A NON-ISOTHERMAL PEMFC MODEL INCLUDING INTERFACE MASS TRANSFER WITHOUT EMPIRICAL COEFFICIENTS

摘要：

This study presents a 3D non-isothermal two-phase CFD model for a PEMFC with the simplified kinetics. The improved two-phase model includes a new submodel for interface mass transfer without empirical coefficients. The model predicts the cell performance, temperature and concentration profiles taking into account two-phase flow in anode and cathode channels. The main advantage of the new submodel is that evaporation and condensation processes are described without using empirical mass transfer coefficients. The model reflects the influence of various parameters on fuel cell performance including flow field design, porosity and polymer properties.

关键词： PEMFC Mass transfer Two-phase flow

作者: V.A.Danilov I.Moon

作者单位: Department of Chemical Engineering,Yonsei University,Seoul 120-749,Korea

会议类型: 国际会议

会议名称: 第四届亚洲过程系统工程会议暨2007年中国国际系统工程年会(The 4th International Symposium on Design,Operation & Control of Chemical Processes)(PSE ASIA 2007)

会议地点: 西安

会议语种:英文

在线出版日期: 2007-08-15（万方平台首次上网日期，不代表论文的发表时间）