Transport phenomena and fouling in vacuum enhanced direct contact membrane distillation: Experimental and modelling
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The effect of vacuum application in DCMD (V-DCMD) was studied.

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Low partial pressure and non-condensable gas removal enhanced V-DCMD flux by 30%.

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V-DCMD mass transport model was represented by dimensionless coefficient (α).

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Simulated empirical fouling predictions correlated with the experimental data.

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V-DCMD for wastewater ROC treatment was found suitable on a lab scale study.

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