TY  - JOUR
UR  - https://www.scopus.com/inward/record.uri?eid=2-s2.0-84927772314&doi=10.1016%2fj.applthermaleng.2015.03.067&partnerID=40&md5=65b608e54bce01180ee570896ad211b0
JF  - Applied Thermal Engineering
A1  - Al-Waked, R.
A1  - Nasif, M.S.
A1  - Morrison, G.
A1  - Behnia, M.
VL  - 84
Y1  - 2015///
N2  - Conjugate heat and mass transfer processes across membrane heat exchangers of variable mass transportation resistance were investigated numerically. One half of flow channel for the hot stream and another for the adjacent cold stream were simulated. Effects of channel height, Reynolds number and flow direction on heat exchanger thermal effectiveness and energy recovered were studied. The validated CFD model showed that values of moisture resistance decrease with the increase in flow rates and/or the decrease in vapour mass fractions on both sides of the membrane. Furthermore, total hydraulic diameter effects on the thermal efficiency within membrane heat exchangers were found strong. © 2015 Elsevier Ltd.
KW  - Channel flow; Computational fluid dynamics; Heat resistance; Heat transfer; Mass transfer; Mass transportation; Membranes; Moisture; Reynolds number
KW  -  Conjugate heat transfer; Conjugate mass transfer; Energy recovery; Heat and mass transfer process; Hydraulic diameter; Moisture resistance; Thermal effectiveness; Variable resistance
KW  -  Heat exchangers
ID  - scholars5925
EP  - 309
SN  - 13594311
PB  - Elsevier Ltd
N1  - cited By 39
TI  - CFD simulation of air to air enthalpy heat exchanger: Variable membrane moisture resistance
SP  - 301
AV  - none
ER  -