CFD SIMULATION IN HOLLOW FIBER AND TUBULAR MEMBRANES
Membrane filtration has become a primary technology for ensuring the safety and efficiency of treatment of wastewater. This work presents a simulation of wastewater using hollow fiber and tubular membranes. Mass transfer and hydrodynamics of the system were investigated by solving conservation equations. The conservation equations solved are the Navier-Stokes and continuity equations which were solved numerically using the computational fluid dynamics (CFD). Finite element analysis was applied for numerical solution of the system equations. The influence of effective parameters on the mass transfer and hydrodynamics of the process removal was investigated. The distribution profiles of concentration, concentration polarization, velocity, and pressure were obtained and compared between the hollow fiber and tubular membranes for the solute. The results of the simulation confirmed that feed and solvent velocities are the most important parameters in the separation. It is also indicated that the hollow fiber membrane reactors showed good results in the removal process from aqueous solutions.
membranes, simulation, CFD, separation, hollow fiber membrane, tubular membrane.
Received: March 20, 2021; Accepted: April 29, 2021; Published: June 15, 2021
How to cite this article: L. Salama, H. Elaouani, C. Motik, A. Guennoun, Z. Laaziz, R. Moultif and A. Dezairi, CFD simulation in hollow fiber and tubular membranes, JP Journal of Heat and Mass Transfer 23(1) (2021), 139-151. DOI: 10.17654/HM023010139
This Open Access Article is Licensed under Creative Commons Attribution 4.0 International License
References:
[1] J. T. Zelikoff et al., Immunotoxicity of sulfuric acid aerosol: effects on pulmonary macrophage effector and functional activities critical for maintaining host resistance against infectious diseases, Toxicology 92(1-3) (1994), 269-286.https://doi.org/10.1016/0300-483X(94)90183-X.[2] S. J. Kim, S. H. Ko, K. H. Kang and J. Han, Direct seawater desalination by ion concentration polarization, Nature Nanotechnology 5(4) (2010), 297-301. doi:10.1038/nnano.2010.34.[3] A. J. Staverman, Non-equilibrium thermodynamics of membrane processes, Trans. Faraday Soc. 48 (1952), 176-185. https://doi.org/10.1039/TF9524800176.[4] R. Prasad and K. K. Sirkar, Hollow fiber solvent extraction: performances and design, Journal of Membrane Science 50 (1990), 153-175.[5] A. Gabelman and S.-T. Hwang, Hollow fiber membrane contactors, Journal of Membrane Science 159 (1999), 61-106.[6] R.-S. Juang, J.-D. Chen and H.-C. Huan, Dispersion-free membrane extraction: case studies of metal ion and organic acid extraction, Journal of Membrane Science 165 (2000), 59-73.[7] H. M. Yeh and C. H. Chen, Recycle effects on solvent extraction through concurrent flow parallel-plate membrane modules, Journal of Membrane Science 190 (2001), 35-44.[8] J.-J. Guo and C.-D. Ho, Theoretical study on membrane extraction of Cu2+ with D2EHPA in laminar flow circular tube modules, Desalination 233 (2008), 247-257.[9] M. Rezakazemi, A. Ghafarinazari, S. Shirazian and A. Khoshsima, Numerical modeling and optimization of wastewater treatment using porous polymeric membranes, Polymer Engineering and Science 53 (2013), 1272-1278.[10] M. Rezakazemi, M. Iravaninia, S. Shirazian and T. Mohammadi, Transient computational fluid dynamics modeling of pervaporation separation of aromatic/ aliphatic hydrocarbon mixtures using polymer composite membrane, Polymer Engineering and Science 53 (2013), 1494-1501.[11] V. G. Gandhi, M. K. Mishra, M. S. Rao, A. Kumar, P. A. Joshi and D. O. Shah, Comparative study on nano-crystalline titanium dioxide catalyzed photocatalytic degradation of aromatic carboxylic acids in aqueous medium, Journal of Industrial and Engineering Chemistry 17 (2011), 331-339.[12] W. H. Zachritz, L. L. Lundie and H. Wang, Benzoic acid degradation by small, pilot-scale artificial wetlands filter (AWF) systems, Ecological Engineering 7 (1996), 105-116.[13] K. Chai and H. Ji, Dual functional adsorption of benzoic acid from wastewater by biological-based chitosan grafted -cyclodextrin, Chemical Engineering Journal 203 (2012), 309-318.[14] L.-G. Yan, J. Wang, H.-Q. Yu, Q. Wei, B. Du and X.-Q. Shan, Adsorption of benzoic acid by CTAB exchanged montmorillonite, Applied Clay Science 37 (2007), 226-230.[15] M. Ghadiri, M. Mohammadi, M. Asadollahzadeh and S. Shirazian, Molecular separation in liquid phase: development of mechanistic model in membrane separation of organic compounds. doi:10.1016/j.molliq.2018.04.101.[16] U. Shavit, G. Bar-Yosef, R. Rosenzweig and S. Assouline, Modified Brinkman equation for a free flow problem at the interface of porous surfaces: the Cantor-Taylor brush configuration case, Water Resources Research 38 (2002), 1320-1334.[17] Mohamed H. Al-Marzouqi, Muftah H. El-Naasa Sayed, A. M. Marzoukb, Mohamed A. Al-Zaroonia Nadia and Abdullatifa RamiFaiz, Modeling of CO2 absorption in membrane contactors, Separation and Purification Technology 59(3) (2008), 286-293.