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A district heating network (DHN) is considered as a heat source for the membrane distillation system.
The system has three major components: the solar-thermal system, solar-PV system, and membrane distillation system.
The investigations on a hybrid photocatalysis direct contact membrane distillation system for removal of ibuprofen sodium salt (IBU) from tap water are described.
A direct contact membrane distillation system (DCMD) was simulated by using Aspen Plus for the purpose of energy efficiency and economic analyses.
A detailed mathematical model, based on mass and energy balances, was developed in order to provide guide lines for the optimal design and operation of a vacuum-multi-effect membrane distillation system.
Effluent discharge from a local coal mine containing 2332 mg/L of TDS (Total Dissolved Solids), 14.4 mg/L of Ca, 2.72 mg/L of Mg, 1.92 mg/L of Fe and 3.38 mg/L of Al is treated by a vacuum membrane distillation system.
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Along with the commonly used MD thermal efficiency, "MD effectiveness" ε should be used to understand the energy efficiency (measured as gained output ratio, GOR) and water vapor flux of single stage membrane distillation systems.
This heat exchanger analogy shows that membrane distillation systems may be characterized using non-dimensional parameters from counter-flow heat exchanger (HX) theory such as effectiveness and number of transfer units (NTU).
This paper presents a theoretical analysis of the monthly average daily and hourly performances of a solar-powered multi-stage direct contact membrane distillation (SMDCMD) system with an energy recovery scheme and dynamic operating system.
This paper describes the development of a solar-assisted multi-stage vacuum membrane distillation (SMVMD) system.
In this paper, a vacuum membrane distillation (VMD) system equipped with a microwave source was designed.
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