Shake Flask Studies Research Articles

Assimilation of Lemonade-Processing Wastewater by Yeasts

Of the five species of yeasts examined in shake-flask studies at 30 degrees C, only Candida utilis and Saccharomyces fragilis gave higher cell yields (>2.5 g /liter) in 32 h and reduced approximately 87% of the biological oxygen demand in lemonade-processing wastewater fortified with 0.05% ammonium sulfate and 0.01% potassium phosphate. The latter, however, settled more rapidly than the former.

Growth of a methanol-utilizing yeast

A halophilic thermotolerant yeast species, identified as Hansenula polymorpha Morais et Maia, was isolated from a mixed culture obtained from sea-water from the Arabian Gulf. The species grew on methanol at 25–42°C, pH 3.5–6.7, and in a medium compounded with 75% sea-water. Either thiamin HCl and biotin or yeast extract proved essential for growth. In shake flask studies a depression of the yield was observed when methanol concentration increased; at concentrations in excess of 0.1%, v/v, inhibition of growth also occurred. In a batch culture grown in a 14 l fermenter, the values of T d, μ and Y s were found to be 3 h, 0.23 h −1 and 0.38, respectively.

Nutritional Studies on Xanthan Production by Xanthomonas campestris NRRL B1459

The nutritional requirements of Xanthomonas campestris NRRL B1459 for optimal xanthan production were studied in a chemically defined medium. Of the carbon sources tested, a 4% sucrose or glucose medium yielded the highest xanthan titers. The further addition of certain organic acids, such as succinate, pyruvate, and alpha-ketoglutarate, stimulated xanthan production; excess concentrations of these organic acids inhibited xanthan formation. Certain amino acids (e.g., glutamate) and nitrate salts were superior to ammonium salts for xanthan production. Concentrations of these nitrogen sources higher than the optimal levels inhibited xanthan production while stimulating growth. Xanthan production was also sensitive to high concentrations of inorganic phosphate. High xanthan potencies, up to 30 g/kg of broth, were achieved in these shake-flask studies, in which completely defined media were used.

Production of tumor-inhibitory L-asparaginase by submerged growth of Serratia marcescens.

Production of a tumor-inhibitory asparaginase by submerged fermentation with Serratia marcescens ATCC 60 was studied to ascertain optimal nutritional conditions for large-scale production leading to enzyme purification studies. Five strains of S. marcescens were screened in shake-flask studies and were found to produce 0.8 to 3.7 IU/ml 48 hr after inoculation. The requirements for asparaginase production with S. marcescens ATCC 60, the high producing strain, included the following: 4% autolyzed yeast extract medium (initial pH 5.0), an incubation temperature of 26 C, and limited aeration for a zero level of dissolved oxygen during the fermentation. Addition of various carbohydrates to the fermentation medium did not enhance yields. The peak cell population in the fermentation medium and the maximal asparaginase yields occurred simultaneously. Highest enzyme yields were found when the pH of the fermentation cycle rose to approximately 8.5. Yields of 4 IU of asparaginase/ml of cell suspension have been obtained consistently in 40 to 42 hr from 10-liter volumes (500 ml/4-liter bottle) produced on a reciprocating shaker. Scale-up to a 60-liter fermentor yielded 3.1 IU/ml in 35 hr.

Production of Tumor-Inhibitory L-Asparaginase by Submerged Growth of Serratia marcescens1

Production of a tumor-inhibitory asparaginase by submerged fermentation with Serratia marcescens ATCC 60 was studied to ascertain optimal nutritional conditions for large-scale production leading to enzyme purification studies. Five strains of S. marcescens were screened in shake-flask studies and were found to produce 0.8 to 3.7 IU/ml 48 hr after inoculation. The requirements for asparaginase production with S. marcescens ATCC 60, the high producing strain, included the following: 4% autolyzed yeast extract medium (initial pH 5.0), an incubation temperature of 26 C, and limited aeration for a zero level of dissolved oxygen during the fermentation. Addition of various carbohydrates to the fermentation medium did not enhance yields. The peak cell population in the fermentation medium and the maximal asparaginase yields occurred simultaneously. Highest enzyme yields were found when the pH of the fermentation cycle rose to approximately 8.5. Yields of 4 IU of asparaginase/ml of cell suspension have been obtained consistently in 40 to 42 hr from 10-liter volumes (500 ml/4-liter bottle) produced on a reciprocating shaker. Scale-up to a 60-liter fermentor yielded 3.1 IU/ml in 35 hr.