994 resultados para Thermotolerant fungus


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铊是一种有毒有害的重金属元素,已经引起了广泛的关注。本论文通过对黔西南铊矿区土壤和沉积物样品的菌株分离、铊高耐受性菌株的筛选、胞外吸附、富集、亚细胞水平区系分布、絮凝实验及ITS序列等实验研究分析,并结合铊的地球化学相关研究,较系统地阐述了真菌--铊的生物地球化学过程机理,得出以下结论: 1、与环境背景区相比,黔西南滥木厂铊矿区内的河流、土壤中铊的已有不同程度的积累,直接导致了当地微生物生物量在很大程度上的降低,微生物生物量与铊含量间有显著的负相关关系。研究区内的沉积物、土壤中的微生物区系结构和数量发生了明显变化,细菌、真菌及放线菌数量均出现显著降低,而且三大微生物对重金属污染的敏感性大小也不一样,即放线菌>细菌>真菌。从土壤样品中分离到的主要菌群仍为常见种属,如青霉属(Penicillium)、木霉属(Trichoderma)、拟青霉(Paecilomyces)等。 2、经过初筛菌株的铊耐受性实验,在1000 mg/L水平筛选得到九株高耐受性菌株。吸附实验表明:微生物菌株对铊的吸附效率在4.63~16.89%,且随着环境中铊浓度的上升而降低,这可能是因为铊浓度的升高加大了对微生物生长的抑制作用,所形成的菌丝体(或菌丝球)减少,表面积也相应减少,从而导致了吸附效率的下降。各种常量元素和铊的关系呈显著相关性,钙、钾和钠等常量元素也是微生物赖以维持生存的因子,可能由于微生物细胞对钙、钾的吸附方式与对铊的吸附方式类似。因此,随着铊处理浓度的上升,钙和钾的吸附量也随之减少,而钠则呈现相反的趋势。 3、富集实验表明,九株菌株对铊的富集量随着铊处理浓度上升而降低,其影响趋势与对生物量的影响趋势基本一致,最高可达到7189 mg/kg,最大富集系数为7.2。九株菌株对常量元素的富集与对铊的富集并无明显的相关性,但在考察铊处理浓度对常量元素的富集影响时发现,铊处理浓度的上升与对钙的富集量表现出较强的正相关;而对钾、钠、镁的富集影响并不明显。 4、亚细胞水平上的铊分布研究表明,铊的富集优先顺序为:细胞质>细胞壁>细胞器。亚细胞水平的区隔化作用是微生物对铊的主要耐受机制,细胞质是赋存铊的主要场所(53.83~79.45 %)。结合各亚细胞组分中常量元素与铊之间的相关性,并联系前人的研究,Tl+主要是通过细胞壁的Na+ -K+ ATPase和K+ -电位门通道进入细胞内的从而影响细胞的正常代谢的,而Ca2+的活化更有助于这一过程。 5、絮凝实验表明,培养三天后的发酵液对矿区废水中铊的去除率最高可达到70.49 %,最佳影响因子组合为:pH=8,温度为16℃,搅拌时间为4分钟。菌株的絮凝活性最高可达到57.32%,最佳影响因子组合为:pH=8,温度为14℃,搅拌时间为4分钟。 6、通过对九株铊高耐受性菌株的ITS序列分析及其在Gene Bank中的BLAST比对结果表明,五株菌株同属于木霉属(Trichoderma),两株菌株同属于青霉属(Penicillium)。这表明这两类真菌对铊的适应性较强,为以后寻找铊高耐受性菌株及其资源化利用提供了理论基础。

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Matthew J. Nicholson, Michael K. Theodorou and Jayne L. Brookman. (2005). Molecular analysis of the anaerobic rumen fungus Orpinomyces - insights into an AT-rich genome. Microbiology, 151 (1), 121-133. Sponsorship: BBSRC RAE2008

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The development of a new bioprocess requires several steps from initial concept to a practical and feasible application. Industrial applications of fungal pigments will depend on: (i) safety of consumption, (ii) stability of the pigments to the food processing conditions required by the products where they will be incorporated and (iii) high production yields so that production costs are reasonable. Of these requirements the first involves the highest research costs and the practical application of this type of processes may face several hurdles until final regulatory approval as a new food ingredient. Therefore, before going through expensive research to have them accepted as new products, the process potential should be assessed early on, and this brings forward pigment stability studies and process optimisation goals. Only ingredients that are usable in economically feasible conditions should progress to regulatory approval. This thesis covers these two aspects, stability and process optimisation, for a potential new ingredient; natural red colour, produced by microbial fermentation. The main goal was to design, optimise and scale-up the production process of red pigments by Penicillium purpurogenum GH2. The approach followed to reach this objective was first to establish that pigments produced by Penicillium purpurogenum GH2 are sufficiently stable under different processing conditions (thermal and non-thermal) that can be found in food and textile industries. Once defined that pigments were stable enough, the work progressed towards process optimisation, aiming for the highest productivity using submerged fermentation as production culture. Optimum production conditions defined at flask scale were used to scale up the pigment production process to a pilot reactor scale. Finally, the potential applications of the pigments were assessed. Based on this sequence of specific targets, the thesis was structured in six parts, containing a total of nine chapters. Engineering design of a bioprocess for the production of natural red colourants by submerged fermentation of the thermophilic fungus Penicillium purpurogenum GH2.

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Kinesins are motor proteins that convert chemical energy from ATP hydrolysis into mechanical energy used to generate force along microtubules, transporting organelles, vesicles, and proteins within the cell. Kar3 kinesins are microtubule minus-end-directed motors with pleiotropic functions in mating and mitosis of budding and fission yeast. In Saccharomyces cerevisiae, Kar3 is multifunctionalized by two non-catalytic companion proteins, Vik1 and Cik1. A Kar3-like kinesin and a single Vik1/Cik1 ortholog are also expressed by the filamentous fungus Ashbya gossypii, which exhibits different nuclear movement challenges and unique microtubule dynamics from its yeast relatives. We hypothesized that these differences in A. gossypii physiology could translate into interesting and novel differences in its versions of Kar3 and Vik1/Cik1. Presented here is a structural and functional analysis of recombinantly expressed and purified forms of these motor proteins. Compared to the previously published S. cerevisiae Kar3 motor domain structure (ScKar3MD), AgKar3MD displays differences in the conformation of the ATPase pocket. Perhaps it is not surprising then that we observed the maximal microtubule-stimulated ATPase rate (kcat) of AgKar3MD to be approximately 3-fold slower than ScKar3MD, and that the affinity of AgKar3MD for microtubules (Kd,MT) was lower than ScKar3MD. This may suggest that elements that compose the ATPase pocket and that participate in conformational changes required for efficient ATP hydrolysis or products release work differently for AgKar3 and ScKar3. There are also subtle structural differences in the disposition of the secondary structural elements in the small lobe (B1a, B1b, and B1c) at the edge of the motor domain of AgKar3 that may reflect the enhanced microtubule-depolymerization activity that we observed for this motor, or they could relate to its interactions with a different regulatory companion protein than its budding yeast counterpart. Although we were unable to gain experimentally determined high-resolution information of AgVik1, the results of Phyre2-based bioinformatics analyses may provide a structural explanation for the limited microtubule-binding activity we observed. These and other fundamental differences in AgKar3/Vik1 could explain divergent functionalities from the ScKar3/Vik1 and ScKar3/Cik1 motor assemblies.

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A total synthesis of phomactin G (3), which is a central intermediate in the biosynthesis of phomactin A (5) in Phoma sp. is described. The synthesis is based on a Cr(II)/Ni(II) macrocyclisation from the aldehyde vinyl iodide 9, leading to 16, followed by sequential conversion of 16 into the -epoxide 21 and the ketone 25 which, on deprotection, led to (±)-phomactin G. Phomactin G (3) shares an interesting structural homology with phomactin D (2), the most potent PAF-antagonist metabolite in Phoma sp. It is most likely converted into phomactin A (5), by initial allylic oxidation to the transient -alcohol phomactin structure 4, known as Sch 49028, followed by spontaneous pyran ring formation.