生物转化高浓度甘油生产1,3-二羟基丙酮及分批发酵动力学

以生物柴油生产的高浓度副产物甘油为唯一碳源筛选甘油高耐受性1,3-二羟基丙酮(DHA)高产菌株,运用响应面与正交试验优化菌株产DHA条件,提高DHA产量。分子生物学鉴定表明:筛选的高产DHA菌种G40为芽胞杆菌属(Bacillus)菌株,DHA产量为29.46g/L。响应面分析和正交试验优化后,在甘油224.22g/L、K_2HPO_41.60g/L、NaCl0.5g/L、KH_2PO_40.5g/L、(NH_4)_2SO_40.5g/L、酵母膏1.60g/L和pH7.2、35℃、200r/min的条件下,G40菌株发酵60h产生DHA86.84g/L,比优化前提高了194.8%。实验建立了一种利用高浓度甘油高效率发酵生产DHA的方法。     

γ-聚谷氨酸高产菌株筛选及发酵条件优化

γ聚谷氨酸是一种生物可降解的高分子材料,可应用于多种领域,因此受到普遍重视。报道了以11株枯草芽孢杆菌菌株为培养菌株,用3种谷氨酸钠含量不同的培养基进行筛选获得1株γ聚谷氨酸高产菌株;再以该菌株为研究对象进行碳源、氮源、谷氨酸钠浓度、初始pH、接种量、通气量等发酵条件的优化实验,结果表明最佳发酵条件为:250ml三角烧瓶装液40ml,接种体积分数5%,麦芽糖50g/L,酵母膏10g/L,谷氨酸钠30g/L,NaCl10g/L,KH₂PO₄5g/L,MgSO₄·7H₂O0.5g/L,初始pH6.0,发酵60h,此时γ聚谷氨酸产量最高,达到30.26g/L,比国外报道的20g/L的产量有显著提高。纯化后产物经红外光谱及核磁共振检测,鉴定为γ聚谷氨酸。     

响应面法优化枯草芽孢杆菌产γ-PGA的条件

对枯草芽孢杆菌液体发酵产γ-聚谷氨酸[γ-poly（glutamic acid）,γ-PGA]条件进行了优化。首先采用单因子实验筛选出最适碳源为玉米糖化液,氮源为蛋白胨和谷氨酸钠,无机盐为KH2PO4,MgCl,MnCl2和NaCl。在此基础上,利用Plackett-Burman设计对影响产量的12个因素进行评价,筛选出具有显著效应的因素蛋白胨、谷氨酸钠和NaCl。用最陡爬坡路径逼近最大产γ-PGA区域后,利用响应面中心组合设计对显著因素进行优化,得出蛋白胨、谷氨酸钠和NaCl的最佳质量分数分别为0.54%,8.13%和0.96%。优化后液体发酵液γ-PGA产量提高到29.00 g/L,比初始γ-PGA产量14.10 g/L提高了2倍。     

渗透压调控对裂殖壶菌发酵产DHA的影响

考察了不同渗透胁迫(0、10、20、30和40 g/L NaCl)对裂殖壶菌HX-308发酵产DHA及脂肪酸构成的影响。结果表明:20 g/L NaCl最有利于裂殖壶菌生长和DHA积累,生物量、总脂肪酸含量、DHA产量及DHA占生物量的比值分别为73 g/L、10.7 g/L、5.0 g/L和68 mg/g,并且DHA在总脂肪酸中所占百分比最高,为45.2%。此外,在低渗透压(10 g/L NaCl)条件下,添加40 mmol/L甘氨酸甜菜碱,DHA产量与未添加相比提高了28.21%;在高渗透压(40 g/L NaCl)条件下添加40 mmol/L海藻糖,DHA产量提高了46.84%;表明添加适量的外源相容性溶质能有效地促进裂殖壶菌积累DHA。     

高产DHA破囊壶菌Aurantiochytrium sp. PKU#SW7诱变株的筛选

【目的】对野生菌株Aurantiochytrium sp.PKU#SW7诱变育种,筛选高产DHA突变株。【方法】采用UV诱变和化学药物胁迫筛选方式,以菌株的生物量、油脂产量、DHA产量作为筛选指标,获得高产DHA突变株。【结果】经鉴定获得一株DHA高产突变株PKU#PM003,该菌株传代4次后仍保持较好的遗传稳定性。摇瓶发酵后,PKU#PM003生物量产量高达6.62 g/L,比原始菌株5.95 g/L提高了11.26%,脂肪酸含量高达4.01 g/L,比原始菌株3.18 g/L提高了26.1%,DHA在脂肪酸中所占比例由29.97%增加到33.43%,产量提高了41.01%,油脂突变效果显著。【结论】突变株PKU#PM003可作为性状优良的工业化发酵生产菌种,并在DHA产量提升上仍具有巨大的空间。     

裂殖壶菌Schizochytrium sp. 20888产DHA培养条件优化

【目的】为了优化裂殖壶菌产DHA的培养条件,提高油脂中DHA含量。【方法】采用单因素试验和正交设计试验方案,针对分批培养时间、培养基碳、氮源的种类和浓度以及培养温度开展试验,采用重量法测定生物量、采用索氏提取法测定油脂总量,采用气相色谱法测定油脂DHA含量,考察培养条件对细胞油脂DHA含量的影响。【结果】最适培养时间为4 d,培养温度23°C,最优碳氮源组成为(g/L):葡萄糖65、甘油80、蛋白胨6、酵母粉4和谷氨酸钠8。【结论】裂殖壶菌Schizochytrium sp.20888在葡萄糖和甘油组成的复合碳源和由蛋白胨、酵母粉和谷氨酸钠组成的复合氮源的培养基中可以得到最优的DHA产量,细胞DHA含量能达到33.68%。     

斯达氏油脂酵母利用混合糖发酵产油脂

研究了斯达氏油脂酵母Lipomyces starkeyi2#利用葡萄糖-木糖混合糖为碳源生长和油脂积累特性。L.star-keyi2#利用70 g/L葡萄糖和70 g/L木糖作为碳源在30℃下摇瓶发酵96 h,糖利用率均达90%以上,菌体生物量分别为14.1 g/L和13.1 g/L,油脂质量分数分别为55.7%和52.6%。相同条件下该菌株利用混合糖(葡萄糖46 g/L,木糖24 g/L)为碳源时总糖利用率、生物量和油脂质量分数分别为75.1%,15.0 g/L和40.0%。借助于P lackett-Burm an设计法和单因子实验法对培养条件进行了优化,结果表明发酵96 h混合糖利用率可达到97.3%,发酵120 h后混合糖利用率、生物量和菌体油脂质量分数分别达99.5%、19.0 g/L和52.6%。生物量得率和油脂得率分别达到27%和14%。     

搅拌和通气对裂殖壶菌LX0809产DHA的影响

利用一株生产DHA专利菌株裂殖壶菌LX0809,在10 L全自动发酵罐中考察了16个搅拌转速和通气量组合对裂殖壶菌LX0809发酵产DHA的影响。生物量和总油脂的产量随搅拌转速和通风量的增加而增加,DHA占总油脂比例随搅拌转速和通风量的增加而降低,最终确定通气量为全程0.3 m3/h(通气比0.83),搅拌转速为前40 h 400 r/min,后56 h 300 r/min。发酵96 h放罐,细胞生物量92 g/L,油脂质量浓度52.3 g/L,DHA占总油脂含量为40.2%,DHA发酵产量高达21 g/L。     

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。     

产鼠李糖脂菌株种子培养条件和C、N源的优化

对自行筛选的3个可利用废弃油脂进行发酵生产鼠李糖脂的铜绿假单胞菌菌株进行评价,并进行了种子培养条件和摇瓶发酵部分条件的优化。种子培养优化实验表明,当培养基pH 6～8,培养温度为30 ℃时最利于菌体生长。菌株均具有一定的耐盐性,在5%的盐度下生长未受到明显抑制,因此在沿海地区采用盐水或海水发酵具有较广阔的应用前景。通过排油圈、表面张力、苯酚-H2SO4比色法比较了这3个菌株的表面活性剂表面活性的大小,以表现较好的Z41进行了摇瓶发酵条件的优化。单因素实验表明,发酵较优条件为发酵温度30 ℃,接种量5%。在此基础上,通过正交试验对Z41菌株发酵培养基中的C、N源进行了研究,实验结果表明,在考虑因素间交互作用和发酵成本的情况下,最佳C源为3%炸货油,最佳N源为3.5 g/L尿素。在此发酵条件下,糖脂产量较高13.024 g/L,且成本较低。     

菌种保藏方法对裂殖壶菌生长及发酵性能的影响

考察保护剂、保藏温度及预冷冻方法对Schizochytrium sp.HX-308菌种存活率及发酵性能保持的影响。结果显示:在-80℃低温保藏6个月后,渗透性保护剂的细胞存活率均比非渗透性保护剂高了5%,其中用60%(质量分数)海藻糖的保护剂最终的株细胞存活率达到80.02%,明显优于其他保护剂。采用液氮-196℃保藏菌种(两步预冷冻法、60%海藻糖保护剂),存储6个月后存活率高达90.70%,生物量、油产量和二十二碳六烯酸(DHA)产量分别达到了61.65、26.41和11.10 g/L,为最优的保藏方法,为裂殖壶菌的实验室研究及工业化生产提供了一种长期安全的保藏法。     

外源添加剂促进裂殖壶菌合成DHA

为提高二十二碳六烯酸（DHA）产量,根据裂殖壶菌生物合成DHA的代谢途径,考察外源添加剂对裂殖壶菌发酵生产DHA影响。研究表明：分生物素、柠檬酸、苹果酸和洛伐他汀均能提高裂殖壶菌DHA的合成能力。同时添加生物素、苹果酸和洛伐他汀时能够显著提高DHA的产量,DHA的最高产量达到11.55 g/L,相比对照提高71.87%。     

Enhanced docosahexaenoic acid production by reinforcing acetyl-CoA and NADPH supply in <Emphasis Type="Italic">Schizochytrium</Emphasis> sp. HX-308

Docosahexaenoic acid (DHA) production in Schizochytrium sp. HX-308 was evaluated by detecting enzymatic activities of ATP:citrate lyase (EC 4.1.3.8), malic enzyme (EC 1.1.1.40) and glucose-6-phosphate dehydrogenase (EC 1.1.1.49) at different fermentation stages. According to the analysis, a regulation strategy was proposed which reinforced acetyl-CoA and NADPH supply at a specific fermentation stage. DHA content of total fatty acids was increased from 35 to 60% by the addition of 4 g/L malic acid at the rapid lipid accumulation stage. Total lipid content also showed an apparent increase of 35% and reached 19 g/L when 40 mL ethanol/L was added at the late lipid accumulation stage.     

添加生物素和浅蓝菌素对裂殖壶菌发酵产DHA的影响

为提高发酵产量,根据裂殖壶菌生物合成二十二碳六烯酸(DHA)的途径,考察添加代谢途径关键酶的辅酶及酶的抑制剂对发酵裂殖壶菌的影响.结果表明:添加生物素可促进油脂积累,添加浅蓝菌素有利于DHA及不饱和脂肪酸含量的提高.添加生物素0.3 mg/L时,DHA占细胞干质量分数达11.26％,相对于对照提高了13％;当添加浅蓝菌素0.1mg/L时,DHA占细胞干质量分数可达12.2％.     

Optimization of docosahexaenoic acid production by Schizochytrium limacinum SR21

Culture conditions of Schizochytrium limacinum SR21 for the purpose of microbial docosahexaenoic acid (DHA) production were investigated. The strain SR21 showed a wide tolerance to salinity; that is, the optimum salinity was between 50% and 200% that of sea water. Monosaccharides (glucose and fructose) and glycerol supported good cell growth and DHA yield. Di- and polysaccharides, oleic acid, and linseed oil gave low DHA yields. A high content of DHA (more than 30% of total fatty acids) was obtained from culture on glucose, fructose, and glycerol, and also the strain had simple polyunsaturated fatty acid profiles. The major polyunsaturated fatty acids other than DHA were n-6 docosapentaenoic acid only, and the contents of icosapentaenoic acid and arachidonic acid were less than 1%. Using corn steep liquor as a nitrogen source, a high total fatty acid content was obtained. The total fatty acid content in the dry cell weight increased as the concentration of the nitrogen source decreased, reached more than 50%. An increase in carbon source concentration led to a high DHA yield. A maximum DHA yield of more than 4 g/l was obtained in both glucose and glycerol media at 9% and 12% respectively. S. limacinum SR21 was thought to be a promising resource for microbial DHA production yielding a good level of productivity as well as a simple polyunsaturated fatty acid profile. Received: 26 June 1997 / Received revision: 29 August 1997  / Accepted: 19 September 1997     

Impact of phosphate concentration on docosahexaenoic acid production and related enzyme activities in fermentation of Schizochytrium sp.

Docosahexaenoic acid (DHA) is an important and widely used infant food additive. In this study, the effects of phosphate concentration on lipid and especially DHA synthesis in the oleaginous fungi Schizochytrium sp. HX-308 have been investigated in batch cultures. The maximum DHA yield (8.9 g/L) and DHA productivity (148.3 mg/L h) in 0.1 g/L KH₂PO₄ concentration were higher than the DHA yield (6.2 g/L) and DHA productivity (86.1 mg/L h) in 4 g/L KH₂PO₄ concentration. Furthermore, differences in related enzyme activities (malic enzyme, glucose-6-phosphate dehydrogenase and NAD⁺-isocitrate dehydrogenase) between phosphate-sufficient and phosphate-limitation conditions were assayed. The results showed that the phosphate-limitation condition could maintain higher activities of malic enzyme and glucose-6-phosphate dehydrogenase in addition to lower activity of NAD⁺-isocitrate dehydrogenase. In addition, glucose-6-phosphate dehydrogenase might be the main supplier of NADPH at the early stage of fermentation while malic enzyme might be the provider at the late stage. This information might explain the regulation mechanism of phosphate limitation for lipid production and be useful for further DHA production enhancement.     

A New Labyrinthulid Isolate That Produces Only Docosahexaenoic Acid

We show here that a new labyrinthulid strain, L72, isolated from a fallen leaf in the Seto Inland Sea of Japan, produced only docohexaenoic acid (DHA) among all the long-chain polyunsaturated fatty acids (LCPUFAs). The main fatty acid composition was 16:0 (28.9%), 18:0 (7.2%), 18:1 (5.7%), 18:2 (10.4%), and DHA (45.9%) without any other LCPUFA. The lipid content of the strain was 27.4%. The cells had many lipid bodies, which were densely located in all of the cells. On phylogenetic analysis using the 18S rDNA sequence, the strain was located in the labyrinthulids group, forming a monophyletic group with Labyrinthula sp. (strain s) and Labyrinthuila sp. (strain L59). We further tested the culture optimization of strain L72 to evaluate the ability of the strain to produce DHA. The optimum salt concentration and the temperature of the strain were 100% of artificial seawater and 20°C. Strain L72 could grow well on soybean oil (SBO) or soybean lecithin (SBL) as the carbon source. When 20 g/l of SBL was added to the medium, DHA production reached the maximum amount at 0.67 g/l for 14 d. The two important facts, that the strain can use SBL as the main nutrient and contains only DHA among the LCPUFAs, will be of great advantage for industry.     

Regulation of docosahexaenoic acid production by Schizochytrium sp.: effect of nitrogen addition

Docosahexaenoic acid (DHA) percentage in total fatty acids (TFAs) is an important index in DHA microbial production. In this study, the change of DHA percentage in response to fermentation stages and the strategies to increase DHA percentage were investigated. Two kinds of conventional nitrogen sources, monosodium glutamate (MSG) and ammonium sulfate (AS), were tested to regulate DHA synthesis. Results showed that MSG addition could accelerate the substrate consumption rate but inhibit lipid accumulation, while AS addition could increase DHA percentage in TFAs effectively but extend fermentation period slightly. Finally, the AS addition strategy was successfully applied in 7,000-L fermentor and DHA percentage in TFAs and DHA yield reached 46.06 % and 18.48 g/L, which was 19.54 and 17.41 % higher than that of no-addition strategy. This would provide guidance for the large-scale production of the other similar polyunsaturated fatty acid, and give insight into the nitrogen metabolism in oil-producing microorganisms.