大豆蛋白复合酶解产物在促微生物生长和发酵中的初步应用研究

为探讨大豆蛋白复合酶解产物在促微生物生长和发酵中的可行性,利用2709碱性蛋白酶和中性纤维素酶复合酶解大豆蛋白,酶解产物经干燥、粉碎后添加到培养基中,通过接种微生物观察其生长状况和发酵情况表征效果。研究发现,大豆蛋白复合酶解产物可以促进微生物生长和发酵产酶,试验结论为微生物培养提供了新的代谢资源。     

使用旋转式生物反应器体外扩增人表皮细胞

目的:使用Cytodex-3微载体和高截面纵横比的旋转式生物反应器容器作为培养系统大规模扩增人表皮细胞(hECs)。方法:使用中性蛋白酶和胰蛋白酶-EDTA两步骤法从人皮肤中分离出人表皮细胞,使用DIL标记细胞后结合微载体后在旋转式生物反应器(RCCS)中培养,细胞贴附微载体的生长状态使用倒置显微镜,扫描电镜观测。并且分析细胞群体倍增时间来比较微重力培养与平面培养的体外增殖能力差异。结果:在旋转式生物反应器的微重力培养体系中,人表皮细胞能快速贴附到微载体表面,在培养过程中达到很大的细胞密度,并且表现出很强的增殖能力和细胞活性。结论:使用旋转式生物反应器和微载体悬浮培养人表皮细胞,是大量制备皮肤组织工程种子细胞的一种有效方法。     

Mechanisms of angiogenesis

Tissue activity of angiogenesis depends on the balance of many stimulating or inhibiting factors. The key signaling system that regulates proliferation and migration of endothelial cells forming the basis of any vessel are vascular endothelium growth factors (VEGF) and their receptors. The VEGF-dependent signaling system is necessary for formation of the embryonic vascular system. Neoangiogenesis during tumor growth is also associated with activation of this signaling system. The biological significance of the effect of such system on the cells depends on the content in tissue of various factors of the VEGF family and their receptors, while in the case of VEGFA it is defined by the ratio of different isoforms of this growth factor. A number of other signaling systems are also involved in regulation of the main steps of vessel formation. The signaling system Dll4/Notch regulates selection of endothelial cells for beginning of angiogenic expansion by endowing particular properties to endothelial cells leading in this process. An important step in vessel stabilization and maturation is vascular wall formation. Signaling system PDGFB/PDGFRbeta as well as angiopoietins Ang1, Ang2, and their receptor Tie2 are involved in recruiting mural cells (pericytes and smooth muscle cells). Identification of key molecules involved in the regulation of angiogenesis may provide new possibilities for development of drugs suitable for inhibition of angiogenesis or its stimulation in various pathologies.     

Design and evaluation of a continuous semipartition bioreactor for in situ liquid‐liquid extractive fermentation

Extractive fermentation (or in situ product removal (ISPR)) is an operational method used to combat product inhibition in fermentations. To achieve ISPR, different separation techniques, modes of operation and physical reactor configurations have been proposed. However, the relative paucity of industrial application necessitates continued investigation into reactor systems. This article outlines a bioreactor designed to facilitate in situ product extraction and recovery, through adapting the reaction volume to include a settler and solvent extraction and recycle section. This semipartition bioreactor is proposed as a new mode of operation for continuous liquid‐liquid extractive fermentation. The design is demonstrated as a modified bench‐top fermentation vessel, initially analysed in terms of fluid dynamic studies, in a model two‐liquid phase system. A continuous abiotic simulation of lactic acid (LA) fermentation is then demonstrated. The results show that mixing in the main reaction vessel is unaffected by the inserted settling zone, and that the size of the settling tube effects the maximum volumetric removal rate. In these tests the largest settling tube gave a potential continuous volumetric removal rate of 7.63 ml/min; sufficiently large to allow for continuous product extraction even in a highly productive fermentation. To demonstrate the applicability of the developed reactor, an abiotic simulation of a LA fermentation was performed. LA was added to reactor continuously at a rate of 33ml/h, while continuous in situ extraction removed the LA using 15% trioctylamine in oleyl alcohol. The reactor showed stable LA concentration of 1 g/L, with the balance of the LA successfully extracted and recovered using back extraction. This study demonstrates a potentially useful physical configuration for continuous in situ extraction.     

Production of poly(D-3-hydroxybutyrate) from CO(2), H(2), and O(2) by high cell density autotrophic cultivation of Alcaligenes eutrophus

Hydrogen-oxidizing bacterium, Alcaligenes eutrophus autotrophically produces biodegradable plastic material, poly(D-3-hydroxybutyrate), P(3HB), from carbon dioxide, hydrogen, and oxygen. In autotrophic cultivation of the microorganism, it is essential to eliminate possible occurrence of gas explosions from the fermentation process. We developed a bench-plant scale, recycled-gas, closed-circuit culture system equipped with several safety features to perform autotrophic cultivation of A. eutrophus by maintaining the oxygen concentration in the substrate gas phase below the lower limit for a gas explosion (6.9%). The culture vessel utilized a baskettype agitator, resulting in a K(L) a value of 2970 h(-1). Oxygen gas was also directly fed to the fermentor separately from the other gases. As a result, 91.3 g . dm(-3) of the cells and 61.9 g . dm(-3) of P(3HB) were obtained after 40 h of cultivation under this oxygen-limited condition. The results compared favorably with those reported for mass production of P(3HB) by heterotrophic fermentation. (c) 1995 John Wiley & Sons, Inc.     

产人表皮生长因子的重组大肠杆菌的发酵动力学

对产人表皮生长因子的重组大肠杆菌Escherichia coli(E.Coli)的发酵动力学进行了研究,采用了发酵体系中含质粒的工程菌与不含质粒的非工程菌的共处模型,分析了细胞生长、底物消耗、基因工程产物生成的过程,由模型计算的结果与实验结果基本吻合。     

酿酒酵母表达系统

酿酒酵母是单细胞真核微生物,人们以酿酒酵母为宿主菌,用载体表达外源基因的过程中,积累了丰富的经验,掌握了酿酒酵母表达的许多优缺点,如它繁殖速度快,可以大规模发酵生产,但在发酵过程中会产生乙醇,而乙醇在培养基中积累会影响酵母的生长代谢和基因产物的表达,尤其是进行高密度发酵时该效应更明显;针对这些缺点,可以采取积极的应对措施.主要就酿酒酵母表达系统的组成、优缺点及高效表达的策略等作一综述.     

Measurement of Tension Release During Laser Induced Axon Lesion to Evaluate Axonal Adhesion to the Substrate at Piconewton and Millisecond Resolution

The formation of functional connections in a developing neuronal network is influenced by extrinsic cues. The neurite growth of developing neurons is subject to chemical and mechanical signals, and the mechanisms by which it senses and responds to mechanical signals are poorly understood. Elucidating the role of forces in cell maturation will enable the design of scaffolds that can promote cell adhesion and cytoskeletal coupling to the substrate, and therefore improve the capacity of different neuronal types to regenerate after injury.Here, we describe a method to apply simultaneous force spectroscopy measurements during laser induced cell lesion. We measure tension release in the partially lesioned axon by simultaneous interferometric tracking of an optically trapped probe adhered to the membrane of the axon. Our experimental protocol detects the tension release with piconewton sensitivity, and the dynamic of the tension release at millisecond time resolution. Therefore, it offers a high-resolution method to study how the mechanical coupling between cells and substrates can be modulated by pharmacological treatment and/or by distinct mechanical properties of the substrate.     

苏云金芽孢杆菌两株溶原性噬菌体的生物学特性

研究苏云金芽孢杆菌(Bacillus thuringiensis)的溶原性及其噬菌体的生物学特性,从生产菌株MZ1中分离了两株溶原性噬菌体。MZ1经诱导后产生直径约为3mm和1mm的噬斑,分离获得属长尾噬菌体科的噬菌体MZTP01和MZTP02两株;分别对6株和7株不同亚种的Bt菌株具有侵染力;免疫血清与相应噬菌体的中和反应K值分别为45和326,且两者无相关抗原性。MZTP01抵抗酸、碱、紫外线和热的能力比MZTP02强,但抵抗有机溶剂的程度比MZTP02弱。MZTP01的潜伏期为80min,裂解量为55;MZTP02的潜伏期为40min,裂解量为175。核酸结构分析均表明为线性dsDNA分子。两基因组DNA的凝胶电泳表明分子量均在9.4~23kb之间,并被HindⅢ酶切分别产生8条和9条清晰条带。该菌株被证明为二元溶原菌,可能是造成生产损失的主要原因;为防治溶原性噬菌体提供了生物学信息。     

Protein Kinase Cα (PKCα) Regulates p53 Localization and Melanoma Cell Survival Downstream of Integrin αv in Three-dimensional Collagen and in Vivo

Protein kinase C α (PKCα) is overexpressed in numerous types of cancer. Importantly, PKCα has been linked to metastasis of malignant melanoma in patients. However, it has been unclear how PKCα may be regulated and how it exerts its role in melanoma. Here, we identified a role for PKCα in melanoma cell survival in a three-dimensional collagen model mimicking the in vivo pathophysiology of the dermis. A pathway was identified that involved integrin αv-mediated up-regulation of PKCα and PKCα-dependent regulation of p53 localization, which was connected to melanoma cell survival. Melanoma survival and growth in three-dimensional microenvironments requires the expression of integrin αv, which acts to suppress p53 activity. Interestingly, microarray analysis revealed that PKCα was up-regulated by integrin αv in a three-dimensional microenvironment-dependent manner. Integrin αv was observed to promote a relocalization of endogenous p53 from the nucleus to the cytoplasm upon growth in three-dimensional collagen as well as in vivo, whereas stable knockdown of PKCα inhibited the integrin αv-mediated relocalization of p53. Importantly, knockdown of PKCα also promoted apoptosis in three-dimensional collagen and in vivo, resulting in reduced tumor growth. This indicates that PKCα constitutes a crucial component of the integrin αv-mediated pathway(s) that promote p53 relocalization and melanoma survival.     

A novel parallel shaken bioreactor system for continuous operation

A novel continuous bioreactor system was developed as a shaken culture vessel for the investigation of the growth kinetics and product formation of microorganisms in milliscale. The novel bioreactor system mainly consists of a specially designed 250-mL shake flask with two inlets, one for gas supply and one for medium supply, and one combined outlet on the side of flask for exhaust gas and culture liquid. As a result of the circulating motion of the fermentation broth in the shake flask, the maximum liquid height reaches the edge of the outlet and the fermentation broth is accelerated into the outlet by centrifugal force. Additionally, the excess fermentation broth leaving the culture vessel is continuously driven by the exhaust gas. Because of the small scale and the simple handling it is possible to operate many of these shaken bioreactor vessels simultaneously. By using parallel vessels operated at different dilution rates on the same shaker, the data for a complete biomass over dilution rate (X-D) diagram of a biological culture can be evaluated in an efficient manner, thus saving money, materials, and time. Continuous fermentations of the yeast Saccharomyces cerevisiae H1022 (ATCC 32167) in the shaken bioreactor system and in a conventional stirred tank fermentor showed very similar results.     

海洋红酵母Y2发酵产类胡萝卜素条件的研究

目的 对海洋红酵母Y2高产类胡萝卜素的发酵条件进行优化.方法 在摇瓶条件下,研究培养基成分和培养条件对海洋红酵母Y2生长和类胡萝卜素合成的影响,同时进行海洋红酵母Y2发酵过程的动态分析.结果 海洋红酵母Y2优化培养基组合为葡萄糖45 g/L,蔗糖15 g/L,酵母粉5 g/L,蛋白胨2.5 g/L,磷酸二氢钾1 g/L,磷酸二氢钠3 g/L,硫酸镁7.5 g/L,氯化钾3 g/L,氯化钠5 g/L.最适培养参数为:温度20℃,培养基初始pH为5,接种量为10％,250 mL摇瓶装液量为10～50 mL.类胡萝卜素的合成主要集中在对数生长期和稳定期.海洋红酵母Y2最适收获时间为72 h.种龄以36 h为宜.结论 利用优化培养基,在最适条件下培养海洋红酵母Y2,类胡萝卜素产量达到4.97 mg/L,比基础培养基提高了60.32％.     

Co-utilization of polymerized carbon sources by Bacteroides ovatus grown in a two-stage continuous culture system.

Bacteroides ovatus NCTC 11153 was grown in a two-stage continuous culture system at various growth rates (vessel 1, D = 0.06 to 0.19 h-1; vessel 2, D = 0.03 to 0.09 h-1) on media containing mixtures of starch and arabinogalactan as carbon sources. The cell-associated enzyme activities needed to hydrolyze both substrates (amylase, arabinogalactanase, alpha-glucosidase, beta-galactosidase, and alpha-arabinofuranosidase) were variously influenced by growth rate and polysaccharide availability but were detected under all growth conditions tested. Measurements of residual carbohydrate in spent culture media showed that both polysaccharides were co-utilized during growth under putative C-limited conditions. The arabinogalactan was partly depolymerized in N-limited chemostats, and significant amounts of arabinose- and galactose-containing oligosaccharides accumulated in the cultures, indicating that starch was being preferentially utilized. Acetate, propionate, and succinate were the major fermentation products formed by C-limited bacteria, but under N limitation, lactate was also produced. Molar ratios of succinate increased concomitantly with the dilution rate in C-limited chemostats, whereas molar ratios of propionate decreased. During N-limited growth, however, decarboxylation of succinate to propionate was relatively independent of growth rate. Cell viability was higher in C-limited cultures compared with those grown under N limitation and was greatest at high dilution rates, irrespective of nutrient limitation.     

Co-utilization of polymerized carbon sources by Bacteroides ovatus grown in a two-stage continuous culture system

Bacteroides ovatus NCTC 11153 was grown in a two-stage continuous culture system at various growth rates (vessel 1, D = 0.06 to 0.19 h-1; vessel 2, D = 0.03 to 0.09 h-1) on media containing mixtures of starch and arabinogalactan as carbon sources. The cell-associated enzyme activities needed to hydrolyze both substrates (amylase, arabinogalactanase, alpha-glucosidase, beta-galactosidase, and alpha-arabinofuranosidase) were variously influenced by growth rate and polysaccharide availability but were detected under all growth conditions tested. Measurements of residual carbohydrate in spent culture media showed that both polysaccharides were co-utilized during growth under putative C-limited conditions. The arabinogalactan was partly depolymerized in N-limited chemostats, and significant amounts of arabinose- and galactose-containing oligosaccharides accumulated in the cultures, indicating that starch was being preferentially utilized. Acetate, propionate, and succinate were the major fermentation products formed by C-limited bacteria, but under N limitation, lactate was also produced. Molar ratios of succinate increased concomitantly with the dilution rate in C-limited chemostats, whereas molar ratios of propionate decreased. During N-limited growth, however, decarboxylation of succinate to propionate was relatively independent of growth rate. Cell viability was higher in C-limited cultures compared with those grown under N limitation and was greatest at high dilution rates, irrespective of nutrient limitation.     

Use of an exchange filtration technique to obtain synchronous sporulation in an extended batch fermentation

A fermentor system with an external filtration loop has been developed to control the growth and sporulation of yeast in a single vessel. Excess growth medium, instead of being removed by centrifugation, is removed by filtration and replaced with acetate sporulation medium. The technique did give 80% sporulation after 20 hr, greatly improving the rate and degree of synchrony of sporulation and it also eliminated the contamination hazard of the conventional harvest technique, centrifugation, and resuspension of vegetative cells in sporulation medium. Furthermore it permits proper control of the environmental conditions throughout the growth, exchange, and sporulation phase. In this technique 100% recycle of biomass is achieved without any packing of the cells on the filter. This technique has wide application in the study of industrial fermentation that involves microbial differentiation such as the production of ergot alkaloids, bacitracin, and cephalosporin.     

Methods for Facilitating Microbial Growth on Pulp Mill Waste Streams and Characterization of the Biodegradation Potential of Cultured Microbes

The kraft process is applied to wood chips for separation of lignin from the polysaccharides within lignocellulose for pulp that will produce a high quality paper. Black liquor is a pulping waste generated by the kraft process that has potential for downstream bioconversion. However, the recalcitrant nature of the lignocellulose resources, its chemical derivatives that constitute the majority of available organic carbon within black liquor, and its basic pH present challenges to microbial biodegradation of this waste material. Methods for the collection and modification of black liquor for microbial growth are aimed at utilization of this pulp waste to convert the lignin, organic acids, and polysaccharide degradation byproducts into valuable chemicals. The lignocellulose extraction techniques presented provide a reproducible method for preparation of lignocellulose growth substrates for understanding metabolic capacities of cultured microorganisms. Use of gas chromatography-mass spectrometry enables the identification and quantification of the fermentation products resulting from the growth of microorganisms on pulping waste. These methods when used together can facilitate the determination of the metabolic activity of microorganisms with potential to produce fermentation products that would provide greater value to the pulping system and reduce effluent waste, thereby increasing potential paper milling profits and offering additional uses for black liquor.     

An automated home-built low-cost fermenter suitable for large-scale bacterial expression of proteins in Escherichia coli

We have developed an automated fermentation system for cost-efficient upscaling of protein expression in bacteria. The system, built for use by nonbiotechnologists, can be assembled mostly from standard laboratory equipment and allows a largely unattended growth of bacteria to OD 25 (at 600 nm) in a 12 L vessel. The typical yield of 250-350 g of wet weight cell pellet per run, which is equivalent to the biomass obtained from 250 shake flask cultures containing 400 mL Luria-Broth medium each, facilitates the production of large amounts of purified recombinant protein without the laborious need for optimization of expression and purification conditions.     

超滤法浓缩谷氨酰胺转胺酶的影响因素研究

对微生物谷氨酰胺转胺酶(MTG)超滤浓缩的工艺条件进行了探讨及优化。实验采用截留分子量为30 kDa的聚醚砜(PES)膜,当发酵液初始pH为7,超滤浓缩倍数为4倍时,可以得到理想的MTG回收率。同时对超滤液中蛋白酶的变化进行了分析,发现随着超滤倍数的提高蛋白酶也逐渐提高,但在浓缩4倍以后达到较稳定的水平。聚醚砜(PES)超滤膜使用后用稀释的NaOH溶液浸泡清洗处理50 min后,膜通量可以恢复98.12%。