不同的底物流加方式对Alcaligenes faecalis发酵生产热凝胶的影响

目的：研究了在不同阶段、不同的底物流加方式及底物浓度对菌体生长和热凝胶合成的影响,并对粪产碱杆菌WX—C12（Alcaligenes faecalis）发酵生产热凝胶的补料工艺进行了优化。方法：15L发酵罐发酵生产热凝胶,改变培养基中氮源、碳源浓度及流加方式,测定残氮、残糖、菌体浓度及热凝胶产量的变化,确定较优的补料工艺。结果：在菌体生长阶段用氨水控制pH在7．0,可使培养基中氮源浓度维持相对稳定状态,且NH,a初始浓度较低（O．5gtL）更适合菌体生长;热凝胶合成阶段采用葡萄糖连续流加优于间歇补加培养。菌体浓度为11．9g／L时,热凝胶产量最高（72g／L）,产物得率Vp／s为78．8％;当菌体浓度再增加时,热凝胶产量反而下降。结论：确定了粪产碱杆菌发酵生产热凝胶的较优工艺条件,热凝胶产量最高为72g／L,比分批发酵28g/L增加了157％。     

聚-ε-赖氨酸补料发酵的初步研究

在5L自动发酵罐中,通过分批发酵和补料分批发酵,对白色链霉菌(Strepomyces albulus)生物合成聚-ε-赖氨酸(ε-PL)进行了初步研究。结果表明,在分批发酵中,利用pH控制策略,ε-PL产量从0.6 g/L提高到2.4 g/L。在分批补料发酵中,采用pH控制策略,当糖浓度在10g/L以下,补加葡萄糖和硫酸铵,则菌体大量生长,ε-PL产量提高到16.81 g/L,为分批培养的27倍。     

植物乳杆菌Lp-2的高密度发酵

高密度培养植物乳杆菌是制作其发酵剂的重要环节。首先,研究了不同的溶氧和pH对植物乳杆菌的分批发酵的影响。在分批发酵的基础上,为进一步提高发酵液中的菌体浓度,进行了补料分批发酵实验。最终通过对蔗糖反馈补料发酵试验对比改造获得了pH反馈补料发酵工艺。此发酵补料工艺可以控制蔗糖残糖量始终处于较低的水平,因此获得了最高的菌体产量。菌体干重达到13.56g/L,较分批培养提高90.05%。     

pH及流加葡萄糖对酵母分批发酵生产谷胱甘肽的影响

在5 L的发酵罐中研究了pH及流加葡萄糖对酵母分批发酵生产谷胱甘肽(GSH)的影响。实验考察了不同浓度的流加葡萄糖和不同的恒pH值的分批发酵对于酵母生产GSH产量的变化。实验结果表明,当pH值控制为5.0,流加葡萄糖流速为5g.L-1.h-1,连续流加30 h,可使GSH产量最高,与之前未流加葡萄糖和控制pH相比,其产量提高了6倍。     

补料工艺对两株法夫酵母菌株产虾青素的影响

【目的】考察不同补料工艺对法夫酵母菌株生长和虾青素合成的影响。【方法】对法夫酵母JMU-VDL668和JMU-MVP14菌株在7 L罐中进行分批及分批补料培养; 同时, 测定发酵过程中生物量、虾青素和葡萄糖含量的变化。【结果】采用恒DO补料, 法夫酵母JMU-VDL668菌株获得的生物量最大(64.6 g/L), 是分批培养的2.2倍; 采用恒pH补料发酵, 虾青素的产量最高(20.6 mg/L), 是分批培养的1.5倍。与JMU-VDL668菌株不同, 虾青素高产菌株JMU-MVP14菌株采用恒pH补料, 获得生物量最大(48.5 g/L), 但虾青素产量大大降低(仅17.5 mg/L); 采用脉冲补料, 虾青素产量最高, 达到414.1 mg/L, 与分批发酵相比提高了200.2%; 采用恒DO补料, 生物量(38.5 g/L)和虾青素产量(403.2?mg/L)增加显著, 与分批发酵相比分别提高了133.1%和192.3%。【结论】不同补料工艺对法夫酵母菌株生产虾青素影响很大。其中, 采用恒pH补料工艺, 法夫酵母JMU-VDL668菌株可以获得最高的虾青素产量, 而采用脉冲补料工艺, 最适于法夫酵母JMU-MVP14菌株发酵生产虾青素。     

高山被孢霉发酵产花生四烯酸油脂的补料工艺

为了缩短高山被孢霉(Mortierella alpina)产花生四烯酸(ARA)油脂发酵周期,以提高ARA油脂生产强度,主要研究了不同底物流加方式对M.alpina产ARA油脂的影响。考察分批发酵、残糖反馈补料分批发酵对ARA油脂发酵的影响,并进一步在残糖反馈补料发酵的基础上建立了一种反复补料分批发酵工艺。结果表明:与分批发酵相比,虽然细胞干质量和油脂浓度变化不显著,但是残糖反馈补料方式ARA生产强度从0.93提高至1.33g/(L·d)。在残糖反馈补料基础上反复补料分批发酵一共进行了4批,细胞干质量稳定在30 g/L左右,油脂含量稳定在50%左右,ARA含量分别达到42.81%、43.17%、42.30%和39.71%。     

蝉拟青霉液体发酵条件优化

采用液体发酵蝉拟青霉,对蝉拟青霉的发酵条件进行优化,以提高蝉拟青霉胞外多糖产量及生物量。摇瓶发酵条件下,在单因素基础上设计正交实验确定各因素的最佳组合。优化后得最佳发酵培养基:蔗糖8%,牛肉膏0.75%,酵母膏0.125%,MgSO_4·7H_2O 0.3%,KH_2PO_4 0.2%,麸皮0.5%。该条件下胞外多糖产量为5.96 g/L,生物量为42 g/L,较优化前提高了1倍。采用发酵罐进行扩大培养,对分批发酵时的初糖浓度进行了优化,并分析了补料分批发酵对发酵过程的影响。发酵罐培养时最适初糖浓度为5%,此时生物量最高为38 g/L,多糖含量最高为5.5 g/L;采用补料分批发酵时,多糖产量最高为5.89 g/L,生物量最高为40 g/L,效果优于分批发酵。     

基因工程FR-008/杀念菌素脱羧衍生物CS103的分离提取及毒性和抗白色念珠菌活性研究

本文在建立了基因工程FR-008/杀念菌素脱羧衍生物CS103分离提取工艺的基础上, 经进一步纯化, 获得一定供试样品。通过对比脱羧FR-008/杀念菌素CS103、FR-008/杀念菌素和两性霉素B三种化合物对人胚肾细胞毒性、对人血红细胞的溶血活性和对白色念珠菌的抗菌效果, 发现脱羧FR-008/杀念菌素CS103的毒性较FR-008/杀念菌素和两性霉素B大大降低, 且保持了较高的抗真菌(Candida albicans)活性。     

L-谷氨酸补料分批发酵的研究

对谷氨酸棒杆菌(Corynebacteriuin glutamicum)HCJ46产L-谷氨酸的补料分批发酵条件进行研究.结果表明:最适初糖质量浓度和最佳残糖维持质量浓度分别为100和(10～20)g/L;对发酵控温方式进行研究,确定了最佳温度控制策略为0～8h维持32℃,8～16h维持34℃、16～32h维持36℃,同时发现相对溶氧控制在30%左右时产酸最高.在以上的优化条件下,L-谷氨酸产量从72g/L提高到95g/L,提高了31.9%.     

鸟苷补料分批发酵的研究

目的:以枯草芽孢杆菌TA208为出发菌株,研究了补料分批发酵方式下各种参数对鸟苷产量的影响。方法:采用补料分批发酵工艺,利用纸层析法测定发酵液中鸟苷的产量。结果:确定了葡萄糖、酵母粉和次黄嘌呤的最优补料方式,使鸟苷产量达到32.05g/L,较分批发酵方式提高了36.3%。结论:发酵工艺过程控制对发酵生产鸟苷具有重大影响。     

Optimizing the medium compositions for accumulation of the novel FR-008/Candicidin derivatives CS101 by a mutant of Streptomyces sp. using statistical experimental methods

Medium compositions for the production of the novel derivatives of FR-008/Candicidin which was produced by a mutant of Streptomyces sp. FR-008 were optimized using two statistical methods including Plackett–Burman design (P–B), which was applied to find the key ingredients for the best medium composition, and response surface methodology (RSM), which was used to determine the optimal concentrations of these components. Results indicated that peptone, copper sulfate and glycerol had significant effects on the production. Under the proposed optimized conditions, the CS101 experimental yield (191.259 mg/L) closely matched the yield (203.536 mg/L) predicted by the statistical model. The optimization of the medium contributed to 10-fold higher antibiotic production than that of the control. It was first revealed that copper could stimulate FR-008/Candicidin and their derivatives synthesis at an optimal concentration in this paper, moreover, the basis of this phenomenon was also explained by investigating the enhancement of the enzymatic pathways.     

Repeated polyketide synthase modules involved in the biosynthesis of a heptaene macrolide by Streptomyces sp. FR-008

Genes for biosynthesis of a Streptomyces sp. FR-008 heptaene macrolide antibiotic with antifungal and mosquito larvicidal activity were cloned in Escherichia coli using heterologous DNA probes. The cloned genes were implicated in heptaene biosynthiesis by gene replacement. The FR-008 antibiotic contains a 38-membered, poiyketide-derived macrolide ring. Southern hybridization using probes encoding domains of the type i modular erythromycin polyketide synthase (PKS) showed that the Streptomyces sp. FR-008 PKS gene cluster contains repeated sequences spanning c. 105 kb of contiguous DNA; assuming c. 5 kb for each PKS module, this is in striking agreement with the expectation for the 21-step condensation process required for synthesis of the FR-008 carbon chain. The methods developed for transformation and gene replacement in Streptomyces sp. FR-008 make it possible to genetically manipulate polyene macrolide production, and may later lead to the biosynthesis of novel polyene macrolides.     

Selective Removal of Aberrant Extender Units by a Type II Thioesterase for Efficient FR-008/Candicidin Biosynthesis in Streptomyces sp. Strain FR-008

Gene fscTE, encoding a putative type II thioesterase (TEII), was associated with the FR-008/candicidin gene cluster. Deletion of fscTE reduced approximately 90% of the FR-008/candicidin production, while the production level was well restored when fscTE was added back to the mutant in trans. FscTE was unable to compensate for the release of the maturely elongated polyketide as site-directed inactivation of the type I thioesterase (TEI) totally abolished FR-008/candicidin production. Direct biochemical analysis of FscTE in parallel with its homologue TylO from the tylosin biosynthetic pathway demonstrated their remarkable preferences for acyl-thioesters (i.e., propionyl-S-N-acetylcysteamine [SNAC] over methylmalonyl-SNAC and acetyl-SNAC over malonyl-SNAC) and thus concluded that TEII could maintain effective polyketide biosynthesis by selectively removing the nonelongatable residues bound to acyl carrier proteins. Overexpression of FscTE under the strong constitutive ermE*p promoter in the wild-type strain did not suppress FR-008/candicidin formation, which confirmed its substrate specificity in vivo. Furthermore, successful complementation of the fscTE mutant was obtained with fscTE and tylO, whereas no complementation was detected with nonribosomal peptide synthetase (NRPS) TEII tycF and srfAD, reflecting substrate specificities of TEIIs distinctive from those of either polyketide synthases or NRPSs.     

亚硝基胍消除链霉菌FR-008的线性质粒

【目的】利用亚硝基胍(NTG)消除链霉菌FR-008线性质粒以简化其基因组,获得背景清晰的菌株,作为抗生素异源生物合成的底盘细胞。【方法】NTG溶液处理链霉菌FR-008孢子悬液,从存活的诱变株中筛选砷敏感的突变株,再通过脉冲场凝胶电泳(PFGE)检测线性质粒是否被消除;用生测实验定性检测各个线性质粒消除突变株杀念菌素合成的能力,最后通过HPLC定量比较突变株和野生型产生杀念菌素的差异。【结果】从103个诱变株中筛选到3株砷敏感的突变株(10#、59#、115#)。PFGE检测发现它们均丢失了大线性质粒p SSFR1,此外,42#突变株的小线性质粒p SSFR2被消除,在此基础上,第二轮NTG诱变获得了双质粒消除的突变株。大线性质粒p SSFR1消除率约为3%,小线性质粒p SSFR2消除率约为1%。发酵结果显示:10#、115#突变株杀念菌素有效组分III产量分别提高了40%和30%。【结论】首次发现NTG是一种有效消除链霉菌线性质粒的诱变剂,2株大线性质粒消除的突变株杀念菌素的产量得到提高。此方法可以用来消除特定链霉菌菌株中的巨型线性质粒以高效简化其基因组,因而是一种有效的抗生素遗传育种的方法。     

High-yield production of lutein by the green microalga Chlorella protothecoides in heterotrophic fed-batch culture

The green microalga Chlorella protothecoides was grown heterotrophically in batch mode in a 3.7-L fermenter containing 40 g/L glucose and 3.6 g/L urea. In the late exponential phase, concentrated nutrients containing glucose and urea were fed into the culture, in which the nitrogen source was sufficient compared to carbon source. As a result, a maximum cell dry weight concentration of 48 g/L was achieved. This cell dry weight concentration was 28.4 g/L higher than that obtained in batch culture under the same growth conditions. In another cultivation run, the culture was provided with the same initial concentrations of glucose (40 g/L) and urea (3.6 g/L) as in the batch mode, followed by a relatively reduced supply of nitrogen source in the fed-batch mode to establish a nitrogen-limited culture. Such a modification resulted in an enhanced lutein production without significantly lowering biomass production. The cellular lutein content was 0.27 mg/g higher than that obtained in the N-sufficient culture. The improvements were also reflected by higher maximum lutein yield, lutein productivity, and lutein yield coefficient on glucose. This N-limited fed-batch culture was successfully scaled up from 3.7 L to 30 L, and a three-step cultivation process was developed for the high-yield production of lutein. The maximum cell dry weight concentration (45.8 g/L) achieved in the large fermenter (30 L) was comparable to that in the small one (3.7 L). The maintenance of the culture at a higher temperature (i.e., 32 degrees C) for 84 h resulted in a 19.9% increase in lutein content but a 13.6% decrease in cell dry weight concentration as compared to the fed-batch culture (30 L) without such a treatment. The enhancement of lutein production resulted from the combination of nitrogen limitation and high-temperature stress.     

营养条件对光滑球拟酵母发酵生产丙酮酸的影响

丙酮酸是多种氨基酸、维生素及其它有用物质的重要前体,广泛应用于化工、制药及农用化学品工业。能够直接发酵生产丙酮酸的菌种主要有Ａｃｉｎｅｔｏｂａｃｔｅｒ[1],Ｅｎｔｅｒｏｂａｃｔｅｒ[2],Ｅｎｔｅｒｏｃｏｃｃｕｓ[3],Ｅｓｃｈｅｒｉｃｈｉａ[4],Ａｇａｒｉｃｕ?..     

Enhanced spore production ofBacillus thuringiensis by fed-batch culture

Summary Fed-batch culture was carried out to increase cell mass followed by batch culture for spore production ofbacillus thuringiensis. High cell mass obtained by increasing the feeding glucose concentration in constant fed-batch culture which supported fast cell growth resulted in good sporulation during subsequent batch culture, and the maximum cell mass of 72.6 g/L and spore concentration of 1.25×10¹⁰ spores/mL could be obtained.     

Production of nattokinase by high cell density fed-batch culture of Bacillus subtilis

Bacillus subtilis was cultivated to high cell density for nattokinase production by pH-stat fed-batch culture. A concentrated mixture solution of glucose and peptone was automatically added by acid-supplying pump when culture pH rose above high limit. Effect of the ratio of glucose to peptone in feeding solution was investigated on cell growth and nattokinase production by changing the ratio from 0.2 to 5 g glucose/g peptone. The highest cell concentration was 77 g/L when the ratio was 0.2 g glucose/g peptone. Cell concentration decreased with increasing the ratio of glucose to peptone in feeding solution, while the optimum condition existed for nattokinase production. The highest nattokinase activity was 14,500 unit/mL at a ratio of 0.33 g glucose/g peptone, which was 4.3 times higher than that in batch culture.