3-Phenyllactic acid production by substrate feeding and pH-control in fed-batch fermentation of Lactobacillus sp. SK007

3-Phenyllactic acid (PLA), which is produced by some strains of lactic acid bacteria (LAB), is a known antimicrobial agent with a broad spectrum. Batch and fed-batch fermentation by the strain Lactobacillus sp. SK007 for PLA production have been reported. With batch fermentation without pH-control, PLA production yield was 2.42 g L⁻¹. When fed-batch fermentation by Lactobacillus sp. SK007 was conducted in 3 L initial volume with pH-control at 6.0 and intermittent feeding, which was developed after fermentation for 12 h and every 2 h with 120 mL 100 g L⁻¹ PPA phenylpyruvic acid (PPA) and 50 mL 500 g L⁻¹ glucose each time, PLA production yield reached 17.38 g L⁻¹. The final conversion ratio of PPA to PLA was 51.1%, and the PLA production rate was 0.241 g L⁻¹ h⁻¹. This indicated that PPA was the ideal substrate for PLA fermentation production, and fed-batch fermentation with intermittent PPA feeding and pH-control was an effective approach to improve PLA production yield.     

Product shifting by controlling medium pH in immobilised Streptomyces coelicolor A3(2) culture

Actinorhodin production by Streptomyces coelicolor A3(2) immobilised naturally in a porous support material was investigated in a 20 l bioreactor. The effect of pH-control on actinorhodin fermentation was conducted by performing different strategies. The combination of pH-control and immobilisation of the cells produced a different result than pH-control with freely suspended cells. The control of pH at 7.2 in an immobilised cell system altered the physiology of the cells shifting the product, actinorhodin, to another pigmented secondary metabolite, undecylprodigiosin. Although the cells were biologically active in such an environment, they were unable to produce actinorhodin. In the freely suspended cell system, however, actinorhodin biosynthesis was not hindered by controlling the medium pH.     

Selection method of pH conditions to establish Pseudomonas taetrolens physiological states and lactobionic acid production

Microbial physiological responses resulting from inappropriate bioprocessing conditions may have a marked impact on process performance within any fermentation system. The influence of different pH-control strategies on physiological status, microbial growth and lactobionic acid production from whey by Pseudomonas taetrolens during bioreactor cultivations has been investigated for the first time in this work. Both cellular behaviour and bioconversion efficiency from P. taetrolens were found to be negatively influenced by pH-control modes carried out at values lower than 6.0 and higher than 7.0. Production schemes were also influenced by the operational pH employed, with asynchronous production from damaged and metabolically active subpopulations at pH values lower than 6.0. Moreover, P. taetrolens showed reduced cellular proliferation and a subsequent delay in the onset of the production phase under acidic conditions (pH?<?6.0). Unlike cultivations performed at 6.5, both pH-shift and pH-stat cultivation strategies performed at pH values lower than 6.0 resulted in decreased lactobionic acid production. Whereas the cellular response showed a stress-induced physiological response under acidic conditions, healthy functional cells were predominant at medium operational pH values (6.5–7.0). P. taetrolens thus displayed a robust physiological status at initial pH value of 6.5, resulting in an enhanced bioconversion yield and lactobionic acid productivity (7- and 4-fold higher compared to those attained at initial pH values of 4.5 and 5.0, respectively). These results have shown that pH-control modes strongly affected both the physiological response of cells and the biological performance of P. taetrolens, providing key information for bio-production of lactobionic acid on an industrial scale.     

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.     

Enhancement of cephamycin C production using soybean oil as the sole carbon source

Vegetable oils were investigated to evaluate their potential to act as the sole carbon source for production of cephamycin C in shake and jar-fermentor cultures. Soybean oil was the best carbon source for cephamycin C production. Bioautography and HPLC analyses showed that cephamycin C was exclusively produced even when soybean oil was used as the sole cabon source. The optimal pH and initial concentration of soybean oil was 7.5 and 7 g/l, respectively. Both pH and the pH-control agent affected cephamycin C production, and among phosphoric acid, acetic acid and sulfuric acid, phosphoric acid was associated with the best production. Soybean oil was slowly consumed after the soluble nitrogen source was consumed. When the initial soybean oil concentration was 7 g/l, cephamycin C production was maximal, 2.0 g/l, which was twice as high as that from starch. The product yield from soybean oil was 4.7 times higher than that from starch. These results show that vegetable oils, which are cheaper than other carbon sources, could be used as the sole carbon source in the production of antibiotics. Correspondence to: M. Okabe     

pH-control modes in a 5-L stirred-tank bioreactor for cell biomass and exopolysaccharide production by Tremella fuciformis spore

The effect of pH-control modes on cell growth and exopolysaccharide production by Tremella fuciformis was evaluated in a 5-L bioreactor. The results show that the maximal dry cell weight (DCW) and exopolysaccharide production were 23.57 and 4.48 g L⁻¹ in pH-stat fermentation, where the maximal specific growth rate (μ_max) and specific production rate of exopolysaccharide (P_P/X) were 1.03 and 0.24 d⁻¹, respectively; under pH-shift cultivation, the maximal DCW and exopolysaccharide production were 30.57 and 3.90 g L⁻¹, where the μ_max and P_P/X were 1.21 and 0.06 d⁻¹. Unlike batch fermentation, maximal DCW and exopolysaccharide production merely reached 15.04 and 2.0 g L⁻¹, where the μ_max and P_P/X were 0.86 and 0.05 d⁻¹, respectively. These results suggest that a pH-stat strategy is a more efficient way of performing the fermentation process to increase exopolysaccharide production. Furthermore, this research has also proved that the three-stage pH-control mode is effective for cell growth.     

Improvement of 5-aminolevulinic acid production by Rubrivivax benzoatilyticus PS-5 with self-flocculation by co-fermentation of precursors and volatile fatty acids under pH-controlled conditions

Photosynthetic bacteria are known to utilize volatile fatty acids as a carbon source for growth and product formation. In this study, a new isolate, Rubrivivax benzoatilyticus PS-5, possessing self-flocculation properties, was cultivated in modified glutamate-malate (GM) medium containing glutamate and malate as carbon sources. The effect of acetic acid, propionic acid and butyric acid (at 1–4 g L^?1) as co-substrates and 7.5 mM glycine, 10 mM succinic acid as precursors for 5-aminolevulinic acid (ALA) production from R. benzoatilyticus PS-5 was investigated. Among the volatile fatty acids tested, acetic acid was preferred to butyric acid and propionic acid, with the optimum concentrations of 3 g L^?1, 1 g L^?1 and 3 g L^?1, respectively. The highest ALA production was 169.71 μM, 162.16 μM and 46.18 μM, respectively, while the highest productivity was 2.57 μM h^?1, 2.25 μM h^?1 and 0.96 μM h^?1, respectively. The precursor was consumed completely (100 %) while the assimilation of the acetic acid and butyric acid was 62.50 % and 48.65 %, respectively. Supplementation of propionic acid (at 1–4 g l^?1) had a negative effect on growth and ALA production. To increase production efficiency, the pH-control strategy (at pH 6.0–8.0) during fermentation was tested. The optimum pH was 7.0, giving the maximum ALA production of 286.18 μM and a productivity of 3.97 μM h^?1. These values were 1.68-fold and 1.54-fold higher, respectively, than those under uncontrolled pH conditions.     

Production of thuringiensin by fed-batch culture of Bacillus thuringiensis subsp. darmstadiensis 032 with an improved pH-control glucose feeding strategy

A improved pH-control fed-batch strategy for Bacillus thuringiensis subsp. darmstadiensis 032 producing thuringiensin was developed based on the analysis of the batch culture, constant rate fed-batch cultures and the original pH-control fed-batch. Having considered the pH variation and the glucose consumption status, the pH was adjusted from 6.5 to 7.0 by adding base in the late cultivation period of batch culture, and then the pH was kept at 7.0 by glucose feeding. The feeding was terminated when the pH could not be controlled by glucose feeding anymore. The proposed fed-batch strategy effectively avoided underfeeding or overfeeding, and it increased the thuringiensin yield and Y_P/X by 89.51% and 103.2% compared to that of the batch culture, respectively.     

氨基酸生产的代谢工程研究进展与发展趋势

氨基酸发酵是我国发酵工业的支柱产业,近年来,随着代谢工程的快速发展,氨基酸的代谢工程育种蓬勃发展。传统的正向代谢工程、基于组学分析与计算机模拟的反向代谢工程以及借鉴自然进化的进化代谢工程,都有越来越多的应用。在氨基酸的工业生产中涌现出了一系列具有高效生产、抗逆性强等优良性状的菌株。日益剧烈的市场竞争对菌株的选育提出了新的要求,如开发高附加值氨基酸品种、菌株代谢的动态调控、适应新工艺的要求等。文中介绍了氨基酸生产相关的代谢工程研究进展以及未来的发展趋势。     

Qualitative and quantitative composition of acids formed by bifidobacteria

The dynamics of acid production in 18 strains of bifidobacteria, belonging to 5 different species, has been studied Bifidobacteria have been found to produce 3 acids, lactic, acetic and formic, in the process of their metabolism. The lactic acid/acetic acid quantitative ratio varies, depending on the culture medium on the average, 1:2 in Blaurock medium, 1:5 in milk hydrolysate medium. Various strains have also been found to differ in the dynamics of acid production with respect to the amounts of lactic and acetic acids. The study has shown that, despite the active production of acids for a period of up to 72 hours, a decrease in the pH of the medium is observed for not more than 48 hours. The existence of a specific mechanism permitting bifidobacteria to regulate the acidity of their environment is supposed.     

Eco-Efficiency Analysis of biotechnological processes

For almost 50 years now, biotechnological production processes have been used for industrial production of amino acids. Market development has been particularly dynamic for the flavor-enhancer glutamate and the animal feed amino acids l-lysine, l-threonine, and l-tryptophan, which are produced by fermentation processes using high-performance strains of Corynebacterium glutamicum and Escherichia coli from sugar sources such as molasses, sucrose, or glucose. But the market for amino acids in synthesis is also becoming increasingly important, with annual growth rates of 5–7%. The use of enzymes and whole cell biocatalysts has proven particularly valuable in production of both proteinogenic and nonproteinogenic l-amino acids, d-amino acids, and enantiomerically pure amino acid derivatives, which are of great interest as building blocks for active ingredients that are applied as pharmaceuticals, cosmetics, and agricultural products. Nutrition and health will continue to be the driving forces for exploiting the potential of microorganisms, and possibly also of suitable plants, to arrive at even more efficient processes for amino acid production.     

Microbial production of organic acids: expanding the markets

Microbial production of organic acids is a promising approach for obtaining building-block chemicals from renewable carbon sources. Although some acids have been produced for some time and in-depth knowledge of these microbial production processes has been gained, further microbial production processes seem to be feasible, but large-scale production has not yet been possible. Citric, lactic and succinic acid production exemplify three processes in different stages of industrial development. Although the questions being addressed by current research on these processes are diverging, a comparison is helpful for understanding microbial organic acid production in general. In this article, through analysis of the current advances in production of these acids, we present guidelines for future developments in this fast-moving field.     

Metabolic engineering of Saccharomyces cerevisiae for production of carboxylic acids: current status and challenges

To meet the demands of future generations for chemicals and energy and to reduce the environmental footprint of the chemical industry, alternatives for petrochemistry are required. Microbial conversion of renewable feedstocks has a huge potential for cleaner, sustainable industrial production of fuels and chemicals. Microbial production of organic acids is a promising approach for production of chemical building blocks that can replace their petrochemically derived equivalents. Although Saccharomyces cerevisiae does not naturally produce organic acids in large quantities, its robustness, pH tolerance, simple nutrient requirements and long history as an industrial workhorse make it an excellent candidate biocatalyst for such processes. Genetic engineering, along with evolution and selection, has been successfully used to divert carbon from ethanol, the natural endproduct of S. cerevisiae , to pyruvate. Further engineering, which included expression of heterologous enzymes and transporters, yielded strains capable of producing lactate and malate from pyruvate. Besides these metabolic engineering strategies, this review discusses the impact of transport and energetics as well as the tolerance towards these organic acids. In addition to recent progress in engineering S. cerevisiae for organic acid production, the key limitations and challenges are discussed in the context of sustainable industrial production of organic acids from renewable feedstocks.     

Production of 7,10-dihydroxy-8(<Emphasis Type="Italic">E</Emphasis>)-octadecenoic acid from olive oil by <Emphasis Type="Italic">Pseudomonas aeruginosa</Emphasis> PR3

Microbial modification of naturally occurring materials is one of the efficient ways to add new values to them. Hydroxylation of free unsaturated fatty acids by microorganism is a good example of those modifications. Among microbial strains studied for that purpose, a new bacterial isolate Pseudomonas aeruginosa PR3 has been well studied to produce several hydroxy fatty acids from different unsaturated fatty acids. Of those hydroxy fatty acids, 7,10-dihydroxy-8(E)-octadecenoic acid (DOD) was efficiently produced from oleic acid by strain PR3. However, it was highly plausible to use vegetable oil containing oleic acid rather than free oleic acid as a substrate for DOD production by strain PR3. In this study, we firstly tried to use olive oil containing high content of oleic acid as a substrate for DOD production. DOD production from olive oil was confirmed by structural determination with GC, TLC, and GC/MS analysis. DOD production yield from olive oil was 53.5%. Several important environmental factors were also tested. Galactose and glutamine were optimal carbon and nitrogen sources, and magnesium ion was critically required for DOD production from olive oil. Results from this study demonstrated that natural vegetable oils containing oleic acid could be used as efficient substrate for the production of DOD by strain PR3.     

Construction of an engineered biocatalyst system for the production of medium-chain α,ω-dicarboxylic acids from medium-chain ω-hydroxycarboxylic acids

Medium-chain α,ω-dicarboxylic acids produced from renewable long-chain fatty acids are valuable as precursors in the chemical industry. However, they are difficult to produce biologically at high concentrations. Although improved biocatalyst systems consisting of engineering of Baeyer–Villiger monooxygenases are used in the production of ω-hydroxycarboxylic acids from long-chain fatty acids, the engineering of biocatalysts involved in the production of α,ω-dicarboxylic acids from ω-hydroxycarboxylic acids has been rarely attempted. Here, we used highly active bacterial enzymes, Micrococcus luteus alcohol dehydrogenase and Archangium violaceum aldehyde dehydrogenase, for the efficient production of α,ω-dicarboxylic acids from ω-hydroxycarboxylic acids and constructed a biocatalyst with cofactor regeneration system by introducing NAD(P)H flavin oxidoreductase as the NAD(P)H oxidase. The inhibition of the biocatalyst by hydrophobic substrates was attenuated by engineering a biocatalyst system with an adsorbent resin, which allowed us to obtain 196 mM decanedioic, 145 mM undecanedioic, and 114 mM dodecanedioic acid from 200 mM of C10, C11, and C12 hydroxyl saturated carboxylic acids, respectively, and 141 mM undecanedioic acid from 150 mM C11 unsaturated carboxylic acids, with molar conversions of 98%, 97%, 95%, and 94%, respectively. The concentration of undecanedioic acid obtained was approximately 40-fold higher than that in the previously highest results. Our results from this study can be applied for the industrial production of medium-chain α,ω-dicarboxylic acids from renewable long-chain fatty acids.     

有机酸对菜地土壤磷素活化的影响

实验室模拟研究两种有机酸(柠檬酸、草酸)对菜地土壤磷素活化的影响。结果表明:有机酸对菜地土壤磷的活化效果较明显,且随有机酸浓度的增加,土壤磷活化效果越显著。两种有机酸的活化效果为草酸>柠檬酸。有机酸对磷的活化效果与土壤Olsen- P含量、有机质含量呈显著正相关关系。土壤中有效磷的释放随着有机酸浸提时间的延长而逐渐增加。     

海芦笋及其生物盐中多酚酸和绿原酸的定量分析

以绿原酸为对照品,利用紫外分光光度法和高效液相色谱法分别建立了测定海芦笋中多酚酸和绿原酸含量的方法.紫外分光光度法检测波长为338 nm;高效液相色谱法采用Zorbax Eclipse XDB-C187(4.6 mm×150mm,5um),以甲醇和0.5％冰醋酸水溶液梯度洗脱.结果发现海芦笋及其生物盐中含有大量的多酚酸和绿原酸,其中多酚酸含量分别为6.49 g/kg,3.37 g/kg,绿原酸含量分别为0.234 9/kg,0.180 g/kg.同时也表明高效液相色谱法可用于海芦笋中多酚酸含量的确定.这两种简单快捷的定量分析多酚酸和绿原酸的方法,不仅可用于海芦笋及其生物盐产品的质量控制,而且也为海芦笋的进一步研究和开发提供了一定的依据.     

Microbial production of odd-chain fatty acids

Odd-chain fatty acids (OcFAs) and their derivatives have attracted much attention due to their beneficial physiological effects and their potential to be alternatives to advanced fuels. However, cells naturally produce even-chain fatty acids (EcFAs) with negligible OcFAs. In the process of biosynthesis of fatty acids (FAs), the acetyl-CoA serves as the starter unit for EcFAs, and propionyl-CoA works as the starter unit for OcFAs. The lack of sufficient propionyl-CoA, the precursor, is usually regarded as the main restriction for large-scale bioproduction of OcFAs. In recent years, synthetic biology strategies have been used to modify several microorganisms to produce more propionyl-CoA that would enable an efficient biosynthesis of OcFAs. This review discusses several reported and potential metabolic pathways for propionyl-CoA biosynthesis, followed by advances in engineering several cell factories for OcFAs production. Finally, trends and challenges of synthetic biology driven OcFAs production are discussed.     

Bioconversion of crude glycerol by fungi

The production of synthetic glycerol from petrochemical feedstocks has been decreasing in recent years. This is largely due to increasing supplies of crude glycerol derived as a co-product from the oleochemical industry, especially biodiesel production. The price of glycerol is at historic lows, and the supply of crude glycerol is projected to grow faster than its industrial uses. This oversupply is driving the transition from glycerol as a product to glycerol as a precursor for new industrial applications, including its use as a substrate for bioconversion. This article reviews the use of fungi for the bioconversion of crude glycerol to the value-added products 1,2-propanediol, ethanol, single cell oil, specialty polyunsaturated fatty acids, biosurfactants, and organic acids. Information on the impurities of crude glycerol from different industrial processes is also included.     

Enhanced production of xylanase from Staphylococcus sp. SG-13 using amino acids

Amino acids such as DL-2-amino-n-butyric acid, DL-alanine, L-lysine monohydrochloride, DL-valine and L-proline enhanced total xylanase production from Staphylococcus sp. SG-13 up to 5.5-fold. The present study showed that xylanase production has mainly been governed by the chemical structure of amino acids and their analogues.