首页> 外文期刊>Journal of Membrane Science & Technology >Modelisation of Membrane Distillation: Mass and Heat Transfer in Air Gap Membrane Distillation
【24h】

Modelisation of Membrane Distillation: Mass and Heat Transfer in Air Gap Membrane Distillation

机译:膜蒸馏的模型化:气隙膜蒸馏中的传质和传热

获取原文
           

摘要

Membrane distillation (MD) is receiving recent attention as a technique to efficiently concentrate aqueous solution such as seawater. It has potential benefits of low temperature and pressure operation with high degrees of separation. In this work, the effect of the membrane thickness was studied to produce of the steam flow in the three different mass transfer mechanisms, and in the different possible combinations of its mechanisms in three different temperatures. The results have been carried using a polynomial approximation through MATLAB. A quite important increase in the flow in the model (DGM, Schofield, and KMPT) was observed with a decrease in the stream rating in the model (KMT). However, the Molecular model, DGM model, KMPT model, and Schofield model are not affected by the membrane’s thickness. After, we have studied the effect of this parameter (Thickness of the membrane) on the transfer of conduction heat and latent heat.
机译:膜蒸馏(MD)作为一种有效浓缩水溶液(如海水)的技术正受到近期关注。它具有低温和高分离度操作的潜在优势。在这项工作中,研究了膜厚度的影响,以在三种不同的传质机理中以及在三种不同的温度下以其机理的不同可能组合产生蒸汽流。结果是通过MATLAB使用多项式逼近法得出的。观察到模型(DGM,Schofield和KMPT)中的流量有非常重要的增加,而模型(KMT)中的流量却降低了。但是,分子模型,DGM模型,KMPT模型和Schofield模型不受膜厚度的影响。之后,我们研究了该参数(膜的厚度)对传导热和潜热传递的影响。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号