International Journal of Energy Science and Engineering
Articles Information
International Journal of Energy Science and Engineering, Vol.1, No.2, May 2015, Pub. Date: Apr. 22, 2015
Heat-Mass Transfer in a Tubular Chemical Reactor
Pages: 49-59 Views: 4787 Downloads: 3227
Authors
[01] Rehena Nasrin, Department of Mathematics, Bangladesh University of Engineering& Technology, Dhaka-1000, Bangladesh.
Abstract
This paper analyzes numerically the effect of double-diffusive forced convection of fluid in a tubular chemical reactor. The model provides a study of an elementary, exothermic, 2nd-order reversible reaction in a tubular reactor (liquid phase, laminar flow regime). The aim of this project is to study numerically the effect of convective Heat and Mass transfer flow of a viscous fluid in the reactor. Assuming that the variations in angular direction around the central axis are negligible makes it possible to reduce the model to a 2D axisymmetric model. The governing equations namely mass, momentum, energy and material conservation equations are solved by Finite Element Method using Galerkin’s weighted residual scheme. The effects of rate of reaction and heat of reaction on the flow pattern and heat and mass transfer have been depicted. Comprehensive average Nusselt and Sherwood numbers, average temperature and concentration and mean subdomain velocity of the tubular reactor are presented as functions of the governing parameters mentioned above. Code validation is also shown with the results available in the literature.
Keywords
Tubular Reactor, Heat-Mass Transfer, Finite Element Method
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