真氧产碱杆菌利用混合有机酸生物合成聚羟基烷酸酯

研究了真氧产碱杆菌利用混合有机酸作为碳源进行聚羟基烷酸酯的生物合成.实验表明,在由乙酸、丙酸、乳酸、丁酸组成的混合酸中,各有机酸在细胞生长以及聚羟基烷酸酯的合成过程中所起的作用各不相同.另外,通过5 L罐进行的分批以及流加发酵实验证实,流加发酵,特别是经优化后的流加发酵,可以获得更高的细胞干质以及PHAs产量,但聚合物中聚羟基戊酸酯组分的比例明显低于分批发酵.     

新型优化策略在青霉素间歇发酵过程中的应用研究

基于全面关注间歇发酵过程中间状态的思想,提出由求解一系列端点时间不固定最优控制子问题形成的新型优化控制策略,并在优化目标函数中加入了菌体平均生长速率和流加时间间隔对发酵产量的影响因素.在此基础上提出基于遗传算法的最优控制策略实现算法,同时获得了最优流加时间间隔及相应的最优流加速率.将该方法在青霉素发酵过程进行仿真,将仿...     

用豆粕发酵生产卡门柏青霉脂肪酶

以廉价的脱脂豆粕为初始培养基和补料培养基,采用不同流加方式,包括间歇补料、高浓度流加和低浓度流加,对发酵生产卡门柏青霉(Penicillium camembertii Thom)脂肪酶进行了研究. 在5 L发酵罐中不外加碳源,以脱脂豆粕为培养基主要成分的条件下,采用流加高浓度脱脂豆粕的方式,发酵99.8 h得到1,3-专一性脂肪酶,最大酶活力392 IU/mL. 由于在培养基中以脱脂豆粕代替了昂贵的霍霍巴油,有可能大幅度降低生产成本.     

碱性纤维素酶基因在巴氏毕赤酵母中的表达及重组酵母菌发酵工艺的优化

目的克隆碱性纤维素酶基因,构建酵母整合型表达质粒,在巴氏毕赤酵母中表达,并对重组菌的发酵工艺进行优化。方法应用PCR技术从嗜碱性芽孢杆菌ATCC21833中扩增碱性纤维素酶基因,克隆至酵母整合型表达载体pGAPZαA中,构建重组表达质粒pGAPZαA-ATCC21833,并转化至巴氏毕赤酵母GS115。通过单因素实验及正交实验,确定重组酵母的最佳发酵培养基。在20L发酵罐中进行高密度发酵,观察碳源对批式发酵的影响,并检测在4种流加方式(连续恒速流加、间歇匀速流加、间歇递减流加、维持底物浓度流加)下的菌体干重及发酵液中的酶活性。结果重组表达质粒pGAPZαA-ATCC21833经酶切及DNA测序证明构建正确,其基因序列与嗜碱性芽孢杆菌KSM-635的碱性纤维素酶基因序列一致。最佳发酵培养基组成为6%葡萄糖、2%硫酸铵、12g/L磷酸二氢钾。碳源浓度对于重组酵母菌体生长及产酶至关重要。SDS-PAGE表明表达产物的相对分子质量约为103000。维持底物浓度的流加方式可获得最高的菌体干重(29.8g/L)及酶活力(24U/ml)。结论已成功构建了表达碱性纤维素酶的巴氏毕赤酵母工程菌,并确定了维持底物浓度的流加方式为最佳发酵方式。     

赖氨酸发酵动力学研究——流加方式优化

在４０Ｌ中试发酵罐上优选菌株进行了Ｌ－赖氨酸分批流加发酵,用实验数据对文献报道的分批发酵动力学模型进行了验证。结果所有模型不能很好的描述赖氨酸分批发酵过程动力学。最后,探讨了赖氨酸分批发酵的动力学机理,给出了流加优化方案。     

基于pH控制的丙酮丁醇间歇发酵过程动力学模型

基于微生物发酵动力学模型和丙酮丁醇发酵工艺的特点,由5组控制pH下的实验数据建立该发酵过程的动力学模型,采用改进的自适应遗传算法对模型的12个参数进行优化,并采用一组控制pH数据对模型进行了外推验证,结果表明,该模型能够较好地描述pH的丙酮丁醇间歇发酵过程.     

赖氨酸发酵工艺参数模式识别优化

在赖氨酸发酵动力学研究的基础上,把发酵过程划分为四个阶段。收集了２２组赖氨酸分批流加发酵实验数据,用模式识别优化技术进行寻优,得到了优化发酵工艺参数及优化流加策略。     

赖氨酸发酵工艺参数模式识别优化

在赖氨酸发酵动力学研究［１］的基础上,把发酵过程划分为四个阶段。收集了２２组赖氨酸分批流加发酵实验数据,用模式识别优化技术进行寻优。得到了优化发酵工艺参数及优化流加策略     

赖氨酸发酵动力学研究——流加方式优化

在４０Ｌ中试发酵罐上用优选菌株进行了Ｌ—赖氨酸分批流加发酵,用实验数据对文献报道的分批发酵动力学模型进行了验证。结果发现所有模型都不能很好的描述赖氨酸分批发酵过程动力学。最后,探讨了赖氨酸分批发酵的动力学机理,给出了流加优化方案。     

同时进行发酵和分离的CO_2气提、活性炭吸附乙醇发酵动力学研究——(三)固定化细胞发酵

研究了应用固定化酵母同时进行发酵和分离的 CO_2气提的乙醇间歇发酵和连续发酵。从实验结果发现,无论是间歇还是连续操作,无论是改变稀释率还是改变进口底物浓度,在实验范围内,发酵速率都基本上保持常数,即,固定化酵母发酵时,发酵液中少量游离酵母的影响可以忽略,固定化酵母密度在发酵过程中不会发生很大变化。由此而导出的简化模型可以满意地关联稳态操作时的实验数据,并进而推算动态响应曲线。     

重组大肠杆菌分批-补料高密度发酵生产类人胶原蛋白的动力学

The kinetics of batch and fed-batch cultures of recombinant Escherichia coli producing human-like collagen was investigated. In the batch culture, a kinetic model of a simple growth-association system was concluded without consideration of cell endogeneous metabolism. The cell lag time, the maximum specific growth rate and growth rates were set at (0.15, 0.2, 0.25h-1) by the method of pseudo-exponential feeding, and the expressions for the specific rate of substrate consumption, the growth kinetics and the product formation kinetics of each phase spectively. The model predictions are in good agreement with the experimental data.     

基于发酵动力学模型的小球藻高密度发酵培养

构建了50 L发酵罐小球藻分批培养动力学模型,采用补料策略高密度发酵培养小球藻,考察了补料发酵过程中碳源的利用情况,采用实时荧光定量PCR技术分析了蛋白质合成关键酶二氨基庚二酸异构酶(dapF)、柠檬酸合成酶(CS)和葡萄糖?6-磷酸脱氢酶(G6PDH)的基因表达情况. 结果表明,小球藻经补料培养120 h,细胞生物量达106.65 g/L,平均生长速率为0.89 g/(L?h),葡萄糖的细胞得率为0.56 g/g,发酵过程中葡萄糖和尿素浓度对小球藻的dspF, CS和G6PDH基因表达量有重要影响.     

重组大肠杆菌分批-补料高密度发酵生产类人胶原蛋白的动力学

The kinetics of batch and fed-batch cultures of recombinant Escherichia coli producing human-like collagen was investigated. In the batch culture, a kinetic model of a simple growth-association system was concluded without consideration of cell endogeneous metabolism. The cell lag time, the maximum specific growth rate and Yx/s were determined as 1.75h, 0.65h^-1 and 0.51g·g^-1, respectively. In the fed-batch culture, different specific growth rates were set at （0.15, 0.2, 0.25h^-1） by the method of pseudo-exponential feeding, and the expressions for the specific rate of substrate consumption, the growth kinetics and the product formation kinetics of each phase were obtained. The result shows that the concentrations of cell and product can reach 77.5g·L^-1 and 10.2g·L^-1 respectively. The modal predictions are in good agreement with the experimental data.     

产烃葡萄藻在气升式光生物反应器中的分批补料培养

在3 L气升式光生物反应器中进行了产烃葡萄藻的培养. 批式培养时，葡萄藻消耗氮、磷的速度较快，培养液中氮、磷营养盐的缺乏限制了藻细胞进一步生长和增殖. 采取分批补料方式，使培养液中KNO3和K2HPO4浓度分别维持在100和30 mg/L，可克服氮、磷限制问题. 与批式培养相比，生物量从1.3 g/L增加到1.9 g/L，烃含量从占细胞干重的22%提高到29%，从而使烃产量从0.286 g/L增加到0.551 g/L，提高了92.6%.     

Production of bacterial cellulose in static conditions by a simple fed-batch cultivation strategy

The current study investigated fed-batch cultivation for the increased productivity of bacterial cellulose (BC) sheets by Gluconacetobacter hansenii PJK in static conditions using chemically defined medium and waste from beer fermentation broth. Fermentations were carried out in a 3 L jar fermenter without any impeller for 30 days. In the proposed fed-batch cultivation, 500 mL of the medium was initially inoculated with pre-culture in a jar fermenter while a fresh medium was fed periodically. BC production was also done by using batch cultivation which was used as a control for comparison. The results obtained revealed an overall of 2–3 times increase in BC production in fed-batch cultivation compared to batch cultivation after 30 days of cultivation. During these experiments, it was found that waste from beer fermentation broth is a superior medium for the BC production using fed-batch cultivation. The production of water soluble oligosaccharides as useful by-products was also monitored during these investigations. Fed-batch cultivation and waste from beer fermentation was also found superior for the production of these by-products. According to literature search and to the best of our knowledge, it is the first report of using fed-batch cultivation for BC production in static conditions.     

白色链霉菌分批发酵ε-聚赖氨酸的动力学分析

发酵过程动力学分析是实现发酵过程优化与控制的关键因素之一.通过运用Sigmoid模型,对白色链霉菌生产ε-聚赖氨酸的分批发酵过程进行分析,拟合得出底物消耗、菌体生长和产物形成的动力学方程,模拟得到的动力学曲线与试验值相符,可为ε-聚赖氨酸生产的分批发酵法和补料分批发酵法提供理论依据.     

Three-stage fermentation and kinetic modeling of bioflocculant by Corynebacterium glutamicum

Fermentation of bioflocculant with Corynebacterium glutamicum was studied by way of kinetic modeling. Lorentzian modified Logistic model, time-corrected Luedeking–Piret and Luedeking–Piret type models ...     

三段式谷氨酸棒杆菌发酵生产生物絮凝剂的过程及动力学模拟(英文)

Fermentation of bioflocculant with Corynebacterium glutamicum was studied by way of kinetic modeling. Lorentzian modified Logistic model, time-corrected Luedeking–Piret and Luedeking–Piret type models were pro-posed and applied to describe the cell growth, bioflocculant synthesis and consumption of substrates, with the correlation of initial biomass concentration and initial glucose concentration, respectively. The results showed that these models could well characterize the batch culture process of C. glutamicum at various initial glucose con-centrations from 10.0 to 17.5 g·L?1. The initial biomass concentration could shorten the lag time of cel growth, while the maximum biomass concentration was achieved only at the optimal initial glucose concentration of 16.22 g·L?1. A novel three-stage fed-batch strategy for bioflocculant production was developed based on the model prediction, in which the lag phase, quick biomass growth and bioflocculant production stages were sequentially proceeded with the adjustment of glucose concentration and dissolved oxygen. Biomass of 2.23 g·L?1 was obtained and bioflocculant concentration was enhanced to 176.32 mg·L?1, 18.62% and 403.63%higher than those in the batch process, respectively, indicating an efficient fed-batch culture strategy for bioflocculant production.     

产朊假丝酵母流加发酵法生产谷胱甘肽

研究了产朊假丝酵母在不同葡萄糖浓度下的谷胱甘肽(GSH)分批发酵过程,在此基础上进一步考察了重复补料、恒速流加和指数流加等不同培养方式对GSH发酵生产的影响. 结果发现,这几种培养方式都可以实现酵母细胞和GSH的高产. 综合比较,无论是从细胞还是从GSH的产量、得率和生产强度的角度来看,指数流加都是较为理想的选择. 经过48 h的指数流加培养,细胞干重达到40.9 g/L, GSH产量和胞内GSH含量分别达到857.2 mg/L和2.25%.     

粘质沙雷氏菌产灵菌红素的碳源分析、菌种诱变及动力学

使用流式细胞仪研究了不同碳源对粘质沙雷氏菌ZSG新陈代谢的影响,发现不同碳源导致ZSG的DNA含量、细胞内部颗粒密度、表面粗糙度和细胞大小在发酵过程中呈现有差异的变化。对ZSG进行复合诱变筛得一株稳定突变菌株ZSG7,在250 ml摇瓶和5 L发酵罐中进行发酵,其灵菌红素（PG）产量比出发菌株分别提高了62.5%和269%。对ZSG7进行发酵培养基优化后PG产量比优化前提高了100%。对ZSG7发酵进行溶氧分段控制模式调控后PG产量比DO调控前提高了30.9%。对ZSG7发酵进行恒定pH调控后比pH调控前提高了35.9%。对ZSG7发酵进行补料组分优化后比补料前提高了47.6%。基于Logistic方程和Luedeking-Piret方程建立了恒定pH7分批发酵和补料分批发酵的菌体生长模型和PG合成模型。拟合模型参数后,模型可以合理地描述恒定pH7分批发酵和补料分批发酵的过程。