Studies on Microbial Metabolisms of Sugar Nucleotides

Effects of various factors including incubation time, water content of airdried cells, concentration and pH of KH₂PO₄–K₂HPO₄ mixture, d-glucose concentration, MgSO₄ concentration, GMP concentration, cell concentration, aeration and various kinds of carbohydrates on the fermentative production of GDP-mannose, GDP and GTP from 5′-GMP by air-dried cells of baker’s yeast were investigated. The water content of air-dried cells was the most important factor in the fermentation. When the air-dried cells of baker’s yeast (100 mg/ml) were incubated with 5′-GMP (20 μmoles/ml), d-glucose (800 μmoles/ml), potassium phosphate buffer (360 μmoles/ml, pH 7.0), and MgSO₄ (20 μmoles/ml), 2-hr incubation gave GDP in 20% yield and GTP in 61.1% yield, GDP-mannose being produced in 45% yield after 8-hr incubation. The phosphorylation of 5′-AMP, 5′-dAMP, 5′-dGMP 5′-CMP and 5′-UMP was also observed in high yields under the same conditions.     

Studies on the Accumulation of 5(4)-Amino-4(5)-imidazolecarboxamide Riboside by Escherichia coli

The acculnulation of 5 (4) -amino-4 (5) -imidazolecarboxamide riboside (AICA-R) in the culture medium of sulfonamide-inhibited Escherichia coli, and E. coli-like bacteria was studied. E. coli strain Band 32 strains of E. coli-like bacteria accumulated more than 50 μmoles of AICA-R in test tube scale experiments, and one of E. coli-like bacteria accumulated 358 μmoles. E. coli B-96 (purine-requiring mutant) had ability to accumulate AICA-R in the glucose-salt medium containing purine bases, especially xanthine. The addition of glycine alone or together with glutamic acid to the glucose-salt medium increased the accumulation of AICA-R by sulfadiazine-inhibited E. coli strain B. The accumulation was considerably increased by the addition of polypeptone or casein hydrolysate.

AICA-R accumulated during sulfadiazine bacteriostasis of E. coli strain B was purified and crystallized according to the procedure of Greenberg and Spilman, and light amber colored crystals were obtained.     

Optimization of D-ribose production with a transketolase-affected Bacillussubtilis mutant strain in glucose and gluconic acid-based media

When the transketolase-deficient and D -ribose-producing Bacillus subtilis strain ATCC 21951 was grown in a glucose (200 g l⁻¹)-based medium (Kintaka et al. 1986), only 11 g l⁻¹ D -ribose was synthesized, in addition to acetic acid (12 g l⁻¹) and acetoin plus 2,3-butanediol (24 g l⁻¹), within 1 week of fermentation. After optimizing the process conditions at 2 l fermentor scale (simplified medium composition, pH 5·0 or 6·0, highly oxidative (1000 rev min⁻¹, 3 vvm)), 40 g l⁻¹ D -ribose was obtained from 200 g l⁻¹ D -glucose, in addition to 14·5 g l⁻¹ acetoin, during 1 week of fermentation. By partially substituting D -glucose with D -gluconic acid (100 g l⁻¹ D -glucose plus 50 g l⁻¹ D -gluconic acid) under highly oxidative (1000 rev min⁻¹, 3 vvm) and pH-controlled (pH 6·5) conditions, D -ribose productivity increased (45 g l⁻¹) and acetoin formation (7·5 g l⁻¹) dropped, as did the fermentation time (3·5 d). The mixed carbon substrate procedure here developed provides an excellent alternative to the less efficient glucose-based processes described so far.     

Efficient production of D-glucosaminic acid from D-glucosamine by Pseudomonas putida GNA5

D-glucosaminic acid was produced efficiently from glucosamine by oxidative fermentation using a newly isolated strain, Pseudomonas putida GNA5. After optimization of the fermentation process, 51.5 g L(-1) D-glucosaminic acid was produced from an initial concentration of 60 g L(-1) D-glucosamine-HCl after 72 h of oxidative fermentation, which corresponded to a molar yield of 95.4%. This production process is potentially of considerable economic significance because very few by-products were detected. Furthermore, D-glucosaminic acid was accumulated stably during the oxidative fermentation process without the addition of an inhibitor of D-glucosaminic acid breakdown, even though D-glucosamine was exhausted. These results suggest that the mechanisms of D-glucosaminic acid-related metabolism differ between Pseudomonas putida GNA5 and the strain Pseudomonas genera, which was previously reported to produce D-glucosaminic acid.     

啤酒糟固态发酵产β-葡萄糖苷酶的研究

利用啤酒糟为培养基对黑曲霉固态发酵产β-葡萄糖苷酶的工艺条件进行了优化和动力学研究。单因素试验表明,最适产酶温度、料液比和接种量分别为30℃、1∶5(啤酒糟∶水,g∶mL)和10%(mL/g);利用L9(34)正交试验优化反应条件,结果表明,在25℃,初始料水比为1:5,接种量10%的条件下,培养4d,β-葡萄糖苷酶的酶活可达10.85U/g。动力学研究表明,β-葡萄糖苷酶在96h进入产酶的高峰期,120h达到酶活最大值。     

Synthesis and characterization of the sweetness-suppressing polypeptide gurmarin and ent-Gurmarin

The sweetness-suppressing polypeptide gurmarin isolated from the leaves of Gymnema sylvestre consists of 35 amino acid residues including three intramolecular disulfide bonds. Herein, the total chemical synthesis of gurmarin was performed by the stepwise fluoren-9-ylmethoxy-carbonyl solid-phase method, the yield of reduced gurmarin being 1.9% based on the starting amino acid resin. Disulfide formation was carried out in the presence of a redox system of reduced glutathione/oxidized glutathione to give gurmarin in a yield of 35.5%. The product was identical to natural gurmarin by analytical reverse phase high performance liquid chromatography (RP-HPLC), mass spectroscopy (MS), and peptide mapping, and suppressed the responses to sucrose, D -glucose, and L -glucose in a rat. The D enantiomer (all D -amino acid gurmarin) was also synthesized, and was shown to be the mirror image of gurmarin. Interestingly, the D enantiomer (ent-gurmarin) also suppressed the responses to sucrose, D -glucose, and L -glucose in a rat. © 1996 John Wiley & Sons, Inc.     

Selective,High Conversion of D-Glucose to 5-Keto-D-gluoconate by Gluconobacter suboxydans

Selective, high-yield production of 5-keto-D-gluconate (5KGA) from D-glucose by Gluconobacter was achieved without genetic modification. 5KGA production by Gluconobacter suffers byproduct formation of 2-keto-D-gluconate (2KGA). By controlling the medium pH strictly in a range of pH 3.5–4.0, 5KGA was accumulated with 87% conversion yield from D-glucose. The pH dependency of 5KGA formation appeared to be related to that of gluconate oxidizing activity.     

Fermentation of <Emphasis Type="SmallCaps">d</Emphasis>-glucose and <Emphasis Type="SmallCaps">d</Emphasis>-xylose mixtures by <Emphasis Type="Italic">Candida tropicalis</Emphasis> NBRC 0618 for xylitol production

The fermentation of d-glucose and d-xylose mixtures by the yeast Candida tropicalis NBRC 0618 has been studied under the most favourable operation conditions for the culture, determining the most adequate initial proportion in these sugars for xylitol production. In all the experiments a synthetic culture medium was used, with an initial total substrate concentration of 25 g L⁻¹, a constant pH of 5.0 and a temperature of 30 °C. From the experimental results, it was deduced that the highest values of specific rates of production and of overall yield in xylitol were achieved for the mixtures with the highest percentage of d-xylose, specifically in the culture with the initial d-glucose and d-xylose concentrations of 1 and 24 g L⁻¹, respectively, with an overall xylitol yield of 0.28 g g⁻¹. In addition, the specific rates of xylitol production declined over the time course of the culture and the formation of this bioproduct was favoured by the presence of small quantities of d-glucose. The sum of the overall yield values in xylitol and ethanol for all the experiments ranged from 0.26 to 0.56 g bioproduct/g total substrate.     

Extracellular melibiose and fructose are intermediates in raffinose catabolism during fermentation to ethanol by engineered enteric bacteria.

Contrary to general concepts of bacterial saccharide metabolism, melibiose (25 to 32 g/liter) and fructose (5 to 14 g/liter) accumulated as extracellular intermediates during the catabolism of raffinose (O-alpha-D-galactopyranosyl-1, 6-alpha-D-glucopyranosyl-beta-D-fructofuranoside) (90 g/liter) by ethanologenic recombinants of Escherichia coli B, Klebsiella oxytoca M5A1, and Erwinia chrysanthemi EC16. Both hydrolysis products (melibiose and fructose) were subsequently transported and further metabolized by all three organisms. Raffinose catabolism was initiated by beta-fructosidase; melibiose was subsequently hydrolyzed to galactose and glucose by alpha-galactosidase. Glucose and fructose were completely metabolized by all three organisms, but galactose accumulated in the fermentation broth with EC16(pLOI555) and P2. MM2 (a raffinose-positive E. coli mutant) was the most effective biocatalyst for ethanol production (38 g/liter) from raffinose. All organisms rapidly fermented sucrose (90 g/liter) to ethanol (48 g/liter) at more than 90% of the theoretical yield. During sucrose catabolism, both hydrolysis products (glucose and fructose) were metabolized concurrently by EC16(pLOI555) and P2 without sugar leakage. However, fructose accumulated extracellularly (27 to 28 g/liter) at early stages of fermentation with KO11 and MM2. Sequential utilization of glucose and fructose correlated with a diauxie in base utilization (pH maintenance). The mechanism of sugar escape remains unknown but may involve downhill leakage via permease which transports precursor saccharides or novel sugar export proteins. If sugar escape occurs in nature with wild organisms, it could facilitate the development of complex bacterial communities which are based on the sequence of saccharide catabolism and the hierarchy of sugar utilization.     

Production of L(+)-lactic acid from glucose and starch by immobilized cells of Rhizopus oryzae in a rotating fibrous bed bioreactor

A rotating fibrous-bed bioreactor (RFB) was developed for fermentation to produce L(+)-lactic acid from glucose and cornstarch by Rhizopus oryzae. Fungal mycelia were immobilized on cotton cloth in the RFB for a prolonged period to study the fermentation kinetics and process stability. The pH and dissolved oxygen concentration (DO) were found to have significant effects on lactic acid productivity and yield, with pH 6 and 90% DO being the optimal conditions. A high lactic acid yield of 90% (w/w) and productivity of 2.5 g/L.h (467 g/h.m(2)) was obtained from glucose in fed-batch fermentation. When cornstarch was used as the substrate, the lactic acid yield was close to 100% (w/w) and the productivity was 1.65 g/L.h (300 g/h.m(2)). The highest concentration of lactic acid achieved in these fed-batch fermentations was 127 g/L. The immobilized-cells fermentation in the RFB gave a virtually cell-free fermentation broth and provided many advantages over conventional fermentation processes, especially those with freely suspended fungal cells. Without immobilization with the cotton cloth, mycelia grew everywhere in the fermentor and caused serious problems in reactor control and operation and consequently the fermentation was poor in lactic acid production. Oxygen transfer in the RFB was also studied and the volumetric oxygen transfer coefficients under various aeration and agitation conditions were determined and then used to estimate the oxygen transfer rate and uptake rate during the fermentation. The results showed that the oxygen uptake rate increased with increasing DO, indicating that oxygen transfer was limited by the diffusion inside the mycelial layer.     

营养及环境因素对黄色短杆菌发酵生产L-亮氨酸的影响

目的:研究葡萄糖、玉米浆、蛋氨酸等主要营养物质以及环境因素对发酵生产L-亮氨酸的影响。方法:应用单因素实验确定发酵条件,采用高效液相色谱法测定产量。结果:在最优发酵条件下,以种龄36h、接种量为10%,摇瓶产L-亮氨酸的量可达19.4g/L,采用10L罐分批补料发酵64h可积累29.47g/L的亮氨酸。结论:营养及环境因素对发酵生产L-亮氨酸具有重要影响。     

敲除frdB基因对大肠杆菌厌氧混合酸发酵的影响

以SPUEC101(产琥珀酸)为出发菌,利用RED同源重组技术敲除延胡索酸还原酶基因frdB,得到重组菌株SPUEC103(△frdB),通过减少延胡索酸生成琥珀酸的通量,实现延胡索酸的积累。实验结果表明:敲除frdB基因后,缺陷菌株生长速率降低,利用葡萄糖的能力也有所降低,同时敲除frdB基因较大程度地改变琥珀酸、延胡索酸等的分布,在两阶段发酵中,当发酵培养基中添加30 g/L的葡萄糖时,琥珀酸和延胡索酸得率最高,对比SPUEC101,SPUEC103的琥珀酸产量产率由24.6%下降为15.4%,并有延胡索酸和少量的苹果酸生成,分别为0.182±0.002 g/L和0.023±0.002 g/L,同时丙酮酸和乙酸含量也略有升高,分别由1.87±0.02 g/L、0.012±0.002 g/L上升到2.36±0.03 g/L、0.862±0.012 g/L。     

Continuous ethanol production by thermotolerant Kluyveromyces marxianus IMB3 immobilized on mineral Kissiris at 45°C

Thermotolerant Kluyveromyces marxianus var. marxianus IMB3 yeast strain was immobilized on Kissiris (mineral glass foam derived from lava) in column packed reactors, and used for ethanol production from glucose or molasses under continuous culture conditions at temperatures between 40 and 50°C. Both ethanol yield and fermentation efficiency were highest at 45°C and a dilution rate (D) of 0.15/h. Increasing sugar concentration led to an increase in ethanol yield of up to 68.6 and 55.9 g/l on approx. 200g glucose or molasses, respectively. Optimum fermentation efficiency (experimental yields over theoretical maximum yields) however was at about 15% sugar for both glucose and molasses. Slight aeration (25 ml of air/min) through the medium addition line was found advantageous due to its mixing effect and probable maintenance of activity.     

Impacts of main factors on bioethanol fermentation from stalk juice of sweet sorghum by immobilized Saccharomyces cerevisiae (CICC 1308)

In order to attain a higher ethanol yield and faster ethanol fermentation rate, orthogonal experiments of ethanol fermentation with immobilized yeast from stalk juice of sweet sorghum were carried out in the shaking flasks to investigate the effect of main factors, namely, fermentation temperature, agitation rate, particles stuffing rate and pH on ethanol yield and CO(2) weight loss rate. The range analysis and analysis of variance (ANOVA) were applied for the results of orthogonal experiments. Results showed that the optimal condition for bioethanol fermentation should be A(4)B(3)C(3)D(4), namely, fermentation temperature, agitation rate, particles stuffing rate and pH were 37 degrees C, 200rpm, 25% and 5.0, respectively. The verification experiments were carried out in shaking flasks and 5L bioreactor at the corresponding parameters. The results of verification experiments in the shaking flasks showed that ethanol yield and CO(2) weight loss rate were 98.07% and 1.020gh(-1), respectively. The results of ethanol fermentation in the 5L bioreactor showed that ethanol yield and fermentation time were 93.24% and 11h, respectively. As a result, it could be concluded that the determined optimal condition A(4)B(3)C(3)D(4) was suitable and reasonable for the ethanol fermentation by immobilized Saccharomyces cerevisiae. The conclusion in the research would be beneficial for application of ethanol fermentation by immobilized S. cerevisiae from stalk juice of sweet sorghum.     

Lactic acid fermentation of crude sorghum extract

Crude extract from sweet sorghum supplemented with vetch juice was utilized as the carbohydrate source for fermentative production of lactic acid. Fermentation of media containing 7%(w/v) total sugar was complex completed in 60–80 hr by Lactobacillus plantarum, product yield averaging 85%. Maximum acid production rates were dependent on pH, initial substrate distribution, and concentration, the rates varying from 2 to 5 g(liter·hr.) The lactic acid yield was lowered to 67% under limited medium supplementation. The fermented ammoniated product contained over eight times as much equivalent crude protein (N × 6.25) as the original medium. Unstructured kinetic models were developed for cell growth, lactic acid formation, and substrate consumption in batch fermentation. With the provision of experimentally determined kinetic parameters, the proposed models accurately the fermentation process.     

Accumulation of 5′ guanine nucleotides by mutants of Brevibacterium ammoniagenes

5′Xanthylic acid was efficiently converted to 5′guanine nucleotides (5′GMP, 5′GDP, and 5′GTP) without being degraded to guanine via 5′GMP by decoyinine resistant mutants of strain KY 13315 which had been isolated from Brevibacterium ammoniagenes and was practically devoid of 5′nucleotide degrading activity. The concentration of phosphate in the medium showed a profound effect on the ratio of the accumulated 5′guanine nucleotides, making it possible to direct the fermentation towards 5′GMP or 5′GTP. A direct accumulation of 5′guanine nucleotides from carbohydrate was possible by mixed cultivation of a 5′XMP accumulating strain and a 5′XMP converting mutant. A maximum concentration of 9.67 mg of 5′guanine nucleotides per ml was obtained directly from glucose in such a mixed culture.     

Production of Nucleic Acid-Related Substances by Fermentative Processes

An adenine-requiring mutant (KY7208) of Brevibacterium ammoniagenes ATTC 6872 was found to accumulate an appreciable quantity of IMP and hypoxanthine in the culture liquid.

Crystalline IMP was isolated from culture broth of KY7208 by the use of ion-exchange columns. The preparation obtained was definitely identified as 5′-IMP, based on the results on paperchromatography, UV and IR absorption spectra, and analyses of its hydrolysates.

Growth responses of this mutant were demonstrated to adenine and adenosine, but not to 5′-AMP, 3′-AMP and 5′-AMP.

Over 5 mg of IMP per ml of broth were produced by the organism in natural medium consisting of glucose, yeast extract, urea, high concentrations of phosphate and magnesim salts, and others. The chemical changes showed that hypoxanthine first accumulated in the earlier stage of fermentation, and IMP synthesis then took place with the disappearance of hypoxanthine in the later stage of fermentation.     

产D-阿拉伯醇菌株的筛选、鉴定及其产D-阿拉伯醇条件的优化

摘要：【目的】产D-阿拉伯醇的耐高渗酵母的筛选、鉴定和产D-阿拉伯醇条件的优化。【方法】通过电镜、Biolog GN、(G+C)含量和26S rDNA D1/D2区序列分析法对所获得的菌株进行了描述。通过红外光谱、核磁共振氢谱和碳谱、质谱以及旋光度实验鉴定纯化产物的结构。通过单因素实验优化产D-阿拉伯醇的发酵条件。【结果】本文筛选得到一株产D-阿拉伯醇的新型菌株,经鉴定属于假丝酵母属并命名为Candida sp. H2。200 mL摇瓶发酵生产D-阿拉伯醇的单因素优化实验表明,最适发酵条件为：葡萄糖250     

Biosynthesis of ochratoxins by Aspergillus ochraceus.

Shaken liquid fermentation of an isolate of Aspergillus ochraceus showed growth-associated production of ochratoxins A and B, followed by production of a related polyketide diaporthin. Later, between 150 and 250 h, mellein accumulated transitorily. In contrast, shaken solid substrate (shredded wheat) fermentation over 14 days produced mainly ochratoxins A and B (ratio ca. 5:1) in very high yield (up to 10 mg/g). In these systems experiments with 14C-labelled precursors and putative intermediates revealed temporal separation of early and late stages of the ochratoxin biosynthetic pathway, but did not support an intermediary role for mellein. The pentaketide intermediate ochratoxin beta was biotransformed very efficiently into both ochratoxins A and B, 14 and 19%, respectively. The already chlorinated ochratoxin alpha was only biotransformed significantly (4.85%) into ochratoxin A, indicating that chlorination is mainly a penultimate biosynthetic step in the biosynthesis of ochratoxin A. This was supported by poor (1.5%) conversion of radiolabelled ochratoxin B into ochratoxin A. Experiments implied that some ochratoxin B may arise by dechlorination of ochratoxin A.     

Lactic acid production by <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> expressing a <Emphasis Type="Italic">Rhizopus oryzae</Emphasis> lactate dehydrogenase gene

This work demonstrates the first example of a fungal lactate dehydrogenase (LDH) expressed in yeast. A L(+)-LDH gene, ldhA, from the filamentous fungus Rhizopus oryzae was modified to be expressed under control of the Saccharomyces cerevisiae adh1 promoter and terminator and then placed in a 2μ-containing yeast-replicating plasmid. The resulting construct, pLdhA68X, was transformed and tested by fermentation analyses in haploid and diploid yeast containing similar genetic backgrounds. Both recombinant strains utilized 92 g glucose/l in approximately 30 h. The diploid isolate accumulated approximately 40% more lactic acid with a final concentration of 38 g lactic acid/l and a yield of 0.44 g lactic acid/g glucose. The optimal pH for lactic acid production by the diploid strain was pH 5. LDH activity in this strain remained relatively constant at 1.5 units/mg protein throughout the fermentation. The majority of carbon was still diverted to the ethanol fermentation pathway, as indicated by ethanol yields between 0.25–0.33 g/g glucose. S. cerevisiae mutants impaired in ethanol production were transformed with pLdhA68X in an attempt to increase the lactic acid yield by minimizing the conversion of pyruvate to ethanol. Mutants with diminished pyruvate decarboxylase activity and mutants with disrupted alcohol dehydrogenase activity did result in transformants with diminished ethanol production. However, the efficiency of lactic acid production also decreased. Electronic Publication