کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
686979 1460116 2012 9 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Numerical simulation and theoretical study on simultaneously effects of operating parameters in direct contact membrane distillation
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی تکنولوژی و شیمی فرآیندی
پیش نمایش صفحه اول مقاله
Numerical simulation and theoretical study on simultaneously effects of operating parameters in direct contact membrane distillation
چکیده انگلیسی

Effect of operating conditions such as feed temperature, feed circulation rate and feed inlet concentration on permeate flux in a direct contact membrane distillation (DCMD) have been simulated. The effects of these parameters on both temperature and concentration polarizations have also been taken into account. A simultaneous heat and mass transfer model has been used in the DCMD system. The model has been solved numerically using MATLAB. Significances of the heat transfer due to mass flux, heat lost by conduction, as well as their contribution to the overall heat flux through the membrane have been determined. The variation of physical and flow properties with temperature and consequently heat transfer coefficients have been considered in this study. The influence of mass transfer on heat transfer coefficients and heat transfer rates has been considered in heat transfer equations. Finally, the simultaneously effects of the operating parameters on response variables have been studied.


► Interaction effects of operating parameters on permeate flux, temperature and concentration polarizations were simulated.
► The influence of mass transfer on the heat transfer coefficient was considered in this study.
► The feed temperature showed the most significant effect on temperature polarization compared to feed inlet concentration.
► The effect of temperature difference on temperature polarization was insignificant, compared to circulation velocity.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Chemical Engineering and Processing: Process Intensification - Volume 61, November 2012, Pages 42–50
نویسندگان
, , ,