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Principles of an enhanced MBR-process with mechanical cleaning

机译:机械清洁增强MBR工艺的原理

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Up to date, different physical and chemical cleaning protocols are necessary to limit membrane fouling in membrane bioreactors. This paper deals with a mechanical cleaning process, which aims at the avoidance of hypochlorite and other critical chemicals in MBR with submerged flat sheet modules. The process basically consists of the addition of plastic particles into the loop circulation within submerged membrane modules. Investigations of two pilot plants are presented: Pilot plant 1 is equipped with a 10 m~2 membrane module and operated with a translucent model suspension; pilot plant 2 is equipped with four 50 m~2 membrane modules and operated with pretreated sewage. Results of pilot plant 1 show that the establishment of a fluidised bed with regular particle distribution is possible for a variety of particles. Particles with maximum densities of 1.05 g/cm~3 and between 3 and 5 mm diameter form a stable fluidised bed almost regardless of activated sludge concentration, viscosity and reactor geometry. Particles with densities between 1.05 g/cm~3 and 1.2 g/cm~3 form a stable fluidised bed, if the velocity at the reactor bottom is sufficiently high. Activities within pilot plant 2 focused on plant optimisation and the development of an adequate particle retention system.
机译:迄今为止,为了限制膜生物反应器中的膜结垢,必须采用不同的物理和化学清洁方案。本文涉及一种机械清洁工艺,旨在避免使用浸没式平板模块的MBR中的次氯酸盐和其他关键化学物质。该过程主要包括将塑料颗粒添加到浸没膜组件内的回路中。介绍了两个中试工厂的调查结果:中试工厂1配备了10 m〜2的膜组件,并使用半透明的模型悬架进行操作;中试工厂2配备了四个50 m〜2的膜组件,并经过预处理的污水运行。中试工厂1的结果表明,对于各种颗粒,可以建立具有规则颗粒分布的流化床。不论活性污泥的浓度,粘度和反应器的几何形状如何,最大密度为1.05 g / cm〜3且直径在3-5 mm之间的颗粒形成稳定的流化床。如果在反应器底部的速度足够高,则密度在1.05 g / cm〜3和1.2 g / cm〜3之间的颗粒形成稳定的流化床。中试工厂2内的活动集中在工厂优化和适当的颗粒保留系统的开发上。

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