Mass transfer in fermentation

An essential consideration in the design and operation of commercial fermenters is to ensure adequate mass transfer. The complex composition of fermentation liquids makes it difficult to predict accurately the mass transfer characteristics in large vessels. Here various aspects of mass transfer are discussed and their relationships examined. Strategies for predicting the most important type of mass transfer — between gases and liquids — in large scale fermentations are presented.     

Crosslinked potato starch as an affinity adsorbent for bacterial α-amylase

Crosslinked potato starch was prepared as an affinity adsorbent for bacterial α-amylase. To this end, reaction parameters for crosslinking in an ethanol/water solvent were investigated. The degree of crosslinking, and consequently the suitability of crosslinked starch as an adsorbent for α-amylase, changed by altering these parameters. An increase in the degree of crosslinking of the adsorbent caused lower affinity for bacterial α-amylase which resulted in an unfavourable decrease in adsorption capacity and a favourable decrease in the degradation of the adsorbent by the enzyme. 1 g of a suitable adsorbent for bacterial α-amylase, prepared with an epichlorohydrin/glucose monomer ratio of 0·65 (starch concentration 150 mg/ml, ethanol/water ratio 2·0, sodium hydroxide/epichlorohydrin ratio 1·0), can adsorb 9·8 mg of an α-amylase from B. licheniformis at 4°C in 20 h.The equilibrium constant between bound and unbound α-amylase is dependent on the temperature. An effective desorption was possible by a shift to higher temperatures. Degradation values smaller than 0·1% were measured after an incubation of 1 h at 70°C in a desorption buffer with 20% glycerol.It was concluded that coulombic interactions and hydrogen bonds are of no or little importance in enzyme adsorption. Van der Waals forces, which are responsible for the large temperature effect, are the main forces in the interaction between α-amylase and crosslinked starch.