微型反应器
过氧化氢
分解
化学
间歇式反应器
催化作用
停留时间(流体动力学)
化学工程
传质
热分解
化学分解
溶剂
氢
有机化学
色谱法
岩土工程
工程类
作者
Bing Sun,Hongwei Zhu,Jin Yan,Kun Qiao,Wei Xu,Jie Jiang
标识
DOI:10.1002/ceat.201800319
摘要
Abstract The rapid decomposition of hydrogen peroxide (H 2 O 2 ) is often desired in the cleanup of excess H 2 O 2 when it is used as an oxidant. Although the decomposition process has been studied in batch reactors, it has never been performed before in a fixed‐bed microreactor with residence time on the scale of seconds. With enhanced mass and heat transfer in microreactors, higher H 2 O 2 decomposition efficiency compared to batch reactors was obtained. A variety of parameters including length of microchannels, flow rate, solvent composition, and gas pressure were examined carefully and a first‐order kinetic model was established. Within a few seconds, more than 70 % of the H 2 O 2 was decomposed successfully. The challenge of catalyst passivation was discussed as well.
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