皮状丝孢酵母B3利用木薯淀粉发酵生产微生物油脂

对皮状丝孢酵母B3以木薯淀粉水解液为碳源发酵生产微生物油脂培养条件进行了优化,并在2 L发酵罐中对菌体生长和油脂积累进行了考察。摇瓶实验表明,木薯淀粉水解液的浓度高于90 g/L时不利于菌体的生长和油脂积累,皮状丝孢酵母B3发酵生产微生物油脂的最适氮源及其浓度、最适C/N比和pH分别为酵母提取物3.0 g/L、116、6.0,在此条件下培养144 h菌体生物量、油脂产量和油脂含量分别达到15.2 g/L、6.22 g/L和40.9％;在2 L发酵罐中分批发酵44 h后菌体生物量、油脂产量和油脂含量分别达28.7 g/L、12.27 g/L和42.8％。以皮状丝孢酵母B3所产油脂制备生物柴油,其主要组成包括棕榈酸甲酯、硬脂酸甲酯、油酸甲酯、亚油酸甲酯等,且理化特性符合相关国家标准,可作为一种有潜力的化石燃料替代品。     

谷氨酸对花生四烯酸产生菌被孢霉发酵的影响

研究了不同浓度谷氨酸对被孢霉生产花生四烯酸的影响,发现当加入谷氨酸浓度为0.8g/L时总油脂和花生四烯酸产量达最高,选择0.8g/L谷氨酸进行花生四烯酸产生菌被孢霉发酵动力学研究的结果表明,在培养基中加入0.8g/L谷氨酸可以明显促进被孢霉的生长,加速基质代谢,提高单位被孢霉中的油脂和花生四烯酸产量,尤其在发酵第7d时生物量、油脂和花生四烯酸产量达到最大,分别为24.43、9.21、1.41g/L,分别是对照组第7d所得的1.13、1.15和1.69倍。     

深黄被孢霉利用不同碳源产油脂比较

本研究主要探讨深黄被孢霉M2菌株对生物质全糖的利用,考察其碳源同化能力、不同碳源下产脂情况以及对玉米皮渣的利用能力。研究结果表明,M2菌株能够利用葡萄糖、木糖、阿拉伯糖和甘露糖进行生长和油脂积累。M2菌株以6%糖浓度的玉米皮渣水解液为底物发酵培养,油脂微生物生物量达18.2g/L,干菌体油脂含量45.7%,单位体积发酵液油脂产量为8.3g/L。     

高山被孢霉产花生四烯酸发酵条件的研究

通过一株高山被孢霉M_(20)(Mortierella alpina)产花生四烯酸的摇瓶发酵研究,确定了其最佳发酵培养基组成及最适摇瓶发酵工艺条件。摇瓶实验确定的最佳培养基组成为(g/L):玉米粉水解液葡萄糖150,酵母粉15,KH_2PO_4 3.0,NaNO_3 3.0,MgSO_4·7H_2O 0.5。最佳发酵工艺条件为:初始pH6.5,装液量为50ml/500ml摇瓶,摇床转速150r/min,温度在菌体生长前三天控制在25℃培养,以后调至20℃培养。在此条件下,发酵培养被孢霉的生物量、菌体总油脂及花生四烯酸分别高达35.5g/L、13.2g/L及2.2g/L,在15L及1000L自动机械搅拌罐进行发酵试验,AA产量分别高达1.86g/L及1.70g/L。     

通气量对气升式反应器培养高山被孢霉生产花生四烯酸的影响

高山被孢霉具有很强的积累花生四烯酸(ARA)的能力,通过对30 L气升式反应器发酵过程的通气量进行调控,结果发现:通气量对高山被孢霉菌体生长、形态及ARA合成具有显著影响。中等大小的球形菌丝形态有利于菌体持续生长和油脂积累,ARA占总油脂的含量最高,而羽状菌丝形态菌体中总油脂含量和ARA含量均小于球形菌丝形态菌体中的含量。通气量为1.0 vvm(1 vvm为每分钟通气量与罐体实际料液体积之比)时有利于菌体保持良好形态和生长,通气量为1.4 vvm有利于发酵对数期后(72~168 h)ARA的积累。提出一种两阶段通气量控制策略,在气升式发酵罐中高山被孢霉的菌丝形态得到显著改善,ARA产量达到4.72 g/L,比对照提高了40.1%。     

响应面法优化木薯淀粉发酵生产单细胞油脂工艺

采用响应面分析法对发酵性丝孢酵母菌株以木薯淀粉水解液为原料合成微生物油脂的培养条件进行优化。首先利用Plackett-Burman试验设计确定影响油脂产量的主要因素,在此基础上再利用Box-Behnken试验设计及响应面分析法对其进行条件优化。结果表明,发酵温度、C/N、pH对油脂产量具有显著影响,产油脂的最佳发酵条件为:发酵温度28.78°C、C/N 126.18、pH 6.69,油脂产量达到14.88g/L,比优化前提高了28.6%。同时,气相色谱分析表明,微生物油脂脂肪酸组成成分主要包括棕榈酸、硬脂酸、油酸、亚油酸酯等,是优良的生物柴油制备原料。     

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。     

产紫杉醇内生真菌枝状枝孢霉MD2的发酵条件优化

[目的]通过优化内生真菌枝状枝孢霉MD2的发酵条件,提高10-去乙酰巴卡亭Ⅲ (10-DAB)和紫杉醇(Taxol)的产量.[方法]采用单因素试验分析不同的培养基初始pH值、培养温度、摇床转速和培养时间对10-DAB和紫杉醇产量的影响,优化枝状枝孢霉MD2的培养条件;以YES为基本培养基,采用单因素试验和正交试验分析添加苯甲酸钠、苯丙氨酸、丝氨酸和甘氨酸4种前体物对10-DAB和紫杉醇产量的影响,优化枝状枝孢霉MD2的培养基组分.[结果]优化后发酵条件为:在初始pH为5.0的300 mL YES培养基中,添加15 mg/L苯甲酸钠、25 mg/L苯丙氨酸、5 mg/L丝氨酸、15 mg/L甘氨酸,接种1 mL枝状枝孢霉MD2的孢子悬液(107-10s个孢子/mL),28.0℃、220 r/min发酵培养12d.在此条件下,枝状枝孢霉MD2的生物量、10-DAB和紫杉醇的产量分别为15.5 g/L、471.5 μg/L和569.5 μg/L,与初始发酵条件相比,分别提高了1.3、3.6和3.4倍.[结论]首次获得了枝状枝孢霉MD2生产10-DAB和紫杉醇的较适摇瓶发酵条件,可为进一步放大发酵培养提供参考.     

高产PUFAs深黄被孢霉菌株的筛选

以深黄被孢霉(Mortierella isabellina As3.3410)为出发菌株,经微波诱变和紫外诱变,乙酰水杨酸与低温(15℃)相结合的筛选方法,获得1株高产多不饱和脂肪酸菌株A35-4,其生物量为17.9 g/L,油脂含量为67.8%,油脂产量为12.12 g/L,PUFAs含量为20.3%,PUFAs产量为2.46 g/L,上述指标比原始菌株A0分别增加32.6%、49.8%、98.69%、14.0%和125.7%。连续斜面传代培养证实该菌株具有较好的遗传稳定性。本研究为直接利用该菌株生产PUFAs以及克隆高效PUFAs相关基因,创造高含PUFAs转基因植物材料奠定基础。     

双液相体系强化氧传递促进微生物油脂生产

文中通过添加氧载体正十二烷进行双液相发酵来提高发酵性丝孢酵母利用木薯淀粉水解液生产微生物油脂的产量。结果表明,在摇瓶发酵液中添加氧载体,能明显缓解发酵过程中的氧限制程度。在2 L发酵罐中添加1%正十二烷进行双液相高密度发酵,其发酵生物量和油脂产量分别达到101.2 g/L和50.28 g/L。气相色谱分析表明,添加了氧载体发酵的微生物油脂中含有更高的饱和脂肪酸含量。     

采用玉米秸秆水解糖和玉米浆发酵生产丁二酸

研究了以玉米秸秆水解糖为碳源,不同氮源条件下琥珀酸放线杆菌Actinobacillus succinogenesSF-9的丁二酸发酵产酸能力。结果表明玉米浆可以替代酵母膏作为丁二酸发酵的廉价氮源。厌氧摇瓶丁二酸发酵单因素试验,得到在初糖浓度50 g/L时,玉米浆的较佳用量为20 g/L。在5 L搅拌罐上,考察了不同初始玉米秸秆水解糖浓度对A.succinogenes SF-9发酵生产丁二酸的影响,结果显示高初始秸秆糖浓度对琥珀酸放线杆菌的生长有抑制作用。采用补料分批发酵,发酵60 h丁二酸的产量达到42.7g/L,丁二酸产率82.7%,生产强度0.81 g/(L·h)。丁二酸的产量和生产强度较分批发酵有明显提高。     

Acetate production from whey lactose using co-immobilized cells of homolactic and homoacetic bacteria in a fibrous-bed bioreactor

Acetate was produced from whey lactose in batch and fed-batch fermentations using co-immobilized cells of Clostridium formicoaceticum and Lactococcus lactis. The cells were immobilized in a spirally wound fibrous sheet packed in a 0.45-L column reactor, with liquid circulated through a 5-L stirred-tank fermentor. Industrial-grade nitrogen sources, including corn steep liquor, casein hydrolysate, and yeast hydrolysate, were studied as inexpensive nutrient supplements to whey permeate and acid whey. Supplementation with either 2.5% (v/v) corn steep liquor or 1.5 g/L casein hydrolysate was adequate for the cocultured fermentation. The overall acetic acid yield from lactose was 0.9 g/g, and the productivity was 0.25 g/(L h). Both lactate and acetate at high concentrations inhibited the homoacetic fermentation. To overcome these inhibitions, fed-batch fermentations were used to keep lactate concentration low and to adapt cells to high-concentration acetate. The final acetate concentration obtained in the fed-batch fermentation was 75 g/L, which was the highest acetate concentration ever produced by C. formicoaceticum. Even at this high acetate concentration, the overall productivity was 0.18 g/(L h) based on the total medium volume and 1.23 g/(L h) based on the fibrous-bed reactor volume. The cells isolated from the fibrous-bed bioreactor at the end of this study were more tolerant to acetic acid than the original culture used to seed the bioreactor, indicating that adaptation and natural selection of acetate-tolerant strains occurred. This cocultured fermentation process could be used to produce a low-cost acetate deicer from whey permeate and acid whey.     

分批补料对木糖发酵生产乙醇的影响

以树干毕赤酵母为发酵菌种,纯木糖为发酵底物,通过分批补料来提高糖利用率以及乙醇得率。结果表明,在24h内,最佳初始木糖浓度为80g/L,在28h的发酵周期中,可以将木糖浓度提高至90g/L,在32h发酵周期内可以将木糖浓度提高至100g/L。通过分批补料,乙醇浓度得到明显提高。当总糖浓度分别为80g/L、90g/L时,24h发酵周期内,分批补料次数以1次为宜,乙醇浓度分别达30.95g/L、32.60g/L,相比于不补料即一次性投料,乙醇浓度分别提高了9.36%、9.18%。总糖浓度100g/L,28h发酵周期内,补料2次效果最佳,乙醇浓度达37.49g/L,比一次性投料下提高了10.36%,较一次性投料达到相同发酵效果缩短了4h。     

Fed-batch sorbose fermentation using pulse and multiple feeding strategies for productivity improvement

Microbial oxidation of D-sorbitol tol-sorbose byAcetobacter suboxydans is of commercial importance since it is the only biochemical process in vitamin C synthesis. The main bottleneck in the batch oxidation of sorbitol to sorbose is that the process is severely inhibited by sorbitol. Suitable fed-batch fermentation designs can eliminate the inherent substrate inhibition and improve sorbose productivity. Fed-batch sorbose fermentations were conducted by using two nutrient feeding strategies. For fed-batch fermentation with pulse feeding highly concentrated sorbitol (600 g/L) along with other nutrients were fed intermittently in four pulses of 0.5 liter in response to the increased DO signal. The fed-batch fermentation was over in 24 h with a sorbose productivity of 13.40 g/L/h and a final sorbose concentration of 320.48 g/L. On the other hand, in fed-batch fermentation with multiple feeds, two pulse feeds of 0.5 liter nutrient medium containing 600 g/L sorbitol was followed by the addition of 1.5 liter nutrient medium containing 600 g/L sorbitol at a constant feed rate of 0.36 L/h till the full working capacity of the reactor. The fermentation was completed in 24 h with an enhanced sorbose productivity of 15.09 g/L/h and a sorbose concentration of 332.60 g/L. The sorbose concentration and productivity obtained by multiple feeding of nutrients was found to be higher than that obtained by pulse feeding and was therefore a better strategy for fed-batch sorbose fermentation.     

氮源种类及溶氧水平对锁掷酵母产类胡萝卜素组分的影响

在锁掷酵母（Sporidioboluspararoseus）发酵产类胡萝卜紊的过程中,发酵产物中类胡萝卜紊种类繁多,而且性质相似,加大了不同色素分离纯化的难度。为定向积累不同种类的类胡萝卜素,以本实验室保藏锁挪酵母JD-2为出发菌,研究了氮源种类和浓度及溶氧对锁掷酵母产类胡萝卜素的影响,并在7L发酵罐中进行了补料分批发酵试验。发现培养基中同时添加有机氮源和无机氮源且溶氧控制较低（5％）时有利于β-胡萝卜素的大量积累,最佳有机氮源和无机氮源分别为玉米浆（20g／L）、硫酸铵（5g／L）。补料分批发酵时β-胡萝卜素产量达到31．28mg／L,红酵母烯12．38mg／L。培养基中只添加有机氮源且相对溶氧控制相对较高（30％）时有利于红酵母烯的大量积累,最佳有机氮源为酵母膏（20g／L）。补料分批发酵时红酵母烯产量达到38．96mg／L,8．胡萝卜素12．36mg／L。     

A two-stage fed-batch heterotrophic culture of Chlorella protothecoides that combined nitrogen depletion with hyperosmotic stress strategy enhanced lipid yield and productivity

In this study, the influences of major nutrients on cell growth and lipid production were investigated in heterotrophic culture of Chlorella protothecoides. The results demonstrated that phosphorus depletion had no effect on lipid accumulation but restricted cell growth; however, nitrogen depletion could enhance lipid accumulation thus benefiting lipid production. Furthermore, the effects of glucose inhibition were comparatively investigated with osmotic stress, showing that the effects of glucose inhibition were similar to the effect of osmotic stress at equivalent osmotic pressures only if the glucose concentration was less than 100 g/L, otherwise the effects of glucose inhibition became much stronger than osmotic stress. Interestingly, it was found that a specific hyperosmotic stress could significantly enhance lipid accumulation, thus providing a new stress strategy for efficient lipid production. Finally, a novel two-stage fed-batch culture consisting of a growth phase and a lipid accumulation phase with nitrogen depletion and hyperosmotic stress was proposed, yielding a final lipid productivity of 177.3 mg/L/h with a very high lipid yield of 207.0 mg/g glucose and lipid content of 39.2% after 180 h culture, which were 1.60, 1.79 and 1.92-fold of those obtained in one-stage fed-batch culture without stress phase, respectively.     

Study of mycelial growth and bioactive polysaccharide production in batch and fed-batch culture of Grifola frondosa

The fermentation of Grifola frondosa was investigated in the shake flasks and a 5-L jar fermenter in batch and fed-batch modes. In the shake-flask experiments, the preferable mycelial growth and exopolysaccharide (EPS) production was observed at relatively low pH; maltose and glucose were preferred carbon sources for high mycelial production. The EPS was doubled after 13 d of cultivation when glucose was increased from 2% to 4%. Yeast extract (YE) (0.4%) in combination with corn steep powder (CSP) (0.6%) and YE (0.8%) in combination with CSP (1.2%) were preferred nitrogen sources for high mycelial production and EPS production, respectively. All plant oils tested significantly stimulate cell growth of G. frondosa but they failed to enhance EPS production. The EPS products usually consisted of two fractions of different molecular sizes varied by the plant oils used. The fed-batch fermentation by glucose feeding was performed when the glucose concentration in the medium was lower than 0.5% (5g/L), which greatly enhanced the accumulation of mycelial biomass and EPS; the mycelial biomass and EPS were 3.97g/L and 1.04g/L before glucose feeding, which reached 8.23g/L and 3.88g/L at 13 d of cultivation. In contrast, the mycelial biomass and EPS in the batch fermentation were 6.7g/L and 3.3g/L at 13 d of cultivation.     

Production of mannitol by Lactobacillus intermedius NRRL B-3693 in fed-batch and continuous cell-recycle fermentations

Improved fermentation processes were developed for the production of mannitol by a heterofermentative lactic acid bacterium (Lactobacillus intermedius NRRL B-3693). A fed-batch fermentation protocol overcame limitations caused by high substrate concentrations. The process was developed using corn steep liquor and glucose as inexpensive industrial nutrient sources, supplemented with a small amount of soy peptone and manganese. The fed-batch process resulted in a concentration of 176 ± 0.5 g mannitol from 184 ± 0 g fructose and 92 ± 0.1 g glucose per L of final fermentation broth in 30 h with a volumetric productivity of 5.9 g/(L h). Further increases in volumetric productivity of mannitol were obtained in a continuous cell-recycle fermentation process that reached more than 40 g/(L h), despite reduced mannitol levels of 78–98 g/L and residual substrate of 10–20 g/L. This is the first report of such a high volumetric productivity of mannitol by a heterofermentative lactic acid bacterium.     

利用克雷伯肺炎杆菌限制性底物发酵生产1，3-丙二醇

研究了克雷伯肺炎杆菌（Klebsiella pneumoniae）批式流加发酵生产1,3-丙二醇的发酵工艺,根据1,3-丙二醇的生产和菌体生长相关的特点,采用营养基质限制性流加的发酵工艺,通过控制氮源氯化铵以保持细胞稳定生长。结果表明：过低的氮源浓度,细胞生长受到限制,影响产物1,3-PD的合成;过高的氮源浓度,细胞比生长速率增加,但1,3-PD关于消耗甘油的得率降低,用于生长和维持代谢所消耗的甘油量增加。以0.41 g/(L·h)的氮源流加速率,残余氯化铵浓度在0.1 g/L时,转化率和生产强度最高。发酵25 h～28 h后,1,3-丙二醇最终浓度达到52.03 g/L,生产强度为2.04 g/(L·h),相对于甘油的摩尔转化率为0.66,分别比氮源限制前提高了28.0 ％、35.1 ％及29.4 ％。通过限制性流加氯化铵,控制细胞的比生长速率,使底物甘油有效转变为发酵的目标产物1,3-PD,有效实现产物1,3-PD的高生产强度以及对甘油的高转化率。     

以糙米为原料流加L-蛋氨酸的S-腺苷蛋氨酸发酵优化

研究了S-腺苷甲硫氨酸(SAM)高产菌啤酒酵母S-W55的廉价培养基及分批补料发酵过程优化.对啤酒酵母S-W55生长和SAM产量影响最为重要的糙米水解糖和酵母粉进行了响应面优化,得到了最优化的配方为糙米水解糖51.4g/L、酵母粉4.74g/L,此条件下啤酒酵母S-W55的SAM产量达2.61 g/L.不同分批补料发酵...