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Utilization of renewable and low-cost lignocellulosic wastes has received major focus in industrial lactic acid production. The use of high solid loadings in biomass pretreatment potentially offers advantages over low solid loadings including higher lactic acid concentration with decreased production and capital costs. In this study, an isolated Enterococcus faecalis SI with optimal temperature 42 °C was used to produce optically pure L-lactic acid (> 99%) from enzyme-saccharified hydrolysates of acid-impregnated steam explosion (AISE)-treated plywood chips. The L-lactic acid production increased by 10% at 5 L scale compared to the similar fermentation scheme reported by Wee et al. The fermentation with a high solid loading of 20% and 35% (w/v) AISE-pretreated plywood chips had been successfully scaled up to process development unit scale (100 L) and pilot scale (9 m), respectively. This is the first report of pilot-scale lignocellulosic lactic acid fermentation by E. faecalis with high lactic acid titer (nearly 92 g L) and yield (0.97 kg kg). Therefore, large-scale L-lactic acid production by E. faecalis SI shows the potential application for industries.

Summary Transforming petrochemical processes into bioprocesses has become an important goal of sustainable development. The chemical synthesis of 2,5‐furandicarboxylic acid (FDCA) from 5‐hydroxymethylfurfural (HMF) is expensive and environmentally unfavourable. The study aims to investigate a whole‐cell biocatalyst for efficient biotransformation of HMF to FDCA. For the first time, a genetically engineered Pseudomonas putida S12 strain expressing 5‐hydroxymethylfurfural oxidase (HMFO) was developed for the biocatalytic conversion of HMF to FDCA. This whole‐cell biocatalyst produced 35.7 mM FDCA from 50 mM HMF in 24 h without notable inhibition. However, when the initial HMF concentration was elevated to 100 mM, remarkable inhibition on FDCA production was observed, resulting in a reduction of FDCA yield to 42%. We solve this substrate inhibition difficulty by increasing the inoculum density. Subsequently, we used a fed‐batch strategy by maintaining low HMF concentration in the culture to maximize the final FDCA titre. Using this approach, 545 mM of FDCA was accumulatively produced after 72 hs, which is the highest production rate per unit mass of cells to the best of our knowledge.

An integration vector capable of stably integrating and maintaining in the chromosomes of several lactobacilli over hundreds of generations has been constructed. The major integration machinery used is based on the ΦAT3 integrase (int) and attP sequences determined previously. A novel core sequence located at the 3' end of the tRNA(leu) gene is identified in Lactobacillus fermentum ATCC 14931 as the integration target by the integration vector though most of such sequences found in other lactobacilli are similar to that determined previously. Due to the lack of an appropriate attB site in Lactococcus lactis MG1363, the integration vector is found to be unable to integrate into the chromosome of the strain. However, such integration can be successfully restored by cotransforming the integration vector with a replicative one harboring both attB and erythromycin resistance sequences into the strain. Furthermore, the integration vector constructed carries a promoter region of placT from the chromosome of Lactobacillus rhamnosus TCELL-1 which is used to express green fluorescence and luminance protein genes in the lactobacilli studied.