用共沉淀法制备了一系列不同硅含量的铁基催化剂,采用N2吸附和原位X射线衍射对催化剂进行了表征,在固定床反应器中考察了催化剂的费-托合成反应活性、选择性和稳定性.结果表明,含硅的催化剂具有较大的比表面积和较小的平均孔径,在CO还原及费-托合成反应中生成的碳化铁物种的稳定性比不含硅的催化剂高.在费-托合成反应中,不含硅的催化剂具有较高的初始活性,但易失活;含硅的催化剂具有较低的初始活性,但稳定性较高.Fe7C3是活性最高的碳化铁物种.随着硅含量的增加,催化剂的费-托合成反应更易生成低碳数产物. A series of SiO2-incorporated precipitated Fe-Si-Cu-K (100Fe: :xSi:3.0Cu:2.0K, x =0, 2.8, 6.4, 8.2, atomic ratio) catalysts were prepared using the co-precipitation method for the Fischer-Tropsch synthesis (FTS). The in-situ X-ray diffraction (XRD) and N2 physisorption were used to characterize the catalysts. The catalytic properties for FTS were tested in a fixed-bed reactor under pressure of 1.0 MPa and temperature of 543 K. The SlOE incorporation increased the surface area and decreased the pore size of the precipitated iron catalysts, and the transition of different iron oxide and iron carbide phases (Fe2O3, Fe3O4, Fe3C, Fe5C2, and FeTC3) was detected by in-situ XRD during the catalyst reduction in CO and FTS reaction in syngas (H2/CO molar ratio= 0.7). The activity of the catalyst without SiO2 increased sharply with time on stream during the FTS process, which was accompanied by the transition of Fe5C2 to Fe7C3. The catalyst without SiO2 deactivated rapidly when the highest CO conversion was achieved, whereas a persistent increase in the activity of catalysts with SiO2 was achieved with time on stream. These indicate that SiO2 can stabilize the activity of the precipitated iron catalyst. The observed effects of SiO2 on the catalytic performance of precipitated iron catalysts can be explained by the fact that SiO2 can improve the dispersity of iron oxides and iron carbides in the catalyst and restrain the conversion of different iron carbide phases during the catalyst reduction and FTS reaction.
出处 《催化学报》 SCIE CAS CSCD 北大核心 2007年第10期925-930,共6页
基金 国家自然科学基金(20473114 20590360)
关键词 费-托合成 沉淀铁催化剂 碳化铁 原位X射线衍射 Fischer-Tropsch synthesis precipitated iron-based catalyst silica iron carbide in-situ X-raydiffraction
  • 相关文献

参考文献22

  • 1Bukur D B, Sivaraj C. Appl Catal A, 2002, 231(1-2): 201
  • 2Davis B H. Catal Today, 2003, 84(1-2): 83
  • 3Bukur D B, Lang X S, Mukesh D, Zimmerman W H, Rosynek M P, Li C P. Ind Eng Chem, Res, 1990, 29 (8) : 1588
  • 4Bukur D B, Nowicki L, Lang X. Chem Eng Sci, 1994, 49(24A) : 4615
  • 5Dry M E. In: Anderson J R, Boudart M eds. Catalysis Science and Technology. Vol. 1. New York: Springer, 1981. 159
  • 6O'Brien R J, Xu L G, Spicer R L, Davis B H. Energy Fuels, 1996, 10(4): 921
  • 7Rao K R P M, Huggins F E, Mahajan V, Huffman G P, Rao V U $, Bhatt B L, Bukur D B, Davis B H, O'Brien R J. Top Catal, 1995, 2(1-4): 71
  • 8Lox E S, Marin G B, de Graeve E, Bussiere P. Appl Catal, 1988, 40(1-2): 197
  • 9Shroff M D, Kalakkad D S, Coulter K E, Kohler S D, Harrington M S, Jackson N B, Sault A G, Datye A K. J Catal, 1995, 156(2): 185
  • 10Zhang H B, Schrader G L. J Catal, 1985, 95(1): 325

二级参考文献71

  • 1阎世润,周敬来,林恒生.助剂对FT合成Fe—Mn共沉淀催化剂的影响 Ⅱ 催化剂的XPS研究[J].天然气化工—C1化学与化工,1993,18(6):8-13. 被引量:1
  • 2KUNDIG W,BMMEL H,CONSTABARIS G,et al. Some properties of supported small alpha-Fe2O3 particles determined with the Mssbauer effect[J]. Phys Rev,1966,142(2-11):327-333.
  • 3JIN Y,DATYE A K. Phase transformation in iron Fischer-Tropsch catalysts during temperature-programmed reduction[J]. J Catal,2000,196(1): 8-17.
  • 4SCHULZ H. Short history and present trends of Fischer-Tropsch synthesis[J]. Appl Catal: A, 1999,186(1-2):3-12.
  • 5RY M E. Practical and theoretical aspects of the catalytic Fischer-Tropsch process [J]. Appl Catal: A,1996,138(2):319-344.
  • 6Wu Baoshan,Bai Liang,Xiang Hongwei,et al. An active iron catalyst containing sulfur for Fischer-Tropsch synthesis[J]. Fuel,2004,83(2):205-212.
  • 7SHROFF M D,KALAKKAD D S,COULTER K E,et al. Activation of precipitated iron Fischer-Tropsch synthesis catalysts [J]. J Catal,1995,156(2):185-207.
  • 8PHAM H N,DATYE A K. The synthesis of attrition resistant slurry phase iron Fischer-Tropsch catalysts[J]. Catal Today,2000,58(4):233-240.
  • 9LUO M,O'BRIEN R J,BAO S, et al. Fischer-Tropsch synthesis: induction and steady-state activity of high-alpha potassium promoted iron catalysts[J]. Appl Catal: A,2003,239(1-2): 111-120.
  • 10WIELERS A F H,KOEBRUGGE G W,GEUS J W. On the properties of silica-supported bimetallic Fe-Cu catalysts[J]. J Catal,1990,121(2):375-385.

共引文献55

同被引文献154

  • 1游震亚,邓卫平,张庆红,王野.非负载型铁催化剂上二氧化碳加氢制低碳烯烃(英文)[J].催化学报,2013,34(5):956-963. 被引量:12
  • 2吕毅军,石玉林,宁文生,吕德义.沉淀铁基催化剂助剂对费托反应性能影响的研究[J].神华科技,2009,7(2):77-82. 被引量:9
  • 3任冬梅,周亚松.铁含量对Fe-Mn-K催化剂上CO_2加氢反应性能的影响[J].工业催化,2004,12(7):32-35. 被引量:4
  • 4吴宝山,白亮,张志新,相宏伟,李永旺,易凡,徐斌富.不同沉淀剂制备的铁基催化剂对浆态床F-T合成反应的催化性能[J].催化学报,2005,26(5):371-376. 被引量:15
  • 5Wan Haijun, Wu Baoshan, Tao Zhichao, et al. Study of an iron- based Fischer-Tropsch synthesis catalyst incorporated with SiO2 [ J ]. Journal of Molecular Catalysis A : Chemical, 2006,260 ( 1 - 2) :255-263.
  • 6Zhao Rong, Sudsakorn K, Goodwin G J, et al. Attrition resistance of spray-driediron F-T catalysts : effect of activation conditions [ J ]. Catal. Today,2002,71 (3-4) :319-326.
  • 7Davis B H. Fischer-Tropsch synthesis: relationship between iron catalyst composition and process variables[J]. Catal Today,2003, 84(1) :83-98.
  • 8Dictor R A, Bell A T. Fischer-Tropsch synthesis over reduced and unreduced iron oxide catalysts [ J ]. J. Catal. , 1986,97 ( 1 ) : 121 - 136.
  • 9Snel R. The nature of hydrocarbon synthesis by means of hydrogenation of carbon monoxide on iron-based catalysts : Part I. Hydrogenation-strength distribution of surface sites[ J]. J. Mol. Catal. , 1989, 53(1) :129-141.
  • 10Yang Yong, Xiang Hongwei, Xu Yuanyuan, et al. Effect of potassium promoter on precipitated iron-manganese catalyst for Fischer-Tropsch synthesis [ J ]. Applied Catalysis A : General, 2004,266 ( 2 ) : 181 - 194.

引证文献7

二级引证文献37

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