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Radial mixing, pipeline flow

FIGURE 35 Pipeline flow showing that time-interval mixing normally must have a volume for retention time, compared to radial flow with usual static mixer elements. [Pg.300]

The process result of heat transfer is a heat transfer coefficient. For dispersion it is a drop or particle size and size distribution. For blending in tanks it is blend time to achieve a certain degree of mixing. The equivalent for mixing in pipeline flow is not as clear. Alloca and Streiff (1980) proposed using a radial coefficient of variation, and this concept is now widely accepted. Since it is unique in the process industries to pipeline flow, it merits some extended discussion. [Pg.410]

See other pages where Radial mixing, pipeline flow is mentioned: [Pg.661]    [Pg.36]    [Pg.329]    [Pg.486]    [Pg.52]    [Pg.809]    [Pg.682]    [Pg.337]    [Pg.817]    [Pg.665]    [Pg.409]    [Pg.409]    [Pg.409]    [Pg.411]    [Pg.413]    [Pg.415]    [Pg.417]    [Pg.417]    [Pg.329]    [Pg.156]    [Pg.62]    [Pg.106]    [Pg.553]   
See also in sourсe #XX -- [ Pg.2 , Pg.409 , Pg.410 , Pg.412 ]



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