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Journal ArticleDOI

Equilibrium staged parametric pumping: II. Multiple transfer steps per half‐cycle and reservoir staging

01 Nov 1977-Aiche Journal (John Wiley & Sons, Ltd)-Vol. 23, Iss: 6, pp 840-851

TL;DR: In this paper, the authors studied the limit regimes of the (one-stage, n transfer) and (one stage, two transfer) parametric pumps in the half-cycle setting.

AbstractThe limit regimes of equilibrium staged batch parametric pumps are studied. The half-cycle comprises several equilibrations at each temperature, each followed by a discrete transfer of fluid. The concentration distribution of the effluent of each half-cycle is conserved by a cascade of reservoirs. The concepts, methods, and McCabe-Thiele representation are first introduced on the example of the (one-stage, two transfer) pump. The generalization to the (one stage, n transfer) pump leads to a limit regime represented by a staircase construction between the two isotherms, the number of steps of the staircase being equal to the number of transfer steps. The limit regime of the general (N stage, n transfer) pump is then analyzed in terms of the properties of the (one stage, n transfer) pump considered above and of the (N stage, one transfer) pump discussed in the preceding paper of this series. An analytical solution for the separation factor is given in the case of linear isotherms. The importance of conserving the effluent concentration distribution is illustrated by graphical and numerical comparisons with pumps where this is not done.

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Citations
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Journal ArticleDOI
TL;DR: In this article, the authors developed a user-friendly package called Visual Pumping (VP) for the simulation of thermal parametric pumping processes with educational and training purposes, based on Visual Basic.
Abstract: Thermal parametric pumping is a cyclic adsorptive process based on cyclic changes in the bed temperature simultaneously with flow reversal. Simplified models are adequate to describe these cyclic processes with long cycle times. Two simplified models are used here: Model I is an equilibrium model plus axial dispersion and Model II accounts for intraparticle mass transfer with LDF approximation. Simulations used parameter values obtained for the system phenol/water/ adsorbent resin Duolite ES861. Model validation is carried out by performing experiments in a pilot plant with the system phenylalanine/water/polymeric adsorbent SP206 and using published experimental data for the system phenol/water/adsorbent resin Duolite ES861. A user-friendly package ‘Visual Pumping’ (VP) is developed in Visual Basic for the simulation of thermal parametric pumping processes with educational and training purposes.

17 citations


Cites methods from "Equilibrium staged parametric pumpi..."

  • ...cess configurations. Equilibrium staged models were used by Grevillot and Tondeur [12, 13 ,14]....

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Book ChapterDOI
01 Jan 1986
TL;DR: The concept of parametric pumping is due to Wilhelm and coworkers (1966, 1968) as mentioned in this paper, whose original results deal with adsorption from the liquid phase, modulated by temperature.
Abstract: The term “parametric pumping” implies the idea of pumping, that is of transport of material (in our case, ionic species) up along some potential scale (in our case, chemical potential), at the cost of degradation of some flux of energy (to be specified later). The term “parametric” refers to the fact that the energy flux just mentionned is obtained by modulating some intensive thermodynamic parameter such as temperature, pressure, ionic strength, pH, electric potential, … Typical examples are temperature-swing ion-exchange and pressure-swing adsorption. The concept of parametric pumping is due to Wilhelm and coworkers (1966, 1968). Their original results deal with adsorption from the liquid phase, modulated by temperature. Let us examine how these phenomena are implemented.

14 citations

Journal ArticleDOI
TL;DR: A detailed model for the recuperative parametric pumping is presented in this paper, which includes intraparticle mass transfer resistance, axial diffusion and non-linear equilibrium represented by Langmuir equation.
Abstract: A detailed model for the recuperative parametric pumping is presented. The model includes intraparticle mass transfer resistance, axial diffusion and non-linear equilibrium represented by Langmuir equation. The sensitivity studies shows that process performance strongly increases when cycle time increases and φB/φT ratio and particle size decreases. It also shows that bottom and top dead volumes do not influence much the process performance. Evolution of the histories of concentrations and temperatures, the bed performance from cycle to cycle and the bed dynamics at the cyclic steady state have been discussed.

14 citations

Book ChapterDOI
01 Jan 1981

14 citations

Journal ArticleDOI
TL;DR: In this article, a multicomponent, non-linear model that takes into account the dissociation reaction in liquid phase is used to predict the separation and to investigate the effect of the resin type on the performance of parametric pumping.
Abstract: Separation of amino acids by thermal parametric pumping is experimentally and theoretically investigated. A multicomponent, non-linear model that takes into account the dissociation reaction in liquid phase is used to predict the separation and to investigate the effect of the resin type on the performance of parametric pumping. Experiments have been done with different mixtures of glutamic acid, leucine, phenylalanine, proline, serine and valine. The experimental results demonstrate the capability of thermal parametric pumping of separating amino acids from aqueous mixtures. The simulations give the correct general behaviour of the experimental results and help to select the resin that is more suitable for the separation.

13 citations