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Porous Media For Catalytic Renewable Energy Conversion

机译:多孔介质用于催化可再生能源转换

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A novel flow-based method is presented to place catalytic nanoparticles into a reactor by sol-gelation of a porous ceramic consisting of copper-based nanoparticles, silica sand, ceramic binder, and a gelation agent. This method allows for the placement of a liquid precursor containing the catalyst into the final reactor geometry without the need of impregnating or coating of a substrate with the catalytic material. The so generated foam-like porous ceramic shows properties highly appropriate for use as catalytic reactor material, e.g., reasonable pressure drop due to its porosity, high thermal and catalytic stability, and excellent catalytic behavior. The catalytic activity of micro-reactors containing this foam-like ceramic is tested in terms of their ability to convert alcoholic biofuel (e.g. methanol) to a hydrogen-rich gas mixture with low concentrations of carbon monoxide (up to 75% hydrogen content and less than 0.2% CO, for the case of methanol). This gas mixture is subsequently used in a low-temperature fuel cell, converting the hydrogen directly to electricity. A low concentration of CO is crucial to avoid poisoning of the fuel cell catalyst. Since conventional Polymer Electrolyte Membrane (PEM) fuel cells require CO concentrations far below 100 ppm and since most methods to reduce the mole fraction of CO (such as Preferential Oxidation or PROX) have CO conversions of up to 99%, the alcohol fuel reformer has to achieve initial CO mole fractions significantly below 1%. The catalyst and the porous ceramic reactor of the present study can successfully fulfill this requirement.
机译:提出了一种新颖的基于流的方法由多孔陶瓷组成的铜基纳米颗粒,硅砂,陶瓷粘合剂,和一种凝胶剂的溶胶 - 凝胶化催化纳米颗粒放入一个反应器中。这种方法允许含有催化剂成最终反应器的几何形状,而不需要浸渍或与所述催化材料的基材的涂层的液体前体的放置。这样产生的泡沫状,由于其多孔性,高的热和催化稳定性,和优良的催化行为高度适合用作催化反应器材料,例如合理压降多孔陶瓷节目属性。含有该微反应器的催化活性泡沫状陶瓷在其转化醇的生物燃料的能力方面(例如甲醇)与低浓度的一氧化碳(高达75%的氢含量和更低的富含氢的气体混合物被测试大于0.2%的CO,甲醇的情况下)。该气体混合物在低温燃料电池随后使用的,氢直接转换为电。 CO的低浓度是为了在燃料电池用催化剂的以免中毒是至关重要的。由于常规的聚合物电解质膜(PEM)燃料电池需要的CO浓度远低于100ppm和因为大多数方法来降低CO的摩尔分数(如选择性氧化或PROX)具有最多的CO转化率至99%,所述醇燃料重整具有实现显著低于1%的初始CO摩尔分数。催化剂和本研究中的多孔陶瓷反应器能够成功地满足这一要求。

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