Production of vanillic acid from vanillin by resting cells of Serratia marcescens

Resting-cell suspensions of Serratia marcescens were able to convert, quantitatively, 0.3% vanillin to vanillic acid. The vanillic acid-producing activity reached a maximum after 28 h of incubation with 0.01% vanillin as an inducer.     

Oxidation of vanillin by Serratia marcescens

A Serratia marcescens strain quantitatively converted vanillin (0·1%, w/v) to vanillic acid, which exerted an inhibitory effect on bacterial growth. Vanillic acid producing activity was found in cell-free extracts of cultures grown in media with and without vanillin, when glucose was the substrate.     

粘质沙雷氏菌发酵生产D-乳酸的研究

本文对粘质沙雷氏菌发酵生产D-乳酸进行了研究。以粘质沙雷氏菌G1(Serratia marcescens G1)为出发菌种,摇瓶试验确定了发酵培养方式:前12 h为菌体生长阶段,有氧培养,温度28℃,pH值7.0;后36 h为D-乳酸合成积累阶段,无氧培养,温度44℃,pH值6.0。且发现使用葡萄糖为碳源时更有利于D-乳酸的合成积累。采用缺失2,3-丁二醇合成能力的基因工程菌株R1为出发株,经筛选后得到耐受较高浓度乳酸盐的菌株R150,以R150为发酵菌种,在3.7 L发酵罐上采用两阶段发酵法,并通过增加起始菌体浓度的方法,发酵生成的D-乳酸浓度达到83.5 g/L,光学纯度达到98.9%。本研究成果为使用粘质沙雷氏菌发酵生产D-乳酸的深入研究打下了基础。     

Whole-cell bioconversion of vanillin to vanillic acid by Streptomyces viridosporus.

A two-step batch fermentation-bioconversion of vanillin (4-hydroxy-3-methoxybenzaldehyde) to vanillic acid (4-hydroxy-3-methoxybenzoic acid) was developed, utilizing whole cells of Streptomyces viridosporus T7A. In the first step, cells were grown in a yeast extract-vanillin medium under conditions where cells produced an aromatic aldehyde oxidase. In the second step, vanillin was incubated with the active cells and was quantitatively oxidized to vanillic acid which accumulated in the growth medium. Vanillic acid was readily recovered from the spent medium by a combination of acid precipitation and ether extraction at greater than or equal to 96% molar yield and upon recrystallization from glacial acetic acid was obtained in greater than or equal to 99% purity.     

Hemolysis of phosphatidylcholine-containing erythrocytes by serratamic acid from Serratia marcescens.

1. The hemolysis by serratamic acid, "N-(D-3-hydroxydecanoyl)-L-serine and N-(D-3-hydroxydodecanoyl)-L-serine", was investigated with human and animal erythrocytes using serratamic acid-containing liposomes. 2. The hemolytic activity was found to depend on the incubation temperature and the concentration of the liposomes. 3. The concentration of serratamic acid for 50% hemolysis was 0.17 mM at 37 degrees C for 0.2% human erythrocyte suspension in the liposomes which composed of phosphatidylserine, cholesteryl nervonate and serratamic acid (1:0.50:0.37 by mol). 4. The hemolysis was shown specifically in human, horse and rabbit erythrocytes containing phosphatidylcholine, but not in sheep or bovine erythrocytes lacking phosphatidylcholine. 5. The hemolytic activity was strongly inhibited by the exogenous addition of phosphatidylcholine. It was suggested that the hemolysis by serratamic acid-containing liposomes was specific for phosphatidylcholine-containing erythrocyte membranes.     

Whole-cell bioconversion of vanillin to vanillic acid by Streptomyces viridosporus

A two-step batch fermentation-bioconversion of vanillin (4-hydroxy-3-methoxybenzaldehyde) to vanillic acid (4-hydroxy-3-methoxybenzoic acid) was developed, utilizing whole cells of Streptomyces viridosporus T7A. In the first step, cells were grown in a yeast extract-vanillin medium under conditions where cells produced an aromatic aldehyde oxidase. In the second step, vanillin was incubated with the active cells and was quantitatively oxidized to vanillic acid which accumulated in the growth medium. Vanillic acid was readily recovered from the spent medium by a combination of acid precipitation and ether extraction at greater than or equal to 96% molar yield and upon recrystallization from glacial acetic acid was obtained in greater than or equal to 99% purity.     

微生物转化方法生产香草酸与香草醛的初步研究

从实验室保藏的菌种中筛选到一株黑曲霉（Aspergillus niger）SW-33,能够将1g/L的阿魏酸底物转化为0.23g/L的香草酸,相应的摩尔转化率为29.35％;流加四次底物阿魏酸后,产物浓度达到1.11g/L,相应的摩尔转化率为44.9％。为了提高产物浓度,对培养基和发酵条件进行优化,使得该菌株能够将1g/l的阿魏酸底物转化为0.46g/L的香草酸,相应的摩尔转化率为57.81％。提取得到的香草酸,经HPLC测定,纯度为85.9％;提取收率为75.2％。用含香草酸的转化液,或者用提取的结晶香草酸,加入朱红密孔菌（Prcnporus cinnabarnus）SW-0203发酵培养液,可得到转化产物香草醛。     

beta-N-acetylhexosaminidases from Serratia marcescens.

Two forms of beta-N-acetylhexosaminidase from Serratia marcescens with an optimum pH of 5.0 and 6.5, respectively, to 4-methylumbelliferyl-2-acetamido-2-deoxy-beta-D-glucopyranoside were separated by DEAE-cellulose chromatography and Sephacryl S-200 chromatography. On the basis of their molecular weights, thermal stability, substrate specificity and isoelectric points, the form with an acidic pH optimum resembled hexosaminidase B, whereas the form with a neutral pH optimum resembled hexosaminidase C. Lectin binding studies showed that the acidic form does not bind to concanavalin-A-Sepharose, Tetragonolobus purpurea-agarose, wheat germ-agglutinin-Sepharose or Ricinus communis-agglutinin-agarose, whereas the neutral form binds to the last two lectin columns.     

Production of 2-Ketogluconic Acid by Serratia marcescens

Production of 2-ketogluconic acid from glucose by fermentation with Serratia marcescens NRRL B-486 was studied in 20-liter stainless-steel fermentors. Conditions for 2-ketogluconic acid production included the following: glucose-salt medium, aeration rate of 0.75 volumes per volume per minute, agitation rate of 400 rev/min, temperature of 30 C, CaCO₃ to neutralize the acid formed, and a 5% (v/v) inoculum. Foaming was controlled with an antifoam agent added at intervals during the fermentation. When 120 g per liter of glucose were supplied, 95 to 100% yields of 2-ketogluconic acid were obtained in 16 hr. Larger amounts of glucose could be used in the fermentation provided that the carbohydrate was fed continuously. Continuous feeding of glucose to a total amount of 180 g per liter gave 95 to 100% yields of 2-ketogluconic acid in 24 hr; feeding glucose to a total amount of 240 g per liter gave 85 to 90% yields in 32 to 40 hr.     

Threonine degradation by Serratia marcescens.

The wild strain of Serratia marcescens rapidly degraded threonine and formed aminoacetone in a medium containing glucose and urea. Extracts of this strain showed high threonine dehydrogenase and "biosynthetic" threonine deaminase activities, but no threonine aldolase activity. Threonine dehydrogenase-deficient strain Mu-910 was selected among mutants unable to grow on threonine as the carbon source. This strain did not form aminoacetone from threonine, but it slowly degraded threonine. Strain D-60, deficient in both threonine dehydrogenase and threonine deaminase, was derived from strain Mu-910 and barely degraded threonine. A glycine-requiring strain derived from the wild strain grew in minimal medium containing threonine as the glycine source, whereas a glycine-requiring strain derived from strain Mu-910 did not grow. This indicates that threonine dehydrogenase participates in glycine formation from threonine (via alpha-amino-beta-ketobutyrate) as well as in threonine degradation to aminoacetone.     

Production of active Serratia marcescens metalloprotease from Escherichia coli by alpha-hemolysin HlyB and HlyD.

Serratia marcescens produces an abundant extracellular metalloprotease. The gene for this protease had previously been cloned and expressed in Escherichia coli, in which no functional protease could be found. However, the protease gene carries the LXGGXGND repeat motif found in alpha-hemolysin and other proteins secreted by homologous systems. Using a dual-plasmid complementation system, we show that the alpha-hemolysin hlyB and hlyD transport determinants are sufficient to allow secretion and activation of a functional metalloprotease species from E. coli, as are the comparable protease secretion functions of Erwinia chrysanthemi. However, strains expressing protease with the hlyBD transport system are unstable and rapidly lose the ability to produce functional protease.     

Epidemiological Differentiation of Serratia marcescens: Typing by Bacteriocin Production

A new method for comparing and differentiating strains of S. marcescens is described which has proved useful in determining the epidemiology of hospital infections. Strains were grown in Trypticase soy broth, and bacteriocin production was induced with mitomycin C for 5 hr. The bacteriocin lysates were then spotted onto nine standard indicator strains, which were chosen with the aid of computer analysis from the 118 indicators tested. After 24 hr at 37 C, zones of inhibition due to bacteriocins were recorded. One hundred twentynine strains were differentiated into 72 different bacteriocin production patterns, but 11 strains were nontypable. None of the 45 other strains of Enterobacteriaceae produced bacteriocins. Bacteriocin production was a stable epidemiological marker. Colonial mutants always had identical patterns, as did the same strain which has passed from patient to patient through cross-infection. The new technique does not require any specialized equipment and can be used in laboratories with limited budgets. The applications of the new method in cross-infection studies and as a supplement to serological typing are discussed.     

Mass balance modeling of vanillin production from vanillic acid by cultures of the fungus Pycnoporus cinnabarinus in bioreactors.

A systematic two-step procedure for the structural identification of bioprocesses is followed in order to establish a mechanistic model for vanillin production by Pycnoporus cinnabarinus. The first step is devoted to the identification of the underlying reaction structure and the development of a validated mass balance model for the growth of P. cinnabarinus and the biotransformation of vanillic acid into vanillin. The second step is devoted to the kinetic modeling, namely, the estimation of the reaction rates and the calibration of the kinetic parameters. The whole procedure leads to the final set up of a simulation model of the process. The results are supported by the data from five cultures of P. cinnabarinus in bioreactors.     

Production of Tumor-Inhibitory L-Asparaginase by Submerged Growth of Serratia marcescens

Production of a tumor-inhibitory asparaginase by submerged fermentation with Serratia marcescens ATCC 60 was studied to ascertain optimal nutritional conditions for large-scale production leading to enzyme purification studies. Five strains of S. marcescens were screened in shake-flask studies and were found to produce 0.8 to 3.7 IU/ml 48 hr after inoculation. The requirements for asparaginase production with S. marcescens ATCC 60, the high producing strain, included the following: 4% autolyzed yeast extract medium (initial pH 5.0), an incubation temperature of 26 C, and limited aeration for a zero level of dissolved oxygen during the fermentation. Addition of various carbohydrates to the fermentation medium did not enhance yields. The peak cell population in the fermentation medium and the maximal asparaginase yields occurred simultaneously. Highest enzyme yields were found when the pH of the fermentation cycle rose to approximately 8.5. Yields of 4 IU of asparaginase/ml of cell suspension have been obtained consistently in 40 to 42 hr from 10-liter volumes (500 ml/4-liter bottle) produced on a reciprocating shaker. Scale-up to a 60-liter fermentor yielded 3.1 IU/ml in 35 hr.     

粘质沙雷氏菌产灵菌红素培养基的筛选

目的：确定菌株S418产生灵菌红素的最优培养基配方及其的分类地位。方法：以花生粉为基础培养基,通过单因素试验和四因素三水平正交试验筛选出了菌株S418产灵菌红素的最佳培养基配方;根据该菌株的16S rRNA基因序列系统发育树分析初步确定了菌株S418的分类地位。结果：培养基最优配方为：花生粉2%,花生油0.5%,L-脯氨酸1%,硫酸镁0.025%。在28℃、pH7.5、250r/min振荡培养24h,灵菌红素产量达67.92mg/L。菌株S418初步鉴定为粘质沙雷氏菌（Serratia marcescensS418）。结论：花生粉培养基是一种适合粘质沙雷氏菌产灵菌红素的优良培养基。