Kinetics of multiproduct acidogenic and solventogenic batch fermentations

Summary Large amounts of data indicated that most of the metabolic processes of the acidogenic (acid producing) and the solventogenic (solvent producing) fermentations were regulated by product accumulation. A simple unstructured model simulated microbial growth, product formation and substrate utilization in six different fermentations, where five different microorganisms produced various combinations of ten different products. Specific growth rates of these microorganisms decreased proportionally with overall product accumulation. The products were excreted in non-growth associated pattern. Excretion of some of these products were inhibited by the overall product accumulation similarly as the microbial growth. A substrate consumption model which considered the biomass and individually all the products as separate substrate sinks simulated the data satisfactorily.     

Kinetic Analysis of Aspergillus oryzae Cultivations on Starch

Cultivation of Aspergillus oryzae on starch is described as a combination of two rate processes: Starch hydrolysis and the cellular activities of the fungi including growth, enzyme production and maintenance. Kinetic models are presented to describe growth, enzyme production, starch hydrolysis and uptake of the hydrolysis products. Numerical values of the model parameters indicated that the rate controlling step of A. oryzae growth on starch was not starch hydrolysis, but the substrate uptake process. Glucose was one of the starch hydrolysis products. About 35% of the substrate consumed for biomass synthesis was glucose. Its accumulation in the medium did not cause repression of the starch hydrolysing enzymes. Steady state starch hydrolysis rates increased with initial starch concentration in the medium. Starch hydrolysing enzymes of A. oryzae have extensive industrial uses. This study may help in a more detailed understanding of the kinetic aspects of the production of these enzymes.     

Kinetics of riboflavin production by Brewers'' yeasts

The kinetics of riboflavin production by Saccharomyces cerevisiae and Saccharomyces carlsbergensis in synthetic media and wort were studied. The results indicated that riboflavin was produced by growing cells only. Riboflavin production rate was proportional to growth rate of the yeasts in the exponential phase. Riboflavin was depleted in the stationary phase. The depletion rate was expressed with a first-order kinetic expression in yeast concentration. The kinetics of substrate utilization and ethanol production were also given to describe better the associated phenomena and fermentation pattern.     

Attachment and growth kinetics of anchorage-dependent BHK cells on microcarriers

Anchorage-dependent Baby Hamster Kidney (BHK) cells were cultivated on polyhydroxyethylmethacrylate (PHEMA), polystyrene (PS), and Cytodex microcarriers. Analysis of the experimental data indicated that there were a finite number of sites on the microcarrier surfaces, available for anchorage. The number of these sites was determined by the chemical and physical structure of the surface. A small fraction of these sites were suitable for attachment of the cells before proliferation. A larger fraction of these sites did not support attachment but the cells could proliferate on them by the help of previously attached mother cells. The attachment and proliferation of the BHK cells on these microcarriers were satisfactorily modeled by surface saturation type of mathematical expressions.     

Microbial growth kinetics of fed-batch fermentations

Summary Fed-batch fermenters are generally operated with the addition of small doses of nutrients, therefore the volume of the fermentation broth increases with time. Batch fermenters generally contain and almost constant volume of broth and a logistic equation has been commonly employed to simulate microbial growth in them. Mass balances were determined with fed-batch fermentation to obtain expressions which account for the effect of volume increase and the subsequent dilution of the biomass. A growth rate expression was obtained for fed-batch fermentations. The new expression was very similar to the logistic equation. Therefore an anology between the values of the parameters of the new model and of the logistic equation was sought. The new model was also employed to simulate six sets of data from the literature and satisfactory results were obtained.