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contributor authorA. T. Shawaqfeh
contributor authorM. M. Farid
date accessioned2017-05-08T23:48:13Z
date available2017-05-08T23:48:13Z
date copyrightAugust, 1995
date issued1995
identifier issn0199-6231
identifier otherJSEEDO-28257#236_1.pdf
identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/115916
description abstractA single-basin solar still may be used for primary concentration of dilute ethanol produced from fermentation. In order to describe the simultaneous heat and mass transfer in the still, different models have been proposed and tested against some experimental measurements on a still having a 1 m × 1 m basin area. Measurements were based on steady-state operation using electrical heating and unsteady-state operation using solar energy. The proposed models were found to have similar trends even though their derivations were based on different approaches. The models were found to overpredict the mass fluxes of ethanol (Me) and water (Mw) at high basin temperature and ethanol concentration, with different degrees.
publisherThe American Society of Mechanical Engineers (ASME)
titleDistillation of Ethanol in a Solar Still: Studies on Heat and Mass Transfer
typeJournal Paper
journal volume117
journal issue3
journal titleJournal of Solar Energy Engineering
identifier doi10.1115/1.2847809
journal fristpage236
journal lastpage241
identifier eissn1528-8986
keywordsHeat
keywordsMass transfer
keywordsEthanol
keywordsSolar stills
keywordsMeasurement
keywordsFlux (Metallurgy)
keywordsTemperature
keywordsSteady state
keywordsWater
keywordsHeating AND Solar energy
treeJournal of Solar Energy Engineering:;1995:;volume( 117 ):;issue: 003
contenttypeFulltext


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