RESUMO
Microbial production of hyaluronic acid (HA) is an attractive substitute for extraction of this biopolymer from animal tissues. Natural producers such as Streptococcus zooepidemicus are potential pathogens; therefore, production of HA by recombinant bacteria that are generally recognized as safe (GRAS) organisms is a viable alternative that is being extensively explored. However, plasmid-based expression systems for HA production by recombinant bacteria have the inherent disadvantage of reduced productivity because of plasmid instability. To overcome this problem, the HA synthesis genes (hasA-hasB and hasA-hasB-hasC) from has-operon of S. zooepidemicus were integrated into the chromosome of Lactococcus lactis by site-directed, double-homologous recombination developing strains VRJ2AB and VRJ3ABC. The chromosomal integration stabilized the genes and obviated the instability observed in plasmid-expressed recombinant strains. The genome-integrated strains produced higher molecular weight (3.5-4 million Dalton [MDa]) HA compared to the plasmid-expressed strains (2 MDa). High molecular weight HA was produced when the intracellular concentration of uridine diphosphate N-acetylglucosamine (UDP-GlcNAc) and uridine diphosphate-glucuronic acid (UDP-GlcUA) was almost equal and hasA to hasB ratio was low. This work suggests an optimal approach to obtain high molecular weight HA in recombinant strains.
Assuntos
Glucuronosiltransferase/genética , Ácido Hialurônico/biossíntese , Lactococcus lactis/genética , Engenharia Metabólica/métodos , Proteínas de Bactérias/genética , Proteínas de Bactérias/metabolismo , Clonagem Molecular , Glucuronosiltransferase/metabolismo , Hialuronan Sintases , Ácido Hialurônico/química , Ácido Hialurônico/metabolismo , Lactococcus lactis/metabolismo , Peso Molecular , Proteínas Recombinantes/genética , Proteínas Recombinantes/metabolismo , Streptococcus equi/enzimologia , Streptococcus equi/genéticaRESUMO
Chemical synthesis of 1,3-propanediol (1,3-PD) is environmentally unfriendly and hence its microbial production is preferred, especially for biomedical, cosmetic and textile applications. In this work, production of 1,3-PD by co-fermentation of glucose and glycerol by Lactobacillus reuteri was investigated under different cultivation conditions such as aeration, acetate concentration and different molar ratios of glucose/glycerol. The final concentration of 1,3-PD and yield attained under unaerated conditions was close to that obtained under anaerobic conditions. Addition of acetate in the initial medium at 5 g/l increased the productivity of 1,3-PD but above this concentration it was found to be inhibitory. Batch reactor experiments showed that the molar ratio of glucose and glycerol in the medium affected the fermentation pattern. The effect of molar ratios was further investigated in fed-batch fermentation and the optimum ratio was found to be 1.5. In repeated fed-batch fermentation with co-feeding of glucose and glycerol in the molar ratio of 1.5, 1,3-PD concentration reached up to 65.3 g/l, which is the highest 1,3-PD concentration reported so far for this strain. The yield (0.97 mol/mol) based on glycerol utilized also approached the theoretical value (1 mol/mol).