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首页> 外文期刊>Applied Catalysis, B. Environmental: An International Journal Devoted to Catalytic Science and Its Applications >CO removal from realistic methanol reformate via preferential oxidation- performance of a Rh/MgO catalyst and comparison to Ru/gamma-Al_2O_3
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CO removal from realistic methanol reformate via preferential oxidation- performance of a Rh/MgO catalyst and comparison to Ru/gamma-Al_2O_3

机译:通过Rh / MgO催化剂的优先氧化性能从现实的甲醇重整产品中去除CO并与Ru /γ-Al_2O_3进行比较

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The performance of a 0.5 wt.% Rh/MgO catalyst for the oxidative removal of CO from H2-rich methanol reformate (1% CO,65% H2,10% H_2O,rest CO_2) was investigated and compared to that of a conventional 0.5 wt.% Pt/gamma-Al_2O_3 catalyst and a 5 wt.% Ru/gamma-Al_2O_3 catalyst.Temperature screening experiments and 10-30h activity measurements reveal a high activity and selectivity in the temperature region between 175 and 300 deg C,in combination with a relatively low deactivation.Water vapor in the feed gas (< 10%) has little effect on the reaction characteristics.The low activity for the reverse water gas shift (RWGS) reaction,whose rate is more than four orders of magnitude lower than the rate for CO oxidation,and for the methanation reaction at temperatures below 300 deg C allow to operate Rh/MgO at higher temperatures,around 250 deg C,while for Pt/gamma-Al_2O_3 and Ru/gamma-Al_2O_3 the reaction temperatures are limited to 200 and 150 deg C,respectively,due to the decrease in selectivity (Pt/gamma-Al_2O_3) and the onset of the methanation reaction (Ru/gamma-Al_2O_3) at higher temperatures.Model calculations,using kinetic data measured in realistic reformate,predict that the minimum amount of noble metal required for the complete removal of CO from the feed gas (< 10 ppm) is by two orders of magnitude lower for Rh/MgO operated at 250 C than for Pt/gamma-Al_2O_3 and Ru/gamma-Al_2O_3 catalysts at 200 and 150 deg C,respectively,at a comparable O_2 excess.Due to the low RWGS activity the CO exit concentration does not increase significantly above the tolerance limit of state-of-the-art Pt-Ru fuel cell anodes of 100 ppm under dynamic load conditions,down to 1% load.For the other two catalysts the CO exit concentration are significantly higher under these conditions,reaching values above 500ppm for Ru/gamma-Al_2O_3 at 1% load and the WGS equilibrium value of 2000ppm for Pt/gamma-Al_2O_3.The predictions are verified by measurements in a microreactor under similar reaction conditions.The reaction characteristics make Rh/MgO an ideal PROX catalyst for reaction at higher temperatures (250 deg C),in particular for applications requiring highly dynamic operation under variable load conditions.
机译:研究了0.5 wt。%Rh / MgO催化剂从富氢重整甲醇(1%CO,65%H2、10%H_2O,剩余CO_2)中氧化去除CO的性能,并将其与常规0.5 wt。%Pt /γ-Al_2O_3催化剂和5 wt。%Ru / gamma-Al_2O_3催化剂。温度筛选实验和10-30h活性测量表明,在175至300摄氏度的温度范围内,具有很高的活性和选择性进料气中的水蒸气(<10%)对反应特性的影响很小。逆向水煤气变换(RWGS)反应的活性较低,其速率比反应气速率低四个数量级以上CO氧化速率以及低于300℃的甲烷化反应可在更高的温度(约250℃)下操作Rh / MgO,而对于Pt /γ-Al_2O_3和Ru /γ-Al_2O_3,反应温度受到限制由于选择降低,分别达到200和150摄氏度ty(Pt / gamma-Al_2O_3)和甲烷化反应的开始(Ru / gamma-Al_2O_3)。模型计算,使用在实际重整产物中测得的动力学数据,可以预测完全去除所需的最少贵金属量在250°C下操作的Rh / MgO的原料气中的CO含量(<10 ppm)比在200和150℃下的Pt /γ-Al_2O_3和Ru /γ-Al_2O_3催化剂分别降低两个数量级由于RWGS活性低,CO出口浓度不会在动态负载条件下(最先进的Pt-Ru燃料电池阳极在动态负载条件下达到100 ppm的公差极限)内不会显着增加对于其他两种催化剂,在这些条件下的CO出口浓度明显更高,Ru /γ-Al_2O_3在1%的负载下达到500ppm以上的值,Pt /γ-Al_2O_3的WGS平衡值达到2000ppm。相似反应下在微反应器中的测量c反应特性使Rh / MgO成为在更高温度(250摄氏度)下反应的理想PROX催化剂,特别是对于要求在可变负载条件下进行高动态操作的应用。

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