欢迎访问《新能源进展》官方网站!今天是
论文

Ni-CeO2/SBA-15电催化甲苯水蒸气重整的实验研究

  • 冉泽朋 ,
  • 陶 君 ,
  • 陆 强 ,
  • 王孝强 ,
  • 董长青
展开
  • 华北电力大学生物质发电成套设备国家工程实验室,北京 102206
冉泽朋(1990-),男,硕士研究生,主要从事生物质热解气化焦油催化转化的研究。

收稿日期: 2014-06-06

  修回日期: 2014-09-23

  网络出版日期: 2014-12-30

基金资助

国家科技支撑计划(2012BAD30B01);
国家自然科学基金(51276062);
中央高校基本科研业务专项资金(2014ZD17)

Electric Current Enhanced Catalytic Steam Reforming of Toluene with Ni-CeO2/SBA-15 Catalyst

  • RAN Ze-peng ,
  • TAO Jun ,
  • LU Qiang ,
  • WANG Xiao-qiang ,
  • DONG Chang-qing
Expand
  • National Engineering Laboratory for Biomass Power Generation Equipment, North China Electric Power University, Beijing 102206, China

Received date: 2014-06-06

  Revised date: 2014-09-23

  Online published: 2014-12-30

摘要

以甲苯为生物质气化焦油的模型化合物,以Ni-CeO2/SBA-15为催化剂,在自行搭建的固定床电化学催化(电催化)水蒸气重整实验台上进行了甲苯的电催化水蒸气重整实验,考察了电流强度、反应温度和水/碳摩尔比(S/C)对甲苯转化率、产气组成的影响,并对该催化剂进行了长时间活性测试。结果表明,电流的引入可以显著提高催化剂对甲苯的转化效率;在电流为4 A、反应温度为800℃、S/C为3时,甲苯转化率可以达到94.7%。

本文引用格式

冉泽朋 , 陶 君 , 陆 强 , 王孝强 , 董长青 . Ni-CeO2/SBA-15电催化甲苯水蒸气重整的实验研究[J]. 新能源进展, 2014 , 2(6) : 407 -412 . DOI: 10.3969/j.issn.2095-560X.2014.06.001

Abstract

Electric current enhanced catalytic steam reforming of toluene, which was selected as the model compound of biomass gasification tar, was performed by a fixed-bed electrochemical catalytic steam reforming experimental set using the Ni-CeO2/SBA-15 catalyst. Experiments were performed to reveal the effects of several factors on the toluene conversion and product gas composition, including the electric current intensity, reaction temperature and steam/carbon (S/C) ratio. Moreover, stability test of the catalyst was conducted over a long experimental period. The results indicated that the presence of the electric current enhanced the catalytic activity remarkably. The toluene conversion reached as high as 94.7% under the electric current of 4 A, temperature of 800 °C and S/C ratio of 3.

参考文献

[1] Shen Y, Yoshikawa K. Recent progresses in catalytic tar elimination during biomass gasification or pyrolysis-A review[J]. Renewable and Sustainable Energy Reviews, 2013, 21: 371-392.

[2] Font Palma C. Modelling of tar formation and evolution for biomass gasification: A review[J]. Applied Energy, 2013, 111: 129-141.

[3] Tao J, Zhao L, Dong C, et al. Catalytic steam reforming of toluene as a model compound of biomass gasification tar using Ni-CeO2/SBA-15 catalysts[J]. Energies, 2013, 6(7): 3284-3296.

[4] Koike M, Ishikawa C, Li D, et al. Catalytic performance of manganese-promoted nickel catalysts for the steam reforming of tar from biomass pyrolysis to synthesis gas[J]. Fuel, 2013, 103: 122-129.

[5] Guan G, Kaewpanha M, Hao X, et al. Steam reforming of tar derived from lignin over pompom-like potassium- promoted iron-based catalysts formed on calcined scallop shell[J]. Bioresource Technology, 2013, 139: 280-284.

[6] Virginie M, Adánez J, Courson C, et al. Effect of Fe–olivine on the tar content during biomass gasification in a dual fluidized bed[J]. Applied Catalysis B: Environmental, 2012, 121: 214-222.

[7] González J F, Román S, Engo G, et al. Reduction of tars by dolomite cracking during two-stage gasification of olive cake[J]. Biomass and Bioenergy, 2011, 35(10): 4324-4330.

[8] Yu Q Z, Brage C, Nordgreen T, et al. Effects of Chinese dolomites on tar cracking in gasification of birch[J]. Fuel, 2009, 88(10): 1922-1926.

[9] Shen Y, Zhao P, Shao Q, et al. In-situ catalytic conversion of tar using rice husk char-supported nickel-iron catalysts for biomass pyrolysis/gasification[J]. Applied Catalysis B: Environmental, 2014, 152-153: 140-151.

[10] Zhang R, Wang H, Hou X. Catalytic reforming of toluene as tar model compound: Effect of Ce and Ce–Mg promoter using Ni/olivine catalyst[J]. Chemosphere, 2014, 97: 40-46.

[11] Li D, Nakagawa Y, Tomishige K. Development of Ni-based catalysts for steam reforming of tar derived from biomass pyrolysis[J]. Chinese Journal of Catalysis, 2012, 33(4/6): 583-594.

[12] Ammendola P, Chirone R, Lisi L, et al. Investigation of the catalytic activity of Rh-LaCoO3 catalyst in the conversion of tar from biomass devolatilization products[J]. Applied Catalysis a-General, 2010, 385(1/2): 123-129.

[13] Ammendola P, Lisi L, Piriou B, et al. Rh-perovskite catalysts for conversion of tar from biomass pyrolysis[J]. Chemical Engineering Journal, 2009, 154(1/3): 361-368.

[14] Yuan L, Chen Y, Song C, et al. Electrochemical catalytic reforming of oxygenated-organic compounds: a highly efficient method for production of hydrogen from bio-oil[J]. Chemical Communications, 2008, (41): 5215-5217.

[15] Yuan L, Ye T, Gong F, et al. Hydrogen production from the current-enhanced reforming and decomposition of ethanol[J]. Energy & Fuels, 2009, 23(6): 3103-3112.

[16] Zhao D, Feng J, Huo Q, et al. Triblock Copolymer Syntheses of Mesoporous Silica with Periodic 50 to 300 Angstrom Pores[J]. Science, 1998, 279(5350): 548-552.

[17] Bartholomew C H, Farrauto R J. Chemistry of nickel-alumina catalysts[J]. Journal of Catalysis, 1976, 45(1): 41-53.

[18] Wang K, Li X J, Ji S F, et al. Effect of CexZr1-xO2 promoter on Ni-based SBA-15 catalyst for steam reforming of methane[J]. Energy & Fuels, 2009, 23(1): 25-31.

[19] Solsona B, Blasco T, López Nieto J M, et al. Vanadium Oxide Supported on Mesoporous MCM-41 as Selective Catalysts in the Oxidative Dehydrogenation of Alkanes[J]. Journal of Catalysis, 2001, 203(2): 443-452.

[20] Vradman L, Landau M V, Herskowitz M, et al. High loading of short WS2 slabs inside SBA-15: promotion with nickel and performance in hydrodesulfurization and hydrogenation[J]. Journal of Catalysis, 2003, 213(2): 163-175.

[21] Kan T, Xiong J, Li X, et al. High efficient production of hydrogen from crude bio-oil via an integrative process between gasification and current-enhanced catalytic steam reforming[J]. International Journal of Hydrogen Energy, 2010, 35(2): 518-532.

[22] Zhao B, Zhang X, Chen L, et al. Steam reforming of toluene as model compound of biomass pyrolysis tar for hydrogen[J]. Biomass and Bioenergy, 2010, 34(1): 140-144.

[23] Hu X, Lu G. Investigation of steam reforming of acetic acid to hydrogen over Ni–Co metal catalyst[J]. Journal of Molecular Catalysis A: Chemical, 2007, 261(1): 43-48.

文章导航

/