Please use this identifier to cite or link to this item: https://doi.org/10.1016/j.apcata.2006.10.038
Title: Evaluation of multiphase microreactors for the direct formation of hydrogen peroxide
Authors: Wang, X.
Nie, Y. 
Lee, J.L.C.
Jaenicke, S. 
Keywords: Heterogeneous catalysis
Hydrogen peroxide
Microreactor
Multi-phase flow
Pd-Pt bimetallic catalysts
Taylor flow
Issue Date: 7-Feb-2007
Source: Wang, X., Nie, Y., Lee, J.L.C., Jaenicke, S. (2007-02-07). Evaluation of multiphase microreactors for the direct formation of hydrogen peroxide. Applied Catalysis A: General 317 (2) : 258-265. ScholarBank@NUS Repository. https://doi.org/10.1016/j.apcata.2006.10.038
Abstract: The direct production of hydrogen peroxide from H2 and O2 has been investigated in two types of microreactors: (1) a single-channel microreactor with a washcoat of catalyst and (2) a multichannel microreactor with eight parallel channels, where the catalyst was grown as a thin film. The multichannel microreactor mimics features of a monolith reactor, where the catalyst is contained in a structured honeycomb. The Taylor (slug) flow in a microchannel reactor under three phase (gas-liquid-solid) conditions enhances the mass transfer over the phase boundaries. The influence of liquid and gas flow rate, pressure drop, solvents, support materials and metal dispersion on the reaction were investigated in order to screen for optimal operation conditions. The productivity in the microchannel reactors increases approximately with the square root of the liquid flow rate, verifying the Taylor-flow model. © 2006 Elsevier B.V. All rights reserved.
Source Title: Applied Catalysis A: General
URI: http://scholarbank.nus.edu.sg/handle/10635/93775
ISSN: 0926860X
DOI: 10.1016/j.apcata.2006.10.038
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