首页> 外文期刊>Applied Catalysis, B. Environmental: An International Journal Devoted to Catalytic Science and Its Applications >The effect of La~(3+)-doping of CeO2 support on the water-gas shift reaction mechanism and kinetics over Pt/Ce_(1-x)La_xO_(2-δ)
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The effect of La~(3+)-doping of CeO2 support on the water-gas shift reaction mechanism and kinetics over Pt/Ce_(1-x)La_xO_(2-δ)

机译:La〜(3+)掺杂CeO2载体对Pt / Ce_(1-x)La_xO_(2-δ)上水煤气变换反应机理和动力学的影响

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摘要

Platinum nanoparticles (d_(Pt) = 1.0-1.2nm) supported on single CeC>2 and La2O3 metal oxides and Ce_(0.8)La_(0.2)O_(2-δ) solid solution were prepared to investigate for the first time the effect of La~(3+)-doping of ceria on important mechanistic and kinetic aspects of the water-gas shift (WGS) reaction, namely: (i) the concentration and chemical structure of active adsorbed reaction intermediates present in the C-path and H-path of WGS at 250 and 300 °C, (ii) the chemical nature of inactive species formed during WGS, and (iii) the prevailing mechanistic path among "redox" and "associative" both proposed in the literature. For this, steady-state isotopic transient kinetic analysis (SSITKA) experiments coupled with in situ DRIFTS and mass spectrometry were performed to follow the H-path (use of D2O) and C-path (use of ~(13)CO) of the WGS. In addition, other transient isotopic experiments using operando methodology (use of DRFTS and mass spectrometry) were designed to follow with time on stream the reactivity toward water of the various adsorbed species formed under WGS. It is proposed that on Pt/Ce_(1-x)La_xO_(2-δ) (x=0.0, 0.2 and 1.0) the WGS reaction follows both the "redox" and "associative" mechanisms but the extent of participation of each mechanism to the overall WGS reaction rate depends on the support chemical composition. The WGS kinetic rate (μmol CO g~(-1) s~(-1)) increased by a factor of 2.0 and 2.8 at 300°C on 0.5 wt% Pt supported on Ce_(0.8)La_(0.2)o_(2-δ) compared to CeO2 and La2O3, respectively. This was explained by (i) the larger concentration of active surface intermediates formed around each Pt nanoparticle (larger extent of reactive zone) and (ii) the higher reactivity of sites (k, s~(-1)) responsible for CO2 and H2 formation on Pt/Ce_(0.8)La_(0.2)o_(2-δ) compared to Pt/CeO2 and Pt/La2O3. Active —OH groups is suggested to be formed on defect sites (Ce~(3+)—□_s) of Ce_(0.8)La_(0.2)o_(2-δ) as a consequence of the introduction of La~(3+) into the ceria lattice, the latter enhancing the concentration of labile oxygen and its surface mobility, important characteristics of the "redox" mechanism.
机译:制备了负载在单一CeC> 2和La2O3金属氧化物上的铂纳米粒子(d_(Pt)= 1.0-1.2nm)和Ce_(0.8)La_(0.2)O_(2-δ)固溶体以首次研究其效果二氧化铈的La〜(3+)掺杂对水煤气变换(WGS)反应的重要机理和动力学方面的影响,即:(i)C路径中存在的活性吸附反应中间体的浓度和化学结构,以及WGS在250和300°C时的H路径,(ii)WGS期间形成的非活性物质的化学性质,和(iii)文献中提出的“氧化还原”和“缔合”之间的主要机理路径。为此,进行了稳态同位素瞬态动力学分析(SSITKA)实验,原位DRIFTS和质谱分析,以追踪H-路径(使用D2O)和C-路径(使用〜(13)CO)。 WGS。此外,还设计了使用操作方法(使用DRFTS和质谱法)的其他瞬态同位素实验,以随着时间的流逝跟踪在WGS下形成的各种吸附物质对水的反应性。建议在Pt / Ce_(1-x)La_xO_(2-δ)(x = 0.0、0.2和1.0)上,WGS反应遵循“氧化还原”和“缔合”机制,但每种机制的参与程度总的WGS反应速率取决于载体的化学组成。在负载于Ce_(0.8)La_(0.2)o_(2)上的0.5 wt%Pt上,在300°C下,WGS动力学速率(μmolCO g〜(-1)s〜(-1))增加了2.0和2.8倍。 -δ)分别与CeO2和La2O3比较。这可以通过以下方式解释:(i)每个Pt纳米粒子周围形成的活性表面中间体的浓度较高(反应区的范围更大),以及(ii)负责CO2和H2的位点(k,s〜(-1))的反应性较高与Pt / CeO2和Pt / La2O3相比,在Pt / Ce_(0.8)La_(0.2)o_(2-δ)上的生成。由于引入了La〜(3+),建议在Ce_(0.8)La_(0.2)o_(2-δ)的缺陷位点(Ce〜(3 +)-□_s)上形成活性-OH基。 )进入二氧化铈晶格,后者增强了不稳定氧的浓度及其表面迁移率,这是“氧化还原”机理的重要特征。

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