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排序方式: 共有221条查询结果,搜索用时 15 毫秒
1.
C. O. Ikediobi G. O. C. Onyia C. E. Eluwah 《Bioscience, biotechnology, and biochemistry》2013,77(12):2803-2809
The well-known alkaline picrate test for cyanide has been improved by incorporating an enzymatic step to make the assay much more specific and quantitative. The sensitivity or detection limit of this method was found to be 0.16 μg/cm3 while the precision as indicated by the coefficient of variation was 3%. The method was, in addition, found to be rapid, simple, inexpensive and ideally suited for the analysis of large number of cassava tissues and products, such as may be encountered in cassava agronomy and breeding work or in industrial quality control laboratories. A trained operator working alone consistently analyzed at least 700 samples/day using this assay method. 相似文献
2.
Marie-Jose de Smet Jaap Kingma Hans Wynberg Bernard Witholt 《Enzyme and microbial technology》1983,5(5):352-360
The bioconversion of hydrocarbons by Pseudomonas oleovorans has been studied in two-phase systems. In these systems, the hydrocarbon substrate is present in sufficient amounts to form the bulk apolar phase. High cell densities (up to 20 mg dry mass per ml water phase) are reached when the apolar phase consists of n-octane, 1-octene or 1-decene. There is considerable cell damage after incubation for 50–70 h. Loss of cell viability and membrane damage as observed by freeze-fracture electron microscopy correlate with a loss of hydrocarbon oxidation, measured as the conversion of 1-octene to 1,2-epoxyoctane. The final yield of oxidized hydrocarbon in the apolar substrate phase can be increased substantially by replacing the damaged cells with freshly grown cells. Yields up to 150 mg 1,2-epoxyoctane per ml 1-octene and up to 20–25 mg 1,2-epoxyoctane per ml culture were obtained with four cycles of the cell renewal procedure. Several other substrates in addition to octene were tested in the optimized two-phase system. Of these, 1-decene was converted into (R)-1,2-epoxydecane with an optical purity of 60%, while allylbenzene was converted into chiral 1,2-epoxy-3-phenylpropane. Some of the future applications of the conversion products are discussed. 相似文献
3.
Genetically modified Saccharomyces cerevisiae strain (YPB-G) which secretes a bifunctional fusion protein that contains both Bacillus subtilis -amylase and Aspergillus awamori glucoamylase activities was used for the direct conversion of starch into ethanol. Starch was either supplied initially to different nutrient media or added instantaneously to the reactor at various discrete time instants (pulse feeding). Stoichiometric modeling was used to investigate the effects of initial substrate concentration and growth rate of the recombinant yeast culture on ethanol production. Reaction stoichiometries describing both the anabolism and catabolism of the microorganism were used as an input to flux balance analysis (FBA), the preferred metabolic modeling approach since the constructed stoichiometric network was underdetermined. Experiments for batch and fed-batch systems at different substrate concentrations were analyzed theoretically in terms of flux distributions using ethanol production rate as the maximization criteria. Calculated ethanol rates were in agreement with experimental measurements, suggesting that this recombinant microorganism is sufficiently evolved to optimize its ethanol production. The function of the main pathways of yeast metabolism (PPP, EMP, TCA) are discussed together with the node analyses of glucose-6-P and pyruvate branch points. Theoretical node analysis revealed that if the split ratio in G6P branch point is changed by genetic manipulations, the ethanol yield would be affected considerably. 相似文献
4.
目的:预处理对木质纤维素降解的影响.方法:从土壤中分离筛选到高纤维素酶活的黏细菌菌株So ce sh1008.该菌具有CMC酶活(CMCase)及微晶纤维素酶活性.研究NaOH联合黏细菌降解盐蒿、稻草、棉花秸秆和甘蔗渣四种木质纤维素的情况.结果:碱(2% NaOH) -黏细菌处理的方法优于黏细菌-碱的方法,其中降解棉花秸秆降解效果最明显,以5.0g木质纤维素为原料,其最终干重损失达2.1g,溶液中总糖含量和还原糖含量均值分别为12.8 mg/mL和0.93 mg/mL.酵母菌发酵产乙醇的研究结果表明,最佳发酵时间为47h,碱-黏细菌甘蔗渣降解液发酵效果最好,乙醇产出达6.0%.结论:黏细菌联合2% NaOH能有效降解甘蔗渣,提高乙醇产量. 相似文献
5.
Fangqing Wei Menglei Li Ming Wang Hongxing Li Zailu Li Wensheng Qin Tiandi Wei Jianzhi Zhao Xiaoming Bao 《Global Change Biology Bioenergy》2021,13(1):83-97
During second‐generation bioethanol production from lignocellulosic biomass, the desired traits for fermenting microorganisms, such as Saccharomyces cerevisiae, are high xylose utilization and high robustness to inhibitors in lignocellulosic hydrolysates. However, as observed previously, these two traits easily showed the antagonism, one rising and the other falling, in the C6/C5 co‐fermenting S. cerevisiae strain. In this study, LF1 obtained in our previous study is an engineered budding yeast strain with a superior co‐fermentation capacity of glucose and xylose, and was then mutated by atmospheric and room temperature plasma (ARTP) mutagenesis to improve its robustness. The ARTP‐treated cells were grown in 50% (v/v) leachate from lignocellulose pretreatment with high inhibitors content for adaptive evolution. After 30 days, the generated mutant LF1‐6 showed significantly enhanced tolerance, with a six‐fold increase in cell density in the above leachate. Unfortunately, its xylose utilization dropped markedly, indicating the recurrence of the negative correlation between xylose utilization and robustness. To alleviate this antagonism, LF1‐6 cells were iteratively mutated with ARTP mutagenesis and then anaerobically grown using xylose as the sole carbon source, and xylose utilization was restored in the resulting strain 6M‐15. 6M‐15 also exhibited increased co‐fermentation performance of xylose and glucose with the highest ethanol productivity reported to date (0.525 g g?1 h?1) in high‐level mixed sugars (80 g L?1 glucose and 40 g L?1 xylose) with no inhibitors. Meanwhile, its fermentation time was shortened by 8 h compared to that of LF1. During the fermentation of non‐detoxified lignocellulosic hydrolysate with high inhibitor concentrations at pH ~3.5, 6M‐15 can efficiently convert glucose and xylose with an ethanol yield of 0.43 g g?1. 6M‐15 is also regarded as a potential chassis cell for further design of a customized strain suitable for production of second‐generation bioethanol or other high value‐added products from lignocellulosic biomass. 相似文献
6.
二氧化碳(carbon dioxide, CO2)资源化利用是全球可持续发展面临的巨大挑战。自然界生物固碳绿色环保,但能效低、速度慢,难以满足工业生产需求;物理化学固碳效率高,但能耗高、产品单一,如何结合生物、物理与化学技术优势,以二氧化碳为原料进行生物转化利用是当前迫切需要解决的科技难题。本文结合中国科学院天津工业生物技术研究所建所10年来的发展,综述了人工固碳元件、途径与系统的设计与构建等前沿基础领域取得的重要进展,特别是首次实现二氧化碳人工合成淀粉,并对建立二氧化碳人工生物转化技术体系进行了展望。相关进展与展望为助力实现“碳达峰、碳中和”目标提供了新思路。 相似文献
7.
Phospholipase A2 selectively hydrolyses the ester linkage at the sn-2 position of phospholipids forming lysocompounds. This bioconversion has importance in biotechnology since lysophospholipids are strong bioemulsifiers. The aim of the present work was to study the kinetic behaviour and properties of immobilized phospholipase A2 from bee venom adsorbed into an ion exchange support. The enzyme had high affinity for CM-Sephadex® support and the non-covalent interaction was optimum at pH 8. The activity of immobilized phospholipase A2 was comparatively evaluated with the soluble enzyme using a phospholipid/Triton X-100 mixed micelle as assay system. The immobilized enzyme showed high retention activity and excellent stability under storage. The activity of the immobilized system remained almost constant after several cycles of hydrolysis. Immobilized phospholipase A2 was less sensitive to pH changes compared to soluble form. The kinetic parameters obtained (Vmax 883.4 μmol mg−1 min−1 and a Km 12.9 mM for soluble form and Vmax = 306 μmol mg−1 min−1 and a Km = 3.9 for immobilized phospholipase A2) were in agreement with the immobilization effect. The results obtained with CM-Sephadex®-phospholipase A2 system give a good framework for the development of a continuous phospholipid bioconversion process. 相似文献
8.
9.
This article addresses the issue of effect of fermentation parameters for conversion of glycerol (in both pure and crude form) into three value-added products, namely, ethanol, butanol, and 1,3-propanediol (1,3-PDO), by immobilized Clostridium pasteurianum and thereby addresses the statistical optimization of this process. The analysis of effect of different process parameters such as agitation rate, fermentation temperature, medium pH, and initial glycerol concentration indicated that medium pH was the most critical factor for total alcohols production in case of pure glycerol as fermentation substrate. On the other hand, initial glycerol concentration was the most significant factor for fermentation with crude glycerol. An interesting observation was that the optimized set of fermentation parameters was found to be independent of the type of glycerol (either pure or crude) used. At optimum conditions of agitation rate (200 rpm), initial glycerol concentration (25 g/L), fermentation temperature (30°C), and medium pH (7.0), the total alcohols production was almost equal in anaerobic shake flasks and 2-L bioreactor. This essentially means that at optimum process parameters, the scale of operation does not affect the output of the process. The immobilized cells could be reused for multiple cycles for both pure and crude glycerol fermentation. 相似文献
10.
Ping Yu Kaifei Chen Xingxing Huang Xinxin Wang Qian Ren 《Preparative biochemistry & biotechnology》2013,43(10):906-913
AbstractThe compound γ-aminobutyric acid (GABA) has many important physiological functions. The effect of glutamate decarboxylases and the glutamate/GABA antiporter on GABA production was investigated in Escherichia coli. Three genes, gadA, gadB, and gadC were cloned and ligated alone or in combination into the plasmid pET32a. The constructed plasmids were transformed into Escherichia coli BL21(DE3). Three strains, E. coli BL21(DE3)/pET32a-gadA, E. coli BL21(DE3)/pET32a-gadAB and E. coli BL21(DE3)/pET32a-gadABC were selected and identified. The respective titers of GABA from the three strains grown in shake flasks were 1.25, 2.31, and 3.98?g/L. The optimal titer of the substrate and the optimal pH for GABA production were 40?g/L and 4.2, respectively. The highest titer of GABA was 23.6?g/L at 36?h in batch fermentation and was 31.3?g/L at 57?h in fed-batch fermentation. This study lays a foundation for the development and use of GABA. 相似文献