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Aeration amount control system and aeration amount control method

机译:曝气量控制系统及曝气量控制方法

摘要

An aeration amount control system and a water treatment method capable of reducing the operation cost of the aeration amount control system are obtained. In the air diffusion amount control system 100 that performs air diffusion on the separation membrane 3 in the membrane separation tank 2 storing the treated water based on the target air diffusion amount, the first target air diffusion amount is determined as the target air diffusion amount. The control device 7 that determines the second target air diffusion amount after determining the first target air diffusion amount, and the air diffusion device that supplies the gas based on the target air diffusion amount and performs air diffusion 5 and a measuring device 6 that measures the amount of change in the transmembrane pressure difference of the separation membrane 3 with respect to the gas supplied by the air diffusing device 5, and the air diffusing device 5 calculated by the measuring device 6 is the first target air diffusing. The first change amount of the transmembrane pressure difference of the separation membrane 3 during the aeration based on the amount was calculated by the measuring device 6, and the aeration device 5 performed the aeration based on the second target aeration amount. When it is larger than the second change amount of the transmembrane pressure difference of the separation membrane 3 between, the control device 7 is smaller than the second target aeration amount as the third target aeration amount. And determining the a values.
机译:获得了一种能够减少曝气量控制系统的运行成本的曝气量控制系统和水处理方法。在基于目标空气扩散量在存储处理水的膜分离槽2中的分离膜3上进行空气扩散的空气扩散量控制系统100中,将第一目标空气扩散量确定为目标空气扩散量。在确定了第一目标空气扩散量之后确定第二目标空气扩散量的控制装置7,以及基于目标空气扩散量供应气体并进行空气扩散的空气扩散装置5和测量该目标空气扩散量的测量装置6。相对于由空气扩散装置5供给的气体和由测量装置6计算出的空气扩散装置5的分离膜3的跨膜压差的变化量是第一目标空气扩散。通过该测定装置6计算出基于该量的分离膜3的通气时的跨膜压差的第一变化量,通气装置5基于第二目标通气量进行通气。当其大于分离膜3之间的跨膜压差的第二变化量时,控制装置7小于作为第三目标充气量的第二目标充气量。并确定a值。

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