Laminar flow and heat transfer in a quasi-counter flow parallel-plate membrane channel (QCPMC)

被引:18
|
作者
Huang, Si-Min [1 ]
Yang, Minlin [1 ]
Chen, Baiman [1 ]
Jiang, Runhua [1 ]
Qin, Frank G. F. [1 ]
Yang, Xiaoxi [1 ]
机构
[1] Dongguan Univ Technol, Dept Energy & Chem Engn, Key Lab Distributed Energy Syst Guangdong Prov, Dongguan 523808, Peoples R China
基金
中国国家自然科学基金;
关键词
Laminar flow; Heat transfer; Quasi-counter flow; Parallel-plate membrane channel; Air humidity control; DESICCANT AIR DEHUMIDIFICATION; ENERGY EXCHANGERS LAMEES; MASS-TRANSFER; CONDITIONING SYSTEM; HVAC SYSTEMS; MODEL;
D O I
10.1016/j.ijheatmasstransfer.2015.03.028
中图分类号
O414.1 [热力学];
学科分类号
摘要
A parallel-plate membrane contactor with side inlets and side outlets has been designed and used for air humidity control. The contactor is comprised of a series of quasi-counter flow parallel-plate membrane channels (QCPMC). The laminar flow and heat transfer in the QCPMC are investigated based on a unit cell including one membrane and half of the channel. The equations governing the momentum and heat transports are established together with a uniform wall temperature boundary condition and numerically solved by a finite volume difference approach. The mean product of friction factor and Reynolds number (fRe) and Nusselt number (Nu(m)) are then obtained and numerically validated by those taken from other well-known publications. Influences of the Reynolds numbers (Re), entrance ratios (x(in)/x(o)), aspect ratios (x(o)/H), and various fluids with different Prandtl numbers (Pr) on the (fRe)(m), and Nu(m) are obtained and analyzed. It can be found that a distinct vortex is generated for the water stream flowing through the QCPMC when the Re is greater than 100. Further, for the same x(o)/H, the Nu(m), of the LiCI stream is the largest, and next the water stream, the least the air stream. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:890 / 897
页数:8
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