2000
DOI: 10.1016/s0376-7388(99)00236-7
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Theory and experiments on sweeping gas membrane distillation

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Cited by 152 publications
(76 citation statements)
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“…permeate side) can be expressed as (9) Similarly, when using air as the sweeping gas, (10) In reality, the vapor partial pressure, humidity ratio and permeate flux associated with the temperature along the membrane surface are not homogenous. In modelling, however, these parameters are often supposed to change homogenously along the membrane based on a series of assumptions [18,19].…”
Section: Relationships Between Vapor Flux Vapor Pressure and Temperamentioning
confidence: 99%
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“…permeate side) can be expressed as (9) Similarly, when using air as the sweeping gas, (10) In reality, the vapor partial pressure, humidity ratio and permeate flux associated with the temperature along the membrane surface are not homogenous. In modelling, however, these parameters are often supposed to change homogenously along the membrane based on a series of assumptions [18,19].…”
Section: Relationships Between Vapor Flux Vapor Pressure and Temperamentioning
confidence: 99%
“…K n <0.01), molecule-molecule collisions become more significant and the mass transfer resistance is caused by the stagnant air trapped within the membrane pore. In this case, water vapor flux can be described by molecule diffusion [4,10,18]: (18) with (19) where D M is the molecular diffusion coefficient, P air-lm is the logarithmic mean pressure of air, D is the water vapor diffusion coefficient and P is the total pressure inside the membrane pore.…”
Section: Mass Transfer Mechanisms Through a Porous Membranementioning
confidence: 99%
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