Strain improvement of <Emphasis Type="Italic">Lactobacillus lactis</Emphasis> for <Emphasis Type="SmallCaps">d</Emphasis>-lactic acid production

Three mutants, isolated by repeated UV mutagenesis of Lactobacillus lactis NCIM 2368, produced increased d-lactic acid concentrations. These mutants were compared with the wild type using 100 g hydrolyzed cane sugar/l in the fermentation medium. One mutant, RM2-24, produced 81 g lactic acid/l which was over three times that of the wild type. The highest d-lactic acid (110 g/l) in batch fermentation was obtained with 150 g cane sugar/l with a 73% lactic acid yield. The mutant utilizes cellobiose efficiently, converting it into d-lactic acid suggesting the presence of cellobiase. Thus, this strain could be used to obtain d-lactic acid from cellulosic materials that are pre-hydrolyzed with cellulase.     

Low-cost effective culture medium optimization for <Emphasis Type="SmallCaps">d</Emphasis>-lactic acid production by <Emphasis Type="Italic">Lactobacillus coryniformis</Emphasis> subsp. <Emphasis Type="Italic">torquens</Emphasis> under oxygen-deprived condition

Lactic acid is considered a commodity and its production is boosted by the synthesis of polylactic acid. d-lactic acid (DLA) isomer offers greater flexibility and biodegradability and it can only be obtained in its pure form through fermentation. The lactate dehydrogenase is stereospecific for homofermentative production of DLA isomer in the metabolic pathway of Lactobacillus coryniformis subsp. torquens, with optical purity of ≥?99.9% under oxygen-deprived condition. A simple culture medium that increases DLA production and reduces fermentation costs is fundamental for industrial applicability. A central composite rotatable design was used to evaluate significant components influencing the DLA production. Concentrations were adjusted using the Design-Expert 7.0 optimization tool with a desirability coefficient of 0.693 and the best concentrations of each component were determined. Finally, an assay in the bioreactor with the modified culture medium resulted in a product yield of 0.95 g/g, volumetric productivity of 0.85 g/L.h and 95% of efficiency.     

Highly efficient production of <Emphasis Type="SmallCaps">d</Emphasis>-lactic acid from chicory-derived inulin by <Emphasis Type="Italic">Lactobacillus bulgaricus</Emphasis>

Inulin is a readily available feedstock for cost-effective production of biochemicals. To date, several studies have explored the production of bioethanol, high-fructose syrup and fructooligosaccharide, but there are no studies regarding the production of d-lactic acid using inulin as a carbon source. In the present study, chicory-derived inulin was used for d-lactic acid biosynthesis by Lactobacillus bulgaricus CGMCC 1.6970. Compared with separate hydrolysis and fermentation processes, simultaneous saccharification and fermentation (SSF) has demonstrated the best performance of d-lactic acid production. Because it prevents fructose inhibition and promotes the complete hydrolysis of inulin, the highest d-lactic acid concentration (123.6 ± 0.9 g/L) with a yield of 97.9 % was obtained from 120 g/L inulin by SSF. Moreover, SSF by L. bulgaricus CGMCC 1.6970 offered another distinct advantage with respect to the higher optical purity of d-lactic acid (>99.9 %) and reduced number of residual sugars. The excellent performance of d-lactic acid production from inulin by SSF represents a high-yield method for d-lactic acid production from non-food grains.     

Enhanced production of lactic acid by an adapted strain of <Emphasis Type="Italic">Lactobacillus</Emphasis><Emphasis Type="Italic">delbrueckii</Emphasis> subsp. <Emphasis Type="Italic">lactis</Emphasis>

Lactobacillus delbrueckii subsp. lactis strains were developed having increased activity, by gradually acclimatizing the bacteria to acidic conditions over repeated batch culture. Cells from one batch culture were used as the inoculum for the subsequent batch culture and thereby an adapted strain of Lactobacillus was obtained showing improved lactic acid productivity, cell growth and total glucose utilization. Furthermore, the acclimatized cells used significantly less nitrogen for a given level of lactic acid production, which is significant from an industrial point of view. The developed procedure decreases fermentation time and nutrient use, leading to reduced operation costs, while providing a lactic acid yield superior to previously reported methods.     

Production of <Emphasis Type="SmallCaps">d</Emphasis>-lactic acid from sugarcane molasses,sugarcane juice and sugar beet juice by <Emphasis Type="Italic">Lactobacillus delbrueckii</Emphasis>

Lactobacillus delbrueckii was grown on sugarcane molasses, sugarcane juice and sugar beet juice in batch fermentation at pH 6 and at 40°C. After 72 h, the lactic acid from 13% (w/v) sugarcane molasses (119 g total sugar l⁻¹) and sugarcane juice (133 g total sugar l⁻¹) was 107 g l⁻¹ and 120 g l⁻¹, respectively. With 10% (w/v) sugar beet juice (105 g total sugar l⁻¹), 84 g lactic acid l⁻¹ was produced. The optical purities of d-lactic acid from the feedstocks ranged from 97.2 to 98.3%.     

Nutritional Requirements of <Emphasis Type="Italic">Lactobacillus delbrueckii</Emphasis> subsp. <Emphasis Type="Italic">lactis</Emphasis> in a Chemically Defined Medium

This study was undertaken to determine the nutritional requirements of Lactobacillus delbrueckii subsp. lactis and to develop a minimal chemically defined medium that supports sustained growth of these microorganisms. The single-omission technique was applied to each component of complete chemically defined medium in order to determine the nutritional requirements. L. delbrueckii subsp. lactis was prototrophic for alanine, glycine, aspartic acid, asparagine, glutamine, threonine, and proline. The lysine requirement was strain-dependent. Magnesium was the only essential oligoelement. These microorganisms also required uracil and guanine and adenine as pyrimidine and purine sources, respectively. In view of the nutritional requirements we designed a new minimal defined medium which supports sustained growth of L. delbrueckii subsp. lactis. This medium is simple and well defined, and should be preferable to complex media for conducting future biochemical, physiological, and genetic studies on L. delbrueckii subsp. lactis.     

Production of <Emphasis Type="SmallCaps">d</Emphasis>-lactic acid by <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> under oxygen deprivation

In mineral salts medium under oxygen deprivation, Corynebacterium glutamicum exhibits high productivity of l-lactic acid accompanied with succinic and acetic acids. In taking advantage of this elevated productivity, C. glutamicum was genetically modified to produce d-lactic acid. The modification involved expression of fermentative d-lactate dehydrogenase (d-LDH)-encoding genes from Escherichia coli and Lactobacillus delbrueckii in l-lactate dehydrogenase (l-LDH)-encoding ldhA-null C. glutamicum mutants to yield strains C. glutamicum ΔldhA/pCRB201 and C. glutamicum ΔldhA/pCRB204, respectively. The productivity of C. glutamicum ΔldhA/pCRB204 was fivefold higher than that of C. glutamicum ΔldhA/pCRB201. By using C. glutamicum ΔldhA/pCRB204 cells packed to a high density in mineral salts medium, up to 1,336 mM (120 g l⁻¹) of d-lactic acid of greater than 99.9% optical purity was produced within 30 h.     

Metabolomic and proteomic analysis of <Emphasis Type="SmallCaps">d</Emphasis>-lactate-producing <Emphasis Type="Italic">Lactobacillus delbrueckii</Emphasis> under various fermentation conditions

As an important feedstock monomer for the production of biodegradable stereo-complex poly-lactic acid polymer, d-lactate has attracted much attention. To improve d-lactate production by microorganisms such as Lactobacillus delbrueckii, various fermentation conditions were performed, such as the employment of anaerobic fermentation, the utilization of more suitable neutralizing agents, and exploitation of alternative nitrogen sources. The highest d-lactate titer could reach 133 g/L under the optimally combined fermentation condition, increased by 70.5% compared with the control. To decipher the potential mechanisms of d-lactate overproduction, the time-series response of intracellular metabolism to different fermentation conditions was investigated by GC–MS and LC–MS/MS-based metabolomic analysis. Then the metabolomic datasets were subjected to weighted correlation network analysis (WGCNA), and nine distinct metabolic modules and eight hub metabolites were identified to be specifically associated with d-lactate production. Moreover, a quantitative iTRAQ–LC–MS/MS proteomic approach was employed to further analyze the change of intracellular metabolism under the combined fermentation condition, identifying 97 up-regulated and 42 down-regulated proteins compared with the control. The in-depth analysis elucidated how the key factors exerted influence on d-lactate biosynthesis. The results revealed that glycolysis and pentose phosphate pathways, transport of glucose, amino acids and peptides, amino acid metabolism, peptide hydrolysis, synthesis of nucleotides and proteins, and cell division were all strengthened, while ATP consumption for exporting proton, cell damage, metabolic burden caused by stress response, and bypass of pyruvate were decreased under the combined condition. These might be the main reasons for significantly improved d-lactate production. These findings provide the first omics view of cell growth and d-lactate overproduction in L. delbrueckii, which can be a theoretical basis for further improving the production of d-lactate.     

Effect of temperature on <Emphasis Type="SmallCaps">d</Emphasis>-arabitol production from lactose by <Emphasis Type="Italic">Kluyveromyces lactis</Emphasis>

d-Arabitol production from lactose by Kluyveromyces lactis NBRC 1903 has been studied by following the time courses of concentrations of cell mass, lactose, d-arabitol, ethanol, and glycerol at different temperatures. It was found that temperature is a key factor in d-arabitol production. Within temperatures ranging from 25 to 39°C, the highest d-arabitol concentration of 99.2 mmol l⁻¹ was obtained from 555 mmol l⁻¹ of lactose after 120 h of batch cultivation at 37°C. The yield of d-arabitol production on cell mass growth increased drastically at temperatures higher than 35°C, and the yield reached 1.07 at 39°C. Increasing the cell mass concentration two-fold after 24 h of culture growth at 37°C, the d-arabitol concentration further increased to 168 mmol l⁻¹. According to the distribution of the metabolic products, metabolic changes related to growth phase were also discussed. The stationary-phase K. lactis cells in the batch culture that is started with exposing the precultured inoculum to high osmotic stress, high oxidative stress, and high heat stress are found to be preferable for d-arabitol production.     

Biotechnological production of enantiomerically pure <Emphasis Type="Italic">d</Emphasis>-lactic acid

The fermentation process of l-lactic acid is well known. Little importance was attached to d-lactic acid, but in the past 10 years, d-lactic acid gained significantly in importance. d-Lactic acid is an interesting precursor for manufacturing heat-resistant polylactic acid (PLA) bioplastics which can be widely used, for example as packaging material, coatings, for textiles or in the automotive industry.This review provides a comprehensive overview of the most recent developments, including a spectrum of studied microorganisms and their capabilities for the production of d-lactic acid. Additionally, the technological achievements in biotechnological d-lactic acid production including fermentation techniques like fed batch, simultaneous saccharification, and fermentation and continuous techniques are presented. Attention is also turned to suitable alternative substrates and their applicability in fermentation processes. Furthermore, advantages and disadvantages of product recovery and purification are discussed. Economic aspects of PLA are pointed out, and the present industrial producers of lactic acid are briefly introduced.     

Enhancement of Nisin Production by <Emphasis Type="Italic">Lactococcus lactis</Emphasis> subsp. <Emphasis Type="Italic">lactis</Emphasis>

Lactococcus lactis subsp lactis BSA (L. lactis BSA) was isolated from a commercial fermented product (BSA Food Ingredients, Montreal, Canada) containing mixed bacteria that are used as starter for food fermentation. In order to increase the bacteriocin production by L. lactis BSA, different fermentation conditions were conducted. They included different volumetric combinations of two culture media (the Man, Rogosa and Sharpe (MRS) broth and skim milk), agitation level (0 and 100 rpm) and concentration of commercial nisin (0, 0.15, and 0.30 µg/ml) added into culture media as stimulant agent for nisin production. During fermentation, samples were collected and used for antibacterial evaluation against Lactobacillus sakei using agar diffusion assay. Results showed that medium containing 50 % MRS broth and 50 % skim milk gave better antibacterial activity as compared to other medium formulations. Agitation (100 rpm) did not improve nisin production by L. lactis BSA. Adding 0.15 µg/ml of nisin into the medium-containing 50 % MRS broth and 50 % skim milk caused the highest nisin activity of 18,820 AU/ml as compared to other medium formulations. This activity was 4 and ~3 times higher than medium containing 100 % MRS broth without added nisin (~4700 AU/ml) and 100 % MRS broth with 0.15 µg/ml of added nisin (~6650 AU/ml), respectively.     

Biosynthesis of <Emphasis Type="SmallCaps">d</Emphasis>-lactic acid from lignocellulosic biomass

d-lactic acid is a versatile and important industrial chemical that can be applied in the synthesis of thermal-resistant poly-lactic acid. Biosynthesis of d-lactic acid can be achieved by a variety of microorganisms, including lactic acid bacteria, yeast, and fungi; however, the final product yield, optical purity, and the utilization of both glucose and xylose are restricted. Consequently, engineered microbial systems are essential to attain high titer, productivity, and complete utilization of sugars. Herein, we critically evaluate the promising wild-type microorganisms, as well as genetically modified microorganisms to produce enantiomerically pure d-lactic acid, particularly from renewable lignocellulosic biomass. In addition, innovative bioreactor operation, metabolic flux analysis, and recent genetic engineering methods for targeted microbial d-lactic acid synthesis will be discussed.     

<Emphasis Type="SmallCaps">d</Emphasis>-Psicose production from <Emphasis Type="SmallCaps">d</Emphasis>-fructose using an isolated strain, <Emphasis Type="Italic">Sinorhizobium</Emphasis> sp.

Sinorhizobium sp., which can convert d-fructose into d-psicose, was isolated from soil. The optimal pH, temperature, and cell concentration for d-psicose production with the isolated strain were 8.5, 40°C, and 60 mg/ml, respectively. The toluene-treated cells showed 2.5- and 4.8-fold increases in the d-psicose concentration and productivity compared with untreated washed cells. Under the optimal conditions, the toluene-treated cells produced 37 g d-psicose/l from 70% (w/v) (3.9 M) d-fructose after 15 h.     

A novel chimeric prophage vB_LdeS-phiJB from commercial <Emphasis Type="Italic">Lactobacillus delbrueckii</Emphasis> subsp. <Emphasis Type="Italic">bulgaricus</Emphasis>

Prophage vB_LdeS-phiJB (phiJB) was induced by mitomycin C and UV radiation from the Lactobacillus delbrueckii subsp. bulgaricus SDMCC050201 isolated from a Chinese yoghurt sample. It has an isometric head and a non-contractile tail with 36,969 bp linear double-stranded DNA genome, which is classified into the group a of Lb. delbrueckii phages. The genome of phiJB is highly modular with functionally related genes clustered together. Unexpectedly, there is no similarity of its DNA replication module to any phages that have been reported, while it consists of open-reading frames homologous to the proteins of Lactobacillus strains. Comparative genomic analysis indicated that its late gene clusters, integration/lysogeny modules and DNA replication module derived from different evolutionary ancestors and integrated into a chimera. Our results revealed a novel chimeric phage of commercial Lb. delbrueckii and will broaden the knowledge of phage diversity in the dairy industry.     

Fermentation performance of an exopolysaccharide-producing strain of<Emphasis Type="Italic"> Lactobacillus delbrueckii</Emphasis> subsp.<Emphasis Type="Italic"> bulgaricus</Emphasis>

The formation of exopolysaccharide (EPS) and extracellular metabolites was studied in a strain of Lactobacillus delbrueckii subsp. bulgaricus (NCFB 2483), grown under batch culture conditions in a semi-defined medium incorporating lactose and casein hydrolysate. Performance parameters were derived from the fermentation data, and kinetic models were applied in order to describe the production of EPS, extracellular metabolites, and biomass produced. Lactose was split intracellularly, with the resultant galactose being exported from the cell, and the glucose being metabolised further to EPS and lactic acid. Production of EPS, lactate, and galactose was closely growth-associated and followed a pattern of primary kinetics. A marginally lower galactose level relative to the modelled levels throughout most of the time course of the fermentation suggests that not all galactose is exported from the cell, and that a low level of flux to other metabolites, such as EPS, might exist.     

Characterization of <Emphasis Type="Italic">Lactococcus lactis</Emphasis> subsp. <Emphasis Type="Italic">lactis</Emphasis> isolated from surface waters

A group of nine presumptive enterococci was isolated on enterococcal selective media Slanetz-Bartley agar and/or kanamycin-esculin-azide agar during a screening of Enterococcus spp. in surface waters. All strains formed a homogeneous cluster separated from all enterococcal species using rep-PCR fingerprinting with the (GTG)(5) primer but they matched fingerprints revealed by Lactococcus lactis subsp. lactis representatives. Further identification using extensive biotyping and automated ribotyping with EcoRI (RiboPrinter(R) microbial characterization system) confirmed all strains as L. lactis subsp. lactis in full correspondence with the (GTG)(5)-PCR. We demonstrated that L. lactis subsp. lactis strains occur in different surface waters and can be confused with enterococci due to their positive growth on selective enterococcal media as well as positive results in tests commonly used for identification of the genus Enterococcus (esculin hydrolysis, acetoin and pyrrolidonyl arylamidase production, growth at 10 degrees C and in 6.5% NaCl). The (GTG)(5)-PCR fingerprinting was revealed as a reliable and fast method for the identification of L. lactis subsp lactis while automated ribotyping with EcoRI proved to be a good tool for intrasubspecies typing purposes.     

Fermentation of <Emphasis Type="SmallCaps">d</Emphasis>-glucose and <Emphasis Type="SmallCaps">d</Emphasis>-xylose mixtures by <Emphasis Type="Italic">Candida tropicalis</Emphasis> NBRC 0618 for xylitol production

The fermentation of d-glucose and d-xylose mixtures by the yeast Candida tropicalis NBRC 0618 has been studied under the most favourable operation conditions for the culture, determining the most adequate initial proportion in these sugars for xylitol production. In all the experiments a synthetic culture medium was used, with an initial total substrate concentration of 25 g L⁻¹, a constant pH of 5.0 and a temperature of 30 °C. From the experimental results, it was deduced that the highest values of specific rates of production and of overall yield in xylitol were achieved for the mixtures with the highest percentage of d-xylose, specifically in the culture with the initial d-glucose and d-xylose concentrations of 1 and 24 g L⁻¹, respectively, with an overall xylitol yield of 0.28 g g⁻¹. In addition, the specific rates of xylitol production declined over the time course of the culture and the formation of this bioproduct was favoured by the presence of small quantities of d-glucose. The sum of the overall yield values in xylitol and ethanol for all the experiments ranged from 0.26 to 0.56 g bioproduct/g total substrate.     

Purification and characterization of <Emphasis Type="SmallCaps">l</Emphasis>-arabinose isomerase from <Emphasis Type="Italic">Lactobacillus plantarum</Emphasis> producing <Emphasis Type="SmallCaps">d</Emphasis>-tagatose

l-arabinose isomerase (EC5.3.1.4. AI) mediates the isomerization of d-galactose into d-tagatose as well as the conversion of l-arabinose into l-ribulose. The AI from Lactobacillus plantarum SK-2 was purified to an apparent homogeneity giving a single band on SDS–PAGE with a molecular mass of 59.6 kDa. Optimum activity was observed at 50°C and pH 7.0. The enzyme was stable at 50°C for 2 h and held between pH 4.5 and 8.5 for 1 h. AI activity was stimulated by Mn²⁺, Fe³⁺, Fe²⁺, Ca²⁺ and inhibited by Cu²⁺, Ag⁺, Hg²⁺, Pb²⁺. d-galactose and l-arabinose as substrates were isomerized with high activity. l-arabitol was the strongest competitive inhibitor of AI. The apparent Michaelis–Menten constant (K _m), for galactose, was 119 mM. The first ten N-terminal amino acids of the enzyme were determined as MLSVPDYEFW, which is identical to L. plantarum (Q88S84). Using the purified AI, 390 mg tagatose could be converted from 1,000 mg galactose in 96 h, and this production corresponds to a 39% equilibrium.     

<Emphasis Type="SmallCaps">d</Emphasis>-Hexosaminate production by oxidative fermentation

Microbial production of d-hexosaminate was examined by means of oxidative fermentation with acetic acid bacteria. In most strains of acetic acid bacteria, membrane-bound d-glucosamine dehydrogenase (synonymous with an alternative d-glucose dehydrogenase distinct from quinoprotein d-glucose dehydrogenase) oxidized d-hexosamines to the corresponding d-hexosaminates in a stoichiometric manner. Conversion of d-hexosamines to the corresponding d-hexosaminates was observed with growing cells of acetic acid bacteria, and d-hexosaminate was stably accumulated in the culture medium even though d-hexosamine was exhausted. Since the enzyme responsible is located on the outer surface of the cytoplasmic membrane, and the enzyme activity is linked to the respiratory chain of the organisms, resting cells, dried cells, and immobilized cells of acetic acid bacteria were effective catalysts for d-hexosaminate production. d-Mannosaminate and d-galactosaminate were also prepared for the first time by means of oxidative fermentation, and three different d-hexosaminates were isolated from unreacted substrate by a chromatographic separation. In this paper, d-hexosaminate production by oxidative fermentation carried out mainly with Gluconobacter frateurii IFO 3264 is exemplified as a typical example.