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One-Dimensional Model with Axial Mixing

Accounting for the velocity profile is practically never done, because it immediately complicates the computation in a serious way. In addition, very few data are available to date and no general correlation could be set up for the velocity profile (Schwartz and Smith [85], Schertz and Bischoff [40], Cairns and Prausnitz [41], and Mickley et al. [42]). [Pg.527]

The steady-state continuity equation for a component A may be written  [Pg.527]

Axial mixing smoothens axial gradients of concentration and temperature so that it decreases the conversion obtained in a given reactor, in principle at least. [Pg.528]

The boundary conditions have given rise to extensive discussion [52, 53, 54, 55, 56]. Those generally used are  [Pg.528]

Luss later refined these conditions and arrived at [59] [Pg.530]


See other pages where One-Dimensional Model with Axial Mixing is mentioned: [Pg.525]    [Pg.491]   


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