2020
DOI: 10.1016/j.memsci.2020.118278
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Modeling of spiral wound membranes for gas separations. Part I: An iterative 2D permeation model

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Cited by 13 publications
(8 citation statements)
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“…The maximum average percentage error (MAPE) for both components are less than 3%. These MAPE values are considered acceptable compared to other similar numerical modeling works [ 20 , 21 , 22 ], which confirms the validity of the numerical model to be employed in the subsequent parametric analysis.…”
Section: Resultssupporting
confidence: 79%
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“…The maximum average percentage error (MAPE) for both components are less than 3%. These MAPE values are considered acceptable compared to other similar numerical modeling works [ 20 , 21 , 22 ], which confirms the validity of the numerical model to be employed in the subsequent parametric analysis.…”
Section: Resultssupporting
confidence: 79%
“…The following assumptions were made in the proposed model: Local permeation and bulk permeate flow are described by a crossflow pattern [ 22 , 23 ]; There is no permeate mixing in the direction of the bulk permeate flow [ 19 , 23 ]; The pressure variation for flow through the permeate spacer channel is characterized by Hagen–Poiseuille equation [ 24 ]; The feed-side pressure drop is negligible [ 15 , 16 , 19 , 20 , 23 , 24 ]; The pressure drop along the central permeate collector tube is neglected (i.e., pressure is considered as atmospheric) [ 25 , 26 ]; The permeability coefficients are independent of concentration, pressure, and temperature [ 15 , 16 , 19 , 20 , 23 , 24 ]; Channel curvature is neglected and the membrane is treated as a flat sheet [ 22 , 26 ]; Operation within the SWM module is isothermal [ 16 , 18 , 19 , 20 , 27 ]. …”
Section: Model Developmentmentioning
confidence: 99%
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“…Furthermore, it allowed the prediction of flow rates and concentrations along the membrane leaf, which are important features for the understanding of membrane operation processes. In addition, a discretization method was proposed to solve the model, which proved to be faster and more efficient than the shooting method [22]. It is also important to emphasize that industrial spiral-wound membrane separation units for CO 2 applications are formed by several leaves, which are wounded onto a central perforated collecting tube, forming one modular separation element.…”
Section: Membrane Separation Processmentioning
confidence: 99%