Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
7055275 | International Journal of Heat and Mass Transfer | 2016 | 12 Pages |
Abstract
The purpose of this study is to develop a new method for analyzing the combined heat and mass transfer characteristics in laminar moist air flow inside vertical plate channels with falling water film evaporation. A two-dimensional computational fluid dynamics (2-D CFD) model is firstly utilized to simulate the laminar convection heat and mass transfer processes. Further, a one-dimensional (1-D) model is utilized to analyze the average Nusselt and Sherwood numbers based on the numerical results of the 2-D model. Thus, the 1-D model can be utilized to retrieve the 2-D model results. Furthermore, a similarity analysis is performed to reduce the original 2-D model equations into dimensionless forms so as to find out the minimum set of grouped dimensionless factors affecting the average Nusselt and Sherwood numbers. Finally, the effects of moist air inlet Reynolds number Reg, the ratio of water to moist air mass flow rate Rwg, the ratio of channel length to half channel width αL and moist air inlet dimensionless temperature θg,i on the average Nusselt and Sherwood numbers are examined in detail. By the detailed examination, it is found that larger average Nusselt and Sherwood numbers result from conditions with higher Rwg, Reg or θg,i values or lower αL values but larger average Lewis factors result from conditions with higher Rwg, αL or θg,i values or lower Reg values.
Keywords
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Fluid Flow and Transfer Processes
Authors
Chengqin Ren, Yangda Wan,