Impact of a biofouling layer on the vapor pressure driving force and performance of a membrane distillation process
The heat and mass transfer resistances of fouling layers can cause a significant flux decline in a membrane distillation (MD) process. In addition, the hydrophilicity and microporous nature of a fouling layer can affect the driving force and correspondingly the flux in MD via curvature effects on th...
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sg-ntu-dr.10356-968152020-03-07T12:48:43Z Impact of a biofouling layer on the vapor pressure driving force and performance of a membrane distillation process Goh, Shuwen Zhang, Qiaoyun Zhang, Jinsong McDougald, Diane Krantz, William B. Liu, Yu Fane, Anthony Gordon School of Civil and Environmental Engineering School of Biological Sciences Nanyang Environment and Water Research Institute Singapore Membrane Technology Centre The heat and mass transfer resistances of fouling layers can cause a significant flux decline in a membrane distillation (MD) process. In addition, the hydrophilicity and microporous nature of a fouling layer can affect the driving force and correspondingly the flux in MD via curvature effects on the vapor pressure as described by the Kelvin equation. This study explores the effect of the hydrophilicity of the sludge on the particle size, vapor pressure and pore-size distribution (PSD) in the biofouling layer and on the permeation flux in cross-flow MD. Two sets of hydrophilic sludge cultures were selected via the Microbial-Adhesion-to-Hydrocarbon method. Cross-flow MD experiments conducted with these two sludges displayed a 60% reduction in the flux relative to using a Milli-Q water feed. However, there was no significant difference in the fluxes for the two sludges. Characterization of the pore-size distribution of the two sludges using evapoporometry, a novel technique based on the vapor-pressure depression caused by small pores, indicated a vapor-pressure depression of 31% and 21% for the more- and less-hydrophilic sludges, respectively. However the effect of the 10% difference in vapor-pressure depression, when combined with the effect of the biofouling layer on the heat- and mass-transfer resistances, could not be detected within the experimental error in this study. Nevertheless, a major conclusion is that the vapor-pressure depression caused by a biofouling layer, or other foulants, could cause a significant reduction in the driving force for MD. 2013-07-17T01:55:31Z 2019-12-06T19:35:23Z 2013-07-17T01:55:31Z 2019-12-06T19:35:23Z 2013 2013 Journal Article Goh, S., Zhang, Q., Zhang, J., McDougald, D., Krantz, W. B., Liu, Y., & Fane, A. G. (2013). Impact of a biofouling layer on the vapor pressure driving force and performance of a membrane distillation process. Journal of Membrane Science, 438, 140-152. 0376-7388 https://hdl.handle.net/10356/96815 http://hdl.handle.net/10220/11631 10.1016/j.memsci.2013.03.023 en Journal of membrane science © 2013 Elsevier B.V. |
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The heat and mass transfer resistances of fouling layers can cause a significant flux decline in a membrane distillation (MD) process. In addition, the hydrophilicity and microporous nature of a fouling layer can affect the driving force and correspondingly the flux in MD via curvature effects on the vapor pressure as described by the Kelvin equation. This study explores the effect of the hydrophilicity of the sludge on the particle size, vapor pressure and pore-size distribution (PSD) in the biofouling layer and on the permeation flux in cross-flow MD. Two sets of hydrophilic sludge cultures were selected via the Microbial-Adhesion-to-Hydrocarbon method. Cross-flow MD experiments conducted with these two sludges displayed a 60% reduction in the flux relative to using a Milli-Q water feed. However, there was no significant difference in the fluxes for the two sludges. Characterization of the pore-size distribution of the two sludges using evapoporometry, a novel technique based on the vapor-pressure depression caused by small pores, indicated a vapor-pressure depression of 31% and 21% for the more- and less-hydrophilic sludges, respectively. However the effect of the 10% difference in vapor-pressure depression, when combined with the effect of the biofouling layer on the heat- and mass-transfer resistances, could not be detected within the experimental error in this study. Nevertheless, a major conclusion is that the vapor-pressure depression caused by a biofouling layer, or other foulants, could cause a significant reduction in the driving force for MD. |
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School of Civil and Environmental Engineering |
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School of Civil and Environmental Engineering Goh, Shuwen Zhang, Qiaoyun Zhang, Jinsong McDougald, Diane Krantz, William B. Liu, Yu Fane, Anthony Gordon |
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Goh, Shuwen Zhang, Qiaoyun Zhang, Jinsong McDougald, Diane Krantz, William B. Liu, Yu Fane, Anthony Gordon |
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Goh, Shuwen Zhang, Qiaoyun Zhang, Jinsong McDougald, Diane Krantz, William B. Liu, Yu Fane, Anthony Gordon Impact of a biofouling layer on the vapor pressure driving force and performance of a membrane distillation process |
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Goh, Shuwen |
title |
Impact of a biofouling layer on the vapor pressure driving force and performance of a membrane distillation process |
title_short |
Impact of a biofouling layer on the vapor pressure driving force and performance of a membrane distillation process |
title_full |
Impact of a biofouling layer on the vapor pressure driving force and performance of a membrane distillation process |
title_fullStr |
Impact of a biofouling layer on the vapor pressure driving force and performance of a membrane distillation process |
title_full_unstemmed |
Impact of a biofouling layer on the vapor pressure driving force and performance of a membrane distillation process |
title_sort |
impact of a biofouling layer on the vapor pressure driving force and performance of a membrane distillation process |
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2013 |
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https://hdl.handle.net/10356/96815 http://hdl.handle.net/10220/11631 |
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