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Kinetics of Hydrogen Peroxide Synthesis in a Microreactor by Direct Combination of Oxygen and Hydrogen

机译:氧气和氢气直接组合微反应器中过氧化氢合成的动力学

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Hydrogen peroxide was formed in a packed-bed microreactor in a three-phase process involving the direct combination (DC) of hydrogen and oxygen over a solid catalyst in the presence of a liquid solvent. Hydrogen and air were combined in all proportions, including explosive regime, over a platinum group catalyst supported on an oxide. The DC process comprises multiple reactions involving formation of hydrogen peroxide, parallel formation of water, hydrogen peroxide reduction by hydrogen, and decomposition by disproportionation. Synthesis of hydrogen peroxide was conducted at conditions where the selectivity for H202 was 100%, so that all reactions except for H_2O_2 synthesis could be neglected. A Langmuir-Hinshelwood rate expression for the synthesis of hydrogen peroxide was determined as part of a program to determine the overall kinetics of hydrogen peroxide formation.
机译:在填充床微反应器中形成过氧化氢,其三相过程中涉及在液体溶剂存在下在固体催化剂上通过固体催化剂的直接组合(DC)和氧的直接组合(DC)。在所有比例中合并氢气和空气,包括爆炸性制度,在氧化物上负载的铂族催化剂。 DC方法包括涉及形成过氧化氢,水,过氧化氢的平行形成的多种反应,并通过歧化分解。在H202的选择性为100%的条件下进行过氧化氢的合成,从而可以忽略除H_2O_2合成之外的所有反应。将过氧化氢合成的Langmuir-hinshelwood率表达被确定为确定过氧化氢形成的整体动力学的程序的一部分。

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