Fermentation of sugar mixtures using Escherichia coli catabolite repression mutants engineered for production of L-lactic acid

Conversion of lignocellulose to lactic acid requires strains capable of fermenting sugar mixtures of glucose and xylose. Recombinant Escherichia coli strains were engineered to selectively produce L-lactic acid and then used to ferment sugar mixtures. Three of these strains were catabolite repression mutants (ptsG ⁻) that have the ability to simultaneously ferment glucose and xylose. The best results were obtained for ptsG ⁻ strain FBR19. FBR19 cultures had a yield of 0.77 (g lactic acid/g added sugar) when used to ferment a 100 g/l total equal mixture of glucose and xylose. The strain also consumed 75% of the xylose. In comparison, the ptsG ⁺ strains had yields of 0.47–0.48 g/g and consumed 18–22% of the xylose. FBR19 was subsequently used to ferment a variety of glucose (0–40 g/l) and xylose (40 g/l) mixtures. The lactic acid yields ranged from 0.74 to 1.00 g/g. Further experiments were conducted to discover the mechanism leading to the poor yields for ptsG ⁺ strains. Xylose isomerase (XI) activity, a marker for induction of xylose metabolism, was monitored for FBR19 and a ptsG ⁺ control during fermentations of a sugar mixture. Crude protein extracts prepared from FBR19 had 10–12 times the specific XI activity of comparable samples from ptsG ⁺ strains. Therefore, higher expression of xylose metabolic genes in the ptsG ⁻ strain may be responsible for superior conversion of xylose to product compared to the ptsG ⁺ fermentations. Received 14 December 2000/ Accepted in revised form 28 June 2002     

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.     

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.     

Continuous <Emphasis Type="SmallCaps">d</Emphasis>-lactic acid production by a novelthermotolerant <Emphasis Type="Italic">Lactobacillus delbrueckii</Emphasis> subsp. <Emphasis Type="Italic">lactis</Emphasis> QU 41

We isolated and characterized a d-lactic acid-producing lactic acid bacterium (d-LAB), identified as Lactobacillus delbrueckii subsp. lactis QU 41. When compared to Lactobacillus coryniformis subsp. torquens JCM 1166 ^T and L. delbrueckii subsp. lactis JCM 1248 ^T, which are also known as d-LAB, the QU 41 strain exhibited a high thermotolerance and produced d-lactic acid at temperatures of 50 °C and higher. In order to optimize the culture conditions of the QU 41 strain, we examined the effects of pH control, temperature, neutralizing reagent, and initial glucose concentration on d-lactic acid production in batch cultures. It was found that the optimal production of 20.1 g/l d-lactic acid was acquired with high optical purity (>99.9% of d-lactic acid) in a pH 6.0-controlled batch culture, by adding ammonium hydroxide as a neutralizing reagent, at 43 °C in MRS medium containing 20 g/l glucose. As a result of product inhibition and low cell density, continuous cultures were investigated using a microfiltration membrane module to recycle flow-through cells in order to improve d-lactic acid productivity. At a dilution rate of 0.87 h⁻¹, the high cell density continuous culture exhibited the highest d-lactic acid productivity of 18.0 g/l/h with a high yield (ca. 1.0 g/g consumed glucose) and a low residual glucose (<0.1 g/l) in comparison with systems published to date.     

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.     

Optimization of L(+)-lactic acid production employing statistical experimental design

Summary An orthogonal 2³-factorial experimental design was used to optimize L(+)-lactic acid production byLactobacillus casei. With a 22 % (v/v) inoculum the optimum concentration of yeast extract for maximum lactic acid concentration and yield was about 2 % (w/v) and that of the initial glucose 9 to 11 %.     

Stabilization of pet operon plasmids and ethanol production in Escherichia coli strains lacking lactate dehydrogenase and pyruvate formate-lyase activities.

In the last decade, a major goal of research in biofuels has been to metabolically engineer microorganisms to ferment multiple sugars from biomass or agricultural wastes to fuel ethanol. Escherichia coli strains genetically engineered to contain the pet operon (Zymomonas mobilis pyruvate decarboxylase and alcohol dehydrogenase B genes) produce high levels of ethanol. Strains carrying the pet operon in plasmid (e.g., E. coli B/pLOI297) or in chromosomal (e.g., E. coli KO11) sites require antibiotics in the media to maintain genetic stability and high ethanol productivity. To overcome this requirement, we used the conditionally lethal E. coli strain FMJ39, which carries mutations for lactate dehydrogenase and pyruvate formate lyase and grows aerobically but is incapable of anaerobic growth unless these mutations are complemented. E. coli FBR1 and FBR2 were created by transforming E. coli FMJ39 with the pet operon plasmids pLOI295 and pLOI297, respectively. Both strains were capable of anaerobic growth and displayed no apparent pet plasmid losses after 60 generations in serially transferred (nine times) anaerobic batch cultures. In contrast, similar aerobic cultures rapidly lost plasmids. In high-cell-density batch fermentations, 3.8% (wt/vol) ethanol (strain FBR1) and 4.4% (wt/vol) ethanol (strain FBR2) were made from 10% glucose. Anaerobic, glucose-limited continuous cultures of strain FBR2 grown for 20 days (51 generations; 23 with tetracycline and then 28 after tetracycline removal) showed no loss of antibiotic resistance. Anaerobic, serially transferred batch cultures and high-density fermentations were inoculated with cells taken at 57 generations from the previous continuous culture. Both cultures continued to produce high levels of ethanol in the absence of tetracycline. The genetic stability conferred by selective pressure for pet-containing cells without requirement for antibiotics suggests potential commercial suitability for E. coli FBR1 and FBR2.     

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).     

Expression of pyruvate formate-lyase of Escherichia coli from the cloned structural gene

It is shown here that a plasmid (p29) derived from the transducing phage aspC2 (Christiansen and Pedersen 1981) codes for pyruvate formate-lyase. The identity of the 80 kilodaltons (kd) gene product of plasmid p29 with the pyruvate formate-lyase polypeptide was proven (i) by comigration of the gene product expressed in the maxicell system with purified enzyme on O'Farrell gels, and (ii) by comparison of the peptide maps obtained from limited proteolysis. In vivo the 80 kd form of the enzyme was proteolytically converted to a 78 kd polypeptide. The two polypeptides (80 kd and 78 kd) and their charge isomers present in purified enzyme preparations are therefore products of a single gene.Aerobically grown cells of Escherichia coli contained a basal level of pyruvate formate-lyase which was derepressed 5-to 10-fold under anaerobiosis. Derepression also occurred during anaerobic growth on glycerol plus fumarate. Presence of plasmid p29 caused overproduction of pyruvate formatelyase, 11-fold upon anaerobic growth on glucose, 14-fold upon aerobic growth on glucose and 33-fold upon aerobic growth at the expense of D-lactate.Non-Standard Abbreviation MOPS 4-morpholine-propane sulfonic     

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).     

Anaerobic synthesis of succinic acid by recombinant <Emphasis Type="Italic">Escherichia coli</Emphasis> strains with activated NAD<Superscript>+</Superscript>-reducing pyruvate dehydrogenase complex

Effect of constitutive expression of the aceEF-lpdA operon genes coding for the enzymes of NAD⁺-reducing pyruvate dehydrogenase complex on the anaerobic production of succinic acid from glucose by recombinant Escherichia coli strains was studied. Basic producer strains were obtained by inactivation of the main pathways for synthesis of acetic and lactic acids through deletion of the genes ackA, pta, poxB, and ldhA (SGM0.1) in E. coli MG1655 strain and by additional introduction of the Bacillus subtilis pyruvate carboxylase (SGM0.1 [pPYC]). A constitutive expression of the genes aceEF-lpdA in derivatives of the basic strains SGM0.1 P_L-aceEF-lpdA and SGM0.1 P_L-aceEF-lpdA [pPYC] was provided by replacing the native regulatory region of the operon with the lambda phage PL promoter. Molar yields of succinic acid in anaerobic glucose fermentation by strains SGM0.1 P_L-aceEF-lpdA and SGM0.1 P_L-aceEF-lpdA [pPYC] exceeded the corresponding yields of control strains by 2 and 33% in the absence and by 9 and 26% in the presence in media of HCO₃⁻ ion. It is concluded that an increase in the succinic acid production by strain SGM0.1 P_L-aceEF-lpdA [pPYC] as compared with the strains SGM0.1 and SGM0.1 [pPYC], which synthesize this substance in the reductive branch of the tricarboxylic acid cycle, is caused by activation of the glyoxylate shunt.     

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.     

Continuous production ofl-lactic acid from whey permeate by immobilizedLactobacillus casei subsp.casei

Summary The production of l-lactic acid from whey permeate, a waste product of the dairy industry, by fermentation with the lactic acid bacterium Lactobacillus casei subsp. casei was investigated. A fermentation medium consisting of permeate and supplements, which enables exponential growth of the organisms, was developed. A fast method for determination of free and immobilized biomass in solid-rich media, based on measurement of cellular ATP, was evolved. Continuous fermentations in a stirred tank reactor (STR) and in a fluidized bed reactor (FBR) with immobilized biomass were compared. In the STR a volumetric productivity of 5.5 g/l per hour at 100% substrate conversion [dilution rate (D) = 0.22 h^–1] was determined. In the FBR porous sintered glass beads were used for immobilization and a maximum biomass concentration of 105 g/kg support was measured. A productivity of 10 g/l per hour was obtained at D = 0.4 h^–1 (substrate conversion 93%) and of 13.5 g/l per hour at D = 1.0 h^–1 (substrate conversion 50%). Offprint requests to: W. Krischke     

Production of optically pure d-lactate by Lactobacillus bulgaricus and purification by crystallisation and liquid/liquid extraction

Optically pure d-lactic acid was produced by fermentation of lactose with Lactobacillus bulgaricus Lb-12, and purified by crystallisation as magnesium d-lactate followed by extraction with butanol. The yield of d-lactate and contaminations with nitrogen and phosphorus were mapped during the purification procedure. The overall yield of d-lactic acid was 72% and the purity was more than 99%. Contaminations in the final d-lactic acid with nitrogen, phosphorus and l-lactic acid were only 0.032% w/w, 0.018% w/w and 0.04% w/w respectively.     

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     

The aerobic growth and product formation of Lactobacillus,Leuconostoc, Brochothrix,and Carnobacterium in batch cultures

Summary The aerobic growth and metabolism of eleven homofermentative and three heterofermentative Lactobacillus strains, three Leuconostoc strains, two Brochothrix thermosphacta strains and two Carnobacterium strains were studied in batch cultures at pH 6.0 and 25°C on a complex substrate containing 10.0 g glucose per litre. All strains, except Carnobacterium divergens 69, grew well aerobically. An oxygen consumption was registered for 18 of the strains—the exceptions being Lactobacillus alimentarius DSM 20249^T, Lactobacillus farciminis DSM 20284^T and Lactobacillus sharpeae DSM 20505^T. The homofermentative lactobacilli showed a maximal oxygen consumption during the stationary growth phase and this was coupled with a low final viable count. Leuconostoc strains, heterofermentative lactobacilli, Brochothrix thermosphacta and Carnobacterium strains showed a maximal oxygen consumption during the exponential growth phase together with a high final viable count. The maximum specific growth rate varied from 0.19 to 0.54 h^-1 while the growth yield varied from 19 to 86 g dry weight per mol glucose consumed. In general, homofermentative lactobacilli produced dl-lactic acid, acetic acid and acetoin. The three heterofermentative lactobacilli produced dl-lactic acid and acetic acid, two strains also produced ethanol Leuconostoc spp. formed d-lactic acid, acetic acid, and ethanol. B. thermosphacta produced acetoin, acetic acid, formic acid, isobutyric acid and isovaleric acid but no lactic acid. Carnobacterium produced l-lactic acid, acetic acid and acetoin. All strains accumulated hydrogen peroxide except L. alimentarius DSM 20249^T, Carnobacterium piscicola 3 and B. thermosphacta.née Blickstad     

<Emphasis Type="SmallCaps">l</Emphasis>(+)-Lactic acid production by co-fermentation of glucose and xylose with <Emphasis Type="Italic">Rhizopus oryzae</Emphasis> obtained by low-energy ion beam irradiation

Low-energy ion beam irradiation (10–200 keV) has been proved to have a wide range of biological effects in recent years. When Rhizopus oryzae PW352 was irradiated with a 15-keV low-energy ion beam an l(+)-lactic acid high-yield mutant, RQ4015, was obtained. When 150 g/l glucose was used as the sole carbon source, l(+)-lactic acid of RQ4015 reached 121 g/l after 36 h shake-flask cultivation. However, the highest lactic acid concentration 74 g/l was obtained when 100 g/l xylose was present in the medium as the sole carbon source. When mixed xylose (25 g/l) and glucose (75 g/l) were present in a bubble column, l(+)-lactic acid production of RQ4015 reached 83 g. A high mutation rate and a wide mutation spectrum of low-energy ion implantation were observed in the experiment, suggesting that ion implantation can be a highly efficient mutagenic means for microorganism breeding in many commercial applications.     

Genetic Engineering of Candida utilis Yeast for Efficient Production of L-Lactic Acid

Polylactic acid is receiving increasing attention as a renewable alternative for conventional petroleum-based plastics. In the present study, we constructed a metabolically-engineered Candida utilis strain that produces L-lactic acid with the highest efficiency yet reported in yeasts. Initially, the gene encoding pyruvate decarboxylase (CuPDC1) was identified, followed by four CuPDC1 disruption events in order to obtain a null mutant that produced little ethanol (a by-product of L-lactic acid). Two copies of the L-lactate dehydrogenase (L-LDH) gene derived from Bos taurus under the control of the CuPDC1 promoter were then integrated into the genome of the CuPdc1-null deletant. The resulting strain produced 103.3 g/l of L-lactic acid from 108.7 g/l of glucose in 33 h, representing a 95.1% conversion. The maximum production rate of L-lactic acid was 4.9 g/l/h. The optical purity of the L-lactic acid was found to be more than 99.9% e.e.     

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.     

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.