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    • 4. 发明专利
    • ACCELERATED OXIDATION TREATING APPARATUS
    • JP2002361272A
    • 2002-12-17
    • JP2001169819
    • 2001-06-05
    • TOSHIBA CORP
    • SUZUKI SETSUOABE NORIMITSUOHASHI YUKIOKUBO KIETAGUCHI KENJIIYASU KYOTARO
    • G01N33/18C02F1/32C02F1/72C02F1/78
    • PROBLEM TO BE SOLVED: To provide an accelerated oxidation treating apparatus which secures a proper amount of ozone injection and a proper amount of irradiation with ultraviolet rays in accordance with a state of water to be treated, enhances the efficiency of decomposition of organic materials in the water to be treated, enables the effective utilization of ozone and miniaturizes the apparatus. SOLUTION: This accelerated oxidation treating apparatus 1 is provided with a treating tank 2 which has such a structure that an ozone injection area 21, an ultraviolet ray irradiation area 22 and a reaction area 23 are integrated as one body. An ozone diffuser 3 is disposed on the ozone injection area 21 and an ultraviolet ray irradiating device 4 is disposed on the ultraviolet ray irradiation area 22. The ozone injection area 21 and the ultraviolet ray irradiation area 22 are partitioned by a first partition 5, and the ultraviolet ray irradiation area 22 and the reaction area 23 are partitioned by a second partition 6, respectively. A combined diffuser cum guide plate 10 is disposed on the ultraviolet ray area 22, the combined diffuser cum guide plate 10 is connected to the treating tank 2 by an ozone return pipe 30 and the reaction area 23 and the ozone injection area 21 are connected by a waste water return pipe 32.
    • 7. 发明专利
    • CONTROL SYSTEM OF OZONE INJECTING DEVICE
    • JPH1043776A
    • 1998-02-17
    • JP21019796
    • 1996-08-08
    • TOSHIBA CORP
    • TAGUCHI KENJIMAKISE RYUTAROUMIGA NOBUYOSHI
    • C02F1/78G01N21/64
    • PROBLEM TO BE SOLVED: To provide a control system of an ozone injecting device capable of surely reducing a generation of trihalomethane. SOLUTION: A relative fluorescence intensity of a water to be treated before an ozone treatment is measured with a fluorescence analyzer 10, and a required ozone injection ratio reducing a trihalomethane forming capacity is required based on this relative fluorescence intensity at a fluorescence intensity data processor 11. In a fluorescence injection control device 4, a target value of a generating ozone concn. is required based on the required ozone injection ratio from the fluorescence intensity data processor 11, a flowing water flow rate from a flowing water flowmeter 12 and a gas flow rate to be sent from a gas flowmeter 6a. The target value of the generating ozone concn. is outputted to an ozone generator 6. In the ozone generator 6, the ozone is generated based on the target value of the generating ozone concn., and the generated ozone is injected into the water to be treated from an ozone injecting part 3.
    • 10. 发明专利
    • EXHAUST OZONE GAS DECOMPOSITION APPARATUS
    • JPH05154344A
    • 1993-06-22
    • JP32192291
    • 1991-12-05
    • TOSHIBA CORP
    • EGASHIRA YASUOISHIKAWA KATSUHIROTAGUCHI KENJI
    • B01D53/04B01D53/86
    • PURPOSE:To keep catalytic treatment capacity over a long period of time by arranging a pretreatment tower on the upstream side of a catalyst tower to pack the same with an adsorbent adsorbing the component bonded to a catalyst and washing the same with hot water when a definite amount of the adsorbed and bonded component on the catalyst is accumulated. CONSTITUTION:Exhaust ozone gas enters a collector 4 from piping 5 and, after a part of the waterdrops in the exhaust ozone gas is collected, said gas passes through a pretreatment tower 9 from piping 3 through a solenoid valve 10. At this time, the component bonded to a catalyst is adsorbed by the adsorbent 8 received in the pretreatment tower 9 and, thereafter, the exhaust ozone gas enters a catalyst tower 2 through a solenoid valve 7 and the ozone gas is separated by the catalyst 1 in the tower 2. When treatment is performed for a definite time, the component bonded to the catalyst is accumulated on the adsorbent 8 and, therefore, the solenoid valves 7, 10 are closed at every definite time and a solenoid valve 14 is opened to supply the hot water heated by a heater 11 to the pretreatment tower 9 by a pump 13. The adsorbed substance is dissolved and separated from the adsorbent 8 and, thereafter, a solenoid valve 15 is opened to drain the dissolved and separated substance. After the washing of the adsorbent is completed, the regular treatment of exhaust gas is again performed.