古尼拟青霉液体发酵液有机粗提物产量的研究

目的:培养基成分对古尼拟青霉液体发酵液有机粗提物产量的影响。方法:采用正交设计方法,考察古尼拟青霉液体发酵培养基3种组分马铃薯、葡萄糖和蛋白胨对其菌丝体与发酵液有机粗提物量的影响。结果:在马铃薯300g/L,蛋白胨8g/L,葡萄糖30g/L时,古尼拟青霉液体发酵液有机粗提物产量可达到136.3mg/L。结论:培养基成分对古尼拟青霉液体发酵有机粗提物产量有显著影响,该文结果对指导古尼拟青霉液体的深层发酵具有参考价值。     

产生物表面活性剂芽孢杆菌培养条件的优化

为了提高生物表面活性剂的表面活性,通过单因素及正交试验对已筛选的产生物表面活性剂芽孢杆菌的培养基及培养条件进行了优化,优化后的培养基成分为可溶性淀粉20 g/L,氯化铵2 g/L,KH2PO46 g/L,K2HPO42 g/L,MgSO4.7H2O 0.3 g/L,NaCl 2 g/L,CaCl20.08 g/L,EDTA 0.4 g/L。培养条件为4%接种量,种龄16 h,初始pH7,培养温度37℃,摇床转速160 r/min,发酵48 h。优化发酵条件后,发酵液表面张力由初始67.5 mN/m降低至24.8 mN/m,生物表面活性剂产量达到1.08 g/L。     

1,3-丙二醇产生菌的诱变育种及培养基优化

以实验室自然筛选的克雷伯氏杆菌(Klebsiella sp.)为出发株,采用紫外诱变及亚硝基胍和超声波协同处理获得一株1,3-丙二醇高产突变株。在摇瓶发酵中,其产1,3-丙二醇产量由17.39 g/L提高到24.11 g/L,提高38.64%。变异株经10次传代培养,发酵能力稳定。对发酵培养基成分进行了优化,优化后1,3-丙二醇产量为30.05g/L,为优化前的1.25倍。     

珍稀药用真菌——樟芝深层发酵培养条件的优化

对樟芝深层发酵培养基进行了筛选,并在此基础上对发酵条件进行了优化。以樟芝深层发酵菌丝体三萜产量为主要目标产物,确定发酵培养条件为:40g/L葡萄糖,6g/L豆饼粉,1g/L K_2HPO_4,0．5g/L MgSO4,VB_1 100mg/L,自然pH,接种量为20%,装液量为100mL/250mL三角瓶,转速100r/min,26℃恒温培养6d,胞内三萜产量达15．25mg/100mL发酵液。     

一株高产Monacolin K紫红曲霉菌株筛选、鉴定及发酵条件优化

为从天然发酵红曲米中分离的30株红曲霉菌株中筛选高产MonacolinK的菌株,并对其产MonacolinK的发酵条件进行优化。实验采用高效液相色谱法(HPLC)筛选到9株具有产MonacolinK能力的红曲霉菌株,其中以编号ZX26的菌株产MonacolinK能力最高,发酵液中Monacolin K产量达到107.6mg/L,并且产MonacolinK能力具有良好的稳定性。微生物形态学结合ITS基因同源性分析结果表明,编号ZX26菌株为紫红曲霉。进一步采用单因素试验和正交试验法优化紫红曲霉ZX26产MonacolinK的发酵条件,结果表明在培养基组分为葡萄糖70g/L,牛肉膏15g/L,NaNO32g/L,MgSO4·7H2O0.5g/L,KH2PO41.5g/L时,其最优发酵条件为:发酵初始pH4.0,接种量为7%,培养温度30℃,发酵10天,在此条件下,紫红曲霉ZX26发酵液中MonacolinK产量达到271.36mg/L,相对于培养条件优化前MonacolinK产量提高152.19%,经验证此培养条件下MonacolinK产量最佳。     

解脂耶氏酵母诱变育种及发酵产α-酮戊二酸条件优化

对具有发酵产α-酮戊二酸能力的解脂耶氏酵母(Yarrowia Lipolytica)ZY-4进行了紫外诱变和NTG诱变育种,筛选得到产量提高的突变株,并对突变株的发酵培养基进行了优化,结果表明,紫外诱变和NTG诱变后筛选到的突变株分别比原始出发菌株产量提高了67.8%和110%。优化后发酵培养基成分为甘油8%,氯化铵5.0 g/L,硫胺素1.0μg/L,磷酸二氢钾1.0 g/L,七水硫酸镁0.5 g/L,培养基优化后α-酮戊二酸产量比原始出发菌株提高了232.4%。     

小克银汉霉γ-亚麻酸高产菌株的快速筛选和发酵条件研究

以小克银汉霉C0为出发菌株,经过5-氟尿嘧啶和紫外线复合诱变,采用抗失水苹果酰肼与抗低温(15℃)相结合的筛选方法,获得一株生产性能比出发菌株显著提高的突变株C23。采用5L全自动发酵罐对小克银汉霉C23发酵生产γ-亚麻酸的pH值控制和补料工艺进行研究,发现将发酵液pH值维持在5.5,当发酵进行到60h、84h、108h时,分别补糖15g/L,发酵192h后收获,结果生物量、油脂产量和γ-亚麻酸产量分别达到49.88g/L、21.93g/L、2.69g/L。     

利用核糖体工程选育丙酮丁醇菌提高丁醇产量

利用核糖体工程技术对丙酮丁醇梭菌Clostridium acetobutylicum L7进行诱变筛选,以获得丁醇高产菌株。使用链霉素诱变C.acetobutylicum L7并结合设计的平板转接逐次提高链霉素浓度的筛选路线,获得丁醇产量较高的菌株S3。结果表明,S3丁醇产量为(12.48±0.03)g/L,乙醇产量为(1.70±0.07)g/L,相对于原始菌分别提高了11.2%及50%;丁醇/葡萄糖转化率由原始菌的0.19提高到0.22,丁醇生产率达到0.24 g/(L.h),相比提高30.5%;耐受丁醇浓度由原始菌的12 g/L提高到14 g/L;发酵液粘度下降到4 mPa/s,同比降低了60%,利于后续分离工作的进行,降低发酵成本。进一步研究工作表明,S3菌株遗传稳定性良好。因此,核糖体工程技术是一种选育丁醇高产菌株的有效方法。     

钝齿棒杆菌中异源表达N-乙酰鸟氨酸脱乙酰基酶合成L-鸟氨酸的研究

目的:对一株产鸟氨酸的钝齿棒杆菌Corynebacterium crenatum SYPA5-5/△proB/△argF(SYPO-1)进行代谢工程改造,筛选不同细菌来源的N-乙酰鸟氨酸脱乙酰基酶在大肠杆菌中克隆与表达,纯化后对其进行酶学性质的比较;将黏质沙雷氏菌Serratia marcescens Y213来源的Smarg E基因编码的N-乙酰鸟氨酸脱乙酰基酶在L-鸟氨酸生产菌株C.crenatum SYPO-1中过量表达,进一步提高L-鸟氨酸的产量。方法:通过利用pDXW10穿梭质粒对不同来源的N-乙酰鸟氨酸脱乙酰化酶进行克隆表达和酶学性质比较,选择性质最优来源的N-乙酰鸟氨酸脱乙酰基酶编码基因Smarg E在产L-鸟氨酸重组钝齿棒杆菌中表达,考察重组菌株发酵过程中参数的变化。结果:来源于S.marcescens Y213的N-乙酰鸟氨酸脱乙酰基酶比酶活最高为798.98U/mg,最适pH为7,最适温度为37℃,0.1mmol/L的Mg~(2+)、Li~+、Mn~(2+)促进酶的比酶活提高了50%;在钝齿棒杆菌中表达N-乙酰鸟氨酸脱乙酰基酶酶活达到128.4U/ml,显著提高了钝齿棒杆菌中胞内乙酰基循环水平;5L发酵罐发酵重组菌株96h,L-鸟氨酸的产量达到38.5g/L,比出发菌株,L-鸟氨酸的产量提高了33.2%,产率达0.401g/(L·h)。结论:筛选出最佳来源的N-乙酰鸟氨酸脱乙酰基酶,在鸟氨酸生产菌株C.crenatum(SYPO-1)中过量表达,可以促进鸟氨酸的前体物质N-乙酰鸟氨酸的快速消耗,实现鸟氨酸的积累。     

D-核糖发酵条件研究

对枯草芽孢杆菌Bacillus subtilis ptn15-1的发酵条件进行优化。采用优化后的培养基对发酵液的pH、发酵温度、摇床转速、接种量、装液量等进行单因素实验。确定发酵最适发酵条件为：pH7.0,发酵温度37℃;摇床转速180r/min,接种量10%,300mL三角瓶装30mL发酵液,发酵时间为68h。在此条件下,该菌的D-核糖产量从31.7g/L提高到43.1g/L,提高了35.9%。     

Acetone-butanol-ethanol fermentation and isoflavone extraction using kudzu roots

The economics of Acetone-butanol-ethanol (ABE) fermentation is greatly affected by raw materials, and the use of readily available starchy materials from marginal farming lands could be a viable option for reducing costs. Kudzu, a rapidly growing perennial leguminous vine, has been planted on marginal farming land and widely distributed in Asia and America. This study investigated ABE fermentation by C. acetobutylicum ATCC 824 using kudzu roots and isoflavone extraction from kudzu fermentation residue (KFR). The kudzu roots could be used as a sole substrate for ABE fermentation without nutritional supplements. Batch culture containing 140 g kudzu/L produced 17.99 ± 1.08 g/L solvent (ABE), including 11.20 ± 0.79 g/L butanol, 5.54 ± 0.20 g/L acetone, and 1.15 ± 0.09 g/L ethanol, with a productivity of 0.19 g/(L/h) and a yield of 0.33 g solvent/g sugar after 96 h of fermentation. Isoflavone yield extracted from KFR was 1.90/100 g KFR, approximately 48% higher compared with that extracted from raw kudzu. A kinetic analysis of the extraction process showed that both the isoflavone yield and the extraction rate obtained from KFR were higher than the corresponding values obtained from raw kudzu. These results indicate that kudzu may provide a new potential raw material for ABE production and the process of ABE fermentation integrated with isoflavone extraction may provide a new way to reduce fermentable substrate costs.     

丙酮酸发酵过程中光滑球拟酵母过程功能的强化

对不同葡萄糖浓度下光滑球拟酵母分批发酵生产丙酮酸的动力学模型分析发现, 葡萄糖浓度是影响光滑球拟酵母发酵生产丙酮酸过程功能的关键因素。在发酵初始阶段, 低浓度葡萄糖可维持较高的菌体比生长速率; 对数生长中前期, 葡萄糖快速进料使菌体浓度接近最大值, 并实现碳流从菌体生长转向丙酮酸积累; 对数生长后期葡萄糖浓度控制在33.4 g/L以维持高丙酮酸对葡萄糖产率系数 (0.71 g/g)。采用奇异控制的葡萄糖流加方式, 在7 L发酵罐上控制不同发酵阶段葡萄糖浓度处于最佳水平以强化光滑球拟酵母过程功能, 丙酮酸产量 (83.1 g/L)、产率 (0.621 g/g)、生产强度[1.00 g/(L·h)]与分批发酵对比, 分别提高了21.3%、21.6%和29.9%。     

Extractive fermentation for butyric acid production from glucose by Clostridium tyrobutyricum

A novel extractive fermentation for butyric acid production from glucose, using immobilized cells of Clostridium tyrobutyricum in a fibrous bed bioreactor, was developed by using 10% (v/v) Alamine 336 in oleyl alcohol as the extractant contained in a hollow-fiber membrane extractor for selective removal of butyric acid from the fermentation broth. The extractant was simultaneously regenerated by stripping with NaOH in a second membrane extractor. The fermentation pH was self-regulated by a balance between acid production and removal by extraction, and was kept at approximately pH 5.5 throughout the study. Compared with conventional fermentation, extractive fermentation resulted in a much higher product concentration (>300 g/L) and product purity (91%). It also resulted in higher reactor productivity (7.37 g/L. h) and butyric acid yield (0.45 g/g). Without on-line extraction to remove the acid products, at the optimal pH of 6.0, the final butyric acid concentration was only approximately 43.4 g/L, butyric acid yield was 0.423 g/g, and reactor productivity was 6.77 g/L. h. These values were much lower at pH 5.5: 20.4 g/L, 0.38 g/g, and 5.11 g/L. h, respectively. The improved performance for extractive fermentation can be attributed to the reduced product inhibition by selective removal of butyric acid from the fermentation broth. The solvent was found to be toxic to free cells in suspension, but not harmful to cells immobilized in the fibrous bed. The process was stable and provided consistent long-term performance for the entire 2-week period of study.     

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。     

Production of L(+)-lactic acid from glucose and starch by immobilized cells of Rhizopus oryzae in a rotating fibrous bed bioreactor

A rotating fibrous-bed bioreactor (RFB) was developed for fermentation to produce L(+)-lactic acid from glucose and cornstarch by Rhizopus oryzae. Fungal mycelia were immobilized on cotton cloth in the RFB for a prolonged period to study the fermentation kinetics and process stability. The pH and dissolved oxygen concentration (DO) were found to have significant effects on lactic acid productivity and yield, with pH 6 and 90% DO being the optimal conditions. A high lactic acid yield of 90% (w/w) and productivity of 2.5 g/L.h (467 g/h.m(2)) was obtained from glucose in fed-batch fermentation. When cornstarch was used as the substrate, the lactic acid yield was close to 100% (w/w) and the productivity was 1.65 g/L.h (300 g/h.m(2)). The highest concentration of lactic acid achieved in these fed-batch fermentations was 127 g/L. The immobilized-cells fermentation in the RFB gave a virtually cell-free fermentation broth and provided many advantages over conventional fermentation processes, especially those with freely suspended fungal cells. Without immobilization with the cotton cloth, mycelia grew everywhere in the fermentor and caused serious problems in reactor control and operation and consequently the fermentation was poor in lactic acid production. Oxygen transfer in the RFB was also studied and the volumetric oxygen transfer coefficients under various aeration and agitation conditions were determined and then used to estimate the oxygen transfer rate and uptake rate during the fermentation. The results showed that the oxygen uptake rate increased with increasing DO, indicating that oxygen transfer was limited by the diffusion inside the mycelial layer.     

萃取耦合技术对玉米秸秆水解液发酵产丁醇的影响

本研究以玉米秸秆水解液为原料,通过萃取发酵技术生产燃料丁醇,以提高丁醇产量,降低生产成本。通过对萃取剂的筛选与条件优化,确定纤维丁醇发酵的萃取剂为油醇,添加时间为发酵0 h,添加比例为1:1 (V/V)。该条件下发酵32 g/L糖浓度的玉米秸秆水解液,丁醇和总溶剂产量分别为3.28 g/L和4.72 g/L,比对照分别提高958.1%和742.9%。以D301树脂脱毒后5%总糖浓度的玉米秸秆水解液进行丁醇萃取发酵,丁醇和总溶剂产量分别达到10.34 g/L和14.72 g/L,发酵得率为0.31 g/g,与混合糖发酵结果相当。研究结果表明萃取发酵技术能够显著提高原料的利用率和丁醇产量,为纤维丁醇工业化生产提供了技术支撑。     

茄尼醇转化高产辅酶Q10菌株的分离鉴定与发酵条件的研究

采用以异戊二烯为唯一碳源的选择性平板筛选模型,从钱塘江沿岸杭州市九堡段土壤中新筛选到一株产辅酶Q10的细菌菌株E03,经形态、生理生化、Biolog碳源利用试验和16S rDNA序列分析,确定E03属于鞘氨醇属(Sphingomonas sp.),命名为Sphingomonas sp.ZUTE03.摇瓶试验确定了该菌发酵生产辅酶Q10的最佳碳源为葡萄糖15 g/L,氮源为硫酸铵10 g/L,初始pH8.0,发酵温度25℃,并考察了该菌转化茄尼醇产辅酶Q.0的发酵工艺,以合适溶剂为溶解体系,于发酵培养基中摇床培养12 h后,加入终浓度为0.75 g/L的茄尼醇粗品,转化12 h,辅酶Q10产值可达96.88 mg/L.     

Robust production of gamma-amino butyric acid using recombinant Corynebacterium glutamicum expressing glutamate decarboxylase from Escherichia coli

Gamma-amino butyric acid (GABA) is a component of pharmaceuticals, functional foods, and the biodegradable plastic polyamide 4. Here, we report a simple and robust system to produce GABA from glucose using the recombinant Corynebacterium glutamicum strain GAD, which expresses GadB, a glutamate decarboxylase encoded by the gadB gene of Escherichia coli W3110. As confirmed by HPLC analysis, GABA fermentation by C. glutamicum GAD cultured at 30°C in GABA Production 1 (GP1) medium containing 50 g/L glucose without the addition of glutamate yielded 8.07 ± 1.53 g/L extracellular GABA after 96 h. Addition of 0.1mM pyridoxal 5'-phosphate (PLP) was found to enhance the production of GABA, whereas Tween 40 was unnecessary for GABA fermentation. Using the optimized GABA Production 2 (GP2) medium, which contained 50 g/L glucose and 0.1mM PLP, fermentation was performed in a flask at 30°C with 10% (v/v) seed culture of C. glutamicum GAD. GABA was produced in the culture supernatant with a yield of 12.37 ± 0.88 g/L after 72 h with a space-time yield of 0.172 g/L/h, which is the highest yield obtained to date for GABA from fermentation with glucose as a main carbon source.