Access the full text.
Sign up today, get DeepDyve free for 14 days.
Loading next page...
/lp/wiley/staged-approach-of-percolation-processes-mVqMlUJgja
References (12)
-
Rodrigues Rodrigues, Tondeur Tondeur (1975)
Influence d'une isotherme nonlinéaire sur l'adsorption‐desorption en réacteurs parfaitement agités ouverts isolé ou en sérieJ. Chim. Phys., 72
-
De Vault De Vault (1943)
The Theory of ChromatographyJ. Am. Chem. Soc., 65
-
Prout Prout, Fernandez Fernandez (1961)
Performance of Anion Resins in Agitated BedsInd. Eng. Chem., 53
-
Michelsen Michelsen (1976)
An Efficient General Purpose Method for the Integration of Stiff ODEAIChE J., 22
-
Slater Slater (1975)
Continuous Ion Exchange in Fluidized BedsCan. J. Chem. Eng., 53
-
Gear Gear (1971)
The Automatic Integration of ODEComm. ACM, 14
-
Marchello Marchello, Davis Davis (1963)
Theoretical Investigation of Agitated Ion Exchange BedsInd. Eng. Chem., 2
-
Chen Chen (1972)
Computer Simulation of Plant‐Scale Multicolumn Adsorption Processes Under Periodic Countercurrent OperationInd. Eng. Chem. Process Design Develop., 11
-
Farkas Farkas, Himsley Himsley (1975)
Some Fundamental Aspects of the Behaviour of Ion Exchange EquipmentCan. J. Che. Eng., 53
-
Gear Gear (1971)
Algorithm 407‐DIFSUB for Solution of ODEComm. ACM, 14
-
Belter Belter (1973)
Development of a Recovery Process for NovobiocinBiotech. Bioeng., 15
-
Martin Martin, Synge Synge (1941)
A New Form of Chromatogram Employing Two Liquid PhasesBiochem. J., 35
- Publisher
- Wiley
- Copyright
- Copyright © 1979 American Institute of Chemical Engineers
- ISSN
- 0001-1541
- eISSN
- 1547-5905
- DOI
- 10.1002/aic.690250305
- Publisher site
- See Article on Publisher Site
Abstract
Sorption processes in a perfectly mixed reactor are analyzed by using two models: The equilibrium model and a kinetic model which considers the effect of the external mass transfer resistance. In both cases, a general non‐linear equilibrium isotherm is considered. The influence of the different model parameters on the response of the perfectly mixed sorber and their effect on a design parameter (the breakthrough time) are discussed. A criterium is derived in order to predict when the equilibrium model is valid.
Journal
Aiche Journal – Wiley
Published: May 1, 1979