黄曲霉发酵薯干粉水解液生产L—苹果酸

经选育和诱变得到一株产苹果酸的黄曲霉菌ＴＨ５００７,通过发酵条件的优化,以薯干粉的水解波为主要原料,发酵５ｄＬ－苹果酸可达到６％左右。在总酸中苹果酸含量平均达７２％以上,杂有机酸主要是柠檬酸,延胡索酸的含量在０．０２％以下。补糖发酵比分批发酸产酸性能更佳。     

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%。     

巴氏醋杆菌高酸度醋发酵过程的能量代谢分析

【目的】初步分析了Acetobacter pasteurianus CICIM B7003-02在醋酸发酵过程中的能量代谢状况, 通过强化细胞能量代谢水平以提升菌株高酸发酵的产酸强度。【方法】探明A. pasteurianus CICIM B7003-02在高酸度醋发酵的不同阶段中三羧酸循环底物含量、乙醇呼吸链酶活及能量代谢酶基因的转录水平等代谢特点, 分析用于醋酸发酵的产能代谢途径及其作用。【结果】发现A. pasteurianus CICIM B7003-02在醋酸发酵初期, 主要通过苹果酸/琥珀酸回补偶联有氧呼吸途径产能。进入醋酸快速积累阶段, 乙醇呼吸链为主要供能代谢途径。发酵后期苹果酸/琥珀酸回补途径配合乙醇呼吸链供能。基于上述研究, 采取添加琥珀酸和苹果酸强化细胞产能, 促进高酸度醋发酵强度。【结论】能量供给影响醋杆菌耐酸能力和醋酸生产能力。确定乙醇呼吸链为醋酸发酵的主要供能系统。强化细胞产能手段可达到提高醋酸发酵强度的目的。     

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。     

L—苹果酸产生菌筛选及高产突变株诱变选育

通过广泛收集和分离,获得根霉属、曲霉属及裂褶菌属等属菌侏８９７侏。产酸指示平板上的变色圈测定结果表明,它们中间６２８株为产酸菌。通过纸层析对产酸菌发酵液酸谱的分析,获得１２９株Ｌ－苹果酸产生菌,经进一步测定发酵液中Ｌ－苹果酸的含量,筛选出以葡萄糖为原料,摇瓶发酵１４０小时,Ｌ－苹果酸产率４８．３７ｇ／Ｌ,对糖转化率４８．３７×１０＾－２的菌株ＬＭ０２。经初步鉴定,这一菌株为曲霉。以ＬＭ０２作为出发     

出芽短梗霉菌株CBS591．75和DSM2404发酵生产聚苹果酸的研究

研究了出芽短梗霉蕾株CBS591.75和DSM2404在2L发酵罐中发酵生产聚苹果酸的过程。并以CBS591．75为菌种进行了20L规模的初步放大试验。结果表明,发酵过程可以分为3个阶段,第一阶段从接种开始。到发酵液的pH上升到最高点并开始下降为止．这一阶段中细胞缓慢增长,没有聚苹果酸产生;第二阶段以pH迅速下降和聚苹果酸大量产生为特征。这一阶段中聚苹果酸的产生与细胞增长相平行;在第三阶段中,聚苹果酸产生速度减慢．pH趋于稳定。试验结果还表明。菌株CBS591．75产生聚苹果酸的能力大于DSM2404,发酵结束时,前者聚苹果酸的产量为6．9g／L,而后者为5．4g／L。CBS591．75菌种在20L规模的初步放大试验表明,发酵144h后发酵液中聚苹果酸浓度为8．Og／L,稍高于2L发酵罐的结果,为今后的放大提供了依据和参考。     

新型气升式反应器在发酵培养中的应用研究

本文以Ｌ－苹果酸生产为例,采用新型的分段内循环气升式反应器分批培养产延胡索酸酶的产氨短杆菌ＭＡ－２,并与同等规模机械搅拌反应器中接着的结果相比较。数据表明,采用气升式发酵设备进行培养,该菌体的收率能提高近３％,且发酵周期能缩短一半左右,显著降低培养成本,该类型的反应器具有广阔的应用前景。     

双酶水解紫贻贝制备酵母调味料研究

利用复合蛋白酶、复合风味蛋白酶、中性蛋白酶对紫贻贝进行双酶水解,水解效果比较后选择使用复合蛋白酶和复合风味蛋白酶作为复合水解酶,同时采用产酯酵母发酵技术制备调味料,通过电位滴定法测定单菌株和多菌株发酵对双酶水解贻贝肉产总酯的影响。结果表明：产酯酵母1274在双酶水解后,接种量为5％,发酵温度28℃,发酵时间72h时总酯含量为0．65％,相同条件下,产酯酵母1274和1202多菌株发酵时总酯含量为0．78％,经产酯酵母发酵后的调味料,酯香味浓郁,给予产品以发酵特有的风味。     

樟绒枝霉(Malbranchea cinnamomea)固体发酵产木聚糖酶的发酵条件优化

[目的] 研究樟绒枝霉(Malbranchea cinnamomea) CAU521利用农业废弃物固体发酵产木聚糖酶的发酵条件.[方法]采用单因素试验法优化影响菌株产酶的各个条件,包括碳源种类、氮源种类、初始pH、初始水分含量、培养温度及发酵时间共6个因素.[结果]获得的最佳产酶条件为:稻草为发酵碳源、2％(W/W)的酵母提取物为氮源、初始pH 7.0、初始水分含量80％和发酵温度45℃.在此条件下发酵6d后木聚糖酶的酶活力达到13 120 U/g干基碳源.[结论]樟绒枝霉固体发酵产木聚糖酶的产酶水平高,生产成本低,具有潜在的工业化应用前景.     

苹果酸-乳酸发酵相关基因克隆及其在酵母中的表达

苹果酸乳酸发酵是不同葡萄酒酿造过程中至关重要的降酸步骤。近20年来,围绕苹果酸乳酸发酵相关基因的克隆以及在酿酒酵母中表达的研究取得了一些进展,就该研究进展和存在的问题进行了综述。此外,也论及了苹果酸-乙醇发酵相关基因的研究,这对于一些不适合苹果酸-乳酸发酵的葡萄酒具有重要意义 。     

A mathematical model of the link between growth and L-malic acid consumption for five strains of Oenococcus oeni

In winemaking, after the alcoholic fermentation of red wines and some white wines, L-malic acid must be converted into L-lactic acid to reduce the acidity. This malolactic fermentation (MLF) is usually carried out by the lactic acid bacteria Oenococcus oeni. Depending on the level of process control, selected O. oeni is inoculated or the natural microbiota of the cellar is used. This study considers the link between growth and MLF for five strains of O. oeni species. The kinetics of growth and L-malic acid consumption were followed in modified MRS medium (20 °C, pH 3.5, and 10 % ethanol) in anaerobic conditions. A large variability was found among the strains for both their growth and their consumption of L-malic acid. There was no direct link between biomass productivities and consumption of L-malic acid among strains but there was a link of proportionality between the specific growth of a strain and its specific consumption of L-malic acid. Experiments with and without malic acid clearly demonstrated that malic acid consumption improved the growth of strains. This link was quantified by a mathematical model comparing the intrinsic malic acid consumption capacity of the strains.     

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。     

Reverse reaction of malic enzyme for HCO3- fixation into pyruvic acid to synthesize L-malic acid with enzymatic coenzyme regeneration

Malic enzyme [L-malate: NAD(P)(+) oxidoreductase (EC 1.1.1.39)] catalyzes the oxidative decarboxylation of L-malic acid to produce pyruvic acid using the oxidized form of NAD(P) (NAD(P)(+)). We used a reverse reaction of the malic enzyme of Pseudomonas diminuta IFO 13182 for HCO(3)(-) fixation into pyruvic acid to produce L-malic acid with coenzyme (NADH) generation. Glucose-6-phosphate dehydrogenase (EC1.1.1.49) of Leuconostoc mesenteroides was suitable for coenzyme regeneration. Optimum conditions for the carboxylation of pyruvic acid were examined, including pyruvic acid, NAD(+), and both malic enzyme and glucose-6-phosphate dehydrogenase concentrations. Under optimal conditions, the ratio of HCO(3)(-) and pyruvic acid to malic acid was about 38% after 24 h of incubation at 30 degrees C, and the concentration of the accumulated L-malic acid in the reaction mixture was 38 mM. The malic enzyme reverse reaction was also carried out by the conjugated redox enzyme reaction with water-soluble polymer-bound NAD(+).     

Kinetics, stereospecificity, and expression of the malolactic enzyme.

Mass spectrometric measurement of carbon dioxide production was used to study malolactic fermentation (MLF) in Lactobacillus collinoides isolated from cider. The kinetics and stereospecificity of the malolactic enzyme (MLE) were studied, and the stoichiometry of the reaction sequence was investigated. The optimum pH for activity of the MLE was 4.9. MLF was more rapid (in both intact cells and cell extracts) when L-malic acid was used than when D-malic acid or the racemic mixture was added. The enzyme was found to be constitutively present in L. collinoides. Addition of L-malic acid (37 mM) to the growth medium resulted in increased MLE activity; addition of the D isomer alone or the racemic mixture resulted in lower activities. Addition of the main sugars in apple juice (fructose, sucrose, and glucose) to the growth medium in the presence of malic acid repressed production of MLE to similar extents in all three cases; in the absence of malic acid, instead of inhibiting MLF, addition of sugars to the growth medium somewhat increased the residual MLE activity.     

A study of the maloalcoholic fermentation pathway in Schizosaccharomyces pombe.

The pathway of the maloalcoholic fermentation in Schizosaccharomyces pombe was investigated by a 1H-, 2H- and 13C-n.m.r.-spectroscopic study of hydrogen and deuterium distribution on the ethanol produced by S. pombe from L-malic acid in 2H2O and from L-[2-2H]malic acid. Our findings rule out a double-decarboxylation mechanism and agree with a pathway that involves acetaldehyde as intermediate.     

The inhibitory activity of wine yeast starters on malolactic bacteria

Malolactic fermentation is a process that is influenced by various factors that can inhibit the growth of the malolactic bacteria. Inhibitory metabolites produced by yeast may have an important role in the correct development of malolactic fermentation. For these reasons, we have investigated the effects of such metabolites on the growth of malolactic bacteria under different environmental conditions, to aid in our understanding of the significance of these interactions in the wine-making environment. Our screening methods to detect interactions between yeast and malolactic bacteria showed a variable and wide diffusion of yeast inhibitory activity on the growth of the malolactic bacteria. However, this first approach to determine this inhibitory activity of yeast gave an overestimation when compared to the results obtained under actual wine-making conditions. The evaluation of malic acid consumption indicated that under inhibitory conditions a partial L-malic acid degradation was seen, indicating that the malolactic activity continued without bacterial growth. However, these yeast-inhibiting effects in addition to other environmental factors could cause a complete failure of malolactic fermentation.     

Production of polymalic acid and malic acid by Aureobasidium pullulans fermentation and acid hydrolysis

Malic acid is a dicarboxylic acid widely used in the food industry and also a potential C4 platform chemical that can be produced from biomass. However, microbial fermentation for direct malic acid production is limited by low product yield, titer, and productivity due to end‐product inhibition. In this work, a novel process for malic acid production from polymalic acid (PMA) fermentation followed by acid hydrolysis was developed. First, a PMA‐producing Aureobasidium pullulans strain ZX‐10 was screened and isolated. This microbe produced PMA as the major fermentation product at a high‐titer equivalent to 87.6 g/L of malic acid and high‐productivity of 0.61 g/L h in free‐cell fermentation in a stirred‐tank bioreactor. Fed‐batch fermentations with cells immobilized in a fibrous‐bed bioreactor (FBB) achieved the highest product titer of 144.2 g/L and productivity of 0.74 g/L h. The fermentation produced PMA was purified by adsorption with IRA‐900 anion‐exchange resins, achieving a ～100% purity and a high recovery rate of 84%. Pure malic acid was then produced from PMA by hydrolysis with 2 M sulfuric acid at 85°C, which followed the first‐order reaction kinetics. This process provides an efficient and economical way for PMA and malic acid production, and is promising for industrial application. Biotechnol. Bioeng. 2013; 110: 2105–2113. © 2013 Wiley Periodicals, Inc.     

Molecular imprinting of proteins and other macromolecules resulting in new adsorbents

When the model protein bovine serum albumin (BSA) was dissolved in a concentrated aqueous solution of the multifunctional ligand L-malic acid, the solution was lyophilized, and the solid residue thoroughly washed with tetrahydrofuran to extract malic acid, then the resultant ("imprinted") protein was capable of binding 26.4 +/-0.9 mol equivalents of the ligand in anhydrous ethyl acetate. The nonimprinted BSA (i.e., that prepared in the same manner apart from the absence of malic acid) bound less then one-tenth of that amount under identical conditions. Furthermore, both imprinted and nonimprinted BSA exhibited little binding of L-malic acid in water. The imprinted BSA retained its "memory" for the ligand in ethyl acetate even after a prolonged incubation under vacuum; dissolution in water, however, eliminated the imprinted protein's binding capacity. The BSA imprinted with L-malic acid displayed affinity for this ligand not only in ethyl acetate but also in many other anhydrous solvents. It was found that the higher the solvent's propensity to form hydrogen bonds, the lower the protein-ligand binding in it, thus pointing to hydrogen bonds as the driving force of this binding. Studies with completely or partially cleaved BSA, with other globular proteins, glutathione, and poly(L-aspartic acid) revealed that the critical requirement for the imprintability is the presence of a sufficiently long polymeric chain. Moreover, many hydrogen-bond-forming macromolecules other than proteins, such as dextrans and their derivatives, partially hydrolyzed starch, and poly(methacrylic acid), also could be imprinted for subsequent binding in ethyl acetate. The mechanism of imprinting and binding inferred from these experiments involves a multipoint hydrogen bonding in water of each ligand molecule with two or more sites on the polymeric chain, thereby folding a segment of the latter into a cavity around the ligand; following lyophilization and extraction of the ligand, the cavities remain in organic solvents (but not in water) and give rise to ligand binding. This conclusion is supported by the results of binding of numerous malic acid analogs and related ligands to BSA imprinted with L-malic acid. Finally, BSA imprinted with malic acid was used as a selective adsorbent for a chromatographic separation of an equimolar mixture of maleic and acrylic acids in ethyl acetate.     

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.