Production of l-Glutamine by a Penicillin-Resistant Mutant of Flavobacterium rigense

To establish a practical method for the fermentative production of l-glutamine, cultural conditions for the accumulation of a large amounts of l-glutamine were investigated by using Flavobacterium rigense 703, which was previously reported by us as a l-glutamine-producing mutant. As a result, a yield of 25 mg of l-glutamine per ml was obtained after a 48-h cultivation in a medium containing glucose, yeast extract, (NH(4))(2)-fumarate, KH(2)PO(4), K(2)HPO(4), MgSO(4).7H(2)O, and CaCO(3) (pH 6.4). Accumulation of l-glutamine was dependent upon the concentration of (NH(4))(2)-fumarate, and a suboptimum growth at a relatively high concentration of (NH(4))(2)-fumarate was essential for the maximum production of l-glutamine. At the optimum conditions, glutamic acid was formed as a by-product at a concentration of less than 1 mg/ml, but accumulation of the other amino acids was negligible. The product was isolated from the culture broth and readily purified by anion-exchange chromatography. The pure crystals of l-glutamine obtained in an 80% yield were optically and chromatographically pure.     

Mechanism of l-Glutamine Production by an l-Glutamine-Producing Mutant of Flavobacterium rigense

Properties of some enzymes involved in l-glutamine biosynthesis in an l-glutamine-producing mutant of Flavobacterium rigense were examined. Glutamate-oxaloacetate transaminase in the mutant was nearly at the same level as that in the parent strain and was the most active among the enzymes participating in glutamate biosynthesis from alpha-ketoglutarate. Glutamine synthetase formation in the mutant was enhanced by increasing the concentration of (NH(4))(2)-fumarate in the medium, but the activity of this enzyme in the parent strain was very low, and its formation was not influenced by the concentration of (NH(4))(2)-fumarate. Glutaminase formation by both strains was similar and was not influenced by the levels of (NH(4))(2)-fumarate. Glutaminase activity of the mutant was inhibited by ammonia and fumarate. Intracellular amino acids and extracellular free amino acids in the mutant were compared with those of the parent strain. It seems reasonable to conclude that l-glutamine leaks out specifically through the cell membrane of strain 703 and that this specific excretion of l-glutamine probably allows a continuous conversion of l-glutamate to l-glutamine inside the cell.     

Physiology of growth and sporulation in Bacillus cereus. I. Effect of glutamic and other amino acids

Buono, F. (Syracuse University, Syracuse, N.Y.), R. Testa, and D. G. Lundgren. Physiology of growth and sporulation in Bacillus cereus. I. Effect of glutamic and other amino acids. J. Bacteriol. 91:2291-2299. 1966.-Growth and sporulation were studied in Bacillus cereus by use of an active culture technique and a synthetic medium. A high level of glutamic acid (70 mm) was required for optimal growth and glucose oxidation followed by sporulation even though relatively little glutamic acid was consumed (14 mm). Optimal growth occurred with a combination of 14 mm glutamic acid and 56 mm (NH(4))(2)SO(4), aspartic acid, or alanine. Ornithine or arginine at 70 mm could replace glutamic acid in the synthetic medium without affecting the normal growth cycle. Glutamic acid was not replaced by any other amino acid, by (NH(4))(2)SO(4), or by a combination of either alpha-ketoglutarate or pyruvate plus (NH(4))(2)SO(4). Enzyme assays of cell-free extracts prepared from cells harvested at different times were used to study the metabolism of glutamic acid. Glutamic-oxaloacetic and glutamic-pyruvate transaminases were completely activated (or derepressed) during early stages of sporulation (period of 6 to 8 hr). Alanine dehydrogenase responded in a similar manner, but the levels of this enzyme were much higher throughout the culture cycle. Neither glutamic dehydrogenase nor alpha-ketoglutarate dehydrogenase was detected. Sporulation in a replacement salts medium was studied with cells harvested at different times from the synthetic medium. Cultures 2 to 6 hr old were unable to sporulate in the replacement salts medium unless glutamic acid (7.0 mm) was present. By the 6th hr, cells were in the early stages of sporulation, showing spore septa development. Cultures 8 hr old sporulated in the replacement salts medium. Other metabolic intermediates able to replace glutamic acid in the replacement salts medium were alanine, aspartic acid, and glutamine at equimolar concentrations. Also, ammonium ions in combination with pyruvic, oxaloacetic, alpha-ketoglutaric, or fumaric acid replaced glutamic acid. The likely role of these metabolites is discussed.     

耐铵型产琥珀酸放线杆菌的选育

以Actinobacillus succinogenes NJ113为出发菌株,经硫酸二乙酯(DES)诱变,在含8～20 g/L硫酸铵平板中筛选到一株耐铵型突变株YZ25,该菌株在含8 g/L硫酸铵培养基中厌氧发酵,琥珀酸产量达32.68 g/L,比出发菌提高了180.5%,对葡萄糖收率达65.4%,副产物乙酸、甲酸产量分别下降3.5%、28.7%,琥珀酸/乙酸比值由0.63提高到2.5。在7.5 L发酵罐中,用氨水调节pH分批实验,发酵34 h琥珀酸产量达27.13 g/L,较出发菌株提高了85.3%。     

Strain development and medium optimization for fumaric acid production

Rhizopus oryzae RUR709 mutant was isolated based on halo size from selection medium via mutagenesis with UV and γ-rays, and the production of fumaric acid in the submerged fermentation was assessed. The maximum concentration of fumaric acid was obtained using 0.5% corn steep liquor (CSL) as the nitrogen source. Organic nitrogen sources were shown to be more effective in fumaric acid production than inorganic nitrogen sources. Using optimum medium obtained by response surface methodology (RSM), the maximum concentration of fumaric acid achieved in flask culture was 26.2 g/L, which is fairly close to the 27.4 g/L predicted by the model. The highest concentration of fumaric acid in the stirred-tank reactor generated by the R. oryzae RUR709 mutant was 32.1 g/L and yield (0.45 g/g) and productivity (0.32 g/L/h) were highest at 4 days.     

不同pH调节剂对产琥珀酸放线杆菌NJ113发酵产丁二酸的影响

在3L发酵罐中分别采用不同的碱性物质作为pH调节剂,考察其对产琥珀酸放线杆菌Actinobacillus succinogenes NJ113厌氧发酵制备丁二酸的影响。结果表明:Ca2+、NH4+调节剂对菌体生长代谢有较大阻碍作用,丁二酸产量较低;采用含Na+调节剂,在发酵中后期菌体出现絮凝现象严重,且产丁二酸能力骤降;采用含Mg2+调节剂,整个发酵过程菌体代谢旺盛,发酵效果较佳。根据各碱性物质的调节能力以及对菌体生长代谢的影响,选择NaOH、Mg(OH)2和Na2CO3、Mg(OH)2分别作为混合碱组分调节pH,并对两组混合碱中各物质的质量比例进行优化。结果表明,以NaOH、Mg(OH)2混合,两者质量比为1:1时,发酵效果最好,丁二酸质量浓度高达到69.8g/L,质量收率74.5%。该种混合碱配比可有效替代碱式MgCO3调节pH,既达到高产丁二酸的目的,又可降低生物制备丁二酸的成本。     

Studies on the biochemistry of Penicillium charlesii. Influence of various dicarboxylic acids on galactocarolose synthesis

1. It has been shown that Penicillium charlesii continues to synthesize galactocarolose when l-malic acid, malonic acid, succinic acid, fumaric acid, maleic acid or oxaloglycollic acid is substituted for dl-tartaric acid in the Raulin-Thom nutrient medium. 2. The quantity of galactocarolose synthesized per g. of mycelia was markedly decreased by substitution of l-malic acid, malonic acid, succinic acid, fumaric acid or maleic acid for dl-tartaric acid. Substitution of oxaloglycollic acid for dl-tartaric acid did not depress the galactocarolose synthesized/g. of mycelia; however, the quantity of fungal mass formed was decreased approximately fivefold. 3. Based upon (14)C incorporation into galactocarolose, succinic acid, fumaric acid or malonic acid did not serve as direct precursors of galactose as did tartaric acid. Oxaloglycollic acid, l-malic acid and maleic acid were not tested. 4. The relative quantity of galactocarolose synthesized per g. of mycelia decreased as the concentration of diammonium dicarboxylate added to the growth medium was increased. Tartaric acid, oxaloglycollic acid, fumaric acid and malonic acid were tested. 5. The quantity of mycelia formed and the quantity of galactocarolose synthesized per g. of mycelia were greater when the growth medium contained l-tartrate than when it contained d-tartrate.     

High-level production of recombinant trypsin in transgenic rice cell culture through utilization of an alternative carbon source and recycling system

Productivity of recombinant bovine trypsin using a rice amylase 3D promoter has been studied in transgenic rice suspension culture. Alternative carbon sources were added to rice cell suspension cultures in order to improve the production of recombinant bovine trypsin. It was demonstrated that addition of alternative carbon sources such as succinic acid, fumaric acid and malic acid in the culture medium could increase the productivity of recombinant bovine trypsin 3.8–4.3-fold compared to those in the control medium without carbon sources. The highest accumulated trypsin reached 68.2 mg/L on day 5 in the culture medium with 40 mM fumaric acid.The feasibility of repeated use of the cells for recombinant trypsin production was tested in transgenic rice cell suspension culture with the culture medium containing the combination of variable sucrose concentration and 40 mM fumaric acid. Among the used combinations, the combination of 1% sucrose and 40 mM fumaric acid resulted in a yield of up to 53 mg/L five days after incubation. It also increased 31% (W/W) of dry cell weight and improved 43% of cell viability compared to that in control medium without sucrose. Based on these data, recycling of the trypsin production process with repeated 1% sucrose and 40 mM fumaric acid supplying-harvesting cycles was developed in flask scale culture. Recombinant bovine trypsin could be stably produced with a yield of up to 53–39 mg/L per cycle during five recycling cycles.     

发酵法生产丁二酸的化学合成培养基的筛选

以产琥珀酸放线杆菌Actinobacillus succinogenes NJ113 为出发菌株,针对该菌株筛选出含有关键生长因子的化学合成培养基,其关键因子为谷氨酸（Glu）、蛋氨酸（Met）和生物素（VH）和烟酸（VPP）。结合原发酵培养基中的磷酸缓冲盐成分,最终得到的化学合成培养基配方（g/L）： CH3COONa 1.36,NaCl 1.0,MgCl2 0.2,CaCl2 0.2,Na2HPO4 0.31,NaH2PO4 1.6, KH2PO4 3,NH4HCO3 1.57,Glu 0.87,Met 0.11,VH 0.010,VPP 0.025。在3 L发酵罐上进行验证实验,50 g/L初始葡萄糖发酵70 h,丁二酸的质量浓度为45.2 g/L,丁二酸收率达到90.4%。与之前的半合成培养基发酵制备丁二酸相比,丁二酸的收率提高了25.2%,副产物也有很大幅度的减少。     

Chemo-enzymatic synthesis of tripeptide RGD diamide in organic solvents

The tripeptide BzArgGlyAsp(NH(2))(2) was synthesized by a combination of chemical and enzymatic methods in this study. First of all, GlyAsp(NH(2))(2) was synthesized by a novel chemical method in three steps including chloroacetylation of L-aspartic acid, esterification of chloroacetyl L-aspartic acid and ammonolysis of chloroacetyl L-aspartic acid diethyl ester. Secondly, kinetically controlled synthesis of BzArgGlyAsp(NH(2))(2) catalyzed by trypsin in organic solvent was conducted. The optimum conditions are pH 8.0, 30 degrees C in ethanol/Tris-HCl buffer system (85:15, v/v) for 80 min in the maximum yield of 74.4%.     

产多聚唾液酸的菌种筛选及产酸条件

通过对40株大肠杆菌进行产多聚唾液酸的筛选,得到一株高产多聚唾液酸菌株C-8,对该菌的一系列培养条件进行了研究。最佳培养基为：山梨醇2.5％,硫酸铵0.5％,磷酸氢二钾90mmol／L,胰蛋白陈1.5％,硫酸镁0.04％,pH7．8。在37℃,250r／min摇床培养65h,可使菌体在每毫升培养液中产多聚唾液酸1200μg。     

Optimization of L-malic acid production by Aspergillus flavus in a stirred fermentor

Effects of various nutritional and environmental factors on the accumulation of organic acids (mainly L-malic acid) by the filamentous fungus Aspergillus flavus were studied in a 16-L stirred fermentor. Improvement of the molar yield (moles acid produced per moles glucose consumed) of L-malic acid was obtained mainly by increasing the agitation rate (to 350 rpm) and the Fe(z+) ion concentration (to 12 mg/L) and by lowering the nitrogen (to 271 mg/L) and phosphate concentrations (to 1.5 mM) in the medium. These changes resulted in molar yields for L-malic acid and total C(4) acids (L-malic, succinic, and fumaric acids) of 128 and 155%, respectively. The high molar yields obtained (above 100%) are additional evidence for the operation of part of the reductive branch of the tricarboxylic acid cycle in L-malic acid accumulation by A. flavus. The fermentation conditions developed using the above mentioned factors and 9% CaCO(3) in the medium resulted in a high concentration (113 g/L L-malic acid from 120 g/L glucose utilized) and a high overall productivity (0.59 g/L h) of L-malic acid. These changes in acid accumulation coincide with increases in the activities of NAD(+)-malate dehydrogenase, fumarase, and citrate synthase.     

Production of fuel ethanol at high temperature from sugar cane juice by a newly isolated Kluyveromyces marxianus

Kluyveromyces marxianus DMKU 3-1042, isolated by an enrichment technique in a sugar cane juice medium supplemented with 4% (w/v) ethanol at 35 degrees C, produced high concentrations of ethanol at both 40 and 45 degrees C. Ethanol production by this strain in shaking flask cultivation in sugar cane juice media at 37 degrees C was highest in a medium containing 22% total sugars, 0.05% (NH(4))(2)SO(4), 0.05% KH(2)PO(4), and 0.15% MgSO(4).7H(2)O and having a pH of 5.0; the ethanol concentration reached 8.7% (w/v), productivity 1.45 g/l/h and yield 77.5% of theoretical yield. At 40 degrees C, a maximal ethanol concentration of 6.78% (w/v), a productivity of 1.13 and a yield 60.4% of theoretical yield were obtained from the same medium, except that the pH was adjusted to 5.5. In a study on ethanol production in a 5l jar fermenter with an agitation speed of 300 rpm and an aeration rate of 0.2 vvm throughout the fermentation, K. marxianus DMKU 3-1042 yielded a final ethanol concentration of 6.43% (w/v), a productivity of 1.3g/l/h and a yield of 57.1% of theoretical yield.     

Purification of human placental alkaline phosphatase. Salt effects in affinity chromatography

Human placental alkaline phosphatase was chromatographed on Sepharose derivatives of d- and l-phenylalanine, l-leucine, glycine, aniline and p-aminobenzoic acid in high concentrations of (NH(4))(2)SO(4). Retention on these columns was greatest at the highest concentrations of (NH(4))(2)SO(4). By using decreasing concentrations and changing the types of salts, elution was effected from each of the columns. The (NH(4))(2)SO(4)-mediated retention appeared to be related to the hydrophobic character of the substituted Sepharose, rather than to any specific binding site of the enzyme. It is suggested that this provides a way of controlling hydrophobic affinity chromatography. By use of chromatography on l-phenylalanine-Sepharose and of DEAE-Sephadex chromatography in the presence of Triton X-100 detergent, a preparation of highly purified (1000-fold) human placental alkaline phosphatase was obtained in 22% yield.     

Economical succinic acid production from cane molasses by Actinobacillus succinogenes

In this work, production of succinic acid by Actinobacillus succinogenes CGMCC1593 using cane molasses as a low cost carbon source was developed. In anaerobic bottles fermentation, succinic acid concentration of 50.6+/-0.9 g l(-1) was attained at 60 h using an optimum medium containing molasses pretreated with sulfuric acid, resulting in a succinic acid yield of 79.5+/-1.1% and sugar utilization of 97.1+/-0.6%. When batch fermentation was carried out in a 5-l stirred bioreactor with pretreated molasses, 46.4 g l(-1) of succinic acid was attained at 48 h and faster cells growth was also observed. Fed batch fermentation was performed to minimize the substrate (sugar) inhibition effect, giving 55.2 g l(-1) of succinic acid and 1.15 g l(-1)h(-1) of productivity at 48 h. The present study suggests that the inexpensive cane molasses could be utilized for the economical and efficient production of succinic acid by A. succinogenes.     

主要营养成分对悬浮培养玫瑰茄细胞生长和花青素合成的影响

本文研究了培养基中碳源和氮源变化对悬浮培养玫瑰茄细胞生长和花青素合成的影响。在８种不同的碳源中,麦芽糖有利于花青素的积累,而蔗糖和葡萄糖适合细胞生长,并有较高的花青素产率。在１％～１０％蔗糖浓度范围内,４％浓度下细胞生长和花青素产率最高,而６％浓度下细胞花青素含量最高,高渗环境较有利于细胞花青素的积累。１３５ｍＭ的氮源总量已足够维持玫瑰茄细胞生长和花青素合成,氮源总量增加对细胞代谢有抑制作用。ＮＨ＋４对细胞有显著抑制作用。总量１３５ｍＭ,ＮＯ－３与ＮＨ＋４比例２５∶２和２３∶４时细胞生长和花青素合成最佳。     

A novel approach for medium formulation for growth of a microalga using motile intensity

Motile intensity of the cells, defined as the specific mean kinetic energy, was measured by image analysis and used to formulate a suitable medium for the cultivation of a motile microalga. Nitrogen source at 60 mg/L was used as the target component. The cells grown in a medium containing urea showed the highest motile intensities during cultivation when compared to the cells grown with NH(4)Cl or (NH(4))(2)SO(4) as the nitrogen source. The urea culture gave the highest biomass yield and lipid content of 1.06+/-0.12 g/L and 22.34+/-2.56%, respectively after 150 h of cultivation. These results indicated a strong dependence of motile intensity on the nitrogen source used in the growth medium. This concept, which requires only a small droplet of the sample, can find potential application in the design and optimization of culture media.     

Production of a Thermostable beta-d-Galactosidase by Alternaria alternata Grown in Whey

In the course of exploring new microbial sources of extracellular beta-d-galactosidase (EC. 3.2.1.23), Alternaria alternata was found to excrete elevated quantities of a thermostable form of the enzyme when cultivated in whey growth medium. Optimum cultural conditions for maximum enzyme production were a whey lactose concentration of 6%, supplementation of the medium with 0.050 M (NH(4))(2)SO(4), an inoculum size of 10 conidia per ml, and a cultivation time at 28 to 30 degrees C of 5 days. The fungus utilized whey lactose for the production of the enzyme most efficiently, and the observed maximum yield, 280 nanokatals of hydrolyzed o-nitrophenyl-beta-d-galactopyranoside per g of whey lactose, was comparable to maximum yields reported for certain commercial fungi. The optimum pH and temperature of the enzymatic reaction were 4.5 to 5.5 and 60 to 70 degrees C, respectively, and the enzyme lost half of its activity when heated at 65 degrees C for 84 min. These properties make the enzyme particularly suitable for processing acid and less-acid (pH 5 to 6) dairy products and by-products.     

Succinic acid production with reduced by-product formation in the fermentation of Anaerobiospirillum succiniciproducens using glycerol as a carbon source

Succinic acid was produced by fermentation of Anaerobiospirillum succiniciproducens using glycerol as a carbon source. When cells were anaerobically cultured in a medium containing 6.5 g/L glycerol, a high succinic acid yield (133%) was obtained while avoiding the formation of by-product acetic acid. The gram ratio of succinic acid to acetic acid was 25.8:1, which is 6.5 times higher than that obtained using glucose (ca. 4:1) as a carbon source. Therefore, succinic acid can be produced with much less by-product formation by using glycerol as a carbon source, which will facilitate its purification. When glucose and glycerol were cofermented with the increasing ratio of glucose to glycerol, the gram ratio of succinic acid to acetic acid and succinic acid yield decreased, suggesting that glucose enhanced acetic acid formation irrespective of the presence of glycerol. Glycerol consumption by A. succiniciproducens required unidentified nutritional components present in yeast extract. By intermittently feeding yeast extract along with glycerol, a high succinic acid yield (160%) could be obtained while still avoiding acetic acid formation. This resulted in the highest ratio of succinic acid to acetic acid (31.7:1).     

茴香酸产生菌发酵条件的优化

为提高微生物降解反式茴脑获得茴香酸的产量,对假单胞菌Pseudomonas sp.NT2的发酵参数进行优化,以提高降解过程的转化率。利用单因素试验考察碳氮源种类及浓度、反式茴脑添加量、发酵温度、接种量、初始pH以及装液量对茴香酸生成量、反式茴脑降解率的影响,通过Plackett-Burman试验和最陡爬坡试验确定影响茴香酸生成量的显著因素并获取中心点,最后采用Box-Behnken模型进行响应面优化得到最佳发酵条件并验证。结果表明氯化铵浓度、初始pH和装液量是显著影响因素,最佳发酵条件为:柠檬酸钠10 g/L,氯化铵1.26 g/L,反式茴脑添加量1%,发酵温度30℃,接种量4%,初始pH 7.9,装液量42 mL/250 mL。优化后茴香酸生成量为7.24 g/L,为优化前的3.5倍,茴香酸摩尔生成率为80.72%,反式茴脑降解率为89.81%,分别比优化前提高了270.28%和97.78%。综上,假单胞菌NT2是生物转化生产茴香酸的潜力菌株。响应面优化可以显著提高反式茴脑的降解率和茴香酸产量,这为大规模生产茴香酸奠定了基础。