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Nickel-Based Ceria, Zirconia, and Ceria-Zirconia Catalytic Systems for Low-Temperature Carbon Dioxide Reforming of Methane

机译:镍基二氧化铈,氧化锆和二氧化铈-氧化锆催化甲烷的低温二氧化碳重整

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摘要

Carbon dioxide reforming of methane (CDRM) was studied over a variety of ZrO_2-, ceria-doped ZrO_2-, and CeO_2-ZrO_2-supported Ni catalysts. Different techniques were used to prepare supports material having different physicochemical properties, and a correlation was established to show the importance of a robust support material. Various characterization of the catalyst further established that the coking behavior of the catalyst depends on the support preparation techniques. Compared to zirconia and ceria-doped zirconia, the use of ceria-zirconia (Ce_xZr(1-x)O_2) solid solution as a support prepared by using a surfactant was found to be the most stable for low-temperature CDRM. It seems the inhibition of reactions leading to carbon deposition is prominent in systems having ZrO_2. Temperature-programmed oxidation (TPO) experiments indicated excellent resistance toward carbon formation for Ni supported on Ce_xZr_(1-x)O_2 compared with other catalysts studied. H_2-TPR (temperature-programmed reduction) analyses also showed that the stability of Ce_xZr_(1-x)O_2 solid solution is a function of its enhanced reducibility at lower temperatures as compared to either pure ceria or ceria-doped ZrO_2. Based on all the catalysts studied, 5% Ni Ce_(0.6)Zr_(0.4)O_2 was found to be the best catalyst as activity was stable for up to 100 h at 650 and 700 ℃, while at 800 ℃ the catalyst activity remained stable for more than 200 h.
机译:在多种ZrO_2-,二氧化铈掺杂的ZrO_2-和CeO_2-ZrO_2负载的Ni催化剂上研究了甲烷的二氧化碳重整(CDRM)。使用了不同的技术来制备具有不同物理化学性质的载体材料,并且建立了相关性以显示坚固的载体材料的重要性。催化剂的各种特征进一步确定了催化剂的焦化行为取决于载体制备技术。与氧化锆和掺杂二氧化铈的氧化锆相比,发现使用二氧化铈-氧化锆(Ce_xZr(1-x)O_2)固溶体作为通过使用表面活性剂制备的载体对低温CDRM最稳定。似乎在具有ZrO_2的系统中,抑制导致碳沉积的反应尤为突出。程序升温氧化(TPO)实验表明,与其他研究的催化剂相比,负载在Ce_xZr_(1-x)O_2上的Ni具有极好的抗碳形成能力。 H_2-TPR(程序升温还原)分析还显示,与纯二氧化铈或二氧化铈掺杂的ZrO_2相比,Ce_xZr_(1-x)O_2固溶体的稳定性是其在较低温度下还原性增强的函数。根据所有研究的催化剂,发现5%Ni Ce_(0.6)Zr_(0.4)O_2是最好的催化剂,因为在650和700℃时,其活性在100 h内稳定,而在800℃时,其活性则保持稳定。超过200小时。

著录项

  • 来源
    《Energy & fuels》 |2007年第6期|p.3113-3123|共11页
  • 作者单位

    Hydrogen Production Research Group, Process Systems Engineering, Faculty of Engineering, University of Regina, Regina, SK, Canada S4S 0A2, and HTC Pure Energy, #001, 2305 Victoria Avenue, Regina, SK, Canada S4P 0S7;

  • 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 TK-;
  • 关键词

  • 入库时间 2022-08-18 00:42:55

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