云南红豆杉细胞的悬浮培养

在云南经豆杉细胞悬浮培养中,适宜的增减基为Ｂ５,接种量为０．５－０．８ｇ干重细胞／１００ｍｌ培养基,２,４－Ｄ浓度为１．０ｍｇ／Ｌ;培养细胞的生长周期约３０ｄ;增减基中较高浓度的蔗糖（４０ｇ／Ｌ）可提高紫杉醇含量;添加的椰子汁（ＣＭ）、酪蛋白氨基酸（ＣＡ）和水解乳蛋白（ＬＨ）３种有机添加剂均能提高培养细胞中紫杉醇的含量,但只有ＣＭ和ＣＡ能促进细胞的生长。于Ｂ５培养基中添国不同浓度的ＮＨ４ＮＯ３对培     

几种促进剂的添加时间对中国红豆杉细胞悬浮培养紫杉醇合成的影响

采用正交实验检测中国红豆杉[Taxus chinensis(Pilger)Rehd.]细胞悬浮培养中水杨酸、硝酸银、氨基酸前体、D-果糖和硫酸镧的添加时间对细胞生长和紫杉醇(taxol)积累的影响.这些促进剂的添加时间对中国红豆杉细胞悬浮培养的生长没有明显的影响,但能明显促进紫杉醇的合成,当在细胞培养的第14 d添加1.67 mg/L硝酸银,第18 d添加0.1 mg/L水杨酸,第21 d添加氨基酸前体,第21 d添加10 g/L D-果糖和2 mg/L硫酸镧时对紫杉醇的促进作用最明显,在此最优组合处理时紫杉醇含量达到10.05 mg/L,相对于最差组合处理时紫杉醇含量仅有1.77 mg/L,紫杉醇含量提高5.7倍,这些因素的添加时间对紫杉醇合成的相互作用达不到显著水平.     

水杨酸对红豆杉细胞的诱导作用

通过添加不同浓度的水杨酸（ＳＡ）,比较了它们对红豆杉细胞过氧化物酶（ＰＯＤ）、苯丙氨酸解氨酶（ＰＡＬ）、过氧化氢（Ｈ２Ｏ２）含量及以细胞生长和紫杉醇含量的影响,结果表明,ＳＡ可提高ＰＯＤ及ＰＡＬ的活性,促进细胞内Ｈ２Ｏ２含量的上升并有利于紫杉醇的合成,其中２０ｍｇ／Ｌ ＳＡ对紫杉醇合成的促进效果最明显,紫极醇含量可达对照组的１３倍。     

利用高山红景天培养细胞生物转化外源酪醇生产红景天甙的研究

高山红景天（ＲｈｏｄｉｏｌａｓａｃｈａｌｉｎｅｎｓｉｓＡ．Ｂｏｒ．）培养细胞中,甙元酪醇在细胞生长静止期大量积累,而此时糖基化反应的效率很低,因而红景天甙（ｓａｌｉｄｒｏｓｉｄｅ）产量较低。考虑到培养细胞中酪醇葡萄糖基转移酶的活性在指数生长期达到最高,考察了在指数生长期添加外源酪醇生物转化生产红景天甙的可能性,并探讨了酪醇添加浓度、添加方法及细胞密度对酪醇转化率及红景天甙产量的影响。结果表明,细胞在酪醇浓度为１ｍｍｏｌ／Ｌ的培养基中培养２４ｈ后可使酪醇转化率达到９５％;过高的酪醇浓度（＞３ｍｍｏｌ／Ｌ）对细胞生长及酪醇转化率都有明显抑制作用;通过较低浓度酪醇的３次重复添加,可使细胞密度为６ｇＤＷ／Ｌ、１２ｇＤＷ／Ｌ及１８ｇＤＷ／Ｌ的培养物中的红景天甙产量分别达到１３２０ｍｇ／Ｌ、１７４０ｍｇ／Ｌ和１９８０ｍｇ／Ｌ。     

低密度和条件培养对红豆杉细胞生长的影响

红豆杉种胚来源的细胞,在改良Ｂ５液体培养基中继代培养的临界接种密度为鲜重４０ｇ／Ｌ．低密度培养下,１０－１６ｄ的条件培养液（ＣＭ）与新鲜培养液按５７：４３的比例混合时,能显著缩短细胞生长的延迟期,提高生长率,１００Ｌ生物反应器中,按４５．５％体积分数添加条件培养液,在鲜重２７ｇ／Ｌ低接种密度下培养５周,生物量增长９倍,达干重１４．３ｇ／Ｌ．对内源植物激素、精胺、维生素和氨基酸等的比较分析表明,吲哚     

红豆杉细胞两相培养生产紫杉醇的研究

研究了两相培养系统中红豆杉细胞的生长与代谢规律,经４０天培养,细胞生物量为１７．８５ｇ／Ｌ（干重）,紫杉醇产量为３０．１９ｍｇ／Ｌ。     

前体物对红豆杉培养细胞中紫杉醇生物合成的影响

本文报道了添加７种紫杉醇前体物／调节物后,红豆杉（Ｔ．ｃｈｉｎｅｎｓｉｓ（Ｐｉｌｇｅｒ）Ｒｅｈｄ）ＴＣ１５８细胞系的反应,在红豆杉细胞悬浮培养２５天时,分别加入不同浓度乙酸钠,苯甲酸钠,Ｌ－苯丙氨酸,甘氨酸,丝氨酸、α－蒎烯,松节油。试验结果表明,各前体物对红豆杉细胞生长无明显影响,均不同程度地促进了紫杉醇的合成。     

云南红豆杉细胞的悬浮培养

在云南红豆杉细胞悬浮培养中,适宜的培养基为B5,接种量为0．5～0．8g干重细胞／100ml培养基,2,4－D浓度为1．0mg／L;培养细胞的生长周期约30d;培养基中较高浓度的蔗糖（40g／L）可提高紫杉醇含量;添加的椰子汁（CM）、酪蛋白氨基酸（C）和水解乳蛋白（LH）3种有机添加剂均能提高培养细胞中紫杉醇的含量,但只有CM和CA能促进细胞的生长。于B5培养基中添加不同浓度的NH4NO3对培养细胞无明显影响。     

天然及氧化修饰脂蛋白对人动脉平滑肌细胞原癌基因表达的影响

动脉平滑肌细胞（ＳＭＣ）的增殖在动脉粥样硬化（ＡＳ）的形成过程中极其重要。我们在建立人主动脉ＳＭＣ体外培养方法的基础上,观察了ＬＤＬ,ＶＬＤＬ及ＨＤＬ和相应的氧化修饰型脂蛋白对培养人ＳＭＣｓｉｓ,ｊｕｎ,Ｈ－ｒａｓ原癌基因及Ｒｂ抗癌基因转录表达的影响。结果表明：（１）ＨＤＬ对ＳＭＣｓｉｓ,ｊｕｎ,ｒａｓ基因表达无影响;（２）ＬＤＬ和ＶＬＤＬ有使这些基因表达增加的趋势;（３）ｏｘ－ＬＤＬ,ｏｘ－ＶＬＤＬ和ｏｘ－ＨＤＬ具有使ＳＭＣｓｉｓ,ｊｕｎ,和ｒａｓ基因表达显著增强的作用（Ｐ＜０．０１）,且其作用较相应的天然脂蛋白大（Ｐ＜０．０１）;（４）天然和氧化修饰型脂蛋白对Ｒｂ基因表达均无影响。据上述结果推测：ＬＤＬ,ＶＬＤＬ,ｏｘ－ＬＤＬ,ｏｘ－ＶＬＤＬ和ｏｘ－ＨＤＬ的致ＡＳ作用可能与刺激ＳＭＣｓｉｓ,ｊｕｎ和ｒａｓ原癌基因表达增加有关。     

红花细胞培养条件的优化及其胞内产物生育酚的

红花（Ｃａｒｔｈａｍｕｓ ｔｉｎｃｔｏｒｉｏｕｓ）的子叶能诱志出愈伤组织,并且该愈伤组织能合成生育酚。正相高效液相色谱测定的结果表明,其主要成分是α－生育酚。在ＭＳ培养基基础上添加０．１％酪蛋白,并将生长调节剂浓度调整为２,４－Ｄ０．３０ｍｇ／Ｌ,６－ＢＡ １．８０ｍｇ／Ｌ,槿使α,β－γ生育酚含量分别达４．１７０６,０．３１２０,０．１６５０μｇ／ｇ鲜重。     

金黄色破囊壶菌发酵生产DHA的研究

顺 4,7,1 0 ,1 3 ,1 6 ,1 9 二十二碳六烯酸 (ｄｏｃｏｓａｈｅｘａｅｎｏｉｃａｃｉｄ ,简称ＤＨＡ)是ω 3系列多不饱和脂肪酸。近年的研究表明 ,ＤＨＡ是组成大脑和视网膜的重要结构物质 ,如大脑灰质结构脂质中 6 0 %的脂肪酸均为ＤＨＡ[1] 。ＤＨＡ对人体健康有益的生理功能主要表现在[2 ] :调节中枢神经系统功能 ;预防和治疗心血管疾病 ;治疗气喘、关节炎等 ;预防和治疗乳腺癌、结肠癌等。由于ＤＨＡ具有上述生理功能 ,已在医药、食品、保健品等领域得到广泛应用。目前 ,商品ＤＨＡ主要来源于深海鱼油 ,如沙丁鱼、金枪鱼等鱼油 ,由于鱼…     

稀土元素对红豆杉细胞悬浮培养及紫杉醇合成的影响

研究了在250mL摇瓶中,不同浓度的硝酸镧、硫酸铈铵、硝酸亚铈3种稀土化合物对细胞生长及紫杉醇分泌和释放的影响。结果表明,在培养初期加入稀土元素。3种不同稀土化合物对细胞生长影响强弱不同,但趋势相似,均使细胞的延迟期缩短。1ppm的Ce^4 促进细胞生长的效果最明显。细胞干重第17d达到10.9g/L。在指数期加入稀土元素。10ppmCe^3 刺激细胞生长的效果最明显,细胞干重最高值达到11.5g/dL,比对照高1.5g/L,而10ppm的La^3 抑制细胞的生长。经稀土元素处理后,细胞胞内和胞外紫杉醇含量都有大幅度的提高,其中以10ppmCe^3 处理,胞外紫杉醇释放率最大,达37.7%。     

人肝细胞生长因子(hdHGF)基因在毕赤酵母中的分泌表达

研究了hdHGF基因在毕赤酵母中的表达 .以人胎盘mRNA为模板 ,经逆转录、重叠PCR获得hdHGF全长和成熟基因片段 .将该基因片段克隆到pPIC9载体上 ,将重组表达质粒转化巴斯德毕赤酵母 (Pichiapastoris)GS115,筛选mut+ 表型 ,经甲醇诱导可实现rhdHGF的分泌表达 .经摇瓶培养筛选出 4株表达水平较高的酵母工程菌株 ,SDS PAGE分析和Western印迹试验表明 ,产物分子量约为80kD ,5L发酵罐高密度培养已使生物量达 13 5g L(干重 ) ,发酵液上清总蛋白量为 8 0g L ,电泳结果表明rhdHGF表达水平为总蛋白的 12 3 % .     

Production of unnatural glucosides of curcumin with drastically enhanced water solubility by cell suspension cultures of Catharanthus roseus

Catharanthus roseus cell suspension cultures converted exogenously supplied curcumin to a series of glucosides, none of which has been found in nature so far. The efficiency of glucosylation was dependent on culture stage of the cells and medium sucrose concentration. Methyl jasmonate and salicylic acid enhanced the glucoside formation only when they were added to the cultures prior to the addition of curcumin. The glucoside yield was 2.5 micromol/g fresh weight of the cells at an optimal culture condition. The water solubility of curcumin-4',4"-O-beta-D-digentiobioside was 0.65 mmol/ml, which was 20 million-fold higher than that of curcumin.     

聚乙二醇对东北红豆杉培养细胞的

在改良的B     

Controlling substrate concentration in fed-batch candida magnoliae culture increases mannitol production

Candida magnoliae HH-01, a yeast strain that is currently used for the industrial production of mannitol, has the highest mannitol production ever reported for a mannitol-producing microorganism. However, when the fructose concentration exceeds 150 g/L, the volumetric mannitol production rate decreases because of a lag in mannitol production, and the yield decreases as a result of the formation of side products. In fed-batch culture, the volumetric production rate and mannitol yield from fructose vary substantially with the fructose concentration and are maximal at a controlled fructose concentration of 50 g/L. In continuous feeding experiments, the maximum mannitol yield was 85% (g/g) at a glucose/fructose feeding ratio of 1/20. A high glucose concentration in the production phase resulted in the formation of ethanol followed by a decrease in yield and productivity. NAD(P)H-dependent mannitol dehydrogenase was purified to homogeneity from C. magnoliae. In vitro, mannitol dehydrogenase was inhibited by increasing ethanol concentration. Mannitol product was also found to be inhibitory with a K(i) of 183 mM. Under optimum conditions, a final mannitol production of 213 g/L was obtained from 250 g fructose/L after 110 h.     

Co-production of biomass and metabolites by cell retention culture of <Emphasis Type="Italic">Leuconostoc citreum</Emphasis>

Cell retention culture of lactic acid bacterium Leuconostoc citreum was carried out in a fermentor equipped with an internal ceramic filtration system to co-produce biomass and metabolites. The filtration system was composed of porous ceramic filter module with pore size of 0.1 μm and total surface area of 330 cm². High cell density cultivation of L. citreum was achieved within the fermentor, while extracellular metabolites such as mannitol and d-lactic acid were produced through the filter with high productivities. In batch culture of L. citreum using a medium containing 50 g/L of glucose and 100 g/L of fructose, the maximum optical density (OD) monitored at 660 nm was 13 with 65 g/L of mannitol and 38 g/L of lactic acid. In cell retention culture of L. citreum with dilution rate of 0.07 h⁻¹, OD increased to 75, which was 6 times higher than that in batch culture. The concentrations of mannitol and lactic acid increased to 85 and 45 g/L, respectively, and were maintained throughout the cultivation to 105 h. By increasing dilution rate to 0.13 h⁻¹, the productivities of mannitol and lactic acid increased to 8.5 and 4.2 g/L/h, respectively, which were 2.7 to 3 times higher than those in batch culture, suggesting that cell retention culture using internal filtration system is highly effective for co-production of useful cell biomass and various extracellular metabolites.     

Production of mannitol and lactic acid by fermentation with Lactobacillus intermedius NRRL B-3693

Lactobacillus intermedius B-3693 was selected as a good producer of mannitol from fructose after screening 72 bacterial strains. The bacterium produced mannitol, lactic acid, and acetic acid from fructose in pH-controlled batch fermentation. Typical yields of mannitol, lactic acid, and acetic acid from 250 g/L fructose were 0.70, 0.16, and 0.12 g, respectively per g of fructose. The fermentation time was greatly dependent on fructose concentration but the product yields were not dependent on fructose level. Fed-batch fermentation decreased the time of maximum mannitol production from fructose (300 g/L) from 136 to 92 h. One-third of fructose could be replaced with glucose, maltose, galactose, mannose, raffinose, or starch with glucoamylase (simultaneous saccharification and fermentation), and two-thirds of fructose could be replaced with sucrose. L. intermedius B-3693 did not co-utilize lactose, cellobiose, glycerol, or xylose with fructose. It produced lactic acid and ethanol but no acetic acid from glucose. The bacterium produced 21.3 +/- 0.6 g lactic acid, 10.5 +/- 0.3 g acetic acid, and 4.7 +/- 0.0 g ethanol per L of fermentation broth from dilute acid (15% solids, 0.5% H(2)SO(4), 121 degrees C, 1 h) pretreated enzyme (cellulase, beta-glucosidase) saccharified corn fiber hydrolyzate.     

盐胁迫下沙棘的渗透调节效应

分别用含有0、100、200和300mmol LNaCl的Hoagland培养液处理1年生沙棘(HippophaerhamnoidesL.)苗30d后,测定其鲜重,干重,含水量,可溶性糖、脯氨酸和无机离子(Na 、Cl-)的含量及叶片渗透势和渗透调节能力。结果表明:100mmol LNaCl处理的沙棘地上部和根的鲜重和干重最大,其含水量也最大;NaCl浓度超过100mmol L时,沙棘地上部分和根的鲜重和干重随盐浓度增加而逐步下降,其下降的趋势为地上部大于根部。随NaCl浓度不断升高,沙棘体内Na 和Cl-浓度随之升高,茎叶和根系中Cl-含量明显高于Na ,对Na 的相对吸收量多于Cl-。沙棘对盐胁迫有一定的适应能力,随NaCl浓度的升高,沙棘叶内脯氨酸含量升高,可溶性糖含量增加,渗透势降低,渗透调节能力增强。本结果可为盐碱地营造沙棘林提供依据。