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Continuous Taylor-flow microreactors

The Taylor-flow microreactor comprised a micromixer for mixing of the precursors for the particle synthesis followed by a gas inlet for separating this continuous mixed liquid stream into segments separated by gas bubbles [328,329]. [Pg.178]

Two classes of gas-liquid microchannel reactors were developed in the past years -continuous-phase contacting falling film, overlapping charmel, mesh, and annular flow approaches, and dispersed-phase contacting by Taylor flow reactors, micromixers for bubble and foam formation, and miniaturized packed bed microreactors, which follow classical trickle-bed operation at smaller scale. Recently integration of operations inside a microdevice has been studied and led to the development of membrane microreactors. [Pg.282]


See other pages where Continuous Taylor-flow microreactors is mentioned: [Pg.139]    [Pg.145]    [Pg.147]    [Pg.178]    [Pg.221]    [Pg.229]    [Pg.295]    [Pg.2483]    [Pg.1514]    [Pg.232]   
See also in sourсe #XX -- [ Pg.232 , Pg.233 , Pg.234 , Pg.235 , Pg.236 ]




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