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Selective hydrogen combustion in the presence of propylene and propane over Pt/A-zeolite catalysts

机译:在Pt / A-沸石催化剂上存在丙烯和丙烷存在下的选择性氢气燃烧

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摘要

The behavior of selective hydrogen combustion (SHC) in the presence of propylene and propane changing with reaction temperature in a range of 100-600 degrees C has been investigated over the Pt catalysts supported on A- zeolites. The effect of Pt loading varying from 0.01 to 2 wt% on the catalytic SHC performance has been studied in the conditions with a feed gas molar composition of C3H8/C3H6/H-2/O-2 = 4/4/4/2 balanced with N-2 and gas hourly space velocity of 15,000 h(-1). The results show that for each Pt/3A catalyst having a different Pt loading there is a maximum of H-2 conversion by combustion appearing between 300 and 400 degrees C, while the selectivity to comprehensive H-2 conversion can maintain 100% when the temperature lower than 300 degrees C. Moreover, the Pt/3A catalyst with a Pt loading of 0.5 wt % performs better than the others at the temperatures higher than 300 degrees C. The maximal H-2 combustion achieved over the 0.5 wt% Pt/3A catalyst is as high as 96.6% along with a selectivity of 100% at 300 degrees C, and a 92.4% H-2 combustion with 98.5% selectivity can be obtained even if at 500 degrees C. The characterization of the catalysts reveals that the distribution of Pt atoms and the number of atoms in Pt clusters may be the key factors for giving rise to the good SHC performance. The influence of three types of A-zeolite supports on the Pt catalyzed SHC process has also been investigated. 3A zeolite is superior to 4A and 5A for supporting 0.5 wt% Pt catalyst in terms of both activity and selectivity. The lower C3H6 conversion on the 0.5 wt% Pt/3A catalyst compared to the 0.5 wt% Pt/5A may be ascribed to the insufficient sites for the C3H6 activation on the surface of Pt/3A due to the limitation of 3A channels inaccessible to C3H6 This contrarily brings about the better SHC performance on the 0.5 wt% Pt/3A catalyst. (C) 2020 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:在α-沸石上负载的Pt催化剂上研究了选择性氢气燃烧(SHC)在丙烯存在下在100-600℃的反应温度下改变的反应温度。在C3H8 / C3H6 / H-2 / O-2 = 4/4 / 4/2平衡的情况下,已经研究了在催化SHC性能下的0.01至2wt%的Pt加载在催化性SHC性能下的影响N-2和燃气小时空间速度为15,000小时(-1)。结果表明,对于具有不同Pt加载的每个Pt / 3a催化剂,通过燃烧,最大的H-2转化出现在300至400℃之间,而在温度时,对综合的H-2转化率的选择性可以保持100%此外,Pt / 3a催化剂的Pt / 3a催化剂0.5wt%的Pt / 3a催化剂比其他温度高于300℃的催化剂更好。在0.5wt%pt / 3a上实现的最大H-2燃烧催化剂高达96.6%,选择性为100%,300℃,即使在500℃下,也可以获得92.4%的H-2燃烧,其选择性为98.5%选择性。催化剂的表征揭示了分布PT簇中的Pt原子和原子数可能是引起良好SHC性能的关键因素。还研究了三种类型的α-沸石载体对Pt催化的SHC工艺的影响。 3A沸石优于4A和5A,用于在活性和选择性方面支持0.5wt%Pt催化剂。与0.5wt%pt / 5a相比的0.5wt%pt / 3a催化剂上的下部C3H6转化可以归因于Pt / 3a表面上的C3H6活化的不足位点,因为C3H6的3A通道的限制为Pt / 3a的表面这相反,在0.5wt%pt / 3a催化剂上提出了更好的SHC性能。 (c)2020氢能源出版物LLC。 elsevier有限公司出版。保留所有权利。

著录项

  • 来源
    《International journal of hydrogen energy》 |2020年第22期|12347-12359|共13页
  • 作者单位

    East China Univ Sci & Technol State Key Lab Chem Engn Shanghai 200237 Peoples R China;

    East China Univ Sci & Technol State Key Lab Chem Engn Shanghai 200237 Peoples R China;

    East China Univ Sci & Technol State Key Lab Chem Engn Shanghai 200237 Peoples R China;

    East China Univ Sci & Technol State Key Lab Chem Engn Shanghai 200237 Peoples R China;

    East China Univ Sci & Technol State Key Lab Chem Engn Shanghai 200237 Peoples R China;

    East China Univ Sci & Technol State Key Lab Chem Engn Shanghai 200237 Peoples R China;

  • 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

    Selective hydrogen combustion; Propylene and propane; Pt catalyst; A-zeolite; Pt loading; Support;

    机译:选择性氢气燃烧;丙烯和丙烷;Pt催化剂;沸石;Pt加载;支持;
  • 入库时间 2022-08-18 22:24:08

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