直接利用糖质原料生产L-苹果酸菌种的选育

从土壤中筛选到一株产L－苹果酸的黄曲霉菌,经紫外线、亚硝基胍（NTG）、硫酸二乙酯（DES）和^60Co辐射等诱变处理,并经多次分离得到一株性能稳定的高产L－苹果酸突变株黄曲霉HA5800,35℃,200r/min摇瓶发酵120h,产L－苹果酸72g/L、糖酸转化率为74．22％,经山东省卫生防疫站检定,该菌株不产黄曲霉素素B1。     

Efficient lipid production with Trichosporon fermentans and its use for biodiesel preparation

Effects of medium components and culture conditions on biomass and lipid production of Trichosporon fermentans were studied. The optimal nitrogen source, carbon source and C/N molar ratio were peptone, glucose and 163, respectively. The favorable initial pH of the medium and temperature were 6.5 and 25 degrees C. Under the optimized conditions, a biomass of 28.1 g/l and a lipid content of 62.4% could be achieved after culture for 7 days, which were much higher than the original values (19.4 g/l and 50.8%) and the results reported by other groups. T. fermentans could grow well in pretreated waste molasses and a lipid yield of 12.8 g/l could be achieved with waste molasses of 15% total sugar concentration (w/v) at pH 6.0, representing the best result with oleaginous microorganisms on agro-industrial residues. Addition of various sugars to the pretreated molasses could efficiently enhance the accumulation of lipid and the lipid content reached as high as above 50%. Similar to vegetable oils, the lipid mainly contains palmitic acid, stearic acid, oleic acid and linoleic acid and the unsaturated fatty acids amount to about 64% of the total fatty acids. The microbial oil with an acid value of 5.6 mg KOH/g was transesterified to biodiesel by base catalysis after removal of free fatty acids and a high methyl ester yield of 92% was obtained.     

产L-苹果酸重组大肠杆菌的构建

基于产琥珀酸重组大肠杆菌E.coli B0013-1050的琥珀酸合成途径,利用Red同源重组技术结合Xer/dif重组系统敲除富马酸酶基因fumB、fumC,苹果酸酶基因maeB,构建L-苹果酸合成途径,最终得到重组大肠杆菌E.coli2030,该菌株在15 L发酵罐中,产L-苹果酸12.5 g/L,葡萄糖-苹果酸转化率为52.1%,同时对发酵产物中主要杂酸丙酮酸和琥珀酸的生产原因进行了初步的探讨与分析。为进一步提高L-苹果酸的转化率,整合表达来源于黄曲霉的苹果酸脱氢酶基因,构建重组菌E.coli 2040,在15 L发酵罐中产L-苹果酸14 g/L,葡萄糖-苹果酸转化率提高到60.3%。     

Glucose degradation, molar growth yields, and evidence for oxidative phosphorylation in Streptococcus agalactiae

In a complex medium with the energy source as the limiting nutrient factor and under anaerobic growth conditions, Streptococcus agalactiae fermented 75% of the glucose to lactic acid and the remainder to acetic and formic acids and ethanol. By using the adenosine triphosphate (ATP) yield constant of 10.5, the molar growth yield suggested 2 moles of ATP per mole of glucose from substrate level phosphorylation. Under similar growth conditions, pyruvate was fermented 25% to lactic acid, and the remainder was fermented to acetic and formic acids. The molar growth yield suggested 0.75 mole of ATP per mole of pyruvate from substrate level phosphorylation. Under aerobic growth conditions about 1 mole of oxygen was consumed per mole of glucose; about one-third of the glucose was converted to lactic acid and the remainder to acetic acid, acetoin, and carbon dioxide. Molar growth yields indicated 5 moles of ATP per mole of glucose. Estimates based on products of glucose degradation suggested that about one-half of the ATP was derived from substrate level phosphorylation and one-half from oxidative phosphorylation. Addition of 0.5 m 2,4-dinitrophenol reduced the growth yield to that occurring in the absence of oxygen. Aerobic pyruvate degradation resulted in 30% of the substrate becoming reduced to lactic acid and the remainder being converted to acetic acid and carbon dioxide, with small amounts of formic acid and acetoin. The molar growth yields and products found suggested that 0.70 mole of ATP per mole of pyruvate resulted from substrate level phosphorylation and 0.4 mole per mole of pyruvate resulted from oxidative phosphorylation.     

寄生曲霉CICC40365利用木糖产L-苹果酸的发酵条件优化

【目的】为提高L-苹果酸产量及木糖利用率,以寄生曲霉(Aspergillus parasiticus CICC40365)为菌种,木糖为碳源,对其发酵工艺及木糖代谢途径进行初步研究。【方法】采用单因素试验和响应曲面法(Box-Behnken设计)对培养基和发酵条件进行优化。【结果】获得最佳培养基配方为:木糖100.0 g/L、硫酸铵2.0 g/L、酵母浸粉3.0 g/L、硫酸镁0.20 g/L、硫酸锰0.15 g/L、硫酸亚铁0.08 g/L、碳酸钙80.00 g/L,L-苹果酸的产量为53.58 g/L,较优化前提高40.5%。发酵条件较好组合为:接种量为8%(体积比)、摇瓶装液量60 mL/250 mL、发酵温度32°C、摇床转速170 r/min、发酵周期8 d,L-苹果酸的产量为55.47 g/L。Mg2+、Mn2+对木糖代谢中相关酶的影响研究结果表明,木酮糖激酶在该菌株代谢木糖过程中起着重要作用。【结论】寄生曲霉CICC40365能够较好地利用木糖发酵产L-苹果酸,其产量及木糖的利用效率均得到提高。     

Histidine decarboxylase production by Lactobacillus hilgardii: Effect of organic acids

Histidine decarboxylase production from Lactobacillus hilgardii 5w, isolated from wine, was inhibited by the presence of l-malic acid in the basal culture medium. The inhibition was related to l-malic acid concentration. The maximal production of the enzyme at 12 h of culture incubated at 30°C was inhibited 71% by 2 g/L l-malic acid and 47% by 0.5 g/L. In these conditions l-malic acid consumption was 16% and 20% respectively. The addition of 300 mg/L citric acid to the basal medium stimulated the enzyme production from 9 to 45 nmoles/min/mg dry weight, and the increase was correlated with citric acid concentration. When different concentrations of l-malic acid were added to the basal medium plus 200 mg/L citric acid, reversion of stimulation was observed, achieving the maximum at a concentration of 2 g/L. In this case, citric acid comsumption was not modified, whereas L-malic acid utilization was higher.     

出芽短梗霉产聚苹果酸发酵条件的优化

【背景】出芽短梗霉可发酵葡萄糖生成聚苹果酸,但存在转化率和转化效率低等瓶颈,阻碍其实现商业化生产。【目的】通过优化发酵培养条件,提高出芽短梗霉的聚苹果酸产量、糖酸转化率和生产强度。【方法】采用单因素试验优化适宜出芽短梗霉BK-10菌株产生聚苹果酸的培养条件,通过Plackett-Burman法对培养基组分筛选显著性影响因素,并对其培养基中无机盐进行正交试验优化,最后进行5 L发酵罐验证。【结果】最优培养基配方和培养条件:100 g/L葡萄糖,1.5 g/L尿素,0.20 g/L KH_2PO_4,0.20 g/L ZnSO_4,0.05 g/L MgSO_4,0.75 g/L KCl,30 g/L CaCO_3,0.01%吐温-80,发酵温度26°C,250 mL摇瓶装液量50 mL。【结论】通过优化,聚苹果酸的糖酸转化率达到0.71 g/g,生产强度达到0.89 g/(L·h),较优化前分别提高了18.33%和71.15%,为发酵葡萄糖合成聚苹果酸进而生产L-苹果酸工艺的工业化生产奠定经济性基础。     

In vitro production of gymnemic acid from cell suspension cultures of Gymnema sylvestre R. Br

Gymnema sylvestre is an important medicinal plant that bears bioactive compound namely gymnemic acids. The present work deals with the optimization of a cell suspension culture system of Gymnema sylvestre for the production of biomass and gymnemic acid, which has anti‐diabetic properties. We investigated the effect of inoculum densities (2.5–20.0 g/L), the strength of the Murashige and Skoog (MS) medium (0.25–2.0), carbon source (sucrose, glucose, fructose, maltose), and the concentration of the sucrose (1–8% w/v) to determine their effects on biomass accumulation and production of gymnemic acid. Overall, 10 g/L of inoculum density, full‐strength MS medium supplemented with 2,4‐dichlorophenoxy acetic acid (2.0 mg/L) and Kinetin (0.1 mg/L), and 3% w/v sucrose was found best for the accumulation of biomass and gymnemic acid content (9.95 mg/g dry weight). The results of the current study will be useful for bioprocess and biochemical engineers for large‐scale production of gymnemic acid in cell culture.     

Effects of nitrogen concentration and media replacement on cell growth and lipid production of oleaginous marine microalga Nannochloropsis oceanica DUT01

Cell growth and lipid production of a marine microalga Nannochloropsis oceanica DUT01 were investigated, and fresh medium replacement with different ratios to promote long term cell growth and lipid accumulation was also tested. The highest lipid content reached 64% in nitrogen deplete f/2 medium containing 37.5 mg/L NaNO₃ combined with 1/5 fresh medium replacement, however, the highest lipid titer (0.6 g/L) and lipid productivity (31 mg/L/d) were achieved using BG11 medium containing 1.5 g/L NaNO₃, taking advantage of 1/5 fresh medium replacement as well, which corresponded to the maximum biomass production of 1.4 g/L, highlighting the importance of high biomass accumulation for efficient lipid production. When biomass compositions were monitored throughout the culture, decreased protein content was found to be coupled with increased lipid production, whereas relatively stable carbohydrate content was observed. The fatty acids in the lipid of N. oceanica DUT01 comprise over 65% saturated fatty acids and monounsaturated acids (i.e. palmitic acid (C16:0) and oleic acid (C18:1)), suggesting that N. oceanica DUT01 is a promising candidate for biodiesel production. Interestingly, very high content of hexadecadienoic acid (C16:2, about 26–33%) was produced by DUT01, which distinguished this microalga with other microalgae strains reported so far.     

Oenococcusoeni苹果酸-乳酸酶基因克隆及其在酿酒酵母中的表达

苹果酸-乳酸酶是苹果酸-乳酸发酵过程中负责苹果酸转化为乳酸的功能酶。在进行酒酒球菌SD2a的苹果酸-乳酸酶基因(mleA)克隆测序基础上,以PGK1强启动子和ADH1终止子为调控元件,以大肠杆菌-酵母菌穿梭质粒YEp352为载体,构建了重组表达质粒并转化酿酒酵母YS58。酵母转化子用SD/Ura平板筛选鉴定。斑点杂交检测表明目的基因mleA转化到受体菌中,SDSPAGE检测表明获得的转化子表达了约60kDa的目标蛋白。获得的转化子在添加了L苹果酸的培养基中培养4d;取培养液上清用HPLC检测L苹果酸及L乳酸含量,采用t检验进行差异显著性分析,结果表明mleA基因进行了功能性的表达,将L苹果酸转化成L乳酸,L苹果酸和L乳酸含量分别与对照差异极显著和显著,苹果酸的相对降低率平均为20.95%。在有选择压力条件下,重组质粒相对稳定,而在无选择压力条件下,传代培养10d后大约有65%的重组质粒丢失。     

温特曲霉转富马酸为L-苹果酸的初步研究*

从大量霉菌中选育到一株具有较高富马酸酶活性的温特曲霉(Aspergillus wentii) A5-61。在摇瓶培养条件下,32℃ 96小时,产L-苹果酸达10.49g/100ml,对富马酸的转化率达90.80%。利用菌体细胞,进行酶转化试验,结果表明：1.6g湿菌体接入25ml含富马酸10.0%（用NaOH中和至pH7.0）的转化液中,35℃16～24小时,连续转化三次,分别产生L—苹果酸9.61g/100ml、9.73g/100ml、6.93g/100ml。对菌体整体细胞酶学性质的研究表明,其最适反应温度35℃,最适反应pH7.0,Cu2＋对该酶有明显的抑制作用,该酶的Km＝0.154mol/L,Vmax＝0.0571mol/L·h。     

Characterization of Schizosaccharomyces pombe malate permease by expression in Saccharomyces cerevisiae

In Saccharomyces cerevisiae, L-malic acid transport is not carrier mediated and is limited to slow, simple diffusion of the undissociated acid. Expression in S. cerevisiae of the MAE1 gene, encoding Schizosaccharomyces pombe malate permease, markedly increased L-malic acid uptake in this yeast. In this strain, at pH 3.5 (encountered in industrial processes), L-malic acid uptake involves Mae1p-mediated transport of the monoanionic form of the acid (apparent kinetic parameters: Vmax = 8.7 nmol/mg/min; Km = 1.6 mM) and some simple diffusion of the undissociated L-malic acid (Kd = 0.057 min(-1)). As total L-malic acid transport involved only low levels of diffusion, the Mae1p permease was further characterized in the recombinant strain. L-Malic acid transport was reversible and accumulative and depended on both the transmembrane gradient of the monoanionic acid form and the DeltapH component of the proton motive force. Dicarboxylic acids with stearic occupation closely related to L-malic acid, such as maleic, oxaloacetic, malonic, succinic and fumaric acids, inhibited L-malic acid uptake, suggesting that these compounds use the same carrier. We found that increasing external pH directly inhibited malate uptake, resulting in a lower initial rate of uptake and a lower level of substrate accumulation. In S. pombe, proton movements, as shown by internal acidification, accompanied malate uptake, consistent with the proton/dicarboxylate mechanism previously proposed. Surprisingly, no proton fluxes were observed during Mae1p-mediated L-malic acid import in S. cerevisiae, and intracellular pH remained constant. This suggests that, in S. cerevisiae, either there is a proton counterflow or the Mae1p permease functions differently from a proton/dicarboxylate symport.     

Glycogen metabolism in human hormone-producing trophoblastic cells in continuous culture

Summary Glycogen metabolism was studied in human hormone-producing trophoblastic cells (BeWo line). Cells supplemented daily with high glucose (3 g per liter in medium) contained 5.5% glycogen and utilized glucose at an initial rate of 12.2 mμmoles per min per mg of protein. In cells supplemented daily with low glucose (1 g per liter), the initial rate of glucose consumption was 23 mμmoles per min per mg of protein and the glycogen content reached only 0.4% of wet weight 24 hr after medium replenishment. When glycogen-depleted cultures were refed glucose, an accumulation of glycogen was observed, with initial deposition occurring in areas near the cell surface. After exhaustion of extracellular glucose, cytoplasmic glycogen was utilized at a rate of 2.8 mμmoles per min per mg of protein. Addition of either low or high glucose to glycogen-depleted cells resulted in the same rate of glycogen synthesis (approximately 8 mμmoles per min per mg of protein). It was suggested that unique regulatory mechanisms function in the control of glycogen metabolism in glycoprotein hormone-producing cytotrophoblastic cells. This work was supported in part by Public Health Service Research Contract PH43-68-1010, Research Grant CA 05524 from the National Cancer Institute, and by grants from the Milwaukee Division of the American Cancer Society, Inc., and the Damon Runyon Memorial Fund for Cancer Research, Inc.     

Organic acid metabolism under different glucose concentrations of Leuconostoc oenos from wine

Leuconostoc oenos M isolated from wine did not grow in the absence of glucose and it was clearly stimulated by the presence of L-malic and citric acids in synthetic medium with different glucose concentrations. In basal medium, D-glucose and L-malic and citric acids were simultaneously consumed. L-Malic acid was metabolized at a higher rate than glucose and citric acid. When the organic acids were completely consumed only 50% of the glucose was utilized. In basal medium 1 mmol of D-lactic acid was produced per mmol of glucose consumed and the amount of ethanol formed was higher with acetate present in the medium. L-Malic acid was completely recovered as L-lactic acid, and in the presence of L-malic acid a carbon imbalance from glucose to D-lactic acid was observed. In the presence of citric acid the amount of D-lactic acid formed was directly proportional to glucose-citrate utilization and acetic acid and ethanol were produced.     

培养条件对头孢霉脂肪酸链长和ω-3脱饱和的影响

为了获得高产量的长链ω-3多不饱和脂肪酸,用十八碳脂肪酸和十六碳脂肪酸的比值考察碳链延长,用α-亚麻酸和亚油酸的比值考察ω-3脱饱和;探讨了八种因子对脂肪酸链长和ω-3脱饱和的影响。有利于碳链延长的条件为：麦芽糖10g/L、(NH4)2SO4 3g/L、起始pH为4.0、500mL三角瓶装50mL培养基、接种20%（V/V）、20℃培养6d。有利于ω-3脂肪酸生成的条件为：蔗糖30g/L、NH4Cl 3g/L、培养基起始pH为4.0、500mL三角瓶装50mL培养基、接种20%（V/V）、10℃培养10d。     

培养条件对头孢霉脂肪酸链长和ω-3脱饱和的影响*

为了获得高产量的长链ω-3多不饱和脂肪酸,用十八碳脂肪酸和十六碳脂肪酸的比值考察碳链延长,用α-亚麻酸和亚油酸的比值考察ω-3脱饱和;探讨了八种因子对脂肪酸链长和ω-3脱饱和的影响。有利于碳链延长的条件为：麦芽糖10g/L、(NH4)2SO4 3g/L、起始pH为4.0、500mL三角瓶装50mL培养基、接种20%（V/V）、20℃培养6d。有利于ω-3脂肪酸生成的条件为：蔗糖30g/L、NH4Cl 3g/L、培养基起始pH为4.0、500mL三角瓶装50mL培养基、接种20%（V/V）、10℃培养10d。     

Effect of amino acid supplement on cell yield and gene product in Escherichia coli harboring plasmid

Escherichia coli harboring a recombinant plasmid was cultivated in fed-batch culture to enhance production of a gene product. Expression of the leucine gene from Thermus thermophilus in the recombinant plasmid was examined by the assay of beta-isopropylmalate dehydrogenase activity at 75 degrees C. When E. coli was cultivated in medium without leucine, biomass concentration reached 15 g/L and the specific activity became 0.082 U/mg protein. When leucine was fed in the medium throughout cultivation, although biomass concentration reached 63 g/L, the specific activity decreased to 0.016 U/mg protein. When E. coli was cultivated in medium containing 1 g leucine/L, the specific activity remained virtually constant (about 0.13 U/mg protein) and biomass concentration reached 32 g dry cells/L. In these cultivations, growth yields of several amino acids and glucose were examined. When leucine was not added to the medium, growth yields except for histidine were lowest. When leucine was fed throughout the cultivation, growth yields of glucose and tryptophan were highest. The pH-stat was useful for feeding amino acids.     

Enzymatic synthesis of isoamyl acetate using immobilized lipase from Rhizomucor miehei

The effects of important reaction parameters for enhancing isoamyl acetate formation through lipase-catalyzed esterification of isoamyl alcohol were investigated in this study. Increase in substrate (acid) concentration led to decrease in conversions. A critical enzyme concentration of 3 g l(-1) was detected for a substrate concentration of 0.06 M (each of alcohol and acid). Solvents with partition coefficient higher than 1000 (log P>3.0) supported enzyme activity to give high conversions. Acetic acid at higher concentrations could not be esterified easily probably owing to its role in lowering the microaqueous pH of the enzyme. Extraneous water/buffer addition decreased the isoamyl acetate yields slightly ( approximately 10%) at 0.005-0.01% v/v of the reaction mixture and drastically (>40%) at above 0.01% v/v. Buffer saturation of the organic solvent employed improved esterification (upto two-fold), particularly at moderately higher substrate concentrations (>0.18 M). Employing acetic anhydride instead of acetic acid resulted in a two-fold increase in the yields (at 0.25 M substrate). Use of excess nucleophile (alcohol) concentration by increasing the alcohol/acid molar ratio resulted in higher conversions in shorter duration (upto eight-fold even at 1.5 M acetic acid). Yields above 80% were achieved with substrate concentrations as high as 1.5 M and more than 150 g l(-1) isoamyl acetate concentrations were obtained employing a relatively low enzyme concentration of 10 g l(-1). The operational stability of lipase was also observed to be reasonably high enabling ten reuses of the biocatalyst.     

忽地笑愈伤组织培养条件对加兰他敏合成的影响

研究了忽地笑次生代谢产物加兰他敏的合成以及各种理化因子对加兰他敏合成的影响。结果表明,蔗糖是忽地笑愈伤组织培养的最佳碳源,而且在90 g/L浓度培养下加兰他敏含量最高,达到0.068%;附加500 mg/L苯丙氨酸前体物也可提高加兰他敏产量。酪氨酸和水杨酸不利于加兰他敏的积累。此外,2,4-D和浓度高于0.5 mg/L的NAA、IBA抑制加兰他敏的合成,但高浓度的6-BA却对加兰他敏的合成起促进作用。     

Comparative metabolic profiling-based improvement of rapamycin production by Streptomyces hygroscopicus

Rapamycin is a clinically important macrocyclic polyketide with immunosuppressive activity produced by Streptomyces hygroscopicus. To rationally guide the improvement of rapamycin production, comparative metabolic profiling analysis was performed in this work to investigate the intracellular metabolic changes in S. hygroscopicus U1-6E7 fermentation in medium M1 and derived medium M2. A correlation between the metabolic profiles and rapamycin accumulation was revealed by partial least-squares to latent structures analysis, and 16 key metabolites that most contributed to the metabolism differences and rapamycin production were identified. Most of these metabolites were involved in tricarboxylic acid cycle, fatty acids, and shikimic acid and amino acids metabolism. Based on the analysis of key metabolites changes in the above pathways, corresponding exogenous addition strategies were proposed as follows: 1.0 g/L methyl oleate was added at 0 h; 1.0 g/L lysine was added at 12 h; 0.5 g/L shikimic acid was added at 24 h; 0.5 g/L sodium succinate, 0.1 g/L phenylalanine, 0.1 g/L tryptophan, and 0.1 g/L tyrosine were added at 36 h, successively, and a redesigned fermentation medium (M3) was obtained finally on the basis of M2. The production of rapamycin in M3 was increased by 56.6 % compared with it in M2, reaching 307 mg/L at the end of fermentation (120 h). These results demonstrated that metabolic profiling analysis was a successful method applied in the rational guidance of the production improvement of rapamycin, as well as other industrially or clinically important compounds.