产氨短杆菌GMA-2802 1.2L罐肌苷发酵试验

采用诱变得来的产氨短杆菌GMA－2802,在1.2L自控发酵罐上进行了5批发酵肌苷试验,发酵周期54小时,平均产肌苷20.4g/L。结果表明该菌档是一株具有较多优良特性的肌苷产生菌。     

产氨短杆菌GMA-1112利用味精母液发酵生产肌苷

通过亚硝基胍或60 Coγ辐照等选育一株产氨短杆菌GMA 1 1 1 2 (Ade +Gua +VB1 +8 AGr+SGr+6 MPr) ,能以味精母液代替传统肌苷发酵添加酵母粉作为有机营养物 ,进行肌苷发酵 ,平均产肌苷率 2 5.4 0 g/L。具有降低发酵成本、提高产肌苷率等优点。     

原生质体融合选育肌苷产生菌产氨短杆菌GMA—2802

以肌苷产生菌产氨短杆菌ＧＭＡ－２７２２（Ａｄｅ－、 Ｇｕａ－、ＶＢ１－、Ｒｉｆｒ）和 ＧＭＡ－２７７６（Ａｄｅ－、 Ｂｉｏｔｉｎ－、ＶＢ１－、Ｓｍｒ）为出发菌株,经原生质体融合,将目的标志加以组合,获得遗传性状稳定、摇瓶发酵６１ｈ,产肌苷２５．４ｇ／Ｌ的融合子 ＧＭＡ－２８０２（Ａｄｅ－、Ｇｕａ－、Ｂｉｏｔｉｎ－、ＶＢ１－、 Ｒｉｆｒ、Ｓｍｒ）。     

新型肌苷新生菌——产氨短杆菌GMBA—800选育和特性的初步研究

采用多种方法诱变获得一株新型肌苷产生菌－－产氨短杆菌ＧＭＢＡ－８００,对其生长和发酵条件进行初步研究。肌苷产量从５ｇ／Ｌ提高到１８．４１ｇ／Ｌ,发酵周期从８４ｈ缩短为６３ｈ。菌株遗传性状稳定。     

新型肌苷产生菌──产氨短杆菌GMBA—800选育和特性的初步研究

采用多种方法诱变获得一株新型肌苷产生菌──产氨短杆菌（Ｂｒｅｖｉｂａｃｔｅｒｉｕｍａｍｍｏｎｉａｇｅｎｅｓ）ＧＭＢＡ－８００（具有腺嘌呤、生物素双重营养缺陷型和对８－氮杂鸟嘌呤、磺胺胍、６－流基嘌呤有抗性）,对其生长和发酵条件进行初步研究。肌苷产量从５ｇ／Ｌ提高到１８．４１ｇ／Ｌ,发酵周期从８４ｈ缩短为６３ｈ。菌株遗传性状稳定。     

采用产氨短杆菌合成辅酶A的研究

用产氨短杆菌鲜菌体在以腺嘌岭代替ATP的反应系统中酶促合成辅酶A(CoA),每毫升反应液的CoA产量达Z21单位(u);在不加任何核苷酸类物质的条件下,也可达185u;合成在5小时左右达高峰。CoA合成主要在细胞内进行。提出了连续式碳一阴离子交换树脂柱提纯CoA的新方法,既提高了收率,又避免了原锌汞齐法的毒物危害,方法简易可行。用本法制得的结晶品含CoA 231u／mg,收率17．0％;阴柱洗脱液不经结晶直接制成CoA注射液,提取率20．9％,经广州药检所检验,各项指标均符合国家标准。     

枯草杆菌JSIM-1019突变株肌苷发酵研究

以肌苷产生菌枯草杆菌7171-9-1为出发菌株,经物理、化学诱变剂连续处理,获得一株腺嘌呤、组氨酸、硫胺素三重营养缺陷型并对8-氮杂鸟嘌呤、6-巯基嘌呤有双重抗性的突变株JSIM-1019。在摇瓶和发酵罐试验中,该变异株的肌苷产量显著高于亲株。摇瓶试验产肌苷达20g/L,最高可达24.83g/L。工业生产试验最高达14.5g/L,稳定在12g/L。发酵周期平均为43.8小时。菌株遗传性状稳定。     

固定化产氨短杆菌MA-2、黄色短杆菌MA-3反应动力学的研究

多年来虽然有不少学者对固定化细胞生产Ｌ 苹果酸的方法进行过探讨[1～ 6] ,但对过程动力学的研究报道并不多见[2 ,7] ,在富马酸铵转化体系中的表观动力学及本征动力学模型还未见报道 ,本文对富马酸铵转化体系中固定化产氨短杆菌ＭＡ 2、黄色短杆菌ＭＡ 3细胞的动力学进行了探讨 ,测定了两种固定化细胞的表观动力学常数 ,并进一步求解了相应的本征动力学常数 ,这一结果便于从理论上指导富马酸铵转化过程的工业化生产。1　材料和方法1 1　试剂富马酸 ,工业级 ,苏州合成化工厂 ,碳酸钙 ,工业级 ,泗联化工厂。1 2　菌株本文所用的菌株是由我院…     

腺嘌呤对枯草杆菌GMI—971发酵生产肌苷的影响

培养基中腺嘌呤含量对腺嘌呤缺陷型的枯草杆菌GMI－971发酵产肌苷有显著影响。在拟定条件下,腺嘌呤浓度在150mg／L时摇瓶肌苷产量最高。对不同来源的四种酵母粉分别添加腺嘌呤,当其含量增加至l50ml／L时,肌苷产量也最高。     

肌苷产生菌B.Subtilis H841在2升罐中的发酵

枯草芽孢杆菌(Bacillus Subtilis)H841肌苷产生菌是腺嘌呤、组氨酸、硫胺素三重缺陷型菌株,并对8—氮杂乌嘌呤、6—巯基嘌呤有抗性。在摇瓶中产肌胺18.1克/升,在2L自控发酵罐中最高可产肌苷19.6克/升,在流加葡萄糖情况下可产肌苷26.2克/升。控制pH较不控制pH发酵肌苷产量有较大的增加,控制pH发酵并补加营养时,肌苷产量可稳定地增长,但对葡萄糖的转化率是相同的。     

Isolation and characterization of two distinct membrane fractions from the Gram-positive nucleotide producer Brevibacterium ammoniagenes ATCC 6872

Abstract Bouyant density gradient centifugation of 'crude membranes' of the coryneform bacterium Brevibacterium ammoniagenes yielded two distinct membrane fractions which differed significantly in equilibrium densities (1.15 and 1.18 g/cm³), NADH dehydrogenase activity (0.29 and 0.09 μmol·min⁻¹·mg⁻¹), protein composition and association of ribosomes. As determined by one dimensional sodium dodecyl sulfate polyacrylamide gel electrophoresis (SDS-PAGE) proteins unique to either the free membrane (FM) fraction or the denser ribosome-containing complexed membrane (CM) fraction were identified.     

高产纤维素酶枯草芽胞杆菌S-16的筛选及其发酵工艺优化

利用刚果红鉴别培养基及基础液体筛选培养基进行菌种筛选,从新疆盐碱地分离得到的16株菌株中筛选获得一株产纤维素酶活力较高的菌株S-16,对该菌株进行16SrDNA鉴定,确定该菌为枯草芽胞杆菌(Bacillus subtilis)。对S-16发酵产纤维素酶的主要影响因素进行研究,分别考察了碳源、氮源、培养基初始pH和接种量等因素对发酵产纤维素酶的影响。结合单因素影响实验得到优化后的培养基配方为:羧甲基纤维素钠1.5%,酵母粉1%,NaCl 1%,MgSO_4·7H_2O 2‰,KH_2PO_4·3H_2_O 1‰。优化后的发酵条件为:初始pH为8,接种量1%,种龄8h,培养时间48h。经过发酵工艺优化,S-16产生的羧甲基纤维素酶活(CMCase)和滤纸酶活(FPase)分别达到4.64IU/mL和0.46IU/mL,与初始培养条件下的酶活相比分别提高了3.14倍和1.30倍。本研究得到的枯草芽胞杆菌S-16及其优化发酵工艺为秸秆的快速腐熟和高产纤维素酶的应用奠定了基础。     

The derepression of enzymes of de novo pyrimidine biosynthesis pathway in Brevibacterium ammoniagenes producing uridine-5-monophosphate and uracil

A mutant of Brevibacterium ammoniagenes producing large quantities of UMP and uracil is described. The mutations render bacteria braditrophic for arginine, sensitive to adenine, resistant to rifampicin and pyrimidine analogues 5-fluorouracil, 5-fluorouridine, azauracil and thiouracil. The activities of enzymes involved in the UMP biosynthesis, i.e. orotate phosphoribosyltransferase, orotate-5-monophosphate decarboxylase, dihydroorotate oxidase, are 4-, 3.5- and 4.5-fold higher in the mutant than in the parent strain when grown in minimal medium. The synthesis of these enzymes in mutant cells is not repressed in the presence of exogenous Ura. True revertants, which completely restore the wild-type phenotype, occur among the Arg+ clones. The nature of the mutation is discussed.     

Genomic organization of purK and purE in Brevibacterium ammoniagenes ATCC 6872: purE locus provides a clue for genomic evolution

Abstract From the genomic library of Brevibacterium ammoniagenes ATCC6872, the purE locus encoding 5'-phosphoribosyl-5aminoimidazole (AIR) carboxylase (EC 4.1.1.21) was cloned and its nucleotide sequence was determined. From the sequence analysis, two distinct open reading frames (ORFs) in the sequence of the purE locus were identified as purK and purE genes ( purK-purE ). An in vivo translation experiment reconfirmed the purK and purE genes to be independent. The genomic organization in the purE locus of B. ammoniagenes is opposite to that of the bacteria Escherichia coli and Bacillus subtilis . However, it coincides with the fused genes ( purKE ) of higher organisms Saccharomyces cerevisiae, Schizosaccharomyces pombe and Vigna aconitifolia . This suggests that the purE locus might be an intermediate form for genomic evolution of bacteria to higher organisms.     

A new strategy to apply Bacillus subtilis MA139 for the production of solid-state fermentation feed

Aim:  The study investigated the potential of using Bacillus subtilis MA139 in combination with Lactobacillus fermentum and Saccharomyces cerevisae to produce solid-state fermentation feed.
Methods and Results:  In a pure fermentation, B. subtilis MA139 was able to grow and synthesize antimicrobial substances at temperatures from 25 to 37°C and at a pH from 5·0 to 9·0. Subsequently, B. subtilis MA139, Lact. fermentum and S. cerevisae were used as starter strains co-inoculated in unsterilized substrate (feed-grade soybean meal and wheat bran). Following 10 days of fermentation in a newly developed plastic bag equipped with a one-way valve, lactic acid bacteria and Bacillus became the predominant strains while S. cerevisae cells decreased slightly. Enterobacteriaceae ( Escherichia coli K88 and Salmonella typhimurium ) were not detected.
Conclusions:  Use of B. subtilis MA139 as a starter strain co-inoculated with S. cerevisae and Lact. fermentum successfully controlled the growth of enterobacteriaceae.
Significance and Impact of the Study:  This study provided a facile and low-cost way to produce solid-state fermentation feed.     

Bioprocess optimization for production of thermoalkali-stable protease from Bacillus subtilis K-1 under solid-state fermentation

Cost-effective production of proteases, which are robust enough to function under harsh process conditions, is always sought after due to their wide industrial application spectra. Solid-state production of enzymes using agro-industrial wastes as substrates is an environment-friendly approach, and it has several advantages such as high productivity, cost-effectiveness, being less labor-intensive, and less effluent production, among others. In the current study, different agro-wastes were employed for thermoalkali-stable protease production from Bacillus subtilis K-1 under solid-state fermentation. Agricultural residues such as cotton seed cake supported maximum protease production (728?U?ml^?1), which was followed by gram husk (714?U?ml^?1), mustard cake (680?U?ml^?1), and soybean meal (653?U?ml^?1). Plackett–Burman design of experiment showed that peptone, moisture content, temperature, phosphates, and inoculum size were the significant variables that influenced the protease production. Furthermore, statistical optimization of three variables, namely peptone, moisture content, and incubation temperature, by response surface methodology resulted in 40% enhanced protease production as compared to that under unoptimized conditions (from initial 728 to 1020?U?ml^?1). Thus, solid-state fermentation coupled with design of experiment tools represents a cost-effective strategy for production of industrial enzymes.     

枯草芽孢杆菌C1-B941的D-核糖发酵中间试验

使用转酮醇酶变异株—枯草芽孢杆菌C1－B941进行了D－核糖发酵中间试验。3000L发酵罐试验结果表明,发酵培养基中的葡萄糖浓度为18％时,发酵周期约为64h,发酵转化率达36．84％。发酵液经离子交换树脂纯化后,可以直接用于生产VBZ合成的中间体—N－D－核糖醇基－3,4－二甲苯胶。     

Commercial riboflavin production by recombinant Bacillus subtilis: down-stream processing and comparison of the composition of riboflavin produced by fermentation or chemical synthesis

A novel process for riboflavin production using a recombinant Bacillus subtilis strain has been developed. Here we describe a down-stream processing procedure to obtain riboflavin qualities having a minimal content of 96% (‘feed-grade’) and 98% (‘food/pharma-grade’) riboflavin, respectively. Compared to riboflavin produced by chemical synthesis, products with improved chemical purity were obtained. All compounds representing more than 0.1% of the final products were identified. Feed-grade riboflavin material ex fermentation contained small amounts of amino acids and amino sugars and the biosynthetic riboflavin precursor dimethyl-ribityl-lumazine. All other side products found were derived from riboflavin, resulted from the purification procedure and were also found in riboflavin obtained by chemical synthesis. The Bacillus-produced riboflavin does not contain DNA. The data presented here were used to obtain product approval for the commercial application in the USA, Japan and the UK. Received 22 July 1998/ Accepted in revised form 8 November 1998     

Biosurfactant production by a thermophilic Bacillus subtilis strain

A strain of Bacillus subtilis was able to grow and produce a biosurfactant on 2% sucrose at 45°C. As a result of biosurfactant synthesis the surface tension of the medium was reduced from 68 dynes cm⁻¹ to 28 dynes cm⁻¹. The strain had the capacity to produce the biosurfactant at high NaCl concentrations (4%) and a wide range of pH (4.5–10.5). The biosurfactant retained its surface-active properties after heating at 100°C for 2 h and at different pH values (4.5–10.5). A maximum amount of biosurfactant was produced when urea or nitrate ions were supplied as nitrogen source. The use of the biosurfactant at high temperatures, acidic, alkaline and saline environments is discussed. As a result of its action, 62% of oil in a sand pack column could be recovered, indicating its potential application in microbiologically enhanced oil recovery. Received 28 March 1996/ Accepted in revised form 16 September 1996