Theory of shock electrodialysis

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Theory of shock electrodialysis ( theory-shock-electrodialysis )

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2.4. Boundary conditions In this part we will give the boundary conditions for the feed channel (including the unsupported elec- trolyte zones) shown in Fig.2(a), which will be combined with the depth-averaged equations to complete the model. At the inlet, we assume Note that since the inlet zone is not charged, 􏱘zkcin = 0 should be satisfied. At the outlet, we assume in in ∂ψv u = u , ck = ck , ∂x = 0. (32) k v ∂ck ∂ψv p =pa, ∂x =0, ∂x =0, (33) where pa is the atmospheric pressure. On all the non-penetrating walls shown in Fig.2(a) (solid black lines or blocks, e.g., the splitter), apply u·n=0, Jk ·n=0. (34) where n is the normal vector of the walls pointing to the outside of the channel. On these walls the viscous boundary layer thickness should be comparable to the channel depth, which is much smaller than the x and y dimensions, so the non-slip boundary condition is not applied here. Finally, we need to give the upper and lower boundary conditions of the charged channel. When only two species exist (one anion, one cation), the previous work [13, 20] just assumes Jy,− = 0 (ideal CEMs) and ψv = ±V/2 at the anode and cathode side membranes. However, this leads to almost perfect ion removal, which cannot be used to predict the magnitude of outlet concentration. Furthermore, these two boundary conditions are not enough for a multi-component system. A possible solution is to assign artificial transference numbers to all the ions, but it turns out this could be too rigid of a boundary condition since transference numbers can depend on electric current. In this paper, we choose to directly simulate the transport in the membranes and electrode channels, so we will give boundary conditions in the electrode channel instead of on the upper and lower boundaries of the charged channel. We will use the depth-averaged equations in the limit of thick EDLs for transport in the membranes. However, since the membrane is porous, we need to modify the Dk to Deff. In this paper, we simply assume Deff/Dk = 0.1 for any k. For the kk electrode channels, which are not charged, we use the homogenized equations and assume plug flow with u = uE. At the inlet, we assume ∂ψv = 0, and ck = cA for the anode and ck = cC for the cathode stream. ∂x k k At the outlet, we assume ∂ck = 0 and ∂ψv = 0. On the non-penetrating walls, also assume Eq.(34). On ∂x ∂x 2.5. Non-dimensionalization In this part, we will non-dimensionalize the PB equation (Eq.(15)), the depth-averaged equations (Eq.(23a)- (23c), (22)-(29)) and the boundary conditions. The scales we choose to non-dimensionalize variables are ˆ summarized in Table 1. We will use the hat accent (f) to represent the dimensionless averaged quantities, ̃ and use the tilde accent (f) to represent all the other dimensionless quantities. Except for the accents, the dimensionless equations and boundary conditions look the same as the dimensional form. Also note that by definition, the integrals αEO, αDO, βP , βEO, βDO, δk themselves are dimensionless. Though we have the electrode surface, assume u · n = 0, Jk · n = 0 for k = 1,2,··· ,Ns, and ψv = ±V/2. Here we assume fast reaction on electrodes so the reaction rate is limited by ionic flux of water ions. Note that V may differ from the true voltage between electrodes due to surface overpotentials. kkkk used h and z to calculate the integrals, their dimensions cancels each other and the two variables can be substituted by 1 and z ̃ = z/h respectively to get the fully dimensionless form. To compare with experiments, we also scale the total current by the advection of positive charges 􏱘z+c+FuinHiohio, where Hio and hio are respectively the width and depth of the inlet and outlet for the feed. 8

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