{"title":"Continuous Species Separation in an Open-Ended Porous Thermogravitational Column Using Mixed Convection","authors":"A. Mojtabi, K. Sioud, M. -C. Charrier Mojtabi","doi":"10.1007/s11242-025-02173-5","DOIUrl":null,"url":null,"abstract":"<div><p>Species separation is usually achieved in closed vertical thermogravitational columns (TGC). To obtain continuous separation, the initially homogeneous binary solution, saturating the porous medium is introduced at a constant volumetric flow rate through one of the two vertical slots of the TGC and retrieved through the opposite slot. However, this process requires the horizontal dimension of the two vertical walls of the cell to be sufficiently large for the mass regime at the exit slot to reach the steady state. The analytical resolution obtained using the parallel flow approximation and numerical simulations developed are in very good agreement. The vertical mass fraction gradient,<span>\\({m}^{*},\\)</span> at steady state was shown not to admit an optimum with respect to the thickness <span>\\(e\\)</span> for a fixed <span>\\(\\Delta T\\)</span> or with respect to <span>\\(\\Delta T\\)</span> for a fixed <span>\\(e\\)</span>, unlike the gradient <i>m</i> obtained in a vertical TGC. The ratio of the two simplified analytical expressions <span>\\({m}_{s}^{*}\\)</span> and <span>\\({m}_{s}\\)</span>, respectively, obtained for the two columns filled with the same binary fluid in porous or fluid media, led to an expression depending only on the ratio of the thermodiffusion coefficient, <span>\\({D}_{T},\\)</span> to the corresponding coefficient, <span>\\({D}_{T}^{*},\\)</span> in the porous medium, the column thickness <span>\\(e,\\)</span> and the permeability of the porous medium. To increase the degree of separation of this mixture, we could simply add another column of height <span>\\(h\\)</span>, at the outlet of the first column of height <span>\\(H,\\)</span> with <span>\\(h<H\\)</span>, and restart the process with a mass fraction higher than the initial fraction, <span>\\({C}_{0}\\)</span>. This technique could be repeated as often as necessary.</p></div>","PeriodicalId":804,"journal":{"name":"Transport in Porous Media","volume":"152 8","pages":""},"PeriodicalIF":2.6000,"publicationDate":"2025-07-02","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://link.springer.com/content/pdf/10.1007/s11242-025-02173-5.pdf","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Transport in Porous Media","FirstCategoryId":"5","ListUrlMain":"https://link.springer.com/article/10.1007/s11242-025-02173-5","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q3","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
引用次数: 0
Abstract
Species separation is usually achieved in closed vertical thermogravitational columns (TGC). To obtain continuous separation, the initially homogeneous binary solution, saturating the porous medium is introduced at a constant volumetric flow rate through one of the two vertical slots of the TGC and retrieved through the opposite slot. However, this process requires the horizontal dimension of the two vertical walls of the cell to be sufficiently large for the mass regime at the exit slot to reach the steady state. The analytical resolution obtained using the parallel flow approximation and numerical simulations developed are in very good agreement. The vertical mass fraction gradient,\({m}^{*},\) at steady state was shown not to admit an optimum with respect to the thickness \(e\) for a fixed \(\Delta T\) or with respect to \(\Delta T\) for a fixed \(e\), unlike the gradient m obtained in a vertical TGC. The ratio of the two simplified analytical expressions \({m}_{s}^{*}\) and \({m}_{s}\), respectively, obtained for the two columns filled with the same binary fluid in porous or fluid media, led to an expression depending only on the ratio of the thermodiffusion coefficient, \({D}_{T},\) to the corresponding coefficient, \({D}_{T}^{*},\) in the porous medium, the column thickness \(e,\) and the permeability of the porous medium. To increase the degree of separation of this mixture, we could simply add another column of height \(h\), at the outlet of the first column of height \(H,\) with \(h<H\), and restart the process with a mass fraction higher than the initial fraction, \({C}_{0}\). This technique could be repeated as often as necessary.
期刊介绍:
-Publishes original research on physical, chemical, and biological aspects of transport in porous media-
Papers on porous media research may originate in various areas of physics, chemistry, biology, natural or materials science, and engineering (chemical, civil, agricultural, petroleum, environmental, electrical, and mechanical engineering)-
Emphasizes theory, (numerical) modelling, laboratory work, and non-routine applications-
Publishes work of a fundamental nature, of interest to a wide readership, that provides novel insight into porous media processes-
Expanded in 2007 from 12 to 15 issues per year.
Transport in Porous Media publishes original research on physical and chemical aspects of transport phenomena in rigid and deformable porous media. These phenomena, occurring in single and multiphase flow in porous domains, can be governed by extensive quantities such as mass of a fluid phase, mass of component of a phase, momentum, or energy. Moreover, porous medium deformations can be induced by the transport phenomena, by chemical and electro-chemical activities such as swelling, or by external loading through forces and displacements. These porous media phenomena may be studied by researchers from various areas of physics, chemistry, biology, natural or materials science, and engineering (chemical, civil, agricultural, petroleum, environmental, electrical, and mechanical engineering).