发酵法生产S-腺苷蛋氨酸前体蛋氨酸补加策略

利用酿酒酵母菌株高密度发酵法生产S-腺苷蛋氨酸关键的影响因素之一是前体L-蛋氨酸的补加策略.本研究采用一支经过常规诱变处理的S-腺苷蛋氨酸优势积累菌株酿酒酵母SAM0801,通过5 L发酵罐高密度发酵实验研究,考察了6种补加策略,最终确定了L-蛋氨酸的加入时机为30h左右,当茵体干重达到100g/L时,补加量为每罐40gL-蛋氨酸,发酵58 h左右达到最高生物量干重168 g/L,产量14.48 g/L.     

S-腺苷-L-蛋氨酸高密度发酵工艺优化

利用酿酒酵母在5L发酵罐高密度发酵生产S-腺苷-L-蛋氨酸(SAM)后期存在稳定性差的问题,本研究考察了在补糖中添加磷酸氢二铵、谷氨酸钠、三磷酸腺苷二钠来提高酿酒酵母发酵后期的稳定性。通过4批5L发酵罐高密度流加发酵实验研究发现:在发酵34h左右,菌体干重超过100g/L后,开始添加50克L-蛋氨酸,并在补糖中加入10g/L三磷酸腺苷二钠,发酵65.7h,最高生物量干重达到180g/L,SAM产量达到17.1g/L。     

代谢过程中相关氨基酸对高密度发酵生产腺苷蛋氨酸的影响

对清酒酵母高密度发酵生产S-腺苷-L-蛋氨酸（SAM）代谢过程中的相关氨基酸进行了考察。分别考察了十二种氨基酸对生物量和SAM产量的影响。实验发现L-胱氨酸、L-半胱氨酸、L-赖氨酸、L-组氨酸和L-蛋氨酸对SAM的积累有利,其中L-赖氨酸和L-组氨酸可以提高生物量,进而提高SAM的产量;L-胱氨酸、L-半胱氨酸和L-蛋氨酸可以提高SAM的含量,但是会抑制生物量的增长。通过3种补加方式的比较,得到最优的补加方式为：L-赖氨酸和L-组氨酸在培养基中加入,L-胱氨酸,L-半胱氨酸和L-蛋氨酸采取在发酵过程前24h流加。通过正交实验确定补加量为：L-赖氨酸为1g／L,L-组氨酸为1g／L,L-胱氨酸为1．5g／L,L-半胱氨酸为1g／L,L-蛋氨酸为1g／L。将此结果应用于5L发酵罐培养,SAM最高产量为5．53g/L,生物量为128g／L。     

发酵生产S-腺苷-L-蛋氨酸培养条件的优化研究

考察了摇瓶发酵生产S-腺苷-L-蛋氨酸过程中碳源、氮源、无机盐和生长因子以及培养过程中补加L-蛋氨酸时间对S-腺苷-L-蛋氨酸的产量、含量及生物量的影响。并通过均匀实验设计对培养基配方进行优化,在30℃、180 r/m in的培养条件下,得到最后的培养基配方为:葡萄糖30g,酵母粉11g,(NH4)2SO412g,K2HPO4.3H2O 5g,KH2PO410g,MnSO4.H2O 0.09g,ZnSO4.7H2O 0.14g,MgC l20.5g,CaC l20.3g,CuSO40.005g,自来水定容至1L。摇瓶中优化后的S-腺苷-L-蛋氨酸产量可以达到0.9g/L,比优化前产量提高了30%。采用优化后的培养基和培养条件在5L发酵罐中间歇培养,24h后一次性补加24g/L葡萄糖和1.0g/L L-蛋氨酸,继续培养24h后产量可达2.66g/L,生物量23.4g/L。     

L-蛋氨酸及甲醇浓度对毕赤酵母摇瓶发酵生产S-腺苷蛋氨酸的影响

利用甲醇传感器及高效液相色谱检测毕赤酵母摇瓶发酵过程的甲醇浓度及S-腺苷蛋氨酸(SAM)浓度,发现L-蛋氨酸浓度及甲醇浓度对毕赤酵母细胞生长及合成S-腺苷蛋氨酸具有影响,据此对摇瓶发酵过程的L-蛋氨酸浓度及甲醇浓度进行优化。优化结果表明:当L-蛋氨酸浓度为7.5 g/L时,最适于SAM积累,产量达到0.83 g/L;进而利用甲醇传感器对发酵过程的甲醇浓度进行检测及控制,考察不同甲醇浓度对SAM产量的影响,毕赤酵母产SAM的最佳甲醇浓度为15 g/L,在此浓度下SAM的产量达到1.41 g/L,比对照实验增加了21%。     

高产腺苷蛋氨酸菌株的诱变选育及培养方式研究

以清酒酵母SAM-04-01为出发菌株,通过紫外线-氯化锂复合诱变的方法,来筛选高产腺苷蛋氨酸菌株。筛菌最终得到一支正突变菌株,其摇瓶产量达到1.0 g/L,比原始菌产量提高了17%。经传代培养考察,该突变菌具有良好的遗传稳定性。同时还考察了两种不同培养方式对腺苷蛋氨酸积累的影响,结果发现一次性补加L-蛋氨酸和葡萄糖溶液对菌体生长有一定的抑制作用,而在菌体达到最大浓度时开始流加前体L-蛋氨酸和葡萄糖溶液则是一种比较好的培养方式,其产量达到了5.34 g/L。     

pH对S-腺苷-L-蛋氨酸发酵的影响

研究了不同pH控制方式对S-腺苷-L-蛋氨酸(SAM)发酵过程及产量的影响。通过对发酵过程中不控制pH、控制恒定pH、两阶段控制pH和三阶段控制pH实验,研究了不同条件下对菌体干重、葡萄糖代谢和SAM产量的影响。控制合适的pH有利于菌体生长与SAM的生物合成,菌体生长最适pH为6.0,SAM转化最适pH为6.5,采用三阶段控制pH,使SAM产量比不控制pH提高了133%,比控制pH6.5提高了18.6%,比两阶段控制pH提高了10%。     

酪氨酸流加方式对重组大肠杆菌发酵生产L-苯丙氨酸的影响

研究了流加浓度对酪氨酸重组大肠杆菌Escherichia coli BR-165(pAP-B03)发酵生产L-苯丙氨酸的影响.结果表明,诱导后L-酪氨酸流加加速了菌体的生长,提高了生产强度,缩短了发酵周期.在流加浓度为75 mg/h时,最大菌体干重达到了40.13 g/L(对照11.48 g/L),生产周期缩短到30 h(对照48 h),生产强度达到1.409 g/h/L(对照0.876 g/h/L).但是L-酪氨酸的流加对L-苯丙氨酸的最终产量没有明显的影响,因此可认为流加酪氨酸是减少发酵时间并提高生产强度的有效方法.本研究获得的酪氨酸流加方式对L-苯丙氨酸的工业化生产具有一定的指导意义.     

毕赤酵母发酵产S-腺苷蛋氨酸的甘油-甲醇混合流加策略

在毕赤酵母发酵生产S-腺苷蛋氨酸(SAM)的诱导阶段,以不同甘油-甲醇比例的甘油-甲醇混合培养基进行诱导培养,结果表明以10%(w/v)甘油含量的甘油-甲醇混合培养基进行诱导培养时最有利于SAM的表达,SAM产量达6.09 g/L,比0%甘油含量条件下的SAM产量提高了20.4%。对诱导方式进行优化,先以100%甲醇诱导24 h,然后再连续流加10%(w/v)甘油含量的甘油-甲醇混合培养基,SAM产量可达7.94 g/L,在此基础上,进一步改进诱导方式,SAM产量得到进一步的提高,达到9.80 g/L。     

发酵生产S-腺苷-L-蛋氨酸培养条件的优化研究*

考察了摇瓶发酵生产S-腺苷-L-蛋氨酸过程中碳源、氮源、无机盐和生长因子以及培养过程中补加L-蛋氨酸时间对S-腺苷-L-蛋氨酸的产量、含量及生物量的影响。并通过均匀实验设计对培养基配方进行优化,在30℃、180 r/m in的培养条件下,得到最后的培养基配方为:葡萄糖30g,酵母粉11g,(NH₄)₂SO₄12g,K₂HPO₄.3H₂O 5g,KH₂PO     

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...     

Production of poly(3-hydroxybutyrate-co-3-hydroxyhexanoate) by Ralstonia eutropha in high cell density palm oil fermentations

Improved production costs will accelerate commercialization of polyhydroxyalkanoate (PHA) polymer and PHA-based products. Plant oils are considered favorable feedstocks, due to their high carbon content and relatively low price compared to sugars and other refined carbon feedstocks. Different PHA production strategies were compared using a recombinant strain of Ralstonia eutropha that produces high amounts of P(HB-co-HHx) when grown on plant oils. This R. eutropha strain was grown to high cell densities using batch, extended batch, and fed batch fermentation strategies, in which PHA accumulation was triggered by nitrogen limitation. While extended batch culture produced more biomass and PHA than batch culture, fed batch cultivation was shown to produce the highest levels of biomass and PHA. The highest titer achieved was over 139 g/L cell dry weight (CDW) of biomass with 74% of CDW as PHA containing 19 mol% HHx. Our data suggest that the fermentation process is scalable with a space time yield (STY) better than 1 g PHA/L/h. The achieved biomass concentration and PHA yield are among the highest reported for the fermentation of recombinant R. eutropha strains producing P(HB-co-HHx).     

强化表达SAM合成酶促进SAM在毕赤酵母中累积

S 腺苷甲硫氨酸 (S adenosyl L methionine ,SAM)是生物体硫代谢的重要中间代谢物质 ,在体内起着转甲基、转硫基、转氨丙基的作用 ,具有重要的药用和保健价值。将酿酒酵母来源的SAM合成酶 2基因置于GAP启动子调控下 ,构建胞内组成型表达质粒 ,并电转化至毕赤酵母菌株GS115。经Zeocin抗性和培养筛选到一株高产SAM的重组菌。对重组菌表达工艺的研究表明 ,碳源、氮源、pH和溶解氧对SAM的累积有较大影响。在优化条件下 ,重组细胞培养 3天 ,SAM累积量可达 2 .49g/L。     

High-cell-density fermentation of recombinant Saccharomyces cerevisiae using glycerol

To obtain a high cell density of recombinant Saccharomyces cerevisiae (INVSc 1 strain bearing a 2 microm plasmid, pYES2 containing a GAL1 promoter for expression of the beta-galactosidase gene), the yeast was grown with glycerol as the substrate by fed-batch fermentation. The feeding strategy was based on an on-line response of the medium pH to the consumption of glycerol. The approach was to feed excess carbon into the medium to create a benign environment for rapid biomass buildup. During cell growth in the presence of glycerol, the release of protons in the medium caused a decrease in pH and the consumption rate of ammonium phosphate served as an on-line indicator for the metabolic rate of the organism. The extent of glycerol feeding in a fed-batch mode with pH control at 5.0 +/- 0.1 was ascertained from the automatic addition of ammonium phosphate to the medium. The glycerol feeding to ammonium phosphate addition ratio was found to be 2.5-3.0. On the basis of the experiments, a maximum dry cell biomass of 140 g per liter and a productivity of 5.5 g DCW/L/h were achieved. The high cell density of S. cerevisiae obtained with good plasmid stability suggested a simple and efficient fermentation protocol for recombinant protein production.     

The role of amino acids in the amplification and quality of DNA vectors for industrial applications

In this study, we have demonstrated that the type and feeding regimen of amino acids have a significant impact on the quality as well as the quantity of DNA vectors produced. Nutrient pool and factorial design experiments were carried out in order to identify the amino acids involved in increased biomass and induction of plasmid amplification. Leucine, glycine, and histidine were responsible for increased biomass and leucine starvation in the presence of histidine was implicated in plasmid amplification. Supercoiling of the plasmid was optimized using a dual feeding strategy. As a result of this, a fed-batch fermentation strategy for the production of a 6.9 kb plasmid, pSVß, in Escherichia coli DH5α was developed. In batch fermentation, a maximum plasmid yield of 39.4 mg/L equivalent to 11.3 mg/g dry cell weight (DCW) was achieved with casein hydrolysate limitation. About 90% of plasmid was in the supercoiled (SC) form after 31 hr of fermentation but only remained so for a short period, leading to a very brief window for harvesting cells at scale. Subsequently, a fed-batch fermentation using a dual feeding strategy was employed. A mean maximum plasmid yield of 44 mg/L equivalent to 9.1 mg plasmid/g DCW was achieved. After 25 hr, 90% of plasmid was in the SC form and remained at this level for the remaining 10 hr of the fermentation, allowing adequate time for the harvesting of cells without the loss of supercoiling of product. This study emphasized that optimizing fermentation strategy and identifying the essential nutrients are beneficial for bioprocessing of plasmid DNA for therapeutic applications.     

营养条件和流加发酵对放射型根瘤菌(Rhizobium radiobacter)产辅酶Q10的影响

利用放射型根瘤菌WSH2 6 0 1(RhizobiumradiobacterWSH2 6 0 1)重点考察了葡萄糖、蔗糖、玉米浆和蛋白胨、添加物以及流加发酵对细胞生长和产辅酶Q1 0 的影响 ,结果表明 ,葡萄糖和蔗糖适合于生产辅酶Q1 0 的最佳浓度分别为 30g L和 40g L ;辅酶Q1 0 发酵时玉米浆和蛋白胨的最适浓度分别为 11g L和 16g L ;添加蕃茄汁、玉米浆能提高发酵液的生物量 ,玉米浆、异戊醇、L 甲硫氨基酸等能促进辅酶Q1 0 的积累 ;与分批发酵相比 ,在 7L罐上流加蔗糖其细胞生物量 (DCW)和辅酶Q1 0 积累量增加 ,若在流加蔗糖的同时流加适当浓度的玉米浆能显著提高辅酶Q1 0 的产量 ,最大产量达到 5 2 .4mg L ;最大生物量 (DCW)和胞内辅酶Q1 0 含量 (C B值 )分别达到 2 6 .4g L和 2 .38mg g DCW ,比不流加的分批发酵分别提高 5 3 %和 33% ,比只流加蔗糖分别提高 2 4%和 2 6 %。