十三碳二元羧酸发酵技术的研究

以一株热带假丝酵母菌(Candida tropicalis) SP1为出发菌株,经紫外线反复诱变获取一株难以同化烷烃的突变株SPUV56,摇瓶培养5d平均产酸量达72g/L,较出发菌株提高了1.25倍,并利用突变株SPUV56在137L自控罐上扩试,补加醋酸盐发酵,144h产酸量达153g/L,比不加醋酸盐发酵提高了29.7%。采用提 高搅拌混合效果和低溶解氧发酵过程控制方法,可有效地提高菌体的产酸能力,在20m3发酵罐中发酵生产十三碳二元羧酸,总培养时间144h,产酸量可达172g/L,放罐体积15.0m3,产量为2.25t。     

富锌酵母的选育及培养条件研究

对402株不同种属的酵母菌株进行了出筛、复筛、单倍体分离、诱变,从亲株Y-6-16-18（a met）accharomyces cerevisiae）和Y378-4-15（α-leu）（Sacharomyces kluyveri）的杂交菌株中选育到一株富锌酵母菌株（编号为ZGH374）。并初步优化了发酵条件：培养基为80g/L糖浓度的麦芽汁、10g/L蛋白胨、锌添加量400μg/mL,pH 6.0,装液量40mL/250mL三角瓶,接种量10%（V/V）,培养起始添加锌盐,培养时间30h。在优化的条件下,杂交菌株ZGH374的生物量（细胞干重）达到14.3g/L,细胞锌含量可达到9.3mg/g,锌总含量达到了133mg/L。     

富养罗尔斯通氏菌菌株 PHB“泄漏”机理的初探

建立了一种分离纯化聚羟基丁酸(Polyhydroxybutyrate, PHB)颗粒的改良方法。采用这种方法从Ralstonia eutropha菌株H16（野生型）、SK1489（Tn5诱变的PHB泄漏菌株）、JMP222（野生的PHB泄漏菌株）分离了PHB颗粒。进一步比较研究了不同菌株的PHB解聚酶和3羟基丁酸脱氢酶的活性。研究结果表明,菌株SK1489的PHB解聚酶活性（48h培养后达1.82 U/mg）明显高于野生型菌株H16(48 h培养后达0.37 U/mg),菌株JMP222的3羟基丁酸脱氢酶活性(培养96 h后达1659 U/mg)比菌株H16培养(96 h后达640 U/mg)高许多。这些结果显示,不同菌株PHB的泄漏有不同的原因,突变株SK1489导致PHB泄漏的原因是解聚酶活性高,而野生型JMP222 PHB泄漏的原因主要是3羟基丁酸脱氢酶活性高。     

絮凝性强的优良面包酵母菌株的选育

通过初筛、单倍体分离、DES诱变、絮凝基因的克隆表达及杂交等育种技术成功构建了高生物量、耐高糖、强絮凝的优良面包酵母菌株(Saccharomyces cerevisiae) ZLTH58(MATa/α,leu,FLO1)。菌株ZLTH58具有双亲的优良性状,遗传性状稳定。对其生物量、耐高糖能力、絮凝特性进行了检测,结果表明,菌株ZLTH58的生物量是原始亲株BL56的1.21倍;耐高糖能力优于原始亲株BL61;絮凝性能明显优于原始亲株BL56和BL61。对其培养条件进行了优化,在优化的培养条件下,生物量可以达到83.06g/L,为初始培养条件下的1.35倍。     

假单胞菌株M18gacA基因对BHL和HHL合成正调控及对PCA合成负调控无相关性

经初步鉴定,假单胞菌株(Pseudomonas sp.)M18至少能产生5种N酰基高丝氨酸内酯类(Nacylhomoserine lactones,AHLs）信号分子,它们是：N丁酰高丝氨酸内酯(NbutyrylLhomoserine lactone,C4HSL,BHL)、N己酰高丝氨酸内酯(NhexanoylLhomoserine lactone,C6HSL,HHL)、N3氧己酰高丝氨酸内酯［N(3oxohexanoyl)Lhomoserine lactone,3OxoC6HSL,OHHL］、N3氧辛酰高丝氨酸内酯［N(3oxooctanoyl)Lhomoserine lactone,3-OxoC8HSL,OOHL］和N3氧癸酰高丝氨酸内酯［N(3oxodecanoyl)Lhomoserine lactone,3OxoC10HSL,ODHL)。在gacA突变菌株M18G中,信号分子的积累量明显减少,且只能检测出其中的4种;同时,吩嗪1羧酸(Phenazine1carboxylic acid,PCA)的合成量比野生株M18提高了2倍左右。在M18菌株中,基因rhlⅠ的编码产物参与BHL和HHL的合成。构建rhlI''lacZ翻译融合表达质粒pMEIZ,分别导入野生株M18和突变株M18G,突变株M18G的半乳糖苷酶活性比野生株M18下降约40%,表明GacA对基因rhlI的表达具有正调控作用。但是,在野生株M18和突变株M18G的发酵液中,分别或同时添加过量的外源BHL和HHL,对PCA合成的影响不显著,表明在突变株M18G中,PCA合成量的增加与BHL和HHL合成量的减少没有明显的相关性。     

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%。     

青霉PT95菌株固态发酵产生类胡萝卜素的研究

本文对青霉Penicillium sp. PT95菌株在固态发酵条件下菌核内产生类胡萝卜素进行了初步研究。结果表明,在3种固态发酵培养基中,玉米粉培养基(SMA)比麸皮培养基和棉籽壳培养基更适合于PT95菌株固态发酵产生类胡萝卜素。为了增加菌核干重和提高类胡萝卜素产率,SMA中需要添加氮源、碳源和植物油。在所试的各种氮、碳源中,以硝酸钠和麦芽糖效果最佳。通过正交试验确定了在培养基盐溶液中添加硝酸钠3g/L,麦芽糖10g/L,豆油2.5g/L能使菌核干重由536g/100g提高到970g/100g(干料);类胡萝卜素产率由2149μg/100g提高到5260μg/100g(干料);β-胡萝卜素在类胡萝卜素中的含量由614%提高到71.3%。     

离子束注入提高Trichosporon lactis T立体拆分布洛芬水平的研究

以从土壤中分离筛选到的可立体选择性水解布洛芬乙酯生成S布洛芬的菌株Trichosporon lactis Ｔ为出发菌株,对其进行能量30KeV,剂量1×1015～5×1015ions/cm2的低能N+注入,筛选立体选择性水解布洛芬乙酯活性高的诱变株。菌株T.lactis T,在4×1015 ions/cm2的诱变剂量下突变率最高,正向和负向突变率分别达32.9%和37.1%,因此选定该剂量为T. lactis T的最佳N+离子注入剂量。经离子束诱变,通过初筛和复筛,共筛选到7株水解布洛芬乙酯的高产菌株,其中诱变株K1培养24h时酶活力比出发菌株T高50%,且具有较好的遗传稳定性。将菌株K1和出发菌株T培养24h,分别加入布洛芬乙酯水解24h,二者水解布洛芬乙酯生成S布洛芬旋光度均为+54.1°,对映体过量值ee%均为98%,K1菌株水解的产量达6.96g/L,而出发株仅为4.24g/L。     

补料培养提高真养产碱杆菌产3-羟基丁酸和3-羟基戊酸共聚物生产强度的研究

对Alcaligeneseutrophus进行高密度培养 ,研究表明在发酵过程中进行有效控制 ,可以较大幅度地提高 3-羟基丁酸和 3 羟基戊酸共聚物 [P(3HB-co-3HV) ]的生产强度。实验中选择使用限氮的方法积累P(3HB-co-3HV) ,分别采用丙酸和戊酸为 3HV前体 ,对摇瓶种子生长状态 ,停氮时机对菌体生产P(3HB-co-3HV)的影响以及补酸 (3HV前体 )策略进行了研究 ,在 6.6L罐中 ,以葡萄糖为碳源 ,以丙酸为 3HV前体培养 5 0h ,细胞干重 ,PHA产量 ,PHA含量分别达到 149.9g L ,12.49g L ,83.3% (其中 3HV组分占PHA的 12 4mol% ) ,生产强度达到 2.50 (g·h^-1·L^-1) ;以戊酸为3HV前体培养 45h ,细胞干重 ,PHA产量 ,PHA含量分别达到 16.02g L、119 0g L、74.2 % (其中 3HV组分占PHA的17.7mol% ) ,生产强度达到 2.64(g·h^-1·L^-1)     

产顺式环氧琥珀酸水解酶的红球菌M1菌株的分离鉴定及其产酶条件优化

从土壤中筛选到一株产顺式环氧琥珀酸水解酶（ESH）的菌株,经生理生化、Biolog碳源利用试验和16S rDNA序列分析系统发育研究,菌株可能为赤红球菌(Rhodococcus ruber) M1。摇瓶试验确定了最佳碳源、氮源、顺式环氧琥珀酸二钠添加时间和添加量。正交优化试验的最佳培养基和培养时间为：葡萄糖12%,硫酸铵06%,酵母膏05%;顺式环氧琥珀酸二钠投加时间为30h,投加量为358%;菌体培养时间70h。摇瓶试验ESH酶活达750U/g湿细胞。目前该菌株已经应用于固定化细胞连续生产L(+)酒石酸。     

The effect of carbon source supplementation on the production of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) by Cupriavidus necator

The objective of the present study was to investigate the ability of Cupriavidus necator to produce poly-(3-hydroxybutyrate-co-3-hydroxyvalerate) on various carbon sources in batch cultivation. These results show that C. necator produces poly-3-hydroxybutyrate from single carbon sources. The highest poly-3-hydroxybutyrate (P3HB) content was achieved at growth on fructose in the exponential growth phase. The maximum yield of the P3HV content was obtained when fructose was mixed with acetate. The highest content P3HB-co-3HV was also achieved by C. necator when we supplied C-excess and N- and P-normal conditions. These results indicate that C. necator accumulates high polyhydroxyalkanoates (PHA) content by depleting these elements in the culture medium. Nitrogen and phosphorus limitation has no significant effect on the PHA production, whereas C-excess leads to an increase in PHA formation of up to 92% PHAs of cell dry weight after growth on 5 g/L acetate and 40 g/L fructose.     

嗜水气单胞菌WQ中PHBHHx的合成及其分子基础研究

聚羟基脂肪酸酯(Polyhydroxyalkanoate,PHA)是一系列生物合成的高分子材料,其单体可由多种3-羟基脂肪酸(3-hydroxyalkanoate,3HA)构成^[1]。PHA物理和机械性能的变化很大,从高脆性到弹性体,这跟它们的单体成分有很大关系^[2]。短链和中长链单体共聚的PHA比短链单体或中长链单体聚合得到的PHA有着更好的性能^[3]。在1994年,豚鼠气单胞菌(Aeromonas caviae)FA440被发现能以偶数碳原子数脂肪酸或植物油作为碳源在体内积累PHBHHx^[4]其PHA生物合成基因被成功克隆^[5]。根据亚基数目和底物特异性,PHA合成的关键酶,即PHA合酶或PhaC,被分成了3种类型。A．caviae的PHA合酶属于第1类PHA合酶^[6]。PHA合酶的一些类型含有一些保守的基因序列,该特征可被用于克隆,特别是第Ⅱ类PHA合酶^[2,8]。嗜水气单胞菌(Aeromonas hydrophila)WQ和A．hydrophila 4AK4是能够合成PHBHHx的另外两种菌株,其中A．hydrophila 4AK4已被用作大规模生产PHBHHx。就目前来说,不管生长条件怎么改变,其合成的PHBHHx中3羟基己酸单体(3-hydroxyhexanoate,3HHx)的含量始终在12％～17％之间变化^[9]。而A．hydrophila WQ合成的PHBHHx中则含有6％～14％ 3HHx。本论文研究了A．hydrophila WQ的PHA生物合成及其分子基础。     

Perfusion strategy for rosmarinic acid production by Anchusa officinalis

The production of an intracellular secondary metabolite rosmarinic acid (RA) by plant cell suspensions of Anchusa officinalis cultivated with intermittent medium exchange is investigated. Initially, a two-stage perfusion culture method was employed. After being cultured in the batch mode for ca. 6 days in B5 medium plus 3% sucrose, 1 mg/L 2,4-dichlorophenoxyacetic acid (2,4-D), and 0.1 mg/L kinetin (2,4-D B5 medium), Anchusa culture was cultivated to high cell density by perfusion during the growth stage using a hormone-free Gamborg B5 medium supplemented with 6% sucrose. This was followed by a production stage, in which a complete medium exchange into B5 medium plus 3% sucrose and 0.25 mg/L naphthleneacetic acid (NAA) was conducted. The two-stage perfusion culture had a higher maximum culture RA concentration but a lower RA content per cell than the batch stock culture maintained in the 2,4-D B5 medium. Higher culture RA concentration was due primarily to high cell density. The high packed cell volume, however, seemed to reduce the synergistic effect of NAA on RA synthesis. Subsequently, a single-stage perfusion culture method was investigated. The best result was obtained by growing the culture in the batch mode for ca. 10 days using B5 medium supplemented with 3% sucrose and 0.25 mg/L NAA, followed by perfusing the culture with B5 medium plus 6% sucrose and 0.25 mg/L NAA at a constant perfusion rate of 0.1/day. A maximum cell dry weight of 35 g/L and a RA concentration of almost 4 g/L were achieved. This is the highest RA concentration ever reported in the Anchusa culture. (c) 1993 John Wiley & Sons, Inc.     

In vitro production of gymnemic acid from cell suspension cultures of Gymnema sylvestre R. Br

Gymnema sylvestre is an important medicinal plant that bears bioactive compound namely gymnemic acids. The present work deals with the optimization of a cell suspension culture system of Gymnema sylvestre for the production of biomass and gymnemic acid, which has anti‐diabetic properties. We investigated the effect of inoculum densities (2.5–20.0 g/L), the strength of the Murashige and Skoog (MS) medium (0.25–2.0), carbon source (sucrose, glucose, fructose, maltose), and the concentration of the sucrose (1–8% w/v) to determine their effects on biomass accumulation and production of gymnemic acid. Overall, 10 g/L of inoculum density, full‐strength MS medium supplemented with 2,4‐dichlorophenoxy acetic acid (2.0 mg/L) and Kinetin (0.1 mg/L), and 3% w/v sucrose was found best for the accumulation of biomass and gymnemic acid content (9.95 mg/g dry weight). The results of the current study will be useful for bioprocess and biochemical engineers for large‐scale production of gymnemic acid in cell culture.     

球形红杆菌积累聚β-羟基链烷酸(PHA)的研究

通过对球形红杆菌(Rhodobacter sphaeroides)生长和积累聚卢-羟基链烷酸(PHA)条件的研究,确定采用两段培养法提高PHA的产量。第一阶段提供适合菌体生长的条件:以葡萄糖作碳源,尿素为氮源,光照微好氧培养。第二阶段则提供使菌体积累PHA的条件:补加乙酸钠厌氧光照培养。经两段培养后菌体PHA含量可占细胞干重的45％,PHA产量每升发酵液可达1.7g。     

Production of polyhydroxyalkanoates by <Emphasis Type="Italic">Azotobacter vinelandii</Emphasis> UWD using swine wastewater: Effect of supplementing glucose,yeast extract,and inorganic salts

This study examined the effect of adding glucose, yeast extract, and inorganic salts to swine wastewater (SWW) in a batch culture on the production of a biodegradable plastic, polyhydroxyalkanoate (PHA). A bacterial strain, Azotobacter vinelandii UWD, was used to produce PHA without limiting the non-carbon nutrients. The addition of glucose (30 g/L) to the SWW medium increased the level of cell growth (4.4∼7.0 times) and PHA production (3.8∼8.5 times) depending upon the dilution of SWW. A 50% dilution of SWW was found to be optimal considering the dry cell weight (9.40 g/L), PHA content (58 wt%), and hydroxyvalerate (HV) mol fraction in the PHA (4.3 mol%). A 75% SWW medium was more advantageous for producing PHA with a higher HV fraction (7.1 mol%) at the expense of losing 22% of PHA production. The undiluted SWW medium produced less than one third of the PHA compared with the 50% SWW medium, but the HV fraction was the highest (10.8 mol%). Regarding the effect of the glucose concentration, at 20 g/L glucose, the dry cell weight and level of PHA production increased to 9.34 g/L (0.63 g PHA/g dry cell weight) and 5.90 g/L, respectively. At 50 g/L glucose, there was no significant increase in PHA production. For the glucose-supplemented (30 g/L) 50% SWW medium, the addition of a nitrogen source (1 g/L of yeast extract) did not increase the level of cell growth or PHA production because the C:N ratio (23:1) was already close to the optimal value (22:1). Better aeration increased the productivity of PHA. External nitrogen supplements (1 g/L of yeast extract) and other essential mineral salts was not necessary for bacterial growth because they were contained in the SWW. These results suggest that SWW is an excellent feedstock for producing larger amounts of the value-added material, PHA, if it is combined with carbohydrate-rich organic waste.     

补料培养提高真养产碱杆菌产3-羟基丁酸和3-羟基戊酸共聚物生产强度的研究

对Alcaligenes eutrophus进行高密度培养,研究表明在发酵过程中进行有效控制,可以较大幅度地提高3－羟基丁酸和3－羟基戊酸共聚物[P(3HB-co-3HV)]的生产强度。实验中选择使用限氮的方法积累P(3HB-co-3HV),分别采用丙酸和戊酸为3HV前体,对摇瓶种子生长状态,停氮时机对菌体生产P(3HB-co-3HV)的影响以及补酸（3HV前体）策略进行了研究,在6．6L罐中,以葡萄糖为碳源,以丙酸为3HV前体培养50h,细胞干重,PHA产量,PHA含量分别达到149．9g/L,149.9g/L,83.3%(其中3HV组分占PHA的12．4mol%),生产强度达到2．50（g.h^-1.L^-1);以戊酸为3HV前体培养45h,细胞干重,PHA产量,PHA含量分别达到160．2g/L,119.0g/L,74.2%（其中3HV组分占PHA的17．7mol%)生产强度达到2．64（g.h^-1.L^-1)。     

白Pian体细胞胚悬浮培养的动力学研究

白(ＰｉｃｅａｍｅｙｅｒｉＲｅｈｄ.ｅｔＷｉｌｓ.)是我国特有的云杉属树种,在林业生产和环境绿化中均具有重要地位。其体细胞胚胎发生的研究,一方面可用于优良种质的大规模快速繁殖,为植树造林和园林绿化提供优质苗木;另一方面可作为遗传转化的再生系统,进行树种遗传...     

The conversion of BTEX compounds by single and defined mixed cultures to medium-chain-length polyhydroxyalkanoate

Here, we report the use of petrochemical aromatic hydrocarbons as a feedstock for the biotechnological conversion into valuable biodegradable plastic polymers-polyhydroxyalkanoates (PHAs). We assessed the ability of the known Pseudomonas putida species that are able to utilize benzene, toluene, ethylbenzene, p-xylene (BTEX) compounds as a sole carbon and energy source for their ability to produce PHA from the single substrates. P. putida F1 is able to accumulate medium-chain-length (mcl) PHA when supplied with toluene, benzene, or ethylbenzene. P. putida mt-2 accumulates mcl-PHA when supplied with toluene or p-xylene. The highest level of PHA accumulated by cultures in shake flask was 26% cell dry weight for P. putida mt-2 supplied with p-xylene. A synthetic mixture of benzene, toluene, ethylbenzene, p-xylene, and styrene (BTEXS) which mimics the aromatic fraction of mixed plastic pyrolysis oil was supplied to a defined mixed culture of P. putida F1, mt-2, and CA-3 in the shake flasks and fermentation experiments. PHA was accumulated to 24% and to 36% of the cell dry weight of the shake flask and fermentation grown cultures respectively. In addition a three-fold higher cell density was achieved with the mixed culture grown in the bioreactor compared to shake flask experiments. A run in the 5-l fermentor resulted in the utilization of 59.6 g (67.5 ml) of the BTEXS mixture and the production of 6 g of mcl-PHA. The monomer composition of PHA accumulated by the mixed culture was the same as that accumulated by single strains supplied with single substrates with 3-hydroxydecanoic acid occurring as the predominant monomer. The purified polymer was partially crystalline with an average molecular weight of 86.9 kDa. It has a thermal degradation temperature of 350 degrees C and a glass transition temperature of -48.5 degrees C.     

Asiaticoside production from centella (Centella asiatica L. Urban) cell culture

Petiole explants of centella plants (Centella asiatica L. Urban) were cultured on Murashige and Skoog (MS) solid medium containing 20 g/L sucrose, supplemented with 1.0 mg/L benzylaminopurine and 1.0 mg/L naphthaleneacetic acid for callus production. To establish a cell suspension culture, 2 g of fresh callus was cultured in 50 mL of the same medium but without solid agent at a 100 rpm agitation speed. Every 2 g of culture was subcultured in fresh MS liquid medium for maintenance. After 24 days of culture at a 120 rpm agitation speed, the centella cell biomass reached a maximum of 9.03 g/50 mL on the same MS medium with 30 g/L sucrose and a 3 g inoculum size. A high performance liquid chromatography analysis showed that asiaticoside content in 24-day old suspension cultured cells (45.35 mg/g dry weight) was significantly higher (4.5 fold) than that of in planta leaves (10.55 mg/g dry weight).