Kinetic Study of the Conversion of Different Substrates to Lactic Acid Using Lactobacillus bulgaricus

• Published in: Biotechnology progress 2000, Vol.16 (3), p.305-314
• Main Authors: Burgos-Rubio, Concepción N., Okos, Martin R., Wankat, Phillip C.
• Format: Article
• Language: English
• Subjects: Bacteria; Biological and medical sciences; Biotechnology; Carbohydrate Metabolism; Cells; Culture Media; Enzymes; Fermentation; Fundamental and applied biological sciences. Psychology; galactose; Glucose; Growth kinetics; Hydrolysis; Kinetics; lactic acid; Lactic Acid - biosynthesis; Lactobacillus - metabolism; Lactobacillus bulgaricus; lactose; Mathematical models; Methods. Procedures. Technologies; Microbial engineering. Fermentation and microbial culture technology; Organic acids; Substrate Specificity
• ISSN: 8756-7938; 1520-6033
• DOI: 10.1021/bp000022p

Lactic acid fermentation includes several reactions in association with the microorganism growth. A kinetic study was performed of the conversion of multiple substrates to lactic acid using Lactobacillus bulgaricus. Batch experiments were performed to study the effect of different substrates (lactose, glucose, and galactose) on the overall bioreaction rate. During the first hours of fermentation, glucose and galactose accumulated in the medium and the rate of hydrolysis of lactose to glucose and galactose was faster than the convesion of these substrates. Once the microorganism built the necessary enzymes for the substrate conversion to lactic acid, the conversion rate was higher for glucose than for galactose. The inoculum preparation was performed in such a way that healthy young cells were obtained. By using this inoculum, shorter fermentation times with very little lag phase were observed. The consumption patterns of the different substrates converted to lactic acid were studied to determine which substrate controls the overall reaction for lactic acid production. A mathematical model (unstructured Monod type) was developed to describe microorganism growth and lactic acid production. A good fit with a simple equation was obtained. It was found experimentally that the approximate ratio of cell to substrate was 1 to 10, the growth yield coefficient (YXS) was 0.10 g cell/g substrate, the product yield (YPS) was 0.90 g lactic acid/g substrate, and the α parameter in the Luedeking‐Piret equation was 9. The Monod kinetic parameters were obtained. The saturation constant (KS) was 3.36 g/L, and the specific growth rate (μm ) was 1.14 l/h.