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不同添加物对D-核糖产量的影响 总被引:3,自引:0,他引:3
采用短小芽孢杆菌转酮酶缺陷突变株 ,通过先后向培养基中添加适量的葡萄糖酸钠、Mn2 + ,直接或间接地影响D 核糖的生物合成途径 ,最终影响D 核糖的产量。此外向培养基中添加芳香族氨基酸中的酪氨酸 ,有机酸中的山梨酸可以促进D 核糖的生物合成 ,使其产量达 6 4.2 g/L。 相似文献
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几种添加物对D—核糖产量的影响 总被引:1,自引:0,他引:1
研究了几种物质对D-核糖产量的影响,研究表明,当发酵培养基中玉米浆的含量为25g/L,D-核糖产量达到最高,为65g/L。发酵培养基中添加适量的粉及山梨醇亦有利于D-核糖的积累,当粉与山梨醇的添加量分别为10g/L及40g/L时,D-核糖产率分别增加7.8%、4.7%,而在发酵培养基中加入丙二酸可抑制D-核的分泌,在40ml发酵培养基中添加1ml丙二酸后,D-核糖的产率下降73.8%。甲醇也可抑制D-核糖的积累,当发酵培养基中的甲醇添加量为16g/L时,D-核糖产率下降66.2%。 相似文献
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D-核糖发酵过程参数的研究与控制 总被引:5,自引:0,他引:5
以7L自控发酵罐进行D-核糖发酵实验,对D-核糖发酵过程参数进行优化,发现对数生长后期接种,溶氧控制在40%左右,以葡萄糖酸补料并调节pH值在7.2左右,可使罐的发酵单位由45g/L提高至65g/L左右。 相似文献
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pH值对D-核糖发酵的影响及补料发酵的研究 总被引:3,自引:1,他引:3
研究了不同 pH值对D 核糖产量的影响。发酵初期pH自然下降时有利于菌体生长 ,菌体生长对数期较长 ,菌体质量浓度最高可达 15 .3g/L ;发酵中后期 pH值控制在 7.0时有利于D 核糖的持续合成 ,同时对D -核糖的流加补料发酵进行了初步研究 ,最终使菌体质量浓度最高达到 2 0 .1g/L ,D 核糖产量达到了 6 2 .5g/L。 相似文献
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研究了初始葡萄糖浓度对D -核糖发酵的影响 ,证实了较高的葡萄糖浓度对D -核糖发酵的抑制作用 ,并确定了较为适宜的初始葡萄糖浓度为 1 0 0g·L-1 或 1 5 0g·L-1 。前者条件下D -核糖的转化率和生产强度均达最大 ,分别为 32 8g·kg-1 和0 .6 8g·L-1 ·h-1 ;后者条件下D -核糖的产量达最大值 39.4 8g·L-1 。针对底物抑制现象 ,研究了补料工艺对D -核糖发酵的影响 ,确定发酵 2 4h后补加 5 0g·L-1 的葡萄糖为较优的补料工艺 ,在此工艺条件下最终D -核糖产量相对于对照组提高了 4 8.3%。 相似文献
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本文研究了不同碳源对须糖多孢菌生长以及丁烯基多杀菌素生物合成的影响,通过寻找优势碳源优化发酵培养基配方,促进须糖多孢菌丁烯基多杀菌素的生物合成。试验共设11个处理,1个对照,通过单因素试验比较不同处理组菌体OD600值和丁烯基多杀菌素产量,筛选获得最优碳源及其发酵培养基配方。结果表明,除可溶性淀粉和木糖外,须糖多孢菌在9种碳源中都能进行生长,对不同构型碳源显示较好的利用率。在以半乳糖、葡萄糖、果糖和甘露糖作为碳源时具有较好的生长速率,而以甘露糖为碳源时能显著促进丁烯基多杀菌素的合成。选择甘露糖最佳添加浓度为5 g/L,须糖多孢菌最高菌体浓度和丁烯基多杀菌素产量分别是初始配方条件的1. 32倍和1. 78倍,显著提高了丁烯基多杀菌素的产量。上述结果为培养基碳源对丁烯基多杀菌素生物合成影响机制的研究及丁烯基多杀菌素大规模工业化发酵生产提供了科学依据和新的技术途径。 相似文献
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为研究发酵碳源对铜绿假单胞菌NY3所产鼠李糖脂结构及性能的影响,从鼠李糖脂的结构组分、性能和应用效果等方面展开研究。薄层实验证明两种鼠李糖脂均含有单糖脂和双糖脂。液质分析发现以橄榄油作碳源时,鼠李糖脂中双糖脂(Rha-Rha-C5-C6:1和Rha-Rha-C8-C8:2)比例更大,约为73.09%。而地沟油作碳源时,单糖脂(Rha-C10-C10和Rha-C16-C16:2)的比例更高,约为76.91%。橄榄油和地沟油为碳源的鼠李糖脂的临界胶束浓度(CMC)分别为55 mg/L和80mg/L。相同投加量时,前者乳化性和乳化稳定性均优于后者。NY3菌降解含油污泥时,投加双糖脂含量高的鼠李糖脂会使C16-C30直链烷烃的去除率更高。 相似文献
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van de Laar T Visser C Holster M López CG Kreuning D Sierkstra L Lindner N Verrips T 《Biotechnology and bioengineering》2007,96(3):483-494
Saccharomyces cerevisiae is a widely used host organism for the production of heterologous proteins, often cultivated in glucose-based fed-batch processes. This production system however has many factors limiting the productivity, mainly towards the end of the fermentation. For the optimised production of a Camelid antibody fragment this process was evaluated. In shake flask cultivations, it was found that ethanol has a strong effect on productivity increase and therefore glucose and ethanol fed-batch fermentations were compared. It appeared that specific heterologous protein production was up to five times higher in the ethanol cultivation and could be further optimised. Then the key characteristics of ethanol fed-batch fermentations such as growth rate and specific production were determined under ethanol limitation and accumulation and growth limiting conditions in the final phase of the process. It appeared that an optimal production process should have an ethanol accumulation throughout the feed phase of approximately 1% v/v in the broth and that production remains very efficient even in the last phase of the process. This productivity increase on ethanol versus glucose was also proven for several other Camelid antibody fragments some of which were heavily impaired in secretion on glucose, but very well produced on ethanol. This leads to the suggestion that the ethanol effect on improved heterologous protein production is linked to a stress response and folding and secretion efficiency. 相似文献
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To decrease the polyhydroxyalkanoate (PHA) production cost by supplying renewable carbon sources has been an important aspect in terms of commercializing this biodegradable polymer. The production of biodegradable poly(3-hydroxyalkanoates) (PHA) from raw potato starch by the Bacillus cereus 64-INS strain isolated from domestic sludge has been studied in a lab-scale fermenter. The bacterium was screened for the degradation of raw potato starch by a starch hydrolysis method and for PHA production by Nile blue A and Sudan black B staining. Shake-flask cultures of the bacterium with glucose [2% (w/v)] or raw potato starch [2% (w/v)] produced PHA of 64.35% and 34.68% of dry cell weight (DCW), respectively. PHA production was also carried out in a 5-L fermenter under control conditions that produced 2.78 g/L of PHA and PHA content of 60.53% after 21 hr of fermentation using potato starch as the sole carbon source. Gas chromatography–mass spectroscopy (GC-MS) analyses confirmed that the extracted PHA contained poly(3-hydroxybutyrate) (PHB) as its major constituent (>99.99%) irrespective of the carbon source used. The article describes, for what we believe to be the first time, PHB production being carried out without any enzymatic or chemical treatment of potato starch at higher levels by fermentation. More work is required to optimize the PHB yield with respect to starch feeding strategies. 相似文献