高密度发酵生产突变型重组人肿瘤坏死因子rhTNFα-DK2的研究

通过对发酵基质和发酵关键参数的优化,确定了发酵培养基的磷酸盐浓度为０．１５Ｍ,甘油浓度为１．２ｍｌ／Ｌ,补料中甘油浓度为２０ｍｌ／Ｌ,发酵过程中溶解氧控制在３０％～６０％,ｐＨ控制在６．８５左右。在５Ｌ在ＮＢＳ－Ｂｉｏｆｌｏ３０００型自动控制发酵罐中采取加速补料的补料分批培养,重组大肠杆菌ＹＫ５３７／ｐＳＢ－ＴＫ经１０ｈ３０°Ｃ培养和５ｈ４２°Ｃ诱导培养,最终密度达到６０ＯＤ６００,ｒｈＴＮＦα－ＤＫ２的表达量占菌体总蛋白的５０％以上,每升发酵液纯化可得到近２ｇ的ｒｈＴＮＦα－ＤＫ２。     

高密度培养大肠杆菌YK537/pSBHL-11生产重组人细胞白介素

在 Ｂ． Ｂｒａｕｎ Ｅ Ｓ１０ 型１５ Ｌ 和 Ｎ Ｂ Ｓ Ｂｉｏ Ｆｌｏ ３０００ 型５ Ｌ 发酵罐中,利用补料分批培养技术高密度表达培养含重组质粒ｐ Ｓ Ｂ Ｈ Ｌ１１ 的大肠杆菌 Ｙ Ｋ５３７ ,生产重组人白细胞介素３（ Ｉ Ｌ３） ,发现在发酵过程中,限制性流加甘油,控制溶解氧在３０ ％ ～４０ ％ 左右、３０ ℃生长１１ｈ ,４２ ℃诱导培养４ｈ ,能将发酵液中最终菌体密度从 Ｏ Ｄ１６６００ 提高到 Ｏ Ｄ５３６００（ 相当于每升发酵液含１０６ 克湿菌体） ,并且保持了白细胞介素３ 的表达量,占菌体总蛋白的３０ ％ 左右,含量超过３３ ％ ｇ／ Ｌ,使 Ｉ Ｌ３ 包涵体产量从湿重２２ｇ／ Ｌ 提高到８５ ｇ／ Ｌ,纯化步骤比较简单,超声破菌后经两次洗涤纯度就达到７０ ％ 以上。     

高密度培养大肠杆菌YK537／pSBHL—11生产重组人细胞白介素—3

在Ｂ．Ｂｒａｕ ＥＳ－１０型１５Ｌ和ＮＢＳ ＤｉｏＦｌｏ３０００型５Ｌ发酵罐中,利用补料分批培养技术高工表达培养含重组质粒ｐＳＢＨＬ－１１的大肠杆菌ＹＫ５３７,生产重组人白细胞介素－３（ＩＬ－３）,发现在发酵过程中,限制性流加甘油,控制溶解氧在３０％－４０％左右,３０℃生长,１１ｈ,４２℃诱导培养４ｈ,能将发酵液中最终菌体密度从ＯＤ１６６００提高到ＯＤ５３６００,并且保持了白细胞介素－３的表达量。     

脱氧雪腐镰刀菌烯醇对K~＋刺激的小麦根质膜ATP酶活性、K~＋吸收、外渗及再分配的影响

１０－８ｍｏｌ／Ｌ的ＤＯＮ毒素加入小麦根质膜制剂中可促进Ｋ＋刺激的ＡＴＰ酶活力,１０－６ｍｏｌ／Ｌ开始呈抑制效应,抑制程度随ＤＯＮ浓度加大而提高。根尖（５ｃｍ）离体根段于０．５ｍｍｏｌ／Ｌ的ＫＣｌ中,１０－８ｍｏｌ／Ｌ的ＤＯＮ能促进根段Ｋ＋吸收,１０－６ｍｏｌ／Ｌ以上浓度则Ｋ＋吸收呈抑制,１０－２ｍｏｌ／Ｌ浓度下根段的净吸收为负值,表明组织中Ｋ＋大量外渗。根段置蒸馏水中６ｈ,４ｍｍｏｌ／Ｌ的ＤＯＮ即导致振段Ｋ＋渗漏。用ＤＯＮ处理整株小麦根,浓度在０．２５ｍｍｏｌ／Ｌ以上可促进Ｋ＋从植株其它部位向根运输,而浓度在８ｍｍｏｌ／Ｌ时即抑制Ｋ＋向根富集,且根内Ｋ＋明显渗漏。     

纤维素硫酸钠-聚二甲基二烯丙基氯化铵微胶囊固定化Candida krusei产甘油条件优化

研究了利用一种新型的纤维素硫酸钠／聚二甲基二烯丙基氯化铵（Nacs／PDMDAAc）中空微胶囊包埋Can—dida krusei ZJU5205制备甘油的过程。通过摇瓶培养过程中对初始包菌量、胶囊和胶珠、初始甘油浓度、胶囊大小、胶囊体积／发酵液体积等关键固定化参数和培养条件的优化,确立了NaCS／PDMDAAC微胶囊固定化Candida krusei的最佳工艺参数为包菌量为0．6g／L,发酵初加入20g／L甘油,胶囊体积／发酵液体积为0．4。     

新组合菌系SCB329-SCB933利用L-山梨糖发酵产生维生素C前体2-酮基-L-古龙酸的研究Ⅲ.发酵过程的特征和条件控制

在分析了新组合菌系ＳＣＢ３２９－ＳＣＢ９３３发酵过程特征的基础上,对流加发酵工艺中的种子培养、ｐＨ、溶氧的控制,以及发酵液初始培养基中的Ｌ－山梨糖浓度和流加起始点进行了优化,获得了比分批发酵更为满意的结果：发酵最终总糖达１３％（ｗ／ｖ）左右,发酵周期４０～５０ｈ,产２－酮基－Ｌ－古龙酸达１１５－１３０ｍｇ／ｍｌ,克分子转化率达８８ｍｏｌ％左右。     

新组合菌系SCB329—SCB933利用L—山梨糖发酵产生维生素C前体2—酮基—L—…

在分析了新组合菌系ＳＣＢ３２９－ＳＣＢ９３３发酵过程特征的基础上,对流加发酵工艺中的种子培养、ｐＨ、溶氧的控制,以及发酵液初始培养基中的Ｌ－山梨糖浓度和流加起始点进行了优化,获得了比分批发酵更为满意的结果：发酵最终总糖达１３％（ｗ／ｖ）左右,发酵周期４０￣５０ｈ,产２－酮基－Ｌ－古龙酸达１１５－１３０ｍｇ／ｍｌ,克分子转化率达８８ｍｏｌ％左右。     

烟草细胞乙醇分解代谢能力的离体调控

报告了一些重要因子对培养在含有乙醇的培养基上的烟草细胞的乙醇分解代谢能力（ＥＣＡ）的调控效果。在供试的５种生长毒和２种细胞分裂素中,ＩＢＡ ４ｍｇ／Ｌ和Ｋｔ０．０５ｍｇ／Ｌ最有地促进ＥＣＡ,而ＮＡＡ２ｍｇ／Ｌ和Ｋｔ０．０２５ｍｇ／Ｌ则最有利于支持处在乙醇胁迫下的细胞的增殖。实验中还发现提高维生素浓度有利于细胞的ＥＣＡ。通过将细胞从低乙醇浓度的培养基转移到较高乙醇浓度的培养基中,能够诱导细胞耐受更高     

自絮凝酵母颗粒连续发酵生产酒精的新工艺

用既有优良酒精发酵性能,又具有强自絮凝能力的融合酵母株ＳＰＳＣ,在单釜有效容积为１０ｍ３的四釜并联气升环流悬浮床生物反应器系统中,进行了连续发酵生产酒精的研究。以玉米为原料,双酶法制糖,过滤得到清糖液作为底物,在稀释速率为０１／ｈ的条件下,终点发酵液中酒精浓度为７０～８０ｇ／Ｌ,残余还原糖和残余总糖分别为２～３ｇ／Ｌ和３～５ｇ／Ｌ,悬浮床反应器的设备生产强度达到７～８ｇ（ＥｔＯＨ）／（Ｌ·ｈ）。     

紫云英汁液单细胞蛋白发酵工艺研究

紫云英汁液含有１０％的糖和２．６６％的有机氮化物,稀释成５倍后,以假丝酵母Ｃａｎｄｉｄａ ａｒｂｏｒｏ Ａｓ２．５６６为生产菌进行单细胞蛋白发酵,通过单因素搜索和正交试验对发酵工艺进行了优化,结果表明：较优培养基为初糖２．５％、酵母粉０．１５％、ＫＨ２Ｐ０Ｒ０．２％、ＭｇＳＯ４、０．０５％,初始ｐＨ值＝５,发酵温度３０℃,接种量５％。在２Ｌ发酵罐中验证,酵母浓度最高达１０．５３ｇ干重／Ｌ,基质生长     

表达血管生长抑制素的重组毕赤酵母在诱导阶段混合碳源的流加

为进行高密度发酵并实现外源基因的高表达,在表型为Mut^S的重组毕赤酵母（Pichia pastoris）表达人血管生长抑制素的诱导阶段,采用了甘油甲醇混合补料的培养方式。以溶氧水平作为甘油代谢指针来控制甘油限制性流加既可维持一定菌体生长,又不会发生发酵液中残余甘油及有害代谢产物（乙醇）阻遏蛋白表达。当表达阶段的菌体平均比生长速率控制于0.012h^-1,菌体浓度达150 g/L,血管生长抑制素浓度最高达到108 mg/L,血管生长抑制素的平均比生产速率为0.02 mg/(g·h),菌体关于甘油的表观得率为0.69 g/g,菌体关于甲醇的表观得率为0.93g/g,较没有采用甘油限制性流加时都有所提高。     

Production of salmosin, a snake venom-derived disintegrin, in recombinant Pichia pastoris using high cell density fed-batch fermentation

Salmosin, a snake venom-derived disintegrin, was successfully expressed in the methylotrophic yeast Pichia pastoris and secreted into the culture supernatant, as a 6 kDa protein. High-cell density fermentation of recombinant P. pastoris was optimized for the mass production of salmosin. In a 5 L jar fermentor, recombinant P. pastoris was fermented in growth medium containing 5% (w/v) glycerol at the controlled pH of 5.0. After culturing for 21 h, glycerol feeding medium was fed at one time into the culture broth. After 7 h (a total of 28 h), induction medium that contained methanol was increasingly added until the culture time totaled 75 h. Finally, these optimized culture conditions produced a high cell density of recombinant P. pastoris (dry cell weight of 113.38 g/L) and led to the mass production of salmosin (a total protein concentration of 369.2 mg/L). The culture supernatant containing salmosin inhibited platelet aggregation, resulting in a platelet aggregation of 9% compared to that of 94% in the control experiment, without culture supernatant. These results demonstrate that recombinant salmosin in culture supernatant from high cell density fed-batch fermentation can serve as a platelet aggregation inhibitor.     

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...     

Decrease of 3-hydroxypropionaldehyde accumulation in 1,3-propanediol production by over-expressing <Emphasis Type="Italic">dha</Emphasis>T gene in <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis> TUAC01

Glycerol can be biologically converted to 1,3-propanediol, a key raw material required for the synthesis of polytrimethylene terephthalate and other polyester fibers. In 1,3-propanediol synthesis pathway, 3-hydroxypropionaldehyde (3-HPA) was an inhibitory intermediary metabolite. The accumulation of 3-HPA in broth would cause an irreversible cessation of the fermentation process. With the object of reducing 3-HPA level in the fermentation broth, dhaT gene which encodes 1,3-propanediol oxidoreductase (PDOR) was cloned and over expressed in 1,3-propanediol producing bacterium Klebsiella pneumoniae TUAC01. dhaT gene was linked downstream of the ptac promoter in an expressing vector pDK6 to form plasmid pDK-dhaT. The newly formed pDK-dhaT was transformed to K. pneumoniae TUAC01. Under the inducement of IPTG, PDOR was over-expressed when the constructed strain was cultured on an LB medium or a fermentation medium. A 5 L scale-up fermentation experiment was done to test the 3-HPA accumulation in broth, with the initial substrate glycerol 30 g/L; the peak levels of 3-HPA in broth were 7.55 and 1.49 mmol/L for control host strain and the constructed strain, respectively. In 50 g/L initial glycerol experiment, the peak level of 3-HPA in broth was 12.57 and 2.02 mmol/l for the control host strain and the constructed strain, respectively. Thus the fermentation cessation caused by the toxicity of 3-HPA was alleviated in the constructed strain.     

重组巴氏毕赤酵母高密度发酵表达rHSA

对基因工程菌Pichiapastoris的摇瓶发酵条件进行了试验 ,并根据摇瓶发酵的优化结果进行了补料分批高密度发酵。在摇瓶发酵时 ,甲醇诱导基因工程菌P .pastoris表达重组人血清白蛋白的发酵周期为 96h ;甲醇的最佳诱导浓度为 1 0g L ;发酵pH范围为 5 72～ 6 5 9;在摇瓶培养时 ,随着接种量的增加 ,虽然目的蛋白表达量缓慢增加 ,但单位细胞光密度的蛋白产率却明显下降 ,符合y =1 2 941x- 0 50 59方程 (线性相关系数r=0 9789) ,其限制性因子很可能为溶氧。在分批发酵 ,接种量为 1 0 %且种子细胞光密度 (OD60 0 )为 2 0左右时 ,细胞生长的延迟期为 2 1 1h左右 ,细胞生长光密度与培养时间的关系模型为 :y =0 7841e0 .2 3 19t(线性相关系数r=0 .993 6 ) ;在补料发酵时细胞干重浓度可达到 1 1 5g L— 1 6 0g L ,在 1 2 0h重组人血清白蛋白表达量最大达到 3 6g L。     

不同甲醇流加策略对重组毕赤醇母高密度发酵生产水蛭素的影响

考察了不同甲醇流加策略对毕赤酵母高密度发酵生产水蛭素的影响。溶氧控制法不能有效地防止甲醇的过量流加。气相色谱离线检测法虽然防止了甲醇流加过量 ,但甲醇浓度的波动较大。利用甲醇传感器在线检测控制甲醇的流加可维持较恒定的甲醇浓度。在流加甲醇的同时 ,以限制性速率流加甘油可以增加表达期间的能量供应 ,提高产物的表达量。经优化后 ,采用甲醇甘油混合流加时细胞干重达到 16 2g L ,水蛭素活性达到 2 4×10 4ATU mL ,即 1 7g L。     

Long-term repeated fed-batch ethanol fermentation in aerated condition

In this study, we attempted to assess the process stability of long-term fed-batch ethanol fermentation in the absence and presence of aeration (0.33 vvm). To examine the effect of aeration, a long-term repeated fed-batch operation was conducted for 396 h to mimic a long-term industrial bioethanol production process. In this long-term repeated fed-batch ethanol fermentation experiments, withdrawal-fill operation were conducted every 36 h for 10 repeat cycles. The whole operation was stably sustained in a quasi-steady state. The average maximal cell concentration and the average maximal ethanol production during operation were increased by 81.63 and 12.12%, respectively, when aeration was used. In addition, since aeration was carried out, the average ethanol yield slightly decreased by 4.03% and the average specific ethanol production rate decreased by 46.75% during operation. However, the average ethanol productivity increased by 17.53% when aeration was carried out. After 396 h of long-term repeated fed-batch ethanol fermentation, 1,908.9 g of ethanol was cumulatively produced when aeration was used, which was 12.47%, higher than when aeration was not used (1,697.2 g). Meanwhile, glycerol production was greatly decreased during long-term repeated fed-batch ethanol fermentation, in which the glycerol concentration in the culture broth decreased from about 34∼15 g/L. Thus, we can conclude that cell growth was greatly improved by overcoming ethanol inhibition and glycerol production was remarkably decreased when aeration was carried out, although aeration in ethanol fermentation decreased the specific ethanol production rate and ethanol yield.     

Production of poly(3-hydroxybutyrate) by high cell density fed-batch culture of Alcaligenes eutrophus with phospate limitation

High cell density fed-batch fermentation of Alcaligenes eutrophus was carried out for the production of poly(3-hydroxybutyrate) (PHB) in a 60-L fermentor. During the fermentation, pH was controlled with NH(4)OH solution and PHB accumulation was induced by phosphate limitation instead of nitrogen limitation. The glucose feeding was controlled by monitoring dissolved oxygen (DO) concentration and glucose concentration in the culture broth. The glucose concentration fluctuated within the range of 0-20 g/L. We have investigated the effect of initial phosphate concentration on the PHB production when the initial volume was fixed. Using an initial phosphate concentration of 5.5 g/L, the fed-batch fermentation resulted in a final cell concentration of 281 g/L, a PHB concentration of 232 g/L, and a PHB productivity of 3.14 g/L . h, which are the highest values ever reported to date. In this case, PHB content, cell yield from glucose, and PHB yield from glucose were 80, 0.46, and 0.38% (w/w), respectively. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 28-32, 1997.     

3-Hydroxypropionaldehyde guided glycerol feeding strategy in aerobic 1,3-propanediol production by <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis>

3-Hydroxypropionaldehyde (3-HPA) is a toxic intermediary metabolite in the biological route of 1,3-propanediol biosynthesis from glycerol. 3-HPA accumulated in culture medium would arouse an irreversible cessation of the fermentation process. The role of substrate (glycerol) on 3-HPA accumulation in aerobic fermentation was investigated in this paper. 1,3-Propanediol oxidoreductase and glycerol dehydratase, two key enzyme catalyzing reactions of 3-HPA formation and consumption, were sensitive to high concentration of 3-HPA. When the concentration of 3-HPA increased to a higher level in medium (ac 10 mmol/L), the activity of 1,3-propanediol oxidoreductase in cell decreased correspondingly, which led to decrease of the 3-HPA conversion rate, then the 3-HPA concentration increasing was accelerated furthermore. 3-HPA accumulation in culture medium was triggered by this positive feedback mechanism. In the cell exponential growth phase, the reaction catalyzed by 1,3-propanediol oxidoreductase was the rate limiting step in 1,3-propanediol production. The level of 3-HPA in culture medium could be controlled by the substrate (glycerol) concentration, and lower level of glycerol could avoid 3-HPA accumulating to a high, lethal concentration. In fed batch fermentation, under the condition of initial glycerol concentration 30 g/L, and keeping glycerol concentration lower than 7–8 g/L in cell exponential growth phase, 3-HPA accumulation could not be incurred. Based on this result, a glycerol feeding strategy was set up in fed batch fermentation. Under the optimized condition, 50.1 g/L of 1,3-propanediol was produced in 24 h, and 73.1 g/L of final 1,3-propanediol concentration was obtained in 54 h.     

Monitoring biomass and glycerol in an Escherichia coli fermentation using near-infrared spectroscopy

Summary Near-infrared spectroscopy was used to determine biomass and glycerol concentrations in E.coli whole broth fermentation samples. For dry cell weight, a standard error of prediction (SEP) of 0.2 g/L and correlation coefficient (r) of 0.991 were obtained. The SEP and r for glycerol, carbon nutrient, were 0.3 g/L and 0.979. respectively. Off-line analysis was accomplished within 2 minutes of sampling and therefore provides the opportunity to monitor fermentations quickly enough to permit in-process development and troubleshooting.