A unified treatment of the inlet boundary condition for dispersive flow models
β Scribed by Cha Y. Choi; D.D. Perlmutter
- Publisher
- Elsevier Science
- Year
- 1976
- Tongue
- English
- Weight
- 217 KB
- Volume
- 31
- Category
- Article
- ISSN
- 0009-2509
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β¦ Synopsis
The justification of boundary conditions for a tubular reactor requires some particular care in the case where the reactor model includes a dispersion term to account for axial mixing: $ Llg -u+o. ( ) Following the pioneer work of Danckwertz[l], the boundary condition at the inlet position was examined by Pearson[2], Bischoff[3], Wehner and Wilhelm[rl], and Kershenbaum and Perkins [S]. The consensus is that a proper condition at y = 0 is: dC -%=I@,-C); y=o+.
(2)
However, as detailed in Table 1, the underlying assumptions that lead to this result are quite varied and appear in some aspects to be inconsistent. In their recent review of the subject Karantb and Hughes [6] conclude that "a completely satisfactory
π SIMILAR VOLUMES
The aim of this article is to describe the development of a mathematical model for the simulation of the flow of polymer melts inside internal mixers. The rheological behavior of the polymeric fluid is assumed to be described by the Carreau equation. The flow regime is considered to be non-isotherma