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contributor authorJesse D. Killion
contributor authorSrinivas Garimella
contributor authorMatthew D. Determan
date accessioned2017-05-09T00:47:00Z
date available2017-05-09T00:47:00Z
date copyrightSeptember, 2011
date issued2011
identifier issn1948-5085
identifier otherJTSEBV-28833#031008_1.pdf
identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/147633
description abstractMoisture management in proton exchange membrane fuel cells is crucial to durability and performance. This frequently requires external humidification of the reactant gas streams to maintain sufficient humidity levels at the membranes, especially at higher operating temperatures. Direct-contact humidifiers using louvered fins brazed to rectangular tubes, similar to those frequently employed in automotive condensers and radiators, can be used to humidify a gas stream. A gas stream in which liquid water is sprayed flows through the passages formed by the louvered fins counter-current to a heating fluid flowing in the rectangular tubes sandwiching the fins. A mathematical model of this type of direct-contact humidifier is presented. The equations of energy and mass conservation are simultaneously solved for a number of segments along the humidifier. An equivalent resistance network is used to capture the temperature profile of the fins and liquid film surrounding them. The thickness of the liquid film is calculated from a shear balance at the film interface. The heat and mass transfer analogy is used with empirically derived transfer coefficients to solve the coupled heat and mass transfer problem in the gas phase. Predicted results are presented for typical operating conditions corresponding to a wide range of fuel cell operating conditions. The results show how the humidification process varies along the length of the humidifier. It is also shown that, although evaporation of the liquid film takes place throughout the entire humidifier, the direction of sensible heat transfer between the gas and liquid film can switch at some distance along the humidifier. This confirms the need for the equivalent resistance network model of the fin and film since simple fin efficiency models would fail in this situation. The model provides a basis for design optimization and performance predictions for this type of direct-contact moisture management device.
publisherThe American Society of Mechanical Engineers (ASME)
titlePerformance Predictions of a Moisture Management Device for Fuel Cell Applications
typeJournal Paper
journal volume3
journal issue3
journal titleJournal of Thermal Science and Engineering Applications
identifier doi10.1115/1.4004426
journal fristpage31008
identifier eissn1948-5093
keywordsFlow (Dynamics)
keywordsHeat
keywordsTemperature
keywordsMass transfer
keywordsHeat transfer
keywordsFluids
keywordsElectrical resistance
keywordsHumidifiers
keywordsFins
keywordsLiquid films
keywordsEvaporation
keywordsWater
keywordsHeating
keywordsNetworks
keywordsEquations
keywordsFuel cell applications
keywordsHeat transfer coefficients
keywordsShear (Mechanics)
keywordsDesign
keywordsProton exchange membrane fuel cells AND Temperature profiles
treeJournal of Thermal Science and Engineering Applications:;2011:;volume( 003 ):;issue: 003
contenttypeFulltext


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