Exergetic Relationship Between the Thermal Properties of Direct Contact Membrane DistillationSource: Journal of Heat Transfer:;2020:;volume( 142 ):;issue: 003DOI: 10.1115/1.4045748Publisher: The American Society of Mechanical Engineers (ASME)
Abstract: Direct contact membrane distillation (DCMD) is a process that has shown promise within the field of desalination due to its less energy intensive methods and widespread applications. DCMD is a thermally driven microfiltration separation process that operates on the principle of vapor–liquid equilibrium conditions where heat and mass transfer occur simultaneously. Fundamentally, DCMD is based on a porous hydrophobic membrane separating the hot solution (feed) from the cold solution (permeate) where desalinated water condenses. The membrane interfacial temperatures determine the vapor pressure difference across the membrane. In this work, a direct simulation Monte Carlo analysis is employed to investigate how the exergy of the system relates to some key thermal properties, namely, the temperature polarization coefficient (TPC) and the thermal efficiency (TE), as other parameters are changed, such as feed temperature, flow speed, and membrane porosity. Through molecular simulation, phase equilibrium is reached by calculating the chemical potential at the membrane interface and the entropy of the system is found. Since exergy is a function of entropy, enthalpy, and temperature, the amount of useful work is calculated. Finally, exergy is compared to the TPC and TE as the flowrate and porosity are varied. We demonstrate that with these exergy calculations, the information about the thermal relationship between microscopic and macroscopic parameters will improve future experimental work.
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contributor author | Perdue, D. | |
contributor author | Chen, L. | |
contributor author | Schaefer, L. | |
date accessioned | 2022-02-04T14:36:04Z | |
date available | 2022-02-04T14:36:04Z | |
date copyright | 2020/01/29/ | |
date issued | 2020 | |
identifier issn | 0022-1481 | |
identifier other | ht_142_03_033001.pdf | |
identifier uri | http://yetl.yabesh.ir/yetl1/handle/yetl/4273998 | |
description abstract | Direct contact membrane distillation (DCMD) is a process that has shown promise within the field of desalination due to its less energy intensive methods and widespread applications. DCMD is a thermally driven microfiltration separation process that operates on the principle of vapor–liquid equilibrium conditions where heat and mass transfer occur simultaneously. Fundamentally, DCMD is based on a porous hydrophobic membrane separating the hot solution (feed) from the cold solution (permeate) where desalinated water condenses. The membrane interfacial temperatures determine the vapor pressure difference across the membrane. In this work, a direct simulation Monte Carlo analysis is employed to investigate how the exergy of the system relates to some key thermal properties, namely, the temperature polarization coefficient (TPC) and the thermal efficiency (TE), as other parameters are changed, such as feed temperature, flow speed, and membrane porosity. Through molecular simulation, phase equilibrium is reached by calculating the chemical potential at the membrane interface and the entropy of the system is found. Since exergy is a function of entropy, enthalpy, and temperature, the amount of useful work is calculated. Finally, exergy is compared to the TPC and TE as the flowrate and porosity are varied. We demonstrate that with these exergy calculations, the information about the thermal relationship between microscopic and macroscopic parameters will improve future experimental work. | |
publisher | The American Society of Mechanical Engineers (ASME) | |
title | Exergetic Relationship Between the Thermal Properties of Direct Contact Membrane Distillation | |
type | Journal Paper | |
journal volume | 142 | |
journal issue | 3 | |
journal title | Journal of Heat Transfer | |
identifier doi | 10.1115/1.4045748 | |
page | 33001 | |
tree | Journal of Heat Transfer:;2020:;volume( 142 ):;issue: 003 | |
contenttype | Fulltext |