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使用纯氧供应好氧条件的浸没式膜生物反应器中的呼吸测量法进行动力学研究和氧传递效率评估。

Kinetic study and oxygen transfer efficiency evaluation using respirometric methods in a submerged membrane bioreactor using pure oxygen to supply the aerobic conditions.

机构信息

Department of Civil Engineering, University of Granada, 18071 Granada, Spain.

出版信息

Bioresour Technol. 2011 May;102(10):6013-8. doi: 10.1016/j.biortech.2011.02.083. Epub 2011 Feb 23.

Abstract

The performance of a wastewater bench-scale ultrafiltration membrane bioreactor (MBR) treatment plant using pure oxygen to supply the aerobic conditions for 95 days was studied. The results showed the capacity of the MBR systems to remove organic material under a hydraulic retention time of 12h and a sludge retention time of 39.91 days. Aeration represents its major power input; this is why the alpha-factor of the aeration and kinetic parameters (design parameters) were determined when the mixed liquid suspended solids (MLSS) was increased from 3420 to 12,600 mg/l in order to understand the system. An alpha-factor in the range 0.462-0.022 and the kinetic parameters measured with the respirometric method (K(M) of 73.954-3.647 mg/l, k(d) of 0.0142-0.104 day(-1), k(H) of 0.1266-0.655 day(-1), and the yield mean coefficient of 0.941) were obtained. Our study suggested significant changes in the behaviour of the biological system when the concentration of MLSS was increased.

摘要

采用纯氧为好氧条件提供氧气的废水中试规模超滤膜生物反应器(MBR)处理厂的性能进行了 95 天的研究。结果表明,MBR 系统在水力停留时间为 12h 和污泥停留时间为 39.91 天的条件下,能够去除有机物质。曝气是其主要的动力输入;这就是为什么当混合液悬浮固体(MLSS)从 3420mg/L 增加到 12600mg/L 时,需要确定曝气的α因子和动力学参数(设计参数),以便了解系统。获得了 0.462-0.022 范围内的α因子和通过呼吸计法测量的动力学参数(K(M)为 73.954-3.647mg/L,k(d)为 0.0142-0.104 天(-1),k(H)为 0.1266-0.655 天(-1)和产率平均系数为 0.941)。我们的研究表明,当 MLSS 浓度增加时,生物系统的行为发生了显著变化。

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