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Mass balance cell layer

At the heart of the model are the heat and mass balance equations governing the chlorine gas, brine and amalgam layers within the cell as illustrated by Fig. 20.3. At a more detailed level each cell is divided into eight zones. Conditions within each zone are assumed to be constant and there is a trade-off between model accuracy and execution time associated with the number of zones. Typically eight zones have been found to be a good compromise. [Pg.263]

The concentration polarization occurring in electrodialysis, that is, the concentration profiles at the membrane surface can be calculated by a mass balance taking into account all fluxes in the boundary layer and the hydrodynamic conditions in the flow channel between the membranes. To a first approximation the salt concentration at the membrane surface can be calculated and related to the current density by applying the so-called Nernst film model, which assumes that the bulk solution between the laminar boundary layers has a uniform concentration, whereas the concentration in the boundary layers changes over the thickness of the boundary layer. However, the concentration at the membrane surface and the boundary layer thickness are constant along the flow channel from the cell entrance to the exit. In a practical electrodialysis stack there will be entrance and exit effects and concentration... [Pg.98]

From the standpoint of mass balances, this required the specification of inlet concentrations. For the energy balances of the outer cell layers (k = 1 and K, and = 1 and L), the specifications included perfect thermal insulation at the outer unit cell walls, to simulate adiabatic behavior. [Pg.182]

In the Westinghouse electrochemical step, hydrogen is released at the cathode interface. In the numerical study, bubble generation is assumed to be localized in the first row of fluid cells neighbouring the electrode. In this special zone analogue to a boundary layer, the rate of gas production is assumed equal to the rate of the reduction process. It is modelled by the source term S2 of the dispersed phase mass-balance equation, assuming a 100% Faradic yield. [Pg.16]

Case 1 the DC current is lower than Jiiml- The mass balance within a layer ofthe solid electrolyte near the cathode indicates that no stoichiometry change is obtained rather, only an oxide ions flux from the cathode to the anode is observed. This flux obeys the Faraday law (i.e., J = I/2F, and the cell functions as an oxygen pump (Figure 12.2). [Pg.400]

To capture the dynamics of PEM fuel cell startup it is essential to include the dynamic mass balance for the water content in the membrane, TV . If water accumulation in the hydrophobic gas diffusion layer is neglected, then the water accumulation in the membrane is the difference between the water produced and the net water removed by convection from the anode and cathode, as given by Eq. (3.4). We measure all the quantities on the right-hand side of Eq. (3.4), so we can determine the accumulation rate of water. [Pg.113]

Figure 11.26 A schematic diagram of an apparatus used to obtain estimates of the passive permeability of a drug candidate across the intestinal mucosa using Caco-2 cells. A monolayer of Caco-2 cells is grown on a porous polyethylene terephthalate (PET) membrane (a so-called confluent monolayer of cells that grows only in two dimensions on such a substrate from an initial small inoculation). In the experiment the cells are submerged in Hanks s Balanced Salt Solution (HBSS) buffer (contains Na+, K+, CP, phosphate, glucose, and in some formulations also Ca +, Mg + and S04 ) the Caco-2 cell layer provides the only connection between an apical (donor) reservoir, into which the drug candidate is dosed, and a basolateral (receiver) reservoir. For the assay, aliquots are removed for analysis from the apical reservoir at Omin, and from both reservoirs at 120 min. Reproduced from Van Pelt, Rapid Commun. Mass Spectrom. 17, 1573 (2003), with permission of John Wiley Sons Ltd. Figure 11.26 A schematic diagram of an apparatus used to obtain estimates of the passive permeability of a drug candidate across the intestinal mucosa using Caco-2 cells. A monolayer of Caco-2 cells is grown on a porous polyethylene terephthalate (PET) membrane (a so-called confluent monolayer of cells that grows only in two dimensions on such a substrate from an initial small inoculation). In the experiment the cells are submerged in Hanks s Balanced Salt Solution (HBSS) buffer (contains Na+, K+, CP, phosphate, glucose, and in some formulations also Ca +, Mg + and S04 ) the Caco-2 cell layer provides the only connection between an apical (donor) reservoir, into which the drug candidate is dosed, and a basolateral (receiver) reservoir. For the assay, aliquots are removed for analysis from the apical reservoir at Omin, and from both reservoirs at 120 min. Reproduced from Van Pelt, Rapid Commun. Mass Spectrom. 17, 1573 (2003), with permission of John Wiley Sons Ltd.
In this compartment, the oxygen mass transport is coupled with a metabolic reaction from the cells. Assuming a zero-order reaction, the mass balance in an infinitesimal volume of length dz and with thickness dr placed in the cell layer is ... [Pg.877]

Other sets of hair cells are formed in specialized parts of the inner ear.964 The three semicircular canals detect angular acceleration in three directions, while the sac-like utricle and saccule detect linear acceleration including gravitational attraction. These two organs each contain a patch of hair cells whose tips project into a gelatinous layer, which is overlain by a field of small crystals of calcium carbonate. These little stones (otoliths) provide an inertial mass, which resists movement causing the hair cell tips to bend and activate mechanoreceptors to send information about balance and orientation to the brain. [Pg.1801]

The model is derived from a basic mass-current balance by the control volume approach. A relaxation method is used to solve the two-point boundary problem. The effects of different parameters on the catalyst layer are studied in detail. The discussions in this paper may help in the optimization design of cathode catalyst layer in PEM fuel cells. [Pg.228]


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See also in sourсe #XX -- [ Pg.877 ]




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