2021
DOI: 10.3390/membranes11040281
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Mass Transfer Analysis of Air-Cooled Membrane Distillation Configuration for Desalination

Abstract: It has been proposed that the air-cooled configuration for air gap membrane distillation is an effective way to simplify the system design and energy source requirement. This offers potential for the practical applications of membrane distillation on an industrial scale. In this work, membrane distillation tests were performed using a typical water-cooled membrane distillation (WCMD) configuration and an air-cooled membrane distillation (ACMD) configuration with various condensing plates and operating conditio… Show more

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Cited by 5 publications
(5 citation statements)
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“…As shown in Figure 4 a, under the conditions of air cooling, the transmembrane flux of membrane distillation can reach a maximum of 2.5 kg/m 2 /h. Compared with the flux of water cooling, under the condition of air temperature at 24 ± 1 °C, the transmembrane flux can reach only 1/10 of the transmembrane flux under water cooling (cooling water temperature at 24 ± 1 °C), and the corresponding σ value is about 0.10, which is lower than the σ value of 0.45 in the forced convection air-cooled membrane distillation device constructed by Cong et.al [ 18 ]. This is because the air flow inside the condensation tube is almost zero for radiation heat transfer between the condensation wall surface and the large space, resulting in the σ value of the tubular membrane distillation being lower than that of the plate membrane distillation under the same conditions.…”
Section: Resultsmentioning
confidence: 88%
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“…As shown in Figure 4 a, under the conditions of air cooling, the transmembrane flux of membrane distillation can reach a maximum of 2.5 kg/m 2 /h. Compared with the flux of water cooling, under the condition of air temperature at 24 ± 1 °C, the transmembrane flux can reach only 1/10 of the transmembrane flux under water cooling (cooling water temperature at 24 ± 1 °C), and the corresponding σ value is about 0.10, which is lower than the σ value of 0.45 in the forced convection air-cooled membrane distillation device constructed by Cong et.al [ 18 ]. This is because the air flow inside the condensation tube is almost zero for radiation heat transfer between the condensation wall surface and the large space, resulting in the σ value of the tubular membrane distillation being lower than that of the plate membrane distillation under the same conditions.…”
Section: Resultsmentioning
confidence: 88%
“…Performance conditions of the membrane distillation device, such as temperature and concentration of the hot feed solution, membrane, and air gap parameters, affect the mass transfer capability of the membrane distillation process. The cooling conditions on the cold side can be characterized by the efficiency coefficient ( σ ) of the membrane distillation process, which can be described by Equation (2) to show the performance of the membrane distillation process [ 18 , 29 ]: where B value is the total mass transfer coefficient including the mass transfer of water vapor in the feed side, the membrane pores, and the air gap. It is related to the configuration of membrane distillation module and the parameters of the membrane, with units of kg/m 2 /Pa/s.…”
Section: Methodsmentioning
confidence: 99%
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