营养条件对pcDNA3\|HBS质粒DNA生产的影响

为了考查营养条件对质粒DNA的生产影响,采用不同的培养基培养含pcDNA33-HBS质粒的大肠杆菌JM109。实验结果表明：碳源、氮源对质粒DNA产量有明显的影响。葡萄糖是质粒合成过程中较佳的碳源,蛋白胨是较佳的氮源。在M9P培养基中,选择合适的硫酸铵浓度对质粒DNA的生产有一定的作用。由于Gly,Asp,Glu能提供合成核苷酸的氮源,在M9G培养基中添加12g/L的Asp,1.0g/L的Glu和0.4g/L的Gly后,经20h培养,质粒产量可达25mg/L。外源核苷也影响质粒DNA的产量,通过添加0.4g/L胞苷与胸苷的混合物(摩尔比为1∶1)到M9P培养基中,质粒DNA的产量可达35mg/L。     

pcD-awte候选疟疾DNA疫苗发酵条件的探索

探索pcD-awte候选疟疾DNA疫苗发酵条件,为该疫苗制备工艺的建立做准备.通过摇瓶和5 L发酵罐水平,考察不同培养基组成及来源、补料变化和温度转换对工程菌生长及质粒产量的影响.结果表明在TB培养基组分中添加Mg2+、微量元素复合物、核苷等成分,补料培养基由葡萄糖代替甘油,对数中期温度由37℃升至42℃等条件,能提高工程菌株pcD-awte质粒的产量.在优化的培养条件下pcD-awte质粒产量可达125～130mg/L培养液.     

高产类胡萝卜素酵母菌株LRY-01发酵条件的优化研究

通过单因子实验研究了不同碳源、氮源、生长因子及通气量对菌株LRY-01生产类胡萝卜素的影响。实验表明,碳源、氮源、生长因子对类胡萝卜素产量的影响较大。进一步对上述因子进行了L9(34)正交实验,得到了最佳培养基配方及发酵条件:葡萄糖40g/L,(NH4)2SO41.0g/L,核黄素0.5mL/L,酵母膏0.5g/L,初始pH 4.5,摇瓶装液量为10%。菌株LRY-01在此条件下摇瓶培养72h的生物量和类胡萝卜素的产量分别可达16.19g/L和1000.06μg/g。     

peD—awte候选疟疾DNA疫苗发酵条件的探索

探索pcD—awte候选疟疾DNA疫苗发酵条件,为该疫苗制备工艺的建立做准备。通过摇瓶和5L发酵罐水平,考察不同培养基组成及来源、补料变化和温度转换对工程菌生长及质粒产量的影响。结果表明在TB培养基组分中添加Mg^2＋、微量元素复合物、核苷等成分,补料培养基由葡萄糖代替甘油,对数中期温度由37％升至42℃等条件,能提高工程菌株pcD—awte质粒的产量。在优化的培养条件下pcD—awte质粒产量可达125—130mg／L培养液。     

碳氮源对转基因鱼腥藻Anabaena sp.PCC7120培养的影响

对碳源、氮源种类和用量对转rhTNF-α基因鱼腥藻7120（Anabaena sp.PCC7120）培养的影响进行了研究,发现最适碳源为蔗糖,最适氮源为NaNO3,最佳用量分别为9g/L和2．25g/L,此时生物量远高于自养方式,达2．52g/L,比相同条件下在BG－11培养基培养高71．66％,ATNF－α表达量为16％－22％,生物活性为10^5U/mg。     

几种生物学因子对薰衣草胚性愈伤组织悬浮培养生长的影响

通过研究接种量、培养基、碳源、氮源及激素组合等生物学因子对薰衣草胚性愈伤组织悬浮培养生长的影响,建立了一种可快速生长的薰衣草胚性愈伤组织悬浮培养体系。结果表明,在添加0.05mg/L2,4-D、0.5mg/L6-BA、30g/L蔗糖及0.5g/L水解酪蛋白的MS培养液中,以50g/L的接种量进行薰衣草胚性愈伤组织的悬浮培养,其生长速率可达24.14g/(L·d)。     

红曲霉液态发酵生产Monacolin K培养基的优化

利用正交试验设计对红曲霉TQ-57发酵生产Monacolin K的摇瓶发酵培养基进行了初步研究。结果表明:Monacolin K的最适发酵碳源为甘油,最佳添加质量分数为14%,最适氮源为蛋白胨,最佳氮源质量分数为3%,培养基初始pH为6.5,培养周期为8 d,在此条件下Monacolin K产量可达27.75 mg/L。     

中国红豆杉细胞悬浮体系营养条件的优化

采用均匀设计的试验方法,对中国红豆杉细胞悬浮体系培养条件进行优化,获得了关于细胞生长与培养基内碳源,氮源,磷浓度的回归方程,表明碳氮是影响细胞生长的关键因素。采用中心组合实验设计对培养基成分继续优化,并通过回归分析,结果表明,较优的培养基为碳源33．9g/L,氮源58．2mmol/L,磷浓度为5mmol/L,此工艺在15L反应器中,也取得了良好效果。     

临床等级质粒DNA的实验室制备

在实验室有效获得100 mg临床试验等级的质粒DNA.摇床发酵3个批次,每批次4 L培养液,产生大约160 g的细菌沉淀物.碱裂解菌体,气浮法结合离心分离浮杂沉淀.裂解液经0.45/0.22 μm囊式过滤器过滤.然后采用阴离子色谱介质富集质粒,异丙醇沉淀.重新溶解沉淀后采用100 kD切向流超滤处理,获得100 mg临床试验等级质粒DNA.体外、体内转染试验对质粒表达效果进行了鉴定.结果表明,纯化的质粒DNA几乎检测不到内毒素、RNA和蛋白质,A260/A280比值在1.82～1.86范围内.纯化的质粒DNA能够满足动物临床试验.     

碳源、氮源对异养单针藻Monoraphidium sp. FXY-10油脂积累和脂肪酸组成的影响

研究了碳源与氮源对单针藻Monoraphidium sp. FXY-10异养培养的影响。以BG-11为基础培养基,通过添加不同类型、浓度梯度碳源和氮源,比较分析微藻生物量、油脂积累以及脂肪酸组成。结果表明,以葡萄糖作碳源,硝酸钠为氮源,微藻细胞积累的油脂是理想的生物柴油制备原料。硝酸钠浓度分别为1.00、3.00和5.00 g/L时,对油脂产量影响不显著(P>0.05)。葡萄糖浓度为10.00 g/L,硝酸钠为氮源油脂产量达到实验最高值0.84 g/L,其油脂脂肪酸组成主要由C16:0和C18:1等短链饱和脂肪酸和单不饱和脂肪酸组成,不饱和度值(DU)为61.98,相对偏低。     

Optimization of medium components for plasmid production by recombinant<Emphasis Type="Italic">E. coli</Emphasis> DH5α pUK21CMVβ1.2

In this study we investigated the effects of carbon and nitrogen sources, and the carbon to nitrogen ratio (C:N) of growth medium on the production of plasmid DNA by pUK21CMVβ1.2 harbouring recombinantE. coli. The results indicated that sucrose and casein peptone were the most suitable carbon and nitrogen sources, respectively, for plasmid production, and the plasmid concentration was significantly influenced by the C:N ratio. A Box-Behnken design and surface response methodology were employed to formulate the optimal medium. In the optimized medium, a plasmid concentration of 51.80 mg/L and a plasmid selectivity of 23.49 mg/g were achieved after 24 h of incubation. These values were approximately 3.5 and 1.7 times higher, respectively, than those obtained on the original LB medium.     

少动鞘脂单胞菌产结冷胶发酵培养基的响应面法优化

通过单因素试验分析不同碳源、氮源、无机盐对（Sphingomonas paucimobilisFJAT-5627）产胶量的影响,确定最适碳源、氮源、无机盐,并在单因素筛选试验的基础上,利用Box-Benhnken设计和响应面分析法对碳源、氮源和无机盐进行优化,得到少动鞘脂单胞菌产生结冷肢发酵培养基最佳优化组合.实验结果表明,少动鞘脂单胞菌产胶量发酵最适碳源、氮源和无机盐分别为淀粉、豆饼粉和KH₂PO₄.响应面法得到产胶量（Y）与碳源淀粉（x₁）、氮源豆饼粉（x₂）和无机盐KH₂PO₄（x₃）的回归方程为:Y=13.87+0.54x₁+0.22x₂-0.42x₃-3.26x₁²-1.85x₂²-1.51x₃²+0.053x₁x₂+0.067x₁x₃+0.4x₂x₃.优化培养基组合为:淀粉浓度为30g/L,豆饼粉浓度为5 g/L,KH₂PO₄的浓度为0.7g/L,且此组合下少动鞘脂假单胞发酵得到结冷胶可达23.87g/L.     

<Emphasis Type="Italic">Escherichia coli</Emphasis> high-cell-density culture: carbon mass balances and release of outer membrane components

Carbon mass balances were calculated in fed-batch cultures of E. coli W3110, using mineral medium with glucose as the limiting substrate. The carbon recovery, based on biomass, CO(2), and acetate was approximately 90% at the end of the culture (25 h, 27 g L(-1) dw). The missing carbon remained as soluble organic compounds in the medium. Outer membrane (OM) constituents, such as lipopolysaccharides (LPS), phospholipids (PL), and carbohydrates (each at approximately 1 g L(-1)) contributed to 63% of the extracellular carbon. The amount of released LPS and PL equaled the total amount of OM bound to the cells in the culture. Small amounts of DNA and protein detected in the medium indicated that no cell lysis had occurred. Acetate, lactate, ethanol, formate, succinate and amino acids (Glu, Gln, Asp, Asn, Ala, Gly, Ser) were detected in the culture medium, but made up only a few percent of the extracellular carbon mass. The remaining 30% was not identified, but was assumed to constitute complex carbohydrates.     

Effects of growth condition on the structure of glycogen produced in cyanobacterium Synechocystis sp. PCC6803

Growth and glycogen production were characterized for Synechocystis sp. strain PCC6803 grown under continuous fluorescent light in four variations of BG-11 medium: either with (G+) or without (G−) 5 mM glucose, and with a normal (N+, 1.5 g sodium nitrate/L) or a reduced (N−, 0.084 g sodium nitrate/L) nitrogen concentration. Glucose-supplemented BG-11 with a normal nitrogen concentration (N+G+) produced the highest growth rate and the greatest cell density. Although the maximum cell mass production was observed in the N+G+ medium, the highest glycogen yield (19.0 mg/g wet cell mass) was achieved under the glucose-supplemented, nitrogen-limiting condition (N−G+). The addition of glucose enhanced cell growth, while nitrogen limitation apparently directed carbon flux into glycogen accumulation rather than cell growth. Transmission electron microscopic analysis showed that, under nitrogen-limiting conditions (N−G+), glycogen particles accumulated in large amounts and filled the cytosol of the cells. Analysis by high-performance size-exclusion chromatography further revealed that the glycogen produced in N−G+ medium had the longest average branch chain-length (DP10.4) among the conditions tested. When the yield and structure of glycogen were examined in different growth phases, the greatest yield (36.6 mg/g wet cell mass) and the longest branch chain-length (DP10.7) were observed 2 days after the fully grown cells in the N+G+ medium were transferred to the growth restricting (N−G+) medium.     

Rhamnolipid production with indigenous Pseudomonas aeruginosa EM1 isolated from oil-contaminated site

Rhamnolipid is one of the most effective and commonly used biosurfactant with wide industrial applications. Systematic strategies were applied to improve rhamnolipid (RL) production with a newly isolated indigenous strain Pseudomonas aeruginosa EM1 originating from an oil-contaminated site located in southern Taiwan. Seven carbon substrates and four nitrogen sources were examined for their effects on RL production. In addition, the effect of carbon to nitrogen (C/N) ratio on RL production was also studied. Single-factor experiments show that the most favorable carbon sources for RL production were glucose and glycerol (both at 40 g/L), giving a RL yield of 7.5 and 4.9 g/L, respectively. Meanwhile, sodium nitrate appeared to be the preferable nitrogen source, resulting in a RL production of 8.6g/L. Using NaNO(3) as the nitrogen source, an optimal C/N ratio of 26 and 52 was obtained for glucose- and glycerol-based culture, respectively. To further optimize the composition of fermentation medium, twenty experiments were designed by response surface methodology (RSM) to explore the favorable concentration of three critical components in the medium (i.e., glucose, glycerol, and NaNO(3)). The RSM analysis gave an optimal concentration of 30.5, 18.1, and 4.9 g/L for glucose, glycerol, and NaNO(3), respectively, predicting a maximum RL yield of 12.6 g/L, which is 47% higher than the best yield (8.6 g/L) obtained from preliminary selection tests and single factor experiments (glucose and NaNO(3) as the carbon and nitrogen source). The NMR and mass spectrometry analysis show that the purified RL product contained L-rhamnosyl-beta-hydroxydecanoyl-beta-hydroxydecanoate (RL1) and L-rhamnosyl L-rhamnosyl-beta-hydroxydecanoyl-beta-hydroxydecanoate (RL2). Meanwhile, HPLC analysis indicates that the molar ratio of RL1 and RL2 in the purified rhamnolipid product was ca. 1:1.     

Characterization of Cellulose Production by a Gluconacetobacter xylinus Strain from Kombucha

The aims of this work were to characterize and improve cellulose production by a Gluconoacetobacter xylinus strain isolated from Kombucha and determine the purity and some structural features of the cellulose from this strain. Cellulose yield in tea medium with both black tea and green tea and in Hestrin and Schramm (HS) medium under both static and agitated cultures was compared. In the tea medium, the highest cellulose yield was obtained with green tea (~0.20 g/L) rather than black tea (~0.14 g/L). Yield in HS was higher (~0.28 g/L) but did not differ between static and agitated incubation. ¹H-NMR and ¹³C-NMR spectroscopy indicated that the cellulose is pure (free of acetan) and has high crystallinity, respectively. Cellulose yield was improved by changing the type and level of carbon and nitrogen source in the HS medium. A high yield of ~2.64 g/L was obtained with mannitol at 20 g/L and corn steep liquor at 40 g/L in combination. In the tea medium, tea at a level of 3 g/L gave the highest cellulose yield and the addition of 3 g/L of tea to the HS medium increased cellulose yield to 3.34 g/L. In conclusion, the G. xylinus strain from Kombucha had different cellulose-producing characteristics than previous strains isolated from fruit. Cellulose was produced in a pure form and showed high potential applicability. Our studies extensively characterized cellulose production from a G. xylinus strain from Kombucha for the first time, indicating both similarities and differences to strains from different sources.     

利用重组Pichia pastoris生产腺苷甲硫氨酸

为改造甲醇利用型酵母Pichia pastoris来生产腺苷甲硫氨酸（SAM,S－adenosyl-L-methionine),我们将一个带有SAM合成酶基因的胞内表达质粒转化入Pichia pastoris菌株GS115,经过G418抗性筛选得到一株有两个基因拷贝的转化子。该菌在含有甲醇和甲硫氨酸的培养基中生长5d后,其细胞内的SAM的产量比原始菌株提高了30余倍。对该菌生产SAM的培养基中的碳源与氮源进行了优化,结果显示碳源的控制对该菌SAM产量的影响很大。在试管水平,该菌在含有0．75％的L-methionine并且碳源和有机氮源经过一定程度优化的培养基中,生长6d后SAM产量达到1．58g/L。     

Sporulation of several biocontrol fungi as affected by carbon and nitrogen sources in a two-stage cultivation system

The development of fungal biopesticides requires the efficient production of large numbers spores or other propagules. The current study used published information concerning carbon concentrations and C:N ratios to evaluate the effects of carbon and nitrogen sources on sporulation of Paecilomyces lilacinus (IPC-P and M-14) and Metarhizium anisopliae (SQZ-1-21 and RS-4-1) in a two-stage cultivation system. For P. lilacinus IPCP, the optimal sporulation medium contained urea as the nitrogen source, dextrin as the carbon source at 1 g/L, a C:N ratio of 5:1, with ZnSO(4)·7H(2)O at 10 mg/L and CaCl(2) at 3 g/L. The optimal sporulation medium for P. lilacinus M-14 contained soy peptone as the nitrogen source and maltose as the carbon source at 2 g/L, a C:N ratio of 10:1, with ZnSO(4)·7H(2)O at 250 mg/L, CuSO(4)·5H(2)O at 10 mg/L, H(3)BO(4) at 5 mg/L, and Na(2)MoO(4)·2H(2)O at 5 mg/L. The optimum sporulation medium for M. anisopliae SQZ-1-21 contained urea as the nitrogen source, sucrose as the carbon source at 16 g/ L, a C:N ratio of 80:1, with ZnSO(4)·7H(2)O at 50 mg/L, CuSO(4)·5H(2)O at 50 mg/L, H(3)BO(4) at 5 mg/L, and MnSO(4)·H(2)O at 10 mg/L. The optimum sporulation medium for M. anisopliae RS-4-1 contained soy peptone as the nitrogen source, sucrose as the carbon source at 4 g/L, a C:N ratio of 5:1, with ZnSO(4)·7H(2)O at 50 mg/L and H(3)BO(4) at 50 mg/L. All sporulation media contained 17 g/L agar. While these results were empirically derived, they provide a first step toward low-cost mass production of these biocontrol agents.     

Growth and biomass production with enhanced β‐glucan and dietary fibre contents of Ganoderma australe ATHUM 4345 in a batch‐stirred tank bioreactor

In this study we maximized biomass production by the basidiomycete Ganoderma australe ATHUM 4345, a species of pharmaceutical interest as it is a valuable source of nutraceuticals, including dietary fibers and glucans. We used the Biolog FF MicroPlate to screen 95 different carbon sources for growth monitoring. The pattern of substrate catabolism forms a substrate assimilation fingerprint, which is useful in selecting components for media optimization of maximum biomass production. Response surface methodology, based on the central composite design was applied to explore the optimum concentrations of carbon and nitrogen sources of culture medium in shake flask cultures. When the improved culture medium was tested in a 20‐L stirred tank bioreactor, using 13.7 g/L glucose and 30.0 g/L yeast extract, high biomass yields (10.1±0.4 g/L) and productivity of 0.09 g L^?1 h^?1 were obtained. The yield coefficients for total glucan and dietary fibers on biomass formed were 94.82±6 and 341.15±12.3 mg/g mycelium dry weight, respectively.     

Optimization of submerged fermentation medium for citrinin-free monascin production by Monascus

Microbial fermentation of citrinin-free Monascus pigments is in favor in the development of food industry. This study investigated the influences of carbon source, nitrogen source, and mineral salts on the cell growth, monascin (MS), and citrinin (CT) production in Monascus M9. A culture medium composition was established for maximizing the production of citrinin-free MS in submerged culture, as follows: 50?g/L Japonica rice powder, 20?g/L NH₄NO₃, 3?g/L NaNO₃, 1.5?g/L KH₂PO₄, 1?g/L MgSO₄?·?7H₂O, 0.2?g/L MnSO₄. Under these conditions, no CT was detectable by high performance liquid chromatography. The yield of MS reached 14.11?mg/g, improving approximately 30% compared with before optimization.