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    • 8. 发明授权
    • Method for treatment of waste water by activated sludge process
    • 活性污泥法处理废水的方法
    • US5573670A
    • 1996-11-12
    • US361455
    • 1994-12-21
    • Yoshimi NagasakiHidetsugu Nakazawa
    • Yoshimi NagasakiHidetsugu Nakazawa
    • C02F1/78C02F3/12C02F3/26
    • C02F3/121C02F3/26Y02W10/15
    • Waste water is treated by an activated sludge process, the equipment for which is provided with an aeration tank unit comprised of three tanks of a first tank, a second tank and a third tank, said waste water and microorganisms being fed into the first tank while the ratio of aeration in the first tank ranges from 0.5 to 0.8 by volume/minute relative to the amount of liquid in the first tank, the ratio of aeration in the second tank ranges from 0. 1 to 0.4 by volume/minute relative to the amount of liquid in the said second tank and the ratio of aeration in the third tank ranges from 0.1 to 0.3 by volume/minute relative to the amount of liquid in the third tank, the improvement which comprises carrying out said treatment by passing air containing ozone in an amount of from 0.01 to 0.16 wt. % relative to the amount of oxygen during the aeration into the first tank.
    • 废水通过活性污泥法处理,其设备设置有由第一罐,第二罐和第三罐的三个罐组成的曝气池单元,所述废水和微生物进料到第一罐中, 相对于第一罐中的液体量,第一罐中的曝气比例为0.5至0.8体积/分钟,第二罐中的曝气比例相对于第一罐的通量为0.1至0.4体积/分钟 所述第二罐中的液体量和第三罐中的曝气量相对于第三罐中的液体量为0.1至0.3体积/分钟,其改进包括通过使含臭氧的空气进行所述处理 其量为0.01至0.16wt。 相对于通入第一罐的氧气量的百分比。