Online estimation of optimal operating conditions for simulated moving bed chromatographic processes.

A new approach for determining optimal operating conditions for simulated moving bed chromatographic processes is presented. The method is based on recursive online estimation and requires only rough initial estimates. It is based on a simple foot point model of the moving concentration fronts and an online measurement of the corresponding retention times in the different zones of the plant. A mathematical representation of the adsorption isotherms is not required. The method is validated experimentally for the separation of bicalutamide enantiomers.

Evaluation of commercial resins for fructo-oligosaccharide separation.

Fructo-oligosaccharides (FOS) produced by fermentative processes are obtained in mixtures containing significant amounts of salts and other non-prebiotic sugars. A demineralisation process using a mixture of a cationic and an anionic resin was proposed. The separation of FOS from a mixture of fructose, glucose and sucrose was evaluated. Experiments were conducted with several commercial cationic exchange resins in calcium, sodium and potassium forms packed in preparative columns (7cm×2.2cm length×diameter). Resins in potassium form obtained the higher retention factor values for sugars when compared to the other ionic forms. However, when compared to calcium and sodium ones, resins in potassium cationic forms were shown to be the less efficient separating sugar mixtures. The resin with best separation performance was the Diaion UBK535Ca. A recovery yield of 92% (w/w) of FOS with 90% (w/w) of purity was obtained from batch experiments conducted in a single column loaded with the Diaion UBK535Ca resin at 25°C. The temperature shown did not influence the separation performance significantly. By increasing the column length, the purity of FOS increased to 92% (w/w), however the recovery yield decreased to 88% (w/w).