Ramachandran, P. A. ; Mashelkar, R. A. (1976) Homogeneous reactions in turbulent pipe flows Chemical Engineering Journal, 11 (1). pp. 73-76. ISSN 1385-8947
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Official URL: http://linkinghub.elsevier.com/retrieve/pii/030094...
Related URL: http://dx.doi.org/10.1016/0300-9467(76)80008-1
Abstract
The turbulent pipe flow reactor analysis of Randhava and Wasan is shown to be in error. An alternative axial dispersion model estimation is provided where the axial dispersion coefficient has been evaluated from a Taylor dispersion analysis. The present work shows that the departure of a turbulent flow reactor from plug flow is likely to be negligible except for rapid gas phase reactions. The influence of non-linear kinetics, non-Newtonian flow behaviour and coiling is assessed.
| Item Type: | Article |
|---|---|
| Source: | Copyright of this article belongs to Elsevier Science. |
| ID Code: | 22292 |
| Deposited On: | 23 Nov 2010 08:49 |
| Last Modified: | 06 Jun 2011 10:46 |
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