Production of optically pure <Emphasis Type="SmallCaps">l</Emphasis>(+)-lactic acid from waste plywood chips using an isolated thermotolerant <Emphasis Type="Italic">Enterococcus faecalis</Emphasis> SI at a pilot scale

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 m³), 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^?1) and yield (0.97 kg kg^?1). Therefore, large-scale l-lactic acid production by E. faecalis SI shows the potential application for industries.     

Efficient production of l-lactic acid by newly isolated thermophilic Bacillus coagulans WCP10-4 with high glucose tolerance

A thermophilic Bacillus coagulans WCP10-4 with tolerance to high concentration of glucose was isolated from soil and used to produce optically pure l-lactic acid from glucose and starch. In batch fermentation at pH?6.0, 240 g/L of glucose was completely consumed giving 210 g/L of l-lactic acid with a yield of 95 % and a productivity of 3.5 g/L/h. In simultaneous saccharification and fermentation at 50 °C without sterilizing the medium, 200 g/L of corn starch was completely consumed producing 202.0 g/L of l-lactic acid. To the best of our knowledge, this strain shows the highest osmotic tolerance to glucose among the strains ever reported for lactic acid production. This is the first report of simultaneous saccharification and fermentation of starch for lactic acid production under a non-sterilized condition.     

Fermentation of corn fiber hydrolysate to lactic acid by the moderate thermophile <Emphasis Type="Italic">Bacillus coagulans</Emphasis>

A strain of Bacillus coagulans that converted mixed sugars of glucose, xylose, and arabinose to l-lactic acid with 85% yield at 50°C was isolated from composted dairy manure. The strain was tolerant to aldehyde growth inhibitors at 2.5 g furfural/l, 2.5 g 5-hydroxymethylfurfural/l, 2.5 g vanillin/l, and 1.2 g p-hydroxybenzaldehyde/l. In a simultaneous saccharification and fermentation process, the strain converted a dilute-acid hydrolysate of 100 g corn fiber/l to 39 g lactic acid/l in 72 h at 50°C. Because of its inhibitor tolerance and ability to fully utilize pentose sugars, this strain has potential to be developed as a biocatalyst for the conversion of agricultural residues into valuable chemicals.     

<Emphasis Type="SmallCaps">l</Emphasis>(+)-Lactic acid production from non-food carbohydrates by thermotolerant <Emphasis Type="Italic">Bacillus coagulans</Emphasis>

Lactic acid is used as an additive in foods, pharmaceuticals, and cosmetics, and is also an industrial chemical. Optically pure lactic acid is increasingly used as a renewable bio-based product to replace petroleum-based plastics. However, current production of lactic acid depends on carbohydrate feedstocks that have alternate uses as foods. The use of non-food feedstocks by current commercial biocatalysts is limited by inefficient pathways for pentose utilization. B. coagulans strain 36D1 is a thermotolerant bacterium that can grow and efficiently ferment pentoses using the pentose-phosphate pathway and all other sugar constituents of lignocellulosic biomass at 50°C and pH 5.0, conditions that also favor simultaneous enzymatic saccharification and fermentation (SSF) of cellulose. Using this bacterial biocatalyst, high levels (150–180 g l⁻¹) of lactic acid were produced from xylose and glucose with minimal by-products in mineral salts medium. In a fed-batch SSF of crystalline cellulose with fungal enzymes and B. coagulans, lactic acid titer was 80 g l⁻¹ and the yield was close to 80%. These results demonstrate that B. coagulans can effectively ferment non-food carbohydrates from lignocellulose to l(+)-lactic acid at sufficient concentrations for commercial application. The high temperature fermentation of pentoses and hexoses to lactic acid by B. coagulans has these additional advantages: reduction in cellulase loading in SSF of cellulose with a decrease in enzyme cost in the process and a reduction in contamination of large-scale fermentations.     

Mutation-Screening in <Emphasis Type="SmallCaps">l</Emphasis>-(+)-Lactic Acid Producing Strains by Ion Implantation

In this paper, in order to obtain some industrial strains with high yield of l-(+)-lactic acid, the wild type strain Lactobacillus casei CICC6028 was mutated by nitrogen ions implantation. By study, it was found that the high positive mutation rate was obtained when the output power was 10 keV and the dose of N⁺ implantation was 50 × 2.6 × 10¹³ ions/cm². In addition, the initial screening methods were also studied, and it was found that the transparent halos method was unavailable, for some high yield strains of l-(+)-lactic acid were missed. Then a mutant strain which was named as N-2 was isolated, its optimum fermentation temperature was 40°C and the l-(+)-lactic acid yield was 136 g/l compared to the original strain whose optimum fermentation temperature was 34°C and l-(+)-lactic acid production was 98 g/l. Finally, High Performance Liquid Chromatography method was used to analyze the purity of l-(+)-lactic acid that was produced by the mutant N-2, and the result showed the main production of N-2 was l-(+)-lactic acid.     

Modelling the influence of pH, temperature, glucose and lactic acid concentrations on the kinetics of lactic acid production by Lactococcus lactis ssp. lactis ATCC 19435 in whole-wheat flour

A kinetic model of the fermentative production of lactic acid from glucose by Lactococcus lactis ssp. lactis ATCC 19435 in whole-wheat flour has been developed. The model consists of terms for substrate and product inhibition as well as for the influence of pH and temperature. Experimental data from fermentation experiments under different physical conditions were used to fit and verify the model. Temperatures above 30 °C and pH levels below 6 enhanced the formation of by-products and d-lactic acid. By-products were formed in the presence of maltose only, whereas d-lactic acid was formed independently of the presence of maltose although the amount formed was greater when maltose was present. The lactic acid productivity was highest between 33 °C and 35 °C and at pH 6. In the concentration interval studied (up to 180 g l⁻¹ glucose and 89  g l⁻¹ lactic acid) simulations showed that both substances were inhibiting. Glucose inhibition was small compared with the inhibition due to lactic acid. Received: 28 October 1997 / Received revision: 3 February 1998 / Accepted: 6 February 1998     

Isolation and characterisation of lactic acid bacterium for effective fermentation of cellobiose into optically pure homo <Emphasis Type="SmallCaps">l</Emphasis>-(+)-lactic acid

Effective utilisation of cellulosic biomasses for economical lactic acid production requires a microorganism with potential ability to utilise efficiently its major components, glucose and cellobiose. Amongst 631 strains isolated from different environmental samples, strain QU 25 produced high yields of l-(+)-lactic acid of high optical purity from cellobiose. The QU 25 strain was identified as Enterococcus mundtii based on its sugar fermentation pattern and 16S rDNA sequence. The production of lactate by fermentation was optimised for the E. mundtii QU25 strain. The optimal pH and temperature for batch culturing were found to be 7.0°C and 43°C, respectively. E. mundtii QU 25 was able to metabolise a mixture of glucose and cellobiose simultaneously without apparent carbon catabolite repression. Moreover, under the optimised culture conditions, production of optically pure l-lactic acid (99.9%) increased with increasing cellobiose concentrations. This indicates that E. mundtii QU 25 is a potential candidate for effective lactic acid production from cellulosic hydrolysate materials.     

Production of <Emphasis Type="SmallCaps">l</Emphasis>-lactic acid by <Emphasis Type="Italic">Rhizopus oryzae</Emphasis> using semicontinuous fermentation in bioreactor

Semicontinuous fermentation using pellets of Rhizopus oryzae has been recognized as a promising technology for l-lactic acid production. In this work, semicontinuous fermentation of R. oryzae AS 3.819 for l-lactic acid production has been developed with high l-lactic acid yield and volumetric productivity. The effects of factors such as inoculations, CaCO₃ addition time, and temperature on l-lactic acid yield and R. oryzae morphology were researched in detail. The results showed that optimal fermentation conditions for the first cycle were: inoculation with 4% spore suspension, CaCO₃ added to the culture medium at the beginning of culture, and culture temperature of 32–34°C. In orthogonal experiments, high l-lactic acid yield was achieved when the feeding medium was (g/l): glucose, 100; (NH₄)₂SO₄, 2; KH₂PO₄, 0.1; ZnSO₄·7H₂O, 0.33; MgSO₄·7H₂O, 0.15; CaCO₃, 50. Twenty cycles of semicontinuous fermentation were carried out in flask culture. l-lactic acid yield was 78.75% for the first cycle and 80–90% for the repeated cycles; the activities of lactate dehydrogenases (LDH) were 7.2–9.2 U/mg; fermentation was completed in 24 h for each repeated cycle. In a 7-l magnetically stirred fermentor, semicontinuous fermentation lasted for 25 cycles using pellets of R. oryzae AS 3.819 under the optimal conditions determined from flask cultures. The final l-lactic acid concentration (LLAC) reached 103.7 g/l, and the volumetric productivity was 2.16 g/(l·h) for the first cycle; in the following 19 repeated cycles, the final LLAC reached 81–95 g/l, and the volumetric productivities were 3.40–3.85 g/(l·h).     

Physiological and fermentation properties of <Emphasis Type="Italic">Bacillus coagulans</Emphasis> and a mutant lacking fermentative lactate dehydrogenase activity

Bacillus coagulans, a sporogenic lactic acid bacterium, grows optimally at 50–55°C and produces lactic acid as the primary fermentation product from both hexoses and pentoses. The amount of fungal cellulases required for simultaneous saccharification and fermentation (SSF) at 55°C was previously reported to be three to four times lower than for SSF at the optimum growth temperature for Saccharomyces cerevisiae of 35°C. An ethanologenic B. coagulans is expected to lower the cellulase loading and production cost of cellulosic ethanol due to SSF at 55°C. As a first step towards developing B. coagulans as an ethanologenic microbial biocatalyst, activity of the primary fermentation enzyme L-lactate dehydrogenase was removed by mutation (strain Suy27). Strain Suy27 produced ethanol as the main fermentation product from glucose during growth at pH 7.0 (0.33 g ethanol per g glucose fermented). Pyruvate dehydrogenase (PDH) and alcohol dehydrogenase (ADH) acting in series contributed to about 55% of the ethanol produced by this mutant while pyruvate formate lyase and ADH were responsible for the remainder. Due to the absence of PDH activity in B. coagulans during fermentative growth at pH 5.0, the l-ldh mutant failed to grow anaerobically at pH 5.0. Strain Suy27-13, a derivative of the l-ldh mutant strain Suy27, that produced PDH activity during anaerobic growth at pH 5.0 grew at this pH and also produced ethanol as the fermentation product (0.39 g per g glucose). These results show that construction of an ethanologenic B. coagulans requires optimal expression of PDH activity in addition to the removal of the LDH activity to support growth and ethanol production.     

A higher optical purity of l-lastic acid produced in Streptococcus faecalis

In fermentation of lactic acid with Streptococcus faecalis, which produces mainly l-lactic acid, the optical purity of the l-lactic acid produced was improved from 97.1% to 99.8% by the addition of 0.5 g/l of diammonium hydrogen phosphate. The fermentation time was reduced from 130 h to 47 h b9y the improved method. Correspondence to: H. Ohara     

Efficient synthesis of enantiomeric ethyl lactate by <Emphasis Type="Italic">Candida antarctica</Emphasis> lipase B (CALB)-displaying yeasts

The whole-cell biocatalyst displaying Candida antarctica lipase B (CALB) on the yeast cell surface with α-agglutinin as the anchor protein was easy to handle and possessed high stability. The lyophilized CALB-displaying yeasts showed their original hydrolytic activity and were applied to an ester synthesis using ethanol and l-lactic acid as substrates. In water-saturated heptane, CALB-displaying yeasts catalyzed ethyl lactate synthesis. The synthesis efficiency increased depending on temperature and reached approximately 74% at 50°C. The amount of l-ethyl lactate increased gradually. l-Ethyl lactate synthesis stopped at 200 h and restarted after adding of l-lactic acid at 253 h. It indicated that CALB-displaying yeasts retained their synthetic activity under such reaction conditions. In addition, CALB-displaying yeasts were able to recognize l-lactic acid and d-lactic acid as substrates. l-Ethyl lactate was prepared from l-lactic acid and d-ethyl lactate was prepared from d-lactic acid using the same CALB-displaying whole-cell biocatalyst. These findings suggest that CALB-displaying yeasts can supply the enantiomeric lactic esters for preparation of useful and improved biopolymers of lactic acid.     

Fermentative production of<Emphasis Type="SmallCaps"> l</Emphasis>-(+)-lactic acid by an alkaliphilic marine microorganism

Of six strains of lactic acid-producing alkaliphilic microorganisms, Halolactibacillus halophilus was most efficient. It produced the highest concentration and yield of lactic acid, with minimal amounts of acetic and formic acid when sucrose and glucose were used as substrate. Mannose and xylose were poorly utilized. In batch fermentation at 30°C, pH 9 with 4 and 8% (w/v) sucrose, lactic acid was produced at 37.7 and 65.8 g l⁻¹, with yields of 95 and 83%, respectively. Likewise, when 4 and 8% (w/v) glucose were used, 33.4 and 59.6 g lactic acid l⁻¹ were produced with 85 and 76% yields, respectively. l-(+)-lactic acid had an optical purity of 98.8% (from sucrose) and 98.3% (from glucose).     

d-lactic acid production from cellooligosaccharides and β-glucan using l-LDH gene-deficient and endoglucanase-secreting Lactobacillus plantarum

In order to achieve direct fermentation of an optically pure d-lactic acid from cellulosic materials, an endoglucanase from a Clostridium thermocellum (CelA)-secreting plasmid was introduced into an l-lactate dehydrogenase gene (ldhL1)-deficient Lactobacillus plantarum (∆ldhL1) bacterial strain. CelA expression and its degradation of β-glucan was confirmed by western blot analysis and enzyme assay, respectively. Although the CelA-secreting ∆ldhL1 assimilated cellooligosaccharides up to cellohexaose (although not cellotetraose), the main end product was acetic acid, not lactic acid, due to the conversion of lactic acid to acetic acid. Cultivation under anaerobic conditions partially suppressed this conversion resulting in the production of 1.27 g/l of D-lactic acid with a high optical purity of 99.5% from a medium containing 2 g/l of cellohexaose. Subsequently, D-lactic acid fermentation from barley β-glucan was carried out with the addition of Aspergillus aculeatus β-glucosidase produced by recombinant Aspergillus oryzae and 1.47 g/l of D-lactic was produced with a high optical purity of 99.7%. This is the first report of direct lactic acid fermentation from β-glucan and a cellooligosaccharide that is a more highly polymerized sugar than cellotriose.     

Efficient production of lactic acid from sucrose and corncob hydrolysate by a newly isolated <Emphasis Type="Italic">Rhizopus oryzae</Emphasis> GY18

The aim of this study is to investigate production of l-lactic acid from sucrose and corncob hydrolysate by the newly isolated R. oryzae GY18. R. oryzae GY18 was capable of utilizing sucrose as a sole source, producing 97.5 g l⁻¹ l-lactic acid from 120 g l⁻¹ sucrose. In addition, the strain was also efficiently able to utilize glucose and/or xylose to produce high yields of l-lactic acid. It was capable of producing up to 115 and 54.2 g l⁻¹ lactic acid with yields of up to 0.81 g g⁻¹ glucose and 0.90 g g⁻¹ xylose, respectively. Corncob hydrolysates obtained by dilute acid hydrolysis and enzymatic hydrolysis of the cellulose-enriched residue were used for lactic acid production by R. oryzae GY18. A yield of 355 g lactic acid per kg corncobs was obtained after 72 h incubation. Therefore, sucrose and corncobs could serve as potential sources of raw materials for efficient production of lactic acid by R. oryzae GY18.     

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%.     

Non-competitive product inhibition in lactic acid fermentation from glucose

Summary A kinetic study regarding product inhibition in lactic acid fermentation by Streptococcus faecalis, which produces l-lactic acid, was performed in a chemostat at various feed concentrations of glucose (10, 20, and 30 g/l) at pH 7.0. Steady-state kinetic constants for the specific consumption rate of glucose and the specific production rate of lactic acid were determined at a residual glucose concentration below 2 g/l, which was accomplished in a chemostat. All the parameters, the specific growth rate, the specific consumption rate of glucose, and the specific production rate of lactic acid, were definitely related to non-competitive inhibition with regard to the concentration of the product, lactic acid.Offprint requests to: K. Hiyama     

Direct fermentation of potato starch wastewater to lactic acid by Rhizopus oryzae and Rhizopus arrhizus

The biochemical kinetic of direct fermentation for lactic acid production by fungal species of Rhizopus arrhizus 3,6017 and Rhizopus oryzae 2,062 was studied with respect to growth pH, temperature and substrate. The direct fermentation was characterized by starch hydrolysis, accumulation of reducing sugar, and production of lactic acid and fungal biomass. Starch hydrolysis, reducing sugar accumulation, biomass formation and lactic acid production were affected with the variations in pH, temperature, and starch source and concentration. A growth condition with starch concentration approximately 20 g/l at pH 6.0 and 30°C was favourable for both starch saccharification and lactic acid fermentation, resulting in lactic acid yield of 0.87–0.97 g/g starch associated with 1.5–2.0 g/l fungal biomass produced in 36 h fermentation. R. arrhizus 3,6017 had a higher capacity to produce lactic acid, while R. oryzae 2,062 produced more fungal biomass under similar conditions.     

Effect of temperature and various nitrogen sources on L(+)-lactic acid production by Lactobacillus casei

 Two homofermentative strains, Lactobacillus casei NRRL B-441 and Lactobacillus casei subsp. rhamnosus NRRL B-445 were selected for further study from 17 lactic acid bacterial strains screened for lactic acid production. The effect of temperature on lactic acid production with the selected strains was investigated by adapting both strains to four different temperatures. The production of L(+)-lactic acid by both strains was most efficient at 37°C, although with L. casei the highest lactic acid concentration was obtained at 41°C. The maximal volumetric productivity with L. casei was 4.1 g l^-1 h^-1 and with L. casei subsp. rhamnosus 3.5 g l^-1 h^-1. The composition of the medium was studied in order to replace the costly yeast extract with less expensive sources of nitrogen and amino acids. From 11 different nitrogen sources investigated at 37°C, barley malt sprouts (88 g l^-1 lactic acid in 66 h) and grass extract (74 g l^-1 lactic acid in 73 h) were the best economic alternatives. The effect of different combinations of yeast extract, peptone and malt sprouts was further studied by using statistical experimental design, and an empirical second-order polynomial model was constructed on the basis of the results. With the right combination most of the yeast extract could be substituted by barley malt sprouts for efficient lactic acid production. A method for extraction of nutrients and growth factors from malt sprouts is also described. Received: 25 September 1995/Accepted: 24 October 1995     

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.     

Improvement of l-lactic acid production by osmotic-tolerant mutant of Lactobacillus casei at high temperature

l-Lactic acid production by Lactobacillus casei was used as a model to study the mechanism of substrate inhibition and the strategy for enhancing l-lactic acid production. It was found that the concentration of cell growth and l-lactate decreased with the increase of glucose concentration and fermentation temperature. To enhance the osmotic stress resistance of the strain at high temperature, a mutant G-03 was screened and selected with 360?g/L glucose at 45°C as the selective criterion. To further increase the cell growth for lactic acid production, 3?g/L of biotin was supplemented to the medium. As a result, l-lactate concentration by the mutant G-03 reached 198.2?g/L (productivity of 5.5?g?L^?1?h^?1) at 41°C in a 7-L fermentor with 210?g/L glucose as carbon source. l-Lactate concentration and productivity of mutant G-03 were 115.2% and 97.8% higher than those of the parent strain, respectively. The strategy for enhancing l-lactic acid production by increasing osmotic stress resistance at high temperature may provide an alternative approach to enhance organic acid production with other strains.