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Si-MCM-41 obtained from different sources of silica and its application as support for nickel catalysts used in dry reforming of methane

机译:从二氧化硅的不同来源获得的Si-MCM-41及其在甲烷干法重整中用作镍催化剂的载体

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摘要

Si-MCM-41 molecular sieves are attractive for use as catalytic supports in reforming processes, requiring the development of catalysts that combine low cost, high activity and resistance to coking for viable conversion of biogas (CH4 + CO2) into higher added value products such as synthesis gas (H-2 + CO). In this work was synthesized Si-MCM-41 from a waste material (rice husk ash - RHA) and compared with Si-MCM-41 synthesized from a commercial silica source (tetraethylorthosilicate - TEOS). Both were evaluated as catalytic support in dry reforming of methane (DRM). Calcined Si-MCM-41 supports were wet impregnated with 10, 20 and 50% of nickel. DRM reactions were performed in a continuous flow tubular reactor using a 1:1 CH4:CO2 molar mixture, at 700 and 800 degrees C, and WHSV of 30 L.h(-1)gcat(-1). The results confirmed that the Si-MCM-41 structure was successfully synthesized by the different methods. The best DRM results were obtained with the 20%Ni/Si-MCM-41_TEOS catalyst. (C) 2019 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:Si-MCM-41分子筛在重整过程中用作催化载体很有吸引力,需要开发结合低成本,高活性和抗结焦性的催化剂,以将沼气(CH4 + CO2)转化为高附加值产品,例如作为合成气(H-2 + CO)。在这项工作中,从废料(稻壳灰-RHA)合成了Si-MCM-41,并与从商业二氧化硅来源(原硅酸四乙酯-TEOS)合成的Si-MCM-41进行了比较。两者均被评估为甲烷干重整(DRM)的催化载体。将煅烧的Si-MCM-41载体用10%,20%和50%的镍湿法浸渍。 DRM反应是在700和800摄氏度,使用WHSV为30 L.h(-1)gcat(-1),使用1:1 CH4:CO2摩尔混合物的连续流管式反应器中进行的。结果证实,通过不同的方法成功地合成了Si-MCM-41结构。使用20%Ni / Si-MCM-41_TEOS催化剂可获得最佳的DRM结果。 (C)2019氢能出版物有限公司。由Elsevier Ltd.出版。保留所有权利。

著录项

  • 来源
    《International journal of hydrogen energy》 |2019年第60期|32003-32018|共16页
  • 作者单位

    Fed Univ Parana UFPR Postgrad Program Bioprod Technol Agribusiness Rua Pioneiro 2153 BR-85950000 Palotina PR Brazil|Fed Univ Parana UFPR Lab Catalysis & Biofuel Prod LabCatProBio R Pioneiro 2153 BR-85950000 Palotina PR Brazil;

    Fed Univ Parana UFPR Lab Catalysis & Biofuel Prod LabCatProBio R Pioneiro 2153 BR-85950000 Palotina PR Brazil|Western Parana State Univ UNIOESTE Postgrad Program Engn Energy Agr R Univ 2069 BR-85814110 Cascavel PR Brazil;

    Fed Univ Parana UFPR Lab Catalysis & Biofuel Prod LabCatProBio R Pioneiro 2153 BR-85950000 Palotina PR Brazil;

    Western Parana State Univ UNIOESTE Postgrad Program Chem Engn R Univ 2069 BR-85814110 Cascavel PR Brazil;

    Fed Technol Univ Parana UTFPR Coordinat Chem Engn R Marcilio Dias 635 BR-86812460 Apucarana PR Brazil;

    Natl Inst Technol INT Catalysis Div Rio De Janeiro RJ Brazil;

    Fed Univ Parana UFPR Postgrad Program Bioprod Technol Agribusiness Rua Pioneiro 2153 BR-85950000 Palotina PR Brazil|Fed Univ Parana UFPR Lab Catalysis & Biofuel Prod LabCatProBio R Pioneiro 2153 BR-85950000 Palotina PR Brazil|Western Parana State Univ UNIOESTE Postgrad Program Engn Energy Agr R Univ 2069 BR-85814110 Cascavel PR Brazil;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Molecular sieves; Mesoporous materials; Silica; Rice husk; Dry reforming of methane;

    机译:分子筛介孔材料;二氧化硅稻壳;甲烷干重整;
  • 入库时间 2022-08-18 05:00:13

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