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    • 2. 发明专利
    • DOWNWARD INJECTING TYPE OZONE TREATING DEVICE
    • JPH09206769A
    • 1997-08-12
    • JP1857596
    • 1996-02-05
    • FUJI ELECTRIC CO LTD
    • KATO YASUHIROMORIOKA TAKAYUKITAKAHASHI RYUTARO
    • C02F1/00B01F1/00C02F1/50C02F1/58C02F1/78
    • PROBLEM TO BE SOLVED: To keep a flow rate of a water to be treated subjected to gas-liq. mixing within a fixed range and secure stable ozone treatment by allowing the water to be treated less than a specified flow rate to flow downward in the first flow passage under a constant head difference and allowing the water to be treated above the specified flow rate to flow downward in the second flow passage. SOLUTION: The minimum flow rate of the water to be treated is allowed to flow downward in the first flow passage 8, and the water to be treated above the minimum flow rate is allowed to flow into the second flow passage 11 by interposing the first overflow part 10 and allowed to flow downward. Then the water to be treated which is subjected to gas-liq. mixing by diffusing a gaseous ozone from an ozone diffuser 3 to the water to be treated flowing in the flow passage 9 and the water to be treated flowing in the second flow passage 11 are joined at a joining point 2, and after allowing the jointed water to flow upward in the third flow passage 5, the jointed water is allowed to flow in a residence tank 14 having a partition plate 15 through the second overflow part 13 and discharged from a discharge port 6. And the unreacted ozone out of the gaseous ozone injected in the water to be treated at that time is subjected to the gas-liq. separation at the upper part of the first flow passage 5, and after decomposing at a waste ozone treating device, discharged out of system.
    • 4. 发明专利
    • DESCENDING DISSOLUTION TYPE OZONE REACTION CHAMBER
    • JPH07195092A
    • 1995-08-01
    • JP102494
    • 1994-01-11
    • FUJI ELECTRIC CO LTD
    • KATO YASUHIROMORIOKA TAKAYUKIOOHANAMORI HIDEYUKITAKAHASHI RYUTARO
    • C02F1/00C02F1/50C02F1/78
    • PURPOSE:To lower the ascending speed of air bubbles in an ascending section of a reaction chamber so as to make the speed nearly equal to the ascending speed of water to be treated and thereby, to obviate generation of short circuit flow and dead water area by disposing members for suppressing the rising speed of the air bubbles consisting of gaseous ozone in the rising section of the reaction chamber. CONSTITUTION:The water 4 to be treated is introduced by a water feed pump 3 into the ozone treating device of a descending dissolution type from an introducing port 2 in the upper part of the reaction chamber 1 formed to a U shape and simultaneously, the gaseous ozone is injected as the air bubbles 7 from a gas diffusion device 6. The mixed flow composed of the water 4 to be treated and the air bubbles 7 falls in the descending dissolution section 1a of the reaction chamber 1 and passes the ascending section 1b until the mixed flow is discharged as treated water 9 from a discharge port 8. Plural sheets of shielding plates 13 are alternately disposed as the bodies 12 for suppressing ascending of the air bubbles within the ascending section 1b of such constitution. As a result, the ascending speed of the air bubbles 7 in the ascending section 1b is so lowered as to be nearly equalled to the ascending speed of the water 4 to be treated, by which the generation of the short circuit flow and the dead water area is obviated.
    • 9. 发明专利
    • WATER TREATING DEVICE USING OZONE AND DEFOAMING METHOD THEREOF
    • JPH0471687A
    • 1992-03-06
    • JP18115890
    • 1990-07-09
    • FUJI ELECTRIC CO LTD
    • MOTOYAMA NOBUYUKIMORIOKA TAKAYUKI
    • B01D19/02C02F1/78
    • PURPOSE:To efficiently remove the foam generated in a contact tank by mounting a water flow control plate to the water treating device having a flow regulating tank and the contact tank 18 and controlling the water flow from the flow regulating tank to the contact tank. CONSTITUTION:The water flow control plate 21 having an inclination with a water surface is mounted slight apart from the water surface near the partition plate 16 in the contact tank 18. The water 2 to be treated flowing into a reaction tank 1 collides against the water flow control plate 21 and flows down along the partition plate 16 to the contact tank 18. On the other hand, the passage rate of the ozonizing air from an air diffusion pipe 11a is decreased and the passage rate of the ozonizing air from an air diffusion pipe 11b is increased, to generate swirling flow in the water 2 to be treated in the contact tank 18. The bubbles 20 accumulating on the water surface are moved to the place of the water flow control plate 21 by this swirling flow and are thereafter withdrawn into the contact tank 18 together with the water 2 to be treated flowing into the spacing between the water flow control plate 21 and the partition plate 16. Then, the stagnation of the bubbles in the space part 16 is obviated.