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Segmented flow gas-liquid-solid reactors

In segmented flow gas-liquid-solid reactors, the hquid usually flows over the sohd surface while the gas flows through the hquid in the form of bubbles or annular flow (see Figure 8.4), depending on the MSR geometry and the catalyst arrangement. [Pg.335]

Kreutzer, M.T. et al. (2005) Multiphase monolith reactors chemical reaction engineering of segmented flow in microchannels. 7th International Conference on Gas-Liquid and Gas-Liquid-Solid, 2005,... [Pg.356]

Both reactor types R3 and R4 use the segmented flow (Taylor) principle. They are divided into two categories R3 has very small channels (<1 mm) and R4 are monolith reactors (honeycomb), well developed on the laboratory scale with at least one example of industrial application. Category R3 includes single-channel and multi-ple-channel reactors [10], etched in silicon [10] or glass [10,11], with wall-coated or immobilized catalysts in the case of gas-liquid-solid additions [12], and capillary microreactors for gas-liquid-liquid systems [13]. [Pg.661]


See other pages where Segmented flow gas-liquid-solid reactors is mentioned: [Pg.54]    [Pg.54]    [Pg.172]    [Pg.902]    [Pg.421]    [Pg.657]    [Pg.448]    [Pg.488]   
See also in sourсe #XX -- [ Pg.340 ]

See also in sourсe #XX -- [ Pg.38 ]




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Flow gas flows

Flow liquid flows

Flowing solids

Gas liquid solid flow

Gas-liquid flow

Gas-liquid reactors

Gas-solid flow

Liquid reactors

Liquid segments

Segmented flow

Segmented reactor

Solid gas liquid

Solids flow

Solids—liquid flow

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