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Kinetics of biofilm growth and substrate uptake in model drinking water systems.

机译:模型饮用水系统中生物膜生长和基质吸收的动力学。

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The effects of different substrates on kinetics of biofilm growth and substrate uptake in model drinking water systems were investigated. Biofilm were grown using rotating annular reactors at 20°C and influent substrate concentrations from 500 to 2000 mug C/L. Substrate groups were amino acids, carbohydrates, humic substances and a mix of the three (mixed substrates). Two reactors were operated in parallel; one was the control and the other was chlorinated.; Growth rates were determined using three methods: (1) mass balance for biomass and substrate across reactors, (2) batch cultures using suspended biofilm cells and, (3) uptake of 3H-leucine by attached biofilm on reactor sample slides. Substrate uptake and yield were evaluated for biofilm in reactors and batch culture.; Specific growth rates based on mass balances for chlorinated reactors were greater than for the control. Chlorinated reactors using carbohydrates or mixed substrates had growth rates greater than for amino acids and humic substances. Growth rates based on mass balance for the control reactor biofilm were statistically the same for all substrates except humic substances, which had the lowest growth rate.; Kinetic parameters determined using biofilm cells in batch culture did not generally apply to biofilm in reactors. Removing cells from the biofilm structure alters important parameters such as mass transfer, impact of nutrients that attach to the biofilm matrix, cell physiology, and the influence of chlorine.; Growth rates determined using leucine uptake were comparable to those based on mass balance for control reactor biofilm, but much less than mass balance based growth rates for the chlorinated biofilm. Chlorination may influence the ability of biofilm cells to utilize amino acids such as leucine.; Fractional carbon removal across reactors was constant by substrate and reactor type over the range of substrate concentrations used. Substrate uptake normalized to biomass was greater for chlorinated biofilm than for control. Yield was less for chlorinated biofilm than for control. Although chlorination reduced biomass in the biofilm, the biomass had greater rates of growth and substrate uptake than in the control. Lower yield in chlorinated biofilm may indicate biofilm cells' need to produce additional exopolymeric substances.
机译:在模型饮用水系统中,研究了不同底物对生物膜生长动力学和底物摄取动力学的影响。使用旋转环形反应器在20°C和进水底物浓度从500到2000杯C / L的条件下生长生物膜。底物组是氨基酸,碳水化合物,腐殖质和这三种的混合物(混合底物)。两个反应器并行运行;一个是对照,另一个是氯化的。使用三种方法确定生长速率:(1)反应器中生物质和底物的质量平衡;(2)使用悬浮生物膜细胞的分批培养;(3)通过附着在反应器样品玻片上的生物膜吸收3H-亮氨酸。评价反应器和分批培养中生物膜的底物吸收和产率。基于氯化反应堆质量平衡的比增长率大于对照。使用碳水化合物或混合底物的氯化反应器的生长速率高于氨基酸和腐殖质。对照反应器生物膜的基于质量平衡的生长速率在统计上对所有底物都相同,除了腐殖质(其增长率最低)。在分批培养中使用生物膜细胞测定的动力学参数通常不适用于反应器中的生物膜。从生物膜结构中去除细胞会改变重要的参数,例如传质,附着在生物膜基质上的养分的影响,细胞生理以及氯的影响。使用亮氨酸摄取确定的增长率与对照反应器生物膜的基于质量平衡的增长率相当,但远小于氯化生物膜的基于质量平衡的增长率。氯化作用可能会影响生物膜细胞利用氨基酸(如亮氨酸)的能力。在不同的底物浓度范围内,反应物的部分碳去除率随底物和反应器类型的变化而恒定。相对于对照,氯化生物膜对生物量标准化的底物吸收量更大。氯化生物膜的产量低于对照。尽管氯化减少了生物膜中的生物量,但与对照相比,生物量具有更高的生长速率和底物摄取。氯化生物膜的较低收率可能表明生物膜细胞需要产生额外的外聚合物质。

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