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Effect of support composition on the origin and reactivity of carbon formed during dry reforming of methane over 5 wt% Ni/Ce1-xMxO2-delta (M = Zr4+, Pr3+) catalysts

机译:载体组成对在5 wt%Ni /Ce1-xMxO2-δ(M = Zr4 +,Pr3 +)催化剂上甲烷干重整过程中甲烷形成的碳的来源和反应性的影响

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Carbon dioxide reforming of methane to synthesis gas in the 550-750 degrees C range over 5 wt% Ni/Ce1-xMxO2-delta (M = Zr4+, Pr3+) solids has been investigated with respect to the effects of support chemical composition and reaction temperature on the amount, reactivity (towards H-2 and O-2) and relative contribution of CH4 and CO2 activation routes towards "carbon" formation. For these "carbon" characterisation studies, various transient isothermal and temperature-programmed oxidation (TPO) and hydrogenation (TPH) experiments coupled with the use of (CO)-C-13 and (CO2)-C-13 isotope gases were conducted. TPO following dry reforming (5%(CO2)-C-13/5%(CH4)-C-12/45%Ar/45%He) demonstrated that the relative amount of the various kinds of "carbon" formed via the CH4 and CO2 activation routes was strongly dependent on reaction temperature and support chemical composition. At 550 degrees C, the ratio of (CO2)-C-12 to (CO2)-C-13 of the C-12-containing and C-13-containing inactive "carbon" formed was 0.4, 0.27 and 0.19, whereas at 750 degrees C was 1.07, 1.06 and 0.29, respectively, for the 5 wt% Ni supported on Ce0.8Zr0.2O2, Ce-0.8 Pr0.2O2 and Ce0.5Zr0.5O2 carriers. The origin of "carbon" formation via the CO2 activation route was illustrated to be the Boudouard reaction (2CO-s -> CO2(g) + C-s + s) through a transient isotopic experiment with a feed gas containing (CO)-C-13 and (CH4)-C-12. It was also found that CO-s derived from the direct dissociation of CO2 and the CH4 activation route can lead to a number of different kinds of "carbon" which depends on support chemical composition. The present 5 wt% Ni/Ce0.8Pr0.2O2 catalytic system exhibited CO2 conversion of 84%, H-2-yield of 48%, and H-2/CO ratio of 1.04 after 50 h of dry reforming of methane at 750 degrees C (20% CH4, 20% CO2, He; GHSV = 30,000 h(-1)) with a relatively low amount (17.5 mg C/g(cat) or 1.75 wt%) of accumulated inactive "carbon". The support chemical composition was found to influence the nickel particle size, which in turn influenced the origin, kinetics and the reactivity of "carbon" deposition under dry reforming reaction conditions. (C) 2015 Elsevier B.V. All rights reserved.
机译:针对载体化学组成和反应温度的影响,已经研究了在550-750摄氏度范围内Ni /Ce1-xMxO2-δ(M = Zr4 +,Pr3 +)固体上将甲烷二氧化碳重整为合成气的方法量,对H-2和O-2的反应性以及CH4和CO2活化途径对“碳”形成的相对贡献。对于这些“碳”表征研究,进行了各种瞬态等温和程序升温氧化(TPO)和氢化(TPH)实验,以及使用(CO)-C-13和(CO2)-C-13同位素气体的实验。干重整后的TPO(5%(CO2)-C-13 / 5%(CH4)-C-12 / 45%Ar / 45%He)表明通过CH4形成的各种“碳”的相对量CO 2的活化途径在很大程度上取决于反应温度和化学成分。在550摄氏度下,形成的含C-12和含C-13的惰性“碳”的(CO2)-C-12与(CO2)-C-13的比率为0.4、0.27和0.19,而在对于负载在Ce0.8Zr0.2O2,Ce-0.8 Pr0.2O2和Ce0.5Zr0.5O2载体上的5 wt%Ni,750℃分别为1.07、1.06和0.29。通过使用含(CO)-C-的进料气的瞬时同位素实验,表明通过CO2活化途径形成“碳”的起源是Boudouard反应(2CO-s-> CO2(g)+ Cs + s)。 13和(CH4)-C-12。还发现源自CO 2的直接解离和CH 4活化途径的CO-可以导致多种不同种类的“碳”,这取决于载体的化学组成。在750度的甲烷干重整50小时后,当前的5 wt%Ni / Ce0.8Pr0.2O2催化体系显示出84%的CO2转化率,48%的H-2收率和1.04的H-2 / CO比。 C(20%CH4、20%CO2,He; GHSV = 30,000 h(-1)),且累积的非活性“碳”量相对较低(17.5 mg C / g(催化剂)或1.75 wt%)。发现载体化学组成会影响镍的粒径,进而影响干重整反应条件下“碳”沉积的来源,动力学和反应性。 (C)2015 Elsevier B.V.保留所有权利。

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