Article ID Journal Published Year Pages File Type
146203 Chemical Engineering Journal 2015 10 Pages PDF
Abstract

•We prepared microreactor with parallel packed beds for H2–O2 reaction to H2O2.•Maldistribution of reaction fluid was overcome to promote reaction performance.•We were also successful in parallel reactor operation to promote productivity.

We designed and fabricated a microreactor with paralleled packed beds suitable for the direct synthesis of hydrogen peroxide from hydrogen and oxygen. The reactor is based on microfluidic design for equal distribution of reaction fluids to each catalyst packed bed, which was validated by the reactor performance and gas- and liquid flow regime visualization. We extended the concept to parallel operation so that 1 kg/day of 4 wt% of hydrogen peroxide was produced by 4-reactor parallel operation. Our strategy gives an alternative opportunity to the scaling-up strategy of flow chemical process technology, by overcoming the fluid maldistribution problem in a gas–liquid and solid multiphase system.

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Related Topics
Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
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