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Hydrogen Generation Using a CuO/ZnO-ZrO2 Nanocatalyst for Autothermal Reforming of Methanol in a Microchannel Reactor

机译:使用CuO / ZnO-ZrO2纳米催化剂在微通道反应器中自动热重整甲醇制氢

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In the present work, a microchannel reactor for autothermal reforming of methanol using a synthesized catalyst porous alumina support-CuO/ZnO mixed with ZrO2 sol washcoat has been developed and its fine structure and inner surface characterized. Experimentally, CuO/ZnO and alumina support with ZrO2 sol washcoat catalyst (catalyst slurries) nanoparticles is the catalytically active component of the microreactor. Catalyst slurries have been dried at 298 K for 5 h and then calcined at 623 K for 2 h to increase the surface area and specific pore structures of the washcoat catalyst. The surface area of BET N2 adsorption isotherms for the as-synthesized catalyst and catalyst/ZrO2 sol washcoat samples are 62 and 108 ± 2 m~2g~(-1), respectively. The intensities of Cu content from XRD and XPS data indicate that Al2O3 with Cu species to form CuAl2O4. The EXAFS data reveals that the Cu species in washcoat samples have Cu-O bonding with a bond distance of 1.88 ± 0.02 A and the coordination number is 3.46 ± 0.05, respectively. Moreover, a hydrogen production rate of 2.16 L h~(-1) is obtained and the corresponding methanol conversion is 98% at 543 K using the CuO/ZnO with ZrO2 sol washcoat catalyst.
机译:在目前的工作中,已经开发了一种微通道反应器,其使用混合有ZrO2溶胶修补基面涂层的合成的催化剂多孔氧化铝载体-CuO / ZnO进行甲醇的自热重整,其微结构和内表面具有特征。实验上,具有ZrO2溶胶修补基面涂层催化剂(催化剂浆料)纳米粒子的CuO / ZnO和氧化铝载体是微反应器的催化活性组分。催化剂浆料已在298 K下干燥5小时,然后在623 K下煅烧2小时,以增加载体涂料催化剂的表面积和比孔结构。合成后的催化剂和催化剂/ ZrO2溶胶修补基面涂层样品的BET N2吸附等温线的表面积分别为62和108±2 m〜2g〜(-1)。 XRD和XPS数据中的Cu含量强度表明Al2O3与Cu形成CuAl2O4。 EXAFS数据表明,修补基面涂层样品中的Cu种类具有Cu-O键,键距为1.88±0.02 A,配位数为3.46±0.05。此外,使用CuO / ZnO和ZrO2溶胶修补基面涂层催化剂,制氢速率为2.16 L h〜(-1),相应的甲醇转化率在543 K下为98%。

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