Production of Mevalonic Acid by Fermentation

The purpose of this investigation was to select microorganisms that produce substantial quantities of mevalonic acid and to develop an economic fermentation process. To screen for mevalonic acid-producing microorganisms, it was necessary to improve the method for the quantitative determination of this acid. The biological assay was modified by shortening the incubation time and simplifying the procedure. The principle of the assay is based on the essential mevalonic acid requirement of the organism Lactobacillus heterohiochii for growth. Screening was carried out by selecting high mevalonic acid-producing organisms from various type cultures. Endomycopsis fibuliger was chosen for medium development studies, and 939 mug of mevalonic acid per ml was produced in the culture filtrate after modifications of medium and fermentation conditions.     

Current Progress on Butyric Acid Production by Fermentation

Several issues of butyric acid production with bacteria through fermentation are presented in this review. The current progress including the utilization of butyric acid, the production strains, the metabolic pathway, and regulation are presented in the paper. Process operation modes such as batch, fed-batch, and continuous fermentation are being discussed. Genetic engineering technologies for microbial strain improvement are also being discussed and fermentation systems have been recommended.     

硅藻变温发酵生产二十碳五烯酸的研究

本文考察不了同温度（10℃～30℃）对硅藻(Nitzschia laevis)合成二十碳五烯酸(EPA)的影响,对不同温度下的发酵过程进行动力学特性分析。在此基础上,提出了EPA合成的变温培养方法：延滞期及对数期初期温度控制在25℃,从对数期中期开始在20℃条件下进行培养。采用此变温培养进行发酵,EPA的含量和产量分别达到了6.00%和291.60 mg·L-1,较采用单一温度(25℃)发酵的最大值分别提高了24.07%和18.81%。     

原生质体诱变选育高产异抗坏血酸菌株

以灰黄青霉菌(Penicillium griseofulvum HL)为出发菌株,试验得到灰黄青霉原生质体制备的优化条件为:菌体培养48h,用0.7mol/L的NaC1溶液作为渗透压稳定剂,用0.5％的蜗牛酶+0.5％的纤维素酶,在pH为6,30℃条件下酶解3h,所得原生质体数最多,达到3.14×107/ml.原生质体再生的最佳条件为采用双层平板培养法,在用0.7mol/L的蔗糖溶液配制的改进察氏培养基上其再生率最高,达到24.93％.灰黄青霉原生质体经过紫外线诱变,DES诱变,紫外线-DES诱变复合诱变,紫外线-氯化锂复合诱变选育异抗坏血酸高产菌株,通过对再生平板上长出的诱变菌株进行初筛和摇瓶复筛,最终获得一株异抗坏血酸产量较高的菌株ZD4,其产量为5.28mg/ml,提高到出发菌株产量(1.08 mg/ml)的488.9％,且连续传代6代遗传稳定.     

Studies on l-Glutamic Acid Fermentation by Microbacterium ammoniaphilum

The present investigation is concerned with the effects of biotin and glucose on glutamic acid fermenation by Microbacterium ammoniaphilum. Both optimal amounts of biotin necessary for maximum growth and maximum accumulation of glutamic acid were determined under the conditoin of various concentration of glucose. As the glucose concentratin was increased, the amounts of biotin required for maximum growth also increased proportionally to the glucose concentrations. The optimal amounts of biotin for maximum accumulation of glutamic acid were smaller than those for maximum growth of cells at any glucose concentration. It is suggested that the process of glutamic acid accumulation is inevitably associated with the process of cell multiplication by both experiments of successive culture of cells grown under the dose of biotin sufficient and deficient for maximum growth.     

Studies on l-Glutamic Acid Fermentation

In the previous paper, most of the enzymes of the Embden-Meyerhof-Parnas pathway and glucose-6-phosphate dehydrogenase have been demonstrated to be present in cell-free extracts of Brevibacterium divaricatum, No. 1627. In this paper, the presence of condensing enzyme, aconitase, TPN-linked isocitric dehydrogenase, succinic dehydrogenase, fumarase, DPN-linked malic dehydrogenase, TPN-linked malic enzyme, oxalacetic carboxylase, isocitritase and malate synthetase in cell-free extracts of this bacterium was also demonstrated. From these results it was concluded that a strain of Brevibacterium divaricatum which has been found to contain all of the enzymes of the tricarboxylic acid cycle, would be capable of forming the key enzymes of the glyoxylate bypass as well. It suggests that the accumulation of α-ketoglutarate involves the glyoxylate bypass besides the tricarboxylic acid cycle in this bacterium.     

Studies on l-Glutamic Acid Fermentation

Micrococcus glutamicus, a glutamate-produeing bacterium, is known to have strong activity of l-glutamic acid dehydrogenase which requires NADP as co-enzyme. In this paper, the NADP-speeifie l-glutamic acid dehydrogenase was purified from M. glutamicus by means of heat treatment with sodium sulfate, precipitation with acetic acid and diethyl-amino-ethyl (DEAE) cellulose column chromatography. The activity of the purified enzyme preparation reached 200-fold as high as that of the crude extract. Some properties of the purified enzyme were investigated. As a result, it was found that the highly purified enzyme preparation acted not only on l-glutamic acid (l-GA) but also on α, ε-diaminopimelic acid (α, ε-DAP) in the presence of NADP. Some of the probable consideration for the dehydrogenation of l-GA and α, ε-DAP are noted.     

Studies on l-Glutamic Acid Fermentation

The authors have carried out a series of studies on l-glutamic acid fermentation with a strain of Brevibacterium divaricatum nov. sp. in the previous papers.

In this paper, some metabolism of l-glutamic acid and oxidative decomposition of several organic acids concerning the tricarboxylic acid cycle by the resting cells have been studied. The results suggest that l-glutamic acid is one of the final fermentative products of this bacterium, and the tricarboxylic acid cycle is working as a glutamic acid forming cycle.

The presence of glucokinase, phosphoglucoisomerase, phosphofructokinase, aldolase, DPN-linked glyceraldehyde-3-phosphate dehydrogenase, and TPN-linked glucose-6-phosphate dehydrogenase in cell-free extracts of this bacterium was also demonstrated.     

Studies on Lactic Acid Fermentation

Resting cells of l. fermentum convert glyceraldehyde to equimolar lactic acid and neither the evolution of carbon dioxide nor the uptake of oxygen was observed. Glyceraldehyde-3-phosphate and 3-phosphoglycerate were identified as intermediates which were equally labeled with inorganic P³² in reaction systems, and the presence of triokinase was suggested.     

电渗析发酵法生产乳酸的研究

在乳酸发酵过程中,所生成的乳酸对进一步发酵有抑制作用。采用电渗析法从发酵液中及时地分离出产物乳酸,使乳酸的生产量提高到86.4g/L,是不控制pH值发酵时的4倍多。结果表明:电渗析法能有效地消除产物乳酸的抑制作用,提高了乳酸生产率,且简化了提取工艺。     

发酵法生产多不饱和脂肪酸

简要介绍微生物产多不饱和脂肪酸的生化研究现状,着重从高产菌株的筛选、工程菌株的构建、发酵条件及产业化现状等方面论述微生物发酵生产多不饱和脂肪酸的主要研究进展;概述多不饱和脂肪酸的提取制备技术,并对发酵法生产多不饱和脂肪酸研究目标和发展前景提出了建议.     

脱落酸的发酵法生产及应用

脱落酸是重要的植物激素之一,可以增强作物对环境逆因子如干旱、寒冷等的抵抗能力,在抵抗农业自然灾害、植树造林、生态植被建设、城市园林绿化等领域有广阔的应用前景.施用脱落酸可减少化学农药的使用,保护自然环境.本文概述了脱落酸生产和应用方面的研究进展,包括产生菌的筛选、诱变、外施脱落酸在提高作物抗逆性上的应用,以及脱落酸抗肿...     

Novel Method of Lactic Acid Production by Electrodialysis Fermentation

In lactic acid fermentation by Lactobacillus delbrueckii, the produced lactic acid affected the lactic acid productivity. Therefore, for the purpose of alleviating this inhibitory effect, an electrodialysis fermentation method which can continuously remove produced lactic acid from the fermentation broth was applied to this fermentation process. As a result, the continuation of fermentation activity was obtained, and the productivity was three times higher than in non-pH-controlled fermentation. In electrodialysis fermentation, the amount of produced lactic acid was 82.2 g/liter, which was about 5.5 times greater than that produced in non-pH-controlled fermentation. It was concluded that these good results were obtained on account of alleviating the lactic acid inhibitory effect by electrodialysis fermentation. However, the fouling of anion-exchange membranes by cells was observed in electrodialysis fermentation.     

金黄色破囊壶菌发酵生产DHA的研究

顺 4,7,1 0 ,1 3 ,1 6 ,1 9 二十二碳六烯酸 (ｄｏｃｏｓａｈｅｘａｅｎｏｉｃａｃｉｄ ,简称ＤＨＡ)是ω 3系列多不饱和脂肪酸。近年的研究表明 ,ＤＨＡ是组成大脑和视网膜的重要结构物质 ,如大脑灰质结构脂质中 6 0 %的脂肪酸均为ＤＨＡ[1] 。ＤＨＡ对人体健康有益的生理功能主要表现在[2 ] :调节中枢神经系统功能 ;预防和治疗心血管疾病 ;治疗气喘、关节炎等 ;预防和治疗乳腺癌、结肠癌等。由于ＤＨＡ具有上述生理功能 ,已在医药、食品、保健品等领域得到广泛应用。目前 ,商品ＤＨＡ主要来源于深海鱼油 ,如沙丁鱼、金枪鱼等鱼油 ,由于鱼…     

生物强化污泥厌氧发酵产酸研究进展*

污泥厌氧发酵生产挥发性脂肪酸相较产甲烷,是更具应用价值的污泥稳定途径及资源化利用方式,得到国内外学者的普遍重视。考虑到产酸量低和产酸过程的不稳定性是限制污泥发酵产酸的主要问题,采用生物强化方法实现挥发性脂肪酸的大量积累,与物理和化学方法相比,具有成本低、无二次污染等优点。根据生物强化制剂的类型,归纳了微生物纯培养物、微生物混合培养物及生物酶强化对污泥厌氧发酵产酸的影响,并在此基础上对生物强化技术控制污泥定向产酸、调控奇偶数碳比率等方面的应用进行讨论。此外,分析了影响挥发性脂肪酸产量和组分的因素,如pH、温度、底物、水力停留时间和污泥龄等。最后对生物强化技术的发展方向进行了展望,以期为深入探究污泥资源化利用提供借鉴。     

Acid Protease Production by Fungi Used in Soybean Food Fermentation

Growth conditions for maximum protease production by Rhizopus oligosporus, Mucor dispersus, and Actinomucor elegans, used in Oriental food fermentations, were investigated. Enzyme yields by all three fungi were higher in solid substrate fermentations than in submerged culture. The level of moisture in solid substrate must be at about 50 to 60%. Very little growth of these fungi was noted when the moisture of substrate was below 35%, whereas many fungi including most storage fungi generally grow well on solid substrate with that level of moisture. Among the three substrates tested—wheat bran, wheat, and soybeans—wheat bran was the most satisfactory one for enzyme production. The optimal conditions for maximum enzyme production of the three fungi grown on wheat bran were: R. oligosporus, 50% moisture at 25 C for 3 to 4 days; M. dispersus, 50 to 63% moisture at 25 C for 3 to 4 days; A. elegans, 50 to 63% moisture at 20 C for 3 days. Because these fungi are fast growing and require high moisture for growth and for enzyme synthesis, the danger of contamination by toxin-producing fungi would be minimal.     

Production of 2-Keto-l-Gulonic Acid from d-Glucose by Two-Stage Fermentation

A practical method for the production of calcium 2-keto-l-gulonate (an intermediate in the Reichstein synthesis of l-ascorbic acid) from d-glucose has been established by using a two-stage fermentation system. d-Glucose was first converted to calcium 2,5-diketo-d-gluconate by a mutant strain of Erwinia sp. in a medium containing d-glucose, corn steep liquor, (NH(4))(2)HPO(4), and CaCO(3). After a 26-h cultivation, 328.6 mg of calcium 2,5-diketo-d-gluconate per ml was obtained, with a 94.5% yield from d-glucose. This broth was used directly for the next conversion without removal of cells by treatment with sodium dodecyl sulfate. The stereospecific reduction of calcium 2,5-diketo-d-gluconate to calcium 2-keto-l-gulonate was performed with a mutant strain of Corynebacterium sp. When the cell growth reached a maximum (about 16 h) in a medium containing d-glucose, corn steep liquor, NaNO(3), KH(2)PO(4), and trace elements, NaNO(3) was added to the culture, and then the calcium 2,5-diketo-d-gluconate broth was fed over a period of about 50 h. Since the mutant strain requires a hydrogen donor for reduction, the calcium 2,5-diketo-d-gluconate broth was mixed with d-glucose before being fed. The results of four two-stage fermentations in 10-m conventional fermentors showed that an average of 106.3 mg of calcium 2-keto-l-gulonate per ml was obtained, with a 84.6% yield from d-glucose, the starting material of calcium 2,5-diketo-d-gluconate production. Calcium 2-keto-l-gulonate was stable in the broth. Neither 2-keto-d-gluconic acid nor 5-keto-d-gluconic acid was detected in the final broth.     

解淀粉乳酸细菌在L-乳酸发酵生产中的应用

对解淀粉乳酸细菌及其产生的淀粉酶和发酵工艺等方面的国内外研究现状进行了综述。解淀粉乳酸细菌具有分泌淀粉酶的能力,可免去原料水解处理工序直接发酵淀粉质原料生产乳酸,可以简化生产工艺,并可节约设备投资,进而降低生产成本。解淀粉乳酸细菌主要分离自传统发酵食品,也可从有机废弃物和厨余垃圾中分离得到。介绍了解淀粉乳酸细菌直接利用淀粉质原料的机理,比较了解淀粉乳酸菌发酵生产L-乳酸的工艺。提出通过诱变育种和基因工程育种等方法获得更加高效的解淀粉乳酸细菌,并结合先进的发酵、分离技术来提高乳酸生产效率。     

泥炭固体发酵生产单细胞蛋白研究

对以泥炭为唯一碳源,固体发酵生产单细胞蛋白(SCP)进行了一系列的研究。选用酵母菌和黑曲霉进行混合发酵培养,考察影响单细胞蛋白生产的各个因素,如菌种接种量,培养基含水量,发酵时间,发酵温度,培养基外加氮源等。通过正交实验设计确定了优化的培养条件。即:菌种接种量为10%,培养基含水量为300%,28℃培养72 h,以蛋白胨为氮源。