Evaluation ofl-lactic acid production in batch, fed-batch, and continuous cultures ofRhizopus sp. MK-96-1196 using an airlift bioreactor

Various processes which producel-lactic acid using ammonia-tolerant mutant strain,Rhizopus sp. MK-96-1196, in a 3 L airlift bioreactor were evaluated. When the fed-batch culture was carried out by keeping the glucose concentration at 30 g/l, more than 140 g/l ofl-lactic acid was produced with a product yield of 83%. In the case of the batch culture with 200 g/l of initial glucose concentration, 121 g/L ofl-lactic acid was obtained but the low product yield based on the amount of glucose consumed. In the case of a continuous culture, 1.5 g/l/h of the volumetric productivity with a product yield of 71% was achieved at dilution rate of 0.024 h⁻¹. Basis on these results three processes were evaluated by simple variable cost estimation including carbon source, steam, and waste treatment costs. The total variable costs of the fed-batch and continuous cultures were 88% and 140%, respectively, compared to that of batch culture. The fed-batch culture with highl-lactic acid concentration and high product yield decreased variable costs, and was the best-suited for the industrial production ofl-lactic acid.     

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.     

Selection ofRhizopus strains forl(+)-lactic acid andγ-linolenic acid production

The production ofl(+)-lactic acid and formation ofγ-linolenic acid by 50Rhizopus strains growing on saccharidic substrates were investigated. Formation of acids was observed on solid cultivation media but mainly during submerged fermentation. Strains with the highest selectivity of bothl(+)-lactic acid production andγ-linolenic acid formation were tested in a laboratory fermenter. The best producer was treated by UV irradiation to increase the fatty acid content in the biomass, especially that ofγ-linolenic acid. The conversion of 10% saccharidic substrate by this newly prepared strainRhizopus arrhizus CCM 8109 results in more than 95% of theoretical yield ofl(+)-lactic acid and permits a volume productivity of 0.4 gγ-linolenic acid per liter.     

Aromatic amino acid biosynthesis in Alcaligenes eutrophus H 16

Properties and regulation of anthranilate synthase from Alcaligenes eutrophus H 16 were investigated. Anthranilate synthase was partially purified from crude extracts by affinity chromatography on tryptophan-substituted Sepharose, and was used for kinetic measurements. During the purification procedure the enzyme was stabilized by 50 mM l-glutamine or during chromatography on DEAE-cellulose and Sephadex G-200 with 30% glycerol, respectively.The glutamine dependent activity of anthranilate synthase was examined; it showed little change between pH 8.4 and pH 9.1. The Arrhenius plot was broken and the activation energy, H, calculated therefrom amounted to 8.9 kcal/mole up to 30°C and 5.5 kcal/mole at higher temperatures. The molecular weight determined by gelfiltration on Sephadex G-200 and by sucrose density gradient centrifugation resulted in 158000 and 126000, respectively. The K _m -values for the two substrates chorismate and glutamine were found to be 5 M and 560 M, respectively.Anthranilate synthase was strongly inhibited by l-tryptophan; the only amino acid that affected enzyme activity. Homotropic interactions for chorismate (Hill coefficient n=1.4) were obtained in the presence of l-tryptophan. 50% inhibition were caused by 10 M l-tryptophan at 100 M chorismate. The inhibition with respect to l-glutamine was noncompetitive.Anthranilate synthase was not associated to phosphoribosyl transferase and easily separable from the latter by different chromatographic methods.Abbreviation TEA triethanolamine     

Homofermentative production of d-lactic acid from sucrose by a metabolically engineered Escherichia coli

Escherichia coli W, a sucrose-positive strain, was engineered for the homofermentative production of d-lactic acid through chromosomal deletion of the competing fermentative pathway genes (adhE, frdABCD, pta, pflB, aldA) and the repressor gene (cscR) of the sucrose operon, and metabolic evolution for improved anaerobic cell growth. The resulting strain, HBUT-D, efficiently fermented 100?g?sucrose?l^?1 into 85?g?d-lactic acid?l^?1 in 72–84?h in mineral salts medium with a volumetric productivity of ~1?g?l^?1?h^?1, a product yield of 85?% and d-lactic acid optical purity of 98.3?%, and with a minor by-product of 4?g?acetate?l^?1. HBUT-D thus has great potential for production of d-lactic acid using an inexpensive substrate, such as sugar cane and/or beet molasses, which are primarily composed of sucrose.     

Biological acidification during grape must fermentation using mixed cultures of <Emphasis Type="Italic">Kluyveromyces thermotolerans</Emphasis> and <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis>

Four mixed culture fermentations of grape must were carried out with Kluyveromyces thermotolerans strain TH941 and Saccharomyces cerevisiae strain SCM952. In the first culture, both yeasts were added together, whereas in the remaining three cultures S. cerevisiae was added 1, 2, and 3 days after the inoculation of K. thermotolerans. The growth and survival of the K. thermotolerans strain and the amount of the produced l-lactic acid depend on the time of inoculation of the S. cerevisiae strain and provided an effective acidification during alcoholic fermentation. The four cultures contained, respectively, at the end of fermentation 0.18, 1.80, 4.28, and 5.13 g l-lactic acid l⁻¹. The grape must with an initial pH of 3.50 was effectively acidified (70% increase in titratable acidity, 0.30 pH unit decrease) by the production of 5.13 g l-lactic acid l⁻¹.     

Reducing by-product formation in L-lactic acid fermentation by Rhizopus oryzae

During L-lactic acid fermentation by Rhizopus oryzae, increasing the phosphate level in the fermentation medium from 0.1 g l^–1 to 0.6 g l^–1 KH₂PO₄ reduced the maximal concentration of L-lactic acid and fumaric acid from 85 g l^–1 to 71 g l^–1 and from 1.36 g l^–1 to 0.18 g l^–1, respectively; and it decreased the fermentation time from 72 h to 52 h. Phosphate at 0.40 g l^–1 KH₂PO₄ was suitable for both minimizing fumaric acid accumulation and benefiting L-lactic acid production.     

Simultaneous and selective production of levan and poly(γ-glutamic acid) by <Emphasis Type="Italic">Bacillus subtilis</Emphasis>

Bacillus subtilis(natto) Takahashi, used to prepare the fermented soybean product natto, was grown in a basal medium containing 5% (w/w) sucrose and 1.5% (w/w) l-glutamate and produced 58% (w/w) poly(-glutamic acid) and 42% (w/w) levan simultaneously. After 21 h, 40–50 mg levan ml^-1had been produced in medium containing 20% (w/w) sucrose but without l-glutamate. In medium containing l-glutamic acid but without sucrose, mainly poly(-glutamic acid) was produced. Revisions requested 28 August 2004/14 October 2004; Revisions received 11 October 2004/22 November 2004     

Potential of solid state fermentation for production of L(+)-lactic acid by Rhizopus oryzae

Production of l(+)-lactic acid by Rhizopus oryzae NRRL 395 was studied in solid medium on sugar-cane bagasse impregnated with a nutrient solution containing glucose and CaCO₃. A comparative study was undertaken in submerged and solid-state cultures. The optimal concentrations in glucose were 120 g/l in liquid culture and 180 g/l in solid-state fermentation corresponding to production of l(+)-lactic acid of 93.8 and 137.0 g/l, respectively. The productivity was 1.38 g/l per hour in liquid medium and 1.43 g/l per hour in solid medium. However, the fermentation yield was about 77% whatever the medium. These figures are significant for l(+)-lactic acid production.     

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.     

Production of l-lactic acid by Rhizopus species

Of 19 Rhizopus spp. only four produced l-lactic acid in shake-flask culture. Aerobically and in the presence of a neutralizing agent, Rhizopus oryzae NRRL 395 produced the highest concentration of l-lactic acid (65 g/l) but with O₂-limited growth ethanol was produced instead.C.R. Soccol and V.I. Stonoga are with the Laboratório de Processos Biotecnológicos, Departmento de Engenharia Química da Universidade Federal do Paraná, 81531-970 Curitiba, PR, Brazil; M. Raimbault is with the Centre ORSTOM, Laboratoire de Biotecnologie, Physiologie et Métabolisme Cellulaires, 911, Avenue Agropolis, 34032 Montpellier, Cedex 1, France.     

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.     

Efficient Production of Optically Pure d-Lactic Acid from Raw Corn Starch by Using a Genetically Modified l-Lactate Dehydrogenase Gene-Deficient and α-Amylase-Secreting Lactobacillus plantarum Strain

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 α-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.Poly-lactic acid (PLA) is an important agro-based plastic that can be produced from inexpensive, renewable, and abundantly available biomass resources, including starchy materials. These resources have advantages over limited oil- and fossil-based sources, as they do not result in any net carbon dioxide release to the atmosphere (7). Recently, stereocomplex PLA, which is composed of both poly-l- and -d-lactic acid, has been attracting much attention due to its high thermostability. Stereocomplex-type polymers show a melting point (ca. 230°C) that is approximately 50°C higher than that of the respective single polymers (8). Therefore, d-lactic acid, in addition to l-lactic acid, which has been the focus of production to date, is of significant importance.Lactic acid bacteria (LAB) are promising microorganisms for the efficient production of lactic acid from various sugars, such as glucose, sucrose, and lactose. However, when starchy materials are used as a carbon source, they must be saccharified by physicochemical and enzymatic treatment because most LAB cannot utilize starchy materials directly (13). This makes the whole process less economically viable. Therefore, many researchers have examined the direct production of lactic acid from starchy materials by using wild amylolytic LAB (ALAB) (6, 24, 25) or genetically modified amylase-producing LAB (15, 16). Although d-lactic acid has been produced by fermentation from pretreated substrates such as rice starch (5) and by simultaneous saccharification and fermentation from cellulose (23), there have been no reports on the direct production of d-lactic acid from starchy materials. This is due to a lack of d-lactic acid-producing ALAB and difficulties in gene manipulation of d-lactic acid-producing LAB, such as Lactobacillus delbrueckii (22).We focused on Lactobacillus plantarum, which is an industrially important strain due to its environmental flexibility and its ability to assimilate a wide range of carbohydrates (9). In recent years, several gene manipulation methods for Lactobacillus plantarum have been established (18, 19). Moreover, the complete genome sequence has been decoded for L. plantarum NCIMB 8826 (9). Based on whole-genome analysis, L. plantarum possesses two types of lactate dehydrogenase (LDH), l-LDH and d-LDH, which convert pyruvate into l- and d-lactic acid, respectively. Ferain et al. (4) reported that chromosomal deletion in the ldhL1 gene of L. plantarum NCIMB 8826 provoked an absence of l-LDH activity and produced d-lactic acid from glucose.In the present study, to produce d-lactic acid directly from starch, we constructed an l-LDH-deficient, α-amylase-secreting L. plantarum strain. The engineered strain expressed α-amylase from Streptococcus bovis 148 (AmyA) (20) and efficiently degraded raw starch with the aid of a C-terminal starch-binding domain (11). Using this strain, we achieved the direct and efficient fermentation of optically pure d-lactic acid from raw corn starch.     

Lactic acid fermentation by Lactobacillus casei in free cell form and immobilised on gluten pellets

A comparative study of the fermentation of a range of carbohydrate substrates, at various temperatures, was carried out using a commercial Lactobacillus casei strain in a free cell form and immobilised on gluten pellets. This strain required yeast extract, l-cysteine HCl and Mn²⁺ at 5, 0.5 and 0.1 g l^–1, respectively, for maximum growth and lactic acid production. Sugar fermentation using free cells showed preference in the order glucose, sucrose, fructose while lactose was poorly utilised. Optimum temperature for growth and lactic acid production over (18–30 h) was 43 °C. L. casei was successfully immobilised on gluten pellets and fermented glucose and sucrose in a shorter time (18 h) with increased lactic acid production (42 and 41 g l^–1 on glucose and sucrose, respectively).     

Somatic embryogenesis and callus production from cotyledon explants of Eastern black walnut

Starting at 8 weeks and continuing until 23 weeks (nut drop) after anthesis,1 m² explants from cotyledons of immature seeds were extracted from Juglans nigra fruits. Explants were placed on Woody Plant Medium with 1 g l^-1 casein hydrolysate and 30 g l^-1 sucrose. The explants remained in light for 4 weeks on primary media containing a 3×3 factorial of 0.05, 0.5, or 5.0 M thidiazuron (TDZ) and 0.1, 1.0, or 10.0 M 2,4-d. Explants were transferred to a secondary medium containing no plant growth regulators and incubated in darkness for 11 weeks. The greatest number of somatic embryos was produced 8, 10, and 12 weeks after anthesis from explants on media with 0.5 or 5.0 M TDZ and 0.1 or 1.0 M 2,4-d. Explants produced the greatest callus volume and dry weight 10, 12, and 14 weeks after anthesis. Throughout the study, callus generally increased with increasing concentrations of both TDZ and 2,4-d.Abbreviations BA 6-benzyladenine - captan 3a,4,7,7a-tetrahydro-2-[(trichloromethyl)thio]-1H-isoindole-1,3(2H)-dione - 2,4-d 2,4-dichlorophenoxyacetic acid - IBA indolebutyric acid - Physan n-alkyl- dimethyl-benzyl ammonium chlorides and n-alkyl-dimethyl-ethylbenzyl ammonium chlorides - TDZ-thidiazuron N-phenyl-N-1,2,3-thiadiazol-5-ylurea     

Induction,purification and characterisation of arabinases produced by Aspergillus niger

The induction of arabinases in Aspergillus niger N400 was studied on different simple and complex carbon sources. Sugar beet pulp was found to be an inducer of three arabinan degrading enzymes (-l-arabinofuranosidase A, -l-arabinofuranosidase B and endoarabinase). These enzymes were purified from A. niger culture fluid after growth of the fungus in medium employing sugar beet pulp as the carbon source and were characterised both physico-chemically (Mw 83 000, 67 000, 43 000 Da and, pI 3.3, 3.5 and 3.0 for -l-arabinofuranosidases A and B and endo-arabinase, respectively) and kinetically (K _m on p-nitrophenyl--l-arabinofuranoside 0.68 and 0.52 mM for -l-arabinofuranosidases A and B, resp.; K _m on sugar beet arabinan 0.24 and 3.7 g/l for -l-arabinofuranosidase B and endoarabinase, resp.). The amino acid compositions of the three enzymes were determined also. The enzymic properties were compared with those of arabinases purified from a commerical A. niger enzyme preparation. Differences were found though the kinetic data suggest considerable similarity between the enzymes from the different sources. Antibodies raised in mice against the three enzymes were found to be highly specific and no crossreactivity with other proteins present in culture filtrates was observed. A mixture of these antibodies has been used to analyze specific induction of these individual enzymes on simple and complex substrates by Western blotting.Abbreviation PNA p-nitrophenyl--l-arabinofuranoside     

Fermentative production of l-lactic acid by Lactobacillus casei DSM 20011 and product recovery using ion exchange resins

In order to produce l(+)-lactic acid to be employed in poly-l-lactic acid polymer production, for biomedical applications, the strain Lactobacillus casei subsp. casei DSM 20011 was studied in a conventional batch mode using different initial concentrations of glucose. The results obtained showed that the initial glucose concentration exerts an influence on the fermentation pattern, modifying the different fermentation parameters. Nevertheless, the product yield remained at a constant value of 0.86 g·g^–1. The proposed novel system of product recovery, based on the use of ion-exchange resins, gave high yields of pure lactic acid. Correspondence to: D. Matteuzzi     

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).     

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.     

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.