JOURNAL OF CHEMICAL ENGINEERING OF JAPAN · 1983 · 128 citations · 0 references
EngineeringChemical EngineeringSeparation ProcessesSeparation ScienceTransport PhenomenaAdsorption ProcessesAdsorptive SeparationsSugar ProcessingAdsorbent InteractionsAdsorption Column ModelingAdsorption SeparationConcentration ProfilesContinuous Adsorptive SeparationPacked-bed AdsorptionSimulated Moving Bed AdsorptionZeolite Sorbents
The continuous separation of a glucose/fructose mixture was experimentally performed using a simulated moving-bed adsorber packed with the Ca2+ ion form of Y zeolite. In the adsorber, the continuous and countercurrent contact of the liquid stream with the solid adsorbent is simulated by advancing adsorption columns against the fixed inlets and outlets of liquid streams, without actual movement of the solid adsorbent. Two mathematical models, i.e., an intermittent moving-bed and a continuous moving-bed type, are presented for calculating the concentration profiles of glucose and fructose in the simulated moving-bed adsorber. The validity of the models is experimentally confirmed, and a criterion for good separation in the simulated moving-bed adsorber is presented.