Mathematical modeling of reverse osmosis systems

被引:67
作者
Jamal, K
Khan, MA
Kamil, M [1 ]
机构
[1] Aligarh Muslim Univ, Dept Petr Studies, Aligarh 202002, Uttar Pradesh, India
[2] Aligarh Muslim Univ, Dept Post Harvest Engn & Technol, Aligarh 202002, Uttar Pradesh, India
关键词
mathematical modeling; reverse osmosis; mass transfer; inhibition; concentration polarization;
D O I
10.1016/S0011-9164(04)90015-X
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The present investigation pertains to modeling of seawater desalination system. A simulation model was developed and verified for a small-scale reverse osmosis system. The proposed model combines material balances on the feed tank, membrane Module and product tank with membrane mass transfer models. Finally a comprehensive simulation model has been developed incorporating the effect of mass transfer inhibition The model is non-linear differential equation representing the feed concentration as a function of operating time and space. The solution of the simultaneous differential equations was obtained using the fourth order Runge-Kutta method, due to self starting and stability. The model was verified using the experimental data from the literature [ 17,24]. Parameter sensitivity was carried out to select the proper step size. The simulation was run for over 1000 h enabling a prediction of operational performance at high overall system recoveries.
引用
收藏
页码:29 / 42
页数:14
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