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.     

A comparative proteomic analysis of Bacillus coagulans in response to lactate stress during the production of l-lactic acid

The growth rate and maximum biomass of Bacillus coagulans 2–6 were inhibited by lactate; inhibition by sodium lactate was stronger than by calcium lactate. The differences of protein expressions by B. coagulans 2–6 under the lactate stress were determined using two-dimensional electrophoresis coupled with mass spectrometric identification. Under the non-stress condition, calcium lactate stress and sodium lactate stress, the number of detected protein spots was 1,571 ± 117, 1,281 ± 231 and 904 ± 127, respectively. Four proteins with high expression under lactate stress were identified: lactate dehydrogenase, cysteine synthase A, aldo/keto reductase and ribosomal protein L7/L12. These proteins are thus potential targets for the reconstruction of B. coagulans to promote its resistance to lactate stress.     

Efficient conversion of phenylpyruvic acid to phenyllactic acid by using whole cells of Bacillus coagulans SDM

Background

Phenyllactic acid (PLA), a novel antimicrobial compound with broad and effective antimicrobial activity against both bacteria and fungi, can be produced by many microorganisms, especially lactic acid bacteria. However, the concentration and productivity of PLA have been low in previous studies. The enzymes responsible for conversion of phenylpyruvic acid (PPA) into PLA are equivocal.

Methodology/Principal Findings

A novel thermophilic strain, Bacillus coagulans SDM, was isolated for production of PLA. When the solubility and dissolution rate of PPA were enhanced at a high temperature, whole cells of B. coagulans SDM could effectively convert PPA into PLA at a high concentration (37.3 g l⁻¹) and high productivity (2.3 g l⁻¹ h⁻¹) under optimal conditions. Enzyme activity staining and kinetic studies identified NAD-dependent lactate dehydrogenases as the key enzymes that reduced PPA to PLA.

Conclusions/Significance

Taking advantage of the thermophilic character of B. coagulans SDM, a high yield and productivity of PLA were obtained. The enzymes involved in PLA production were identified and characterized, which makes possible the rational design and construction of microorganisms suitable for PLA production with metabolic engineering.     

Bioprocess development for endospore production by Bacillus coagulans using an optimized chemically defined medium

Bacillus coagulans is a promising probiotic, because it combines probiotic properties of Lactobacillus and the ability of Bacillus to form endospores. Due to this hybrid relationship, cultivation of this organism is challenging. As the probiotics market continues to grow, there is a new focus on the production of these microorganisms. In this work, a strain-specific bioprocess for B. coagulans was developed to support growth on one hand and ensure sporulation on the other hand. This circumstance is not trivial, since these two metabolic states are contrary. The developed bioprocess uses a modified chemically defined medium which was further investigated in a one-factor-at-a-time assay after adaptation. A transfer from the shake flask to the bioreactor was successfully demonstrated in the scope of this work. The investigated process parameters included temperature, agitation and pH-control. Especially the pH-control improved the sporulation in the bioreactor when compared to shake flasks. The bioprocess resulted in a sporulation efficiency of 80%–90%. This corresponds to a sevenfold increase in sporulation efficiency due to a transfer to the bioreactor with pH-control. Additionally, a design of experiment (DoE) was conducted to test the robustness of the bioprocess. This experiment validated the beforementioned sporulation efficiency for the developed bioprocess. Afterwards the bioprocess was then scaled up from a 1 L scale to a 10 L bioreactor scale. A comparable sporulation efficiency of 80% as in the small scale was achieved. The developed bioprocess facilitates the upscaling and application to an industrial scale, and can thus help meet the increasing market for probiotics.     

Efficient co‐production of propionic acid and succinic acid by Propionibacterium acidipropionici using membrane separation coupled technology

To improve the fermentation efficiency of Propionibacterium acidipropionici, a semi‐continuous coupled fermentation process was established to achieve co‐production of propionic acid (PA) and succinic acid (SA). First, the optimal proportion of glucose (Glc) and glycerol (Gl) as a mixed carbon source was determined, and the feeding procedure of Gl was optimized to make more energy flow in the direction of product synthesis. Then, ZGD630 anion exchange resin was used for efficient adsorption of PA, thereby eliminating the feedback inhibition effect of PA. Finally, an efficient, coupled fermentation process of P. acidipropionici characterized by membrane separation and chromatography technology was developed. The concentrations of PA and SA reached 62.22 ± 2.32 and 20.45 ± 1.34 g L⁻¹, with corresponding productivity of 0.43 and 0.14 g L⁻¹ h⁻¹, increased by 65.38% and 48.54%, respectively. Membrane separation coupled fermentation of PA and SA could significantly improve the process economics of P. acidipropionici, and has good prospects for industrial application.     

Strain improvement of Lactobacillus delbrueckii using nitrous acid mutation for l-lactic acid production

Insertional mutagenesis is impractical in the mechanisms for protection against low pH, high solute concentration etc. due to the involvement of large number of loci and multiple genes. An attempt was made to improve Lactobacillus delbrueckii NCIM 2025 strain by classical mutation using nitrous acid. In the present investigation, classical mutation was proved to be successful and the selected mutants had improved qualities like increased lactic acid productivity, acid tolerance and sugar tolerance. Mutants showed better growth rate and lesser generation time than the wild type.     

Continuous biodiesel production using in situ glycerol separation by membrane bioreactor system

Biodiesel is one of the most promising renewable fuel sources. Candida antarctica lipase B (CalB) has been used for biodiesel production because of its high activity and stability. However, CalB can only be utilized in industrial biodiesel production if the enzyme deactivation by methanol and the negative effects of glycerol can be mitigated. Methanol inhibition can be avoided by utilizing a stepwise addition of methanol, but there is no suitable method to reduce the glycerol effect. This study aims to use a membrane bioreactor system to remove glycerol during biodiesel production. In addition, methanol inhibition can be reduced by continuously feeding methanol through the membrane system. This continuous membrane bioreactor system can be used for efficient biodiesel production.     

凝结芽胞杆菌生物学特性及其在家禽生产中的应用

作为一种新兴的微生物饲料添加剂,凝结芽胞杆菌既表现出类乳酸菌的益生特性,又具有芽胞杆菌抗逆性好、易储存的优点,有利于产业化及市场推广。凝结芽胞杆菌能够产生有机酸及多种酶类、修复受损的肠黏膜、抑制病原菌繁殖及促进营养物质的消化吸收,在家禽生产中受到广泛关注和应用。目前关于凝结芽胞杆菌的研究不够深入,其生物学特性及作用机制还在进一步研究中,还需加深其在畜牧业中的应用研究。本文主要对凝结芽胞杆菌近几年的研究进展及其在家禽生产中的应用进行综述,为今后凝结芽胞杆菌的研发及应用提供参考依据。     

New application of Bacillus strains for optically pure l-lactic acid production: general overview and future prospects

Members of the genus Bacillus are considered to be both, among the best studied and most commonly used bacteria as well as the most still unexplored and the most wide-applicable potent bacteria because novel Bacillus strains are continuously being isolated and used in various areas. Production of optically pure l-lactic acid (l-LA), a feedstock for bioplastic synthesis, from renewable resources has recently attracted attention as a valuable application of Bacillus strains. l-LA fermentation by other producers, including lactic acid bacteria and Rhizopus strains (fungi) has already been addressed in several reviews. However, despite the advantages of l-LA fermentation by Bacillus strains, including its high growth rate, utilization of various carbon sources, tolerance to high temperature, and growth in simple nutritional conditions, it has not been reviewed. This review article discusses new findings on LA-producing Bacillus strains and compares them to other producers. The future prospects for LA-producing Bacillus strains are also discussed.     

Glycine feeding improves pristinamycin production during fermentation including resin for in situ separation

Seven amino acids were tested as precursors to affect pristinamycin production by a mutant strain derived from Streptomyces pristinaespiralis ATCC25486. Of those, glycine was selected as the best precursor to facilitate both cell growth and pristinamycin production at the feeding time of 36-h incubation and the feeding rate of 0.75 g L⁻¹ flask culture. The optimized time and concentration of glycine feeding were applied to enlarged 3-L bioreactor fermentation with a resin added at the time of 20-h fermentation for in situ separation. As a result, a combination of the glycine feeding and the added resin resulted in the maximal pristinamycin yield of 616 mg L⁻¹ culture 12 h after glycine feeding. The yield from the combined treatment was 1.71-, 2.77- and 4.32-fold of those from the mere glycine and resin treatments and the control, respectively. Other parameters, including intracellular nucleic acid content, animo nitrogen content and pH level, during 72-h fermentation were also given in association with the pristinamycin yields in the different treatments. The results indicate that glycine feeding is an effective approach to enhance pristinamycin production in the culture of S. pristinaespiralis F213 with supplemented resin for in situ separation.     

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     

Efficient production of protopectinases by Bacillus subtilis using medium based on soybean flour

We have developed a culture system for efficient production of protopectinases (PPases) by Bacillus subtilis. PPase shows the pectin-releasing activity and is expected to be utilized in the enzymatic cotton scouring. B. subtilis IFO3134 was cultivated using defatted soybean flour as a main component of culture media. This strain produced three different types of PPases, namely, PPase-C, -N and -R performing endo-arabinase activity, pectate-lyase activity and pectin-lyase activity, respectively. The effects of alkaline solubilization and autoclave treatments to extract nutrients from soybean flour and initial soybean flour concentration (20-80g/l) on production of PPases in batch fermentation were investigated. Alkaline solubilization of soybean flour with NaOH remarkably reduced enzyme productivity. In addition, a higher initial concentration of soybean flour reduced the enzyme productivity of cells. The pectin-releasing activity was the largest and reached up to 2200-2400U/ml, when the culture medium containing an initial soybean flour concentration of 40g/l was autoclaved for 45-60min without alkaline solubilization treatment.     

Influence of carbohydrates and polyols on l-lactic acid production and fatty acid formation by Rhizopus arrhizus

Growth and l-lactic acid production on 24 different carbohydrates and polyols (glycerol, mannitol and sorbitol) by Rhizopus arrhizus CCM 8109 were determined. The d- but not the l-forms of xylose, fructose, galactose, mannose, glucose, cellobiose, maltose and sucrose and partially hydrolysed starch were converted to l-lactic acid. Changes in lipid formation and fatty acid composition were detected in biomass grown on the different sugars. In the presence of polyols, growth and considerable production of lipids were observed with little or no lactate production. Invertase was mainly associated with the mycelium during growth on sucrose, whereas glucoamylase and -amylase were produced extracellularly during growth on starch.The authors are with the Department of Biochemical Technology, Faculty of Chemical Technology, Slovak Polytechnical University, Radlinského 9, SK-812 37 Bratislava, Slovak Republic     

Efficient acetic acid production by repeated fed-batch fermentation using two fermentors

Summary In acetic acid fermentation, the number of viable cells decrease as the acetic acid concentration increases to more than about 40 g/l, which means that the productivity attainable by conventional fed-batch and repeated fed-batch operations using one fermentor is limited. In this paper, based on a fed-batch experiment using Acetobacter aceti 2096, a mathematical model was developed. The optimization carried out showed the superiority of repeated fed-batch operation using two fermentors. The performance evaluation was made with respect to productivity and product concentration. It was shown to be attractive in practice to use multiple fermentors, in particular for high product concentrations. Experiments were then conducted to ascertain the simulation results. Offprint requests to: T. Kobayashi     

Determination of gliclazide in human serum by high-performance liquid chromatography using an anion-exchange resin

A method for the routine clinical examination of serum gliclazide by high-performance liquid chromatography (HPLC) on a column packed with a macroporous anion-exchange resin, Diaion CDR-10, was developed. The elution was performed with acetonitrile—methyl alcohol—1.2 M ammonium perchlorate (4:3:7, v/v/v) at a flow-rate of 0.4 ml/min. The retention time of gliclazide was 15 min. It seems that the retention mechanism of gliclazide under the HPLC conditions described is not only ion-exchange mode but reversed-phase mode between the anion-exchange resin and the mobile phase. The detection limit of gliclazide was 0.2 μg/ml in plasma. The coefficient of variation for the within-day assay was 5.0% (0.2 μg/ml, n=8). The decay curve of serum gliclazide in diabetic patients was determined.     

Efficient production of l-lactic acid from hydrolysate of Jerusalem artichoke with immobilized cells of Lactococcus lactis in fibrous bed bioreactors

Hydrolysate of Jerusalem artichoke was applied for the production of l-lactic acid by immobilized Lactococcus lactis cells in a fibrous bed bioreactor system. Preliminary experiments had indicated that the high quality hydrolysate, which was derived from the 40min acid treatment at 95°C and pH 1.8, was sufficient to support the cell growth and synthesis of l-lactic acid. With the addition of 5g/l yeast extract, the fermentative performance of free cell system was evidently improved. After the basal settlement of hydrolysate based fermentation, the batch mode and the fed-batch mode fermentation were carried out in the free cell system and the fibrous bed bioreactor system, respectively. In all cases the immobilized cells presented the superior ability to produce l-lactic acid. The comparison of batch mode and fed-batch mode also indicated that the growth-limiting feeding strategy could reduce the lag phase of fermentation process and enhance the production of l-lactic acid. The achieved maximum concentration of l-lactic acid was 142g/l in the fed-batch mode. Subsequent repeated-batch fermentation of the fibrous bed bioreactor system had further exhibited the persistence and stability of this system for the high production of l-lactic acid in a long term. Our work suggested the great potential of the fibrous bed bioreactor system and hydrolysate of J. artichoke in the economical production of l-lactic acid at industrial scale.     

Process and metabolic characteristics of Bacillus coagulans as a lactic acid producer

The main autoregulation parameters of the lactic acid fermentation using an untypical producer, Bacillus coagulans , were studied with the help of NMR spectroscopy. Some important intermediate concentrations, estimated in different process conditions, indicate a key role of phosphofructokinase and pyruvate kinase in the glycolytic flux of B. coagulans cells.     

The function of galactosyl phosphorylpolyprenol in biosynthesis of lipoteichoic acid in Bacillus coagulans

Incubation of UDP-[14C]galactose with membranes of Bacillus coagulans led to the formation of a radioactive glycolipid, which was tentatively characterized as beta-galactosyl phosphorylpolyprenol (Gal-P-prenol) on the basis of its chromatographic behavior and data from structural analysis of its sugar 1-phosphate moiety. The sugar moiety of [14C]Gal-P-prenol was shown to be incorporated into a membrane-bound polymer, which coincided with the diacyl form of lipoteichoic acid in its chromatographic behavior on columns of Sephacryl S-300, DEAE-Sephacel and octyl-Sepharose. Hydrogen fluoride hydrolysis of the polymer afforded an alpha-galactoside identical with Gal(alpha 1----2)Gro obtained from lipoteichoic acids. The incorporation of galactose residues from [14C]Gal-P-prenol into the polymer was greatly enhanced by exogenous lipoteichoic acids, especially of the diacyl and monoacyl forms. The optimal pH and metal concentration for the Gal-P-prenol formation, respectively, were found to be 8.4 and 10 mM (MgCl2), whereas those for the transfer of galactose from this lipid intermediate to polymer were 4.5 and 16 mM (CaCl2). The above results lead to the conclusion that Gal-P-prenol serves as the direct galactosyl donor in the synthesis of lipoteichoic acids in B. coagulans.