发明名称 Activated sludge treatment method, and method for upgrading existing waste water treatment equipment using said method
摘要 The object is to provide an activated sludge treatment method whereby production of excess sludge is brought substantially to zero; and a method for upgrading existing waste water treatment equipment, employing this method. The method includes a step (1) in which sludge (2) produced in a sedimentation tank is supplied to a waste water aeration-conditioning tank for activated sludge treatment; a step (2) in which waste water into which the sludge (2) has been mixed is subjected to aeration-conditioning to bring the oxidation-reduction potential to a positive value, and supplied to a pressurized flotation concentration-separation tank; a step (3) in which the sludge (1) produced through treatment in the pressurized flotation concentration-separation tank is supplied to the bioreactor; a step (4) in which the treated waste water (1) separated from the pressurized flotation concentration-separation tank is supplied to a dilute activated sludge aeration tank; a step (5) in which released water and the sludge (3) produced by treatment in the bioreactor are supplied to the dilute activated sludge aeration tank; and a step (6) in which the treated waste water (2) separated from the dilute activated sludge aeration tank is supplied to the sedimentation tank.
申请公布号 US9446972(B2) 申请公布日期 2016.09.20
申请号 US201214383077 申请日期 2012.03.07
申请人 JAPAN ALSI CO., LTD. 发明人 Fujino Kiyoharu
分类号 C02F3/30;C02F3/12;C02F3/00;C02F101/32;C02F103/32 主分类号 C02F3/30
代理机构 Hedman & Costigan, P.C. 代理人 Hedman & Costigan, P.C. ;Costigan James V.;Costigan Kathleen A.
主权项 1. An activated sludge treatment method for treatment of wastewater by a circulation system equipped with a waste water aeration-conditioning tank, a pressurized flotation concentration-separation tank, a dilute activated sludge aeration tank, a bioreactor, and a sedimentation tank, sludge being circulated among the tanks, wherein the activated sludge treatment method is characterized by comprising: a step 1 in which sludge 2 produced in the sedimentation tank is supplied to the waste water aeration-conditioning tank supplied with waste water prior to treatment; a step 2 in which waste water into which the sludge 2 has been mixed is subjected to aeration-conditioning in the waste water aeration-conditioning tank, to bring the oxidation-reduction potential to a positive value, and the conditioned waste water is then supplied to the pressurized flotation concentration-separation tank; a step 3 in which the sludge 1 produced through treatment in the pressurized flotation concentration-separation tank is supplied to the bioreactor; a step 4 in which the treated waste water 1 separated from the pressurized flotation concentration-separation tank is supplied to the dilute activated sludge aeration tank; a step 5 in which released water and the sludge 3 produced by treatment in the bioreactor are supplied to the dilute activated sludge aeration tank; and a step 6 in which the treated waste water 2 separated from the dilute activated sludge aeration tank is supplied to the sedimentation tank wherein the bioreactor is equipped with an outer tank; a cylindrical inner tank situated in the interior of the outer tank and having openings at top and bottom; a circulation rate control device provided in an upper part of the cylindrical inner tank, and adapted for controlling the rate of circulation of treated water inside the tank; a cylindrical control plate provided to the outside perimeter in an upper part of the cylindrical inner tank, and adapted for inducing sedimentation of the sludge; treated water quality measurement devices provided outside and inside the cylindrical inner tank; a waste water supply port provided to a circulation pathway of the treated water circulated within the outer tank and the inner tank; and a treated water release port provided to an upper part of the outer tank; the cylindrical inner tank being divided, by a partitioning wall having a passage hole in a center part, into a cylindrical top part and a cylindrical bottom part, the cylindrical top part constituting an aerobic microorganism treatment tank having a conical trapezoidal apical part open at the top face and the bottom face and provided with a plurality of air injection ports in a peripheral edge part of the partitioning wall and surrounding the passage hole within the cylindrical top part, and the cylindrical bottom part constituting an anaerobic microorganism treatment tank having an open part at the bottom face; the bioreactor being provided with stirring devices for stirring the aerobic microorganism treatment tank and the anaerobic microorganism treatment tank; and provided with means for detecting at least one measured value selected from the hydrogen ion concentration, the oxidation-reduction potential, and the dissolved oxygen content of the treated water measured by the treated water quality measurement devices, and with means provided to the circulation rate control device according to the detected measured value, and adapted for controlling the rate at which water circulates within the tank to 3-20, through control of at least one quantity selected from opening-closing of a fluid level adjustment valve, vertical movement of a fluid level adjustment control panel, and the quantity of air blown in from the air injection ports; wherein anaerobic microorganism treatment and aerobic microorganism treatment take place in successive fashion through circulation of activated sludge, together with waste water supplied from the waste water supply port, within the tank, through the interior of the cylindrical inner tank, the outside peripheral face of the cylindrical inner tank, and within activated sludge that has sedimented to a bottom part of the outer tank.
地址 Mie JP