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Fluidized beds flow regimes, heating process

In general, nonuniform structures, in both time and space, is widespread in bubbling, turbulent, and fast fluidization regimes. On the one hand, such nonuniformity can enhance the mass and heat transfer of a bed. On the other hand, it decreases the contact efficiency of gas and solids and makes the scale-up rather difficult. Internals are usually introduced not to eliminate the nonuniform flow structure completely but to control its effect on chemical reactions. The function of internals varies in different fluidization regimes, as do the types and parameters of internals. Taking these purposes into consideration, internals may be successfully applied to catalytic reactors with high conversion and selectivity, and some other physical processes. [Pg.184]


See other pages where Fluidized beds flow regimes, heating process is mentioned: [Pg.456]    [Pg.573]    [Pg.405]    [Pg.69]    [Pg.713]    [Pg.82]    [Pg.328]    [Pg.345]    [Pg.118]    [Pg.1018]    [Pg.236]   
See also in sourсe #XX -- [ Pg.227 , Pg.228 ]




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Flow regimes

Fluidization processes

Fluidization regime

Fluidized Bed Processing

Fluidized bed process

Fluidized beds flow regimes

Fluidized beds heating process

Fluidized process

Fluidized regimes

Heat processes

Process flow

Process flow processing

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