“…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 ].
…”