ABSTRACT
By a monospore isolation technique, Rhizopus sp. MK-96-1 was selected from colonies of Rhizopus sp. MK-96, which was isolated from the soil sample collected in Fujieda, Japan, and used as a parent strain. By the ammonia-concentration-gradient agar plate technique after mutation using N-methyl-N'-nitro-N-nitrosoguanidine (NTG) method, a mutant strain designated Rhizopus sp. MK-96-1196 producing more than 90 g/l L-lactic acid under pH control using liquid ammonia in an airlift bioreactor was successfully isolated. Compared with the parent strain, this mutant strain produced about twofold the amount of L-lactic acid in half fermentation time under the same culture conditions. Ammonium L-lactate was recovered and purified as free L-lactic acid via n-butyl L-lactate. The ammonia used for pH control in the fermentation broth was recovered as liquid ammonia during the recovery and purification process and subsequently reused for the next fermentation. Thus, we have developed a new highly purified L-lactic acid production process without producing recalcitrant wastes, e.g., CaSO4 (gypsum).
ABSTRACT
We determined the optimum culture conditions such as inoculum size, initial starch concentration, pH during the fermentation and aeration rate for L-lactic acid production by Rhizopus sp. MK-96-1196 in a 3-l airlift bioreactor. More than 90 g/l of L-lactic acid was produced from only partially enzymatically hydrolyzed corn starch with a production rate of 2.6 g/l/h and a product yield of 87% based on the starch consumed under the optimum conditions in the 3-l airlift bioreactor. Scale-up from the 3-l to a 100-l airlift bioreactor for L-lactic acid fermentation was carried out using V(s)(cm/s) as a scale-up criterion. The production rates and yields of L-lactic acid in both bioreactors appeared to be fairly well correlated with k(L)a (1/h).