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2009, Journal of Bioscience and Bioengineering
In order to achieve direct and efficient fermentation of optically pure D-lactic acid from raw corn starch, we constructed L-lactate dehydrogenase gene (ldhL1)-deficient Lactobacillus plantarum and introduced a-amylase from a Streptococcus bovis 148 (AmyA)-secreting plasmid. The resulting strain produced only D-lactic acid from glucose and successfully expressed amyA. With the aid of secreting AmyA, direct D-lactic acid fermentation from raw corn starch was accomplished. After 48 h of fermentation, 73.4 g/l of lactic acid was produced with high yield (0.85 g/g of consumed sugar) and an optical purity of 99.6k. Moreover, a strain substituting the ldhL1 gene with an amyA-secreting expression cassette was constructed. Using this strain, direct D-lactic acid fermentation from raw corn starch was accomplished in the absence of selective pressure by antibiotics.
Applied and Environmental Microbiology, 2009
In order to achieve direct and efficient fermentation of optically pure D-lactic acid from raw corn starch, we constructed L-lactate dehydrogenase gene (ldhL1)-deficient Lactobacillus plantarum and introduced a plasmid encoding Streptococcus bovis 148 ␣-amylase (AmyA). The resulting strain produced only D-lactic acid from glucose and successfully expressed amyA. With the aid of secreting AmyA, direct D-lactic acid fermentation from raw corn starch was accomplished. After 48 h of fermentation, 73.2 g/liter of lactic acid was produced with a high yield (0.85 g per g of consumed sugar) and an optical purity of 99.6%. Moreover, a strain replacing the ldhL1 gene with an amyA-secreting expression cassette was constructed. Using this strain, direct D-lactic acid fermentation from raw corn starch was accomplished in the absence of selective pressure by antibiotics. This is the first report of direct D-lactic acid fermentation from raw starch.
BMC biotechnology, 2016
A thermal tolerant stereo-complex poly-lactic acid (SC-PLA) can be made by mixing Poly-D-lactic acid (PDLA) and poly-L-lactic acid (PLLA) at a defined ratio. This environmentally friendly biodegradable polymer could replace traditional recalcitrant petroleum-based plastics. To achieve this goal, however, it is imperative to produce optically pure lactic acid isomers using a cost-effective substrate such as cellulosic biomass. The roadblock of this process is that: 1) xylose derived from cellulosic biomass is un-fermentable by most lactic acid bacteria; 2) the glucose effect results in delayed and incomplete xylose fermentation. An alternative strain devoid of the glucose effect is needed to co-utilize both glucose and xylose for improved D-lactic acid production using a cellulosic biomass substrate. A previously engineered L-lactic acid Escherichia coli strain, WL204 (ΔfrdBC ΔldhA ΔackA ΔpflB ΔpdhR ::pflBp6-acEF-lpd ΔmgsA ΔadhE, ΔldhA::ldhL), was reengineered for production of D-lac...
Microbial Cell Factories, 2013
Background Polylactic acid (PLA), a biodegradable polymer, has the potential to replace (at least partially) traditional petroleum-based plastics, minimizing “white pollution”. However, cost-effective production of optically pure L-lactic acid is needed to achieve the full potential of PLA. Currently, starch-based glucose is used for L-lactic acid fermentation by lactic acid bacteria. Due to its competition with food resources, an alternative non-food substrate such as cellulosic biomass is needed for L-lactic acid fermentation. Nevertheless, the substrate (sugar stream) derived from cellulosic biomass contains significant amounts of xylose, which is unfermentable by most lactic acid bacteria. However, the microorganisms that do ferment xylose usually carry out heterolactic acid fermentation. As a result, an alternative strain should be developed for homofermentative production of optically pure L-lactic acid using cellulosic biomass. Results In this study, an ethanologenic Escheric...
Applied and Environmental Microbiology, 2009
Applied Microbiology and Biotechnology, 2007
To achieve direct and efficient lactic acid production from starch, a genetically modified Lactococcus lactis IL 1403 secreting α-amylase, which was obtained from Streptococcus bovis 148, was constructed. Using this strain, the fermentation of soluble starch was achieved, although its rate was far from efficient (0.09 g l−1 h−1 lactate). High-performance liquid chromatography revealed that maltose accumulated during fermentation, and this was thought to lead to inefficient fermentation. To accelerate maltose consumption, starch fermentation was examined using L. lactis cells adapted to maltose instead of glucose. This led to a decrease in the amount of maltose accumulation in the culture, and, as a result, a more rapid fermentation was accomplished (1.31 g l−1 h−1 lactate). Maximum volumetric lactate productivity was further increased (1.57 g l−1 h−1 lactate) using cells adapted to starch, and a high yield of lactate (0.89 g of lactate per gram of consumed sugar) of high optical purity (99.2% of l-lactate) was achieved. In this study, we propose a new approach to lactate production by α-amylase-secreting L. lactis that allows efficient fermentation from starch using cells adapted to maltose or starch before fermentation.
Applied and Environmental Microbiology, 2009
Food Microbiology, 2008
A new Lactococcus lactis subsp. lactis B84, capable of utilizing starch as a sole carbon source and producing L(+)-lactate, was isolated from spontaneously fermented rye sourdough. Aiming at maximum lactic acid productivity, the components of the media and the cultivation conditions were varied. In MRS-starch medium (with absence of yeast and meat extracts), at 33 1C, agitation 200 rpm and pH 6.0 for 6 days complete starch hydrolysis occurred and 5.5 g l À1 lactic acid were produced from 18 g l À1 starch.
World Journal of Microbiology and Biotechnology, 2020
High-quality environmentally-friendly bioplastics can be produced by mixing poly-L-lactate with poly-D-lactate. On an industrial scale, this process simultaneously consumes large amounts of both optically pure lactate stereoisomers. However, because optimal growth conditions of L-lactate producers often differ from those of D-lactate producers, each stereoisomer is produced in a specialised facility, which raises cost and lowers sustainability. To address this challenge, we metabolically engineered Lactobacillus gasseri JCM 1131 T , a bioprocess-friendly and genetically malleable strain of homofermentative lactic acid bacterium, to efficiently produce either pure L-or pure D-lactate under the same bioprocess conditions. Transformation of L. gasseri with plasmids carrying additional genes for L-or D-lactate dehydrogenases failed to affect the ratio of produced stereoisomers, but inactivation of the endogenous genes created strains which yielded 0.96 g of either L-or D-lactate per gram of glucose. In this study, the plasmid pHBintE, routinely used for gene disruption in Bacillus megaterium, was used for the first time to inactivate genes in lactobacilli. Strains with inactivated genes for endogenous lactate dehydrogenases efficiently fermented sugars released by enzymatic hydrolysis of alkali pre-treated wheat straw, an abundant lignocellulose-containing raw material, producing 0.37-0.42 g of lactate per gram of solid part of alkali-treated wheat straw. Thus, the constructed strains are primed to serve as producers of both optically pure L-lactate and D-lactate in the next-generation biorefineries.
Biotechnology Advances, 2008
Lactic acid, an enigmatic chemical has wide applications in food, pharmaceutical, leather, textile industries and as chemical feed stock. Novel applications in synthesis of biodegradable plastics have increased the demand for lactic acid. Microbial fermentations are preferred over chemical synthesis of lactic acid due to various factors. Refined sugars, though costly, are the choice substrates for lactic acid production using Lactobacillus sps. Complex natural starchy raw materials used for production of lactic acid involve pretreatment by gelatinization and liquefaction followed by enzymatic saccharification to glucose and subsequent conversion of glucose to lactic acid by Lactobacillus fermentation. Direct conversion of starchy biomass to lactic acid by bacteria possessing both amylolytic and lactic acid producing character will eliminate the two step process to make it economical. Very few amylolytic lactic acid bacteria with high potential to produce lactic acid at high substrate concentrations are reported till date. In this view, a search has been made for various amylolytic LAB involved in production of lactic acid and utilization of cheaply available renewable agricultural starchy biomass. Lactobacillus amylophilus GV6 is an efficient and widely studied amylolytic lactic acid producing bacteria capable of utilizing inexpensive carbon and nitrogen substrates with high lactic acid production efficiency. This is the first review on amylolytic bacterial lactic acid fermentations till date.
Journal of industrial microbiology & biotechnology, 2015
A newly isolated Bacillus sp. MC-07 showed 99.2 % 16S rRNA gene sequence similarity with the Bacillus thermoamylovorans LMG 18084(T). It demonstrated optimum and maximum growth temperatures of 50 and 62 °C, respectively. The ability of MC-07 to produce optically pure L-lactic acid via direct fermentation of starch without enzymatic hydrolysis was investigated at different pH values (6.0-8.0) by intermittent adjustments every 12 h. During batch fermentation in mineral salt medium containing 0.001 % yeast extract at pH 7.0, 20 g/L of soluble starch was utilized to produce 16.6 g/L L-lactic acid at 50 °C within 24 h of fermentation, with 100 % optical purity, 92.1 % lactic acid selectivity, and an L-lactic acid yield of 0.977 g/g. Direct starch fermentation at pHs 6.0, 6.5, 7.5, and 8.0 resulted in considerably lower concentrations of lactic acid than did at pH 7.0. Compared with B. thermoamylovorans LMG 18084(T), the ability of strain MC-07 to produce L-lactic acid was superior.
Bioprocess and Biosystems Engineering, 2013
Poly-lactic acid (PLA) derived from renewable resources is considered to be a good substitute for petroleum-based plastics. The number of poly L-lactic acid applications is increased by the introduction of a stereocomplex PLA, which consists of both poly-L and D-lactic acid and has a higher melting temperature. To date, several studies have explored the production of L-lactic acid, but information on biosynthesis of D-lactic acid is limited. Pulp and corn stover are abundant, renewable lignocellulosic materials that can be hydrolyzed to sugars and used in biosynthesis of D-lactic acid. In our study, saccharification of pulp and corn stover was done by cellulase CTec2 and sugars generated from hydrolysis were converted to D-lactic acid by a homofermentative strain, L. delbrueckii, through a sequential hydrolysis and fermentation process (SHF) and a simultaneous saccharification and fermentation process (SSF). 36.3 g L-1 of Dlactic acid with 99.8% optical purity was obtained in the batch fermentation of pulp and attained highest yield and productivity of 0.83 g g-1 and 1.01 g L-1 h-1 , respectively. Luedeking-Piret model described the mixed growth-associated production of D-lactic acid with a maximum specific growth rate 0.2 h-1 and product formation rate 0.026 h-15 1 ,obtained for this strain. The efficient synthesis of D-lactic acid having high optical 16 purity and melting point will lead to unique stereo-complex PLA with innovative 17 applications in polymer industry. 18 Keywords D-lactic acid, fermentation, corn stover, pulp, biosynthesis List of symbols µ max Maximum specific growth rate (h-1) 21 C 0 Initial glucose concentration (g L-1) 22 C p Product concentration (g L-1) 3 Y PS Product yield (g lactic acid g-1 glucose) Y ´P S Product overall yield (g lactic acid g-1 biomass) Y XS Yield of cell dry mass from substrate (g cell dry mass g-1 glucose) Y PX Yield of product from cell dry mass (g D-lactic acid g-1 cell dry mass) q PS Product formation rate (h-1) calculated based on the equation q PS= dt dP S 1 5 Q p Productivity (g L-1 h-1
World Journal of Microbiology & Biotechnology, 2002
Lactobacillus amylophilus GV6 fermented a variety of pure and natural starches directly to L(+) lactic acid. Starch to lactic acid conversion efficiency was more than 90% by strain GV6 at low substrate concentrations with all starches. The strain GV6 produced high yields of lactic acid per g of substrate utilized with pure starches such as soluble starch, corn starch, and potato starch, yielding 92–96% at low substrate concentrations in 2 days and 78–89% at high substrate (10%) concentrations in 4–6 days. Strain GV6 also produced high yields of lactic acid per g of substrate utilized with crude starchy substrates such as wheat flour, sorghum flour, cassava flour, rice flour and barley flour yielding 90–93% at low substrate concentrations in 2 days and 80% or more at high substrate concentrations in 6–7 days. Lactic acid yields by L. amylophilus GV6 with pure starches were comparable when low cost crude starchy substrates were used. Lactic acid productivity by strain GV6 is higher than for any other previously reported strains of L. amylophilus.
Microbial Cell Factories
Background Bioplastics, like polylactic acid (PLA), are renewable alternatives for petroleum-based plastics. Lactic acid, the monomer of PLA, has traditionally been produced biotechnologically with bacteria. With genetic engineering, yeast have the potential to replace bacteria in biotechnological lactic acid production, with the benefits of being acid tolerant and having simple nutritional requirements. Lactate dehydrogenase genes have been introduced to various yeast to demonstrate this potential. Importantly, an industrial lactic acid producing process utilising yeast has already been implemented. Utilisation of D-xylose in addition to D-glucose in production of biochemicals such as lactic acid by microbial fermentation would be beneficial, as it would allow lignocellulosic raw materials to be utilised in the production processes.ResultsThe yeast Candida sonorensis, which naturally metabolises D-xylose, was genetically modified to produce L-lactic acid from D-xylose by integratin...
Journal of Industrial Microbiology and Biotechnology, 2001
Recombinant Escherichia coli have been constructed for the conversion of glucose as well as pentose sugars into L -lactic acid. The strains carry the lactate dehydrogenase gene from Streptococcus bovis on a low copy number plasmid for production of L -lactate. Three E. coli strains were transformed with the plasmid for producing L -lactic acid. Strains FBR9 and FBR11 were serially transferred 10 times in anaerobic cultures in sugar -limited medium containing glucose or xylose without selective antibiotic. An average of 96% of both FBR9 and FBR11 cells maintained pVALDH1 in anaerobic cultures. The fermentation performances of FBR9, FBR10, and FBR11 were compared in pH -controlled batch fermentations with medium containing 10% w / v glucose. Fermentation results were superior for FBR11, an E. coli B strain, compared to those observed for FBR9 or FBR10. FBR11 exhausted the glucose within 30 h, and the maximum lactic acid concentration ( 7.32% w / v ) was 93% of the theoretical maximum. The other side -products detected were cell mass and succinic acid ( 0.5 g / l ).
Journal of Industrial Microbiology, 1991
An alternative process for industrial lactic acid production was developed using a starch degrading lactic acid producing organism, Lactobacillus amylovorus B-4542. In this process, saccharification takes place during the fermentation, eliminating the need for complete hydrolysis of the starch to glucose prior to fermentation. The cost savings of this alternative are substantial since it eliminates the energy input, separate reactor tank, time, and enzyme associated with the typical pre-fermentation saccharification step. The only pre-treatment was gelatinization and enzyme-thinning of the starch to overcome viscosity problems associated with high starch concentrations and to make the starch more rapidly degradable. This fermentation process was optimized for temperature, substrate level, nitrogen source and level, mineral level, B-vitamins, volatile fatty acids, pH, and buffer source. The rate of the reaction and the final level of lactic acid obtained in the optimized liquefied starch process was similar to that obtained with L. delbrueckii B-445 using glucose as the substrate.
Food Technology and Biotechnology
Batch cultivation of mono-culture of Lactobacillus sp. and two-membered mixed culture of Lactobacillus sp. and Lactobacillus amylovorus DSM 20531T was carried out with the aim of producing L-(+)- and D-(-)/L-(+)-lactic acid to be implemented in poly(lactic acid) polymer production. Metabolic capacity of the two Lactobacillus strains to ferment different carbon sources (glucose, sucrose or soluble starch) from MRS medium at 40 C during cultivation in a lab-scale stirred tank bioreactor was defined. Lactobacillus sp. showed similar affinity toward mono- and disaccharide and homofermentatively converted both substrates mostly to L-(+)-lactic acid. L. amylovorus DSM 20531T has been characterized as an D/L-lactate producer and it is capable of conducting simultaneous saccharification and fermentation. Due to interaction of Lactobacillus sp. and L. amylovorus DSM 20531T starch was hydrolysed and fermented to the mixture of L-(+)- and D-(-)-lactic acid. Modified Luedeking-Piret kinetics w...
Bioprocess and Biosystems Engineering, 2000
Lactobacillus amylophilus strain GV6, isolated from corn starch processing industrial wastes, was amylolytic and produced 0.96 g L(+) lactic acid per gram of soluble starch. The optimum temperature and pH for growth and L(+) lactic acid production were 37°C and 6.5, respectively. At low substrate concentrations, the lactic acid production on corn starch was almost similar to soluble starch. The strain is fermenting various naturally available starches directly to lactic acid. The total amylase activity of the strain is 0.59 U/ml/min. The strain produced 49 and 76.2 g/l L(+) lactic acid from 60 g/l corn starch and 90 g/l soluble starch, respectively. This is the highest L(+) lactic acid among the wild strains of L. amylophilus reported so far.
A new amylolytic strain of Lactobacillus paracasei able to convert starch directly into L-(þ)lactic acid (LA) was isolated. The identification of the by 16S rDNA sequencing proved that this strain, B41, is the first amylolytic representative of Lactobacillus casei group. The amylase activity assay revealed that L. paracasei B41 produced extracellular amylolytic enzyme, reaching 62 U/mL in the cell-free supernatants. The optimal conditions for its action were pH 5.0 and temperature 458C. The gene amy1 (1779 bp) encoding the putative B41 amylopullulanase was cloned, sequenced, and analyzed. The deduced protein contained a leader peptide of 28 amino acids and a mature peptide of 564 amino acids. Compared to the amylases of closely related species, B41 enzyme had several amino acid substitutions. An inducible control at amy1 expression was demonstrated. The starch fermentation abilities of L. paracasei B41 were studied in batch processes performed with and without pH control. The highest amount of LA from starch was obtained during 48 h fermentation from 40 g/L substrate at pH maintained at 5.0-37.3 g/L. In addition, 93.3% starch conversion into LA and the highest reported productivity for 24 h were achieved -1.30 g/L/h.
Applied and Environmental Microbiology, 2006
We developed a new cell surface engineering system based on the PgsA anchor protein from Bacillus subtilis. In this system, the N terminus of the target protein was fused to the PgsA protein and the resulting fusion protein was expressed on the cell surface. Using this new system, we constructed a novel starch-degrading strain of Lactobacillus casei by genetically displaying ␣-amylase from the Streptococcus bovis strain 148 with a FLAG peptide tag (AmyAF). Localization of the PgsA-AmyA-FLAG fusion protein on the cell surface was confirmed by immunofluorescence microscopy and flow cytometric analysis. The lactic acid bacteria which displayed AmyAF showed significantly elevated hydrolytic activity toward soluble starch. By fermentation using AmyAF-displaying L. casei cells, 50 g/liter of soluble starch was reduced to 13.7 g/liter, and 21.8 g/liter of lactic acid was produced within about 24 h. The yield in terms of grams of lactic acid produced per gram of carbohydrate utilized was 0.60 g per g of carbohydrate consumed at 24 h. Since AmyA was immobilized on the cells, cells were recovered after fermentation and used repeatedly. During repeated utilization of cells, the lactic acid yield was improved to 0.81 g per g of carbohydrate consumed at 72 h. These results indicate that efficient simultaneous saccharification and fermentation from soluble starch to lactic acid were carried out by recombinant L. casei cells with cell surface display of AmyA.
Enzyme and Microbial Technology, 2014
Lactobacillus coryniformis is known to produce d-lactic acid as a dominant fermentation product at a cultivation temperature of approximately 30 • C. However, the considerable production of l-lactic acid is observed when the fermentation temperature is greater than 40 • C. Because optically pure lactates are synthesized from pyruvate by the catalysis of chiral-specific d-or l-lactate dehydrogenase, the higher thermostability of l-LDHs is assumed to be one of the key factors decreasing the optical purity of d-lactic acid produced from L. coryniformis at high temperature. To verify this hypothesis, two types of d-ldh genes and six types of l-ldh genes based on the genomic information of L. coryniformis were synthesized and expressed in Escherichia coli. Among the LDHs tested, five LDHs showed activity and were used to construct polyclonal antibodies. d-LDH1, l-LDH2, and l-LDH3 were found to be expressed in L. coryniformis by Western blotting analysis. The half-life values (t 1/2 ) of the LDHs at 40 • C were estimated to be 10.50, 41.76, and 2311 min, and the T 50 10 values were 39.50, 39.90, and 58.60 • C, respectively. In addition, the T m values were 36.0, 41.0, and 62.4 • C, respectively, which indicates that l-LDH has greater thermostability than d-LDH. The higher thermostability of l-LDHs compared with that of d-LDH1 may be a major reason why the enantiopurity of d-lactic acid is decreased at high fermentation temperatures. The key enzymes characterized will suggest a direction for the design of genetically modified lactic acid bacteria to produce optically pure d-lactic acid.
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