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    • 31. 发明专利
    • Ozone gas injection control system
    • 臭氧注射控制系统
    • JP2005324124A
    • 2005-11-24
    • JP2004144680
    • 2004-05-14
    • Toshiba CorpToshiba Plant Systems & Services Corp東芝プラントシステム株式会社株式会社東芝
    • MURAYAMA SEIICHINAKANO SOICHIROUMIGA NOBUYOSHI
    • G01N21/64C02F1/78G01N33/18
    • PROBLEM TO BE SOLVED: To provide an ozone gas injection control system which can control generation of energy useless for ozone gas generation, and control generation of a bromate ion by preventing dissolved ozone concentration from going to excess, and keep the proper quality of ozone-treated water.
      SOLUTION: An ozone reaction tank 3 comprises a plurality of ozone contact tanks 3a, 3b, 3c, 3d into which ozone is injected from an ozone gas injection device 7. The plurality of the ozone contact tanks 3a, 3b, 3c, 3d are divided into at least two groups G1, G2. An ozone gas injection control device 10 controls the ozone gas injection device 7 based on the fluorescence intensities measured by fluorescence intensity analyzers 6a, 6b, 6c to adjust the injection rate of ozone gas injected into each of the ozone contact tanks 3a, 3b, 3c, 3d for the groups G1, G2 respectively.
      COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题:提供一种臭氧气体注入控制系统,其可以控制臭氧气体产生无用的能量的产生,并且通过防止溶解的臭氧浓度过剩来控制溴酸根离子的产生,并保持适当的质量 的臭氧处理水。 解决方案:臭氧反应罐3包括从臭氧气体注入装置7向其中注入臭氧的多个臭氧接触罐3a,3b,3c,3d。多个臭氧接触罐3a,3b,3c, 3d分为至少两组G1,G2。 臭氧气体注入控制装置10基于由荧光强度分析器6a,6b,6c测量的荧光强度来控制臭氧气体注入装置7,以调节注入每个臭氧接触罐3a,3b,3c中的臭氧气体的喷射速率 ,分别为组G1,G2的3d。 版权所有(C)2006,JPO&NCIPI
    • 36. 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.
    • 37. 发明专利
    • WATER TREATMENT APPARATUS
    • JPH0966294A
    • 1997-03-11
    • JP22422195
    • 1995-08-31
    • TOSHIBA CORP
    • UMIGA NOBUYOSHIKANAMARU KOJI
    • C02F3/34
    • PROBLEM TO BE SOLVED: To treat water by using two or more kinds of bacteria different in alteration of generations and discharging these bacteria to the outside in proper timing to perform proper water treatment. SOLUTION: A first biological activated carbon bed 3 where bacteria relatively short in alteration of generations are propagated and a second biological activated carbon bed 4 where bacteria relatively long in alteration of generations are propagated are formed. The first biological activated carbon bed 3 is washed backward at a short interval by first backward washing devices 6, 8, 10 and the second biological activated carbon bed 4 is washed backward as a long interval by second backward washing devices 7, 9, 11. The turbid water generated from the first biological activated carbon bed 3 at a time of the initial supply of water is discharged out of a discharge pipe 16.
    • 38. 发明专利
    • WATER TREATMENT APPARATUS
    • JPH07256286A
    • 1995-10-09
    • JP5594594
    • 1994-03-25
    • TOSHIBA CORP
    • UMIGA NOBUYOSHIKANAMARU KOJI
    • C02F3/06C02F1/28C02F3/10C02F3/26
    • PURPOSE:To keep the activity of bacteria even when the movement of activated carbon particles is generated by backwashing, in a water treatment apparatus equipped with a biological activated carbon bed, by arranging a dissolved oxygen supply device having a dissolved oxygen injection port provided thereto in the biological activated carbon bed. CONSTITUTION:Bacteria grown using an ozone oxidation product as a nutrition source consume dissolved oxygen in the upper bed part of an activated carbon bed 2 to propagate and, when nutrients are rich and propagation is actively performed, oxygen becomes deficient in the lower bed part of the activated carbon bed 4. Oxygen is sent out of an oxygen cylinder 4 but, at this time, the pressure of oxygen is adjusted by a pressure adjusting valve 5 so that oxygen is not blown in as oxygen gas bubbles and oxygen is introduced into the intermediate bed part of the activated carbon bed 2 from oxygen injection ports 3. Bacteria are propagated using activated carbon particles as a carrier but, when the gaps between particles are filled with bacteria, the pressure loss of water passage becomes large and, therefore, the supply of water from an inflow pipe 9 is stopped in a specific ratio and an air washing valve 12A and a backwashing valve 13A are opened to send air and backwashing water to backwash the biological activated carbon bed 2.
    • 39. 发明专利
    • METHOD FOR STERILIZING SEWAGE DISPOSAL WATER
    • JPH07185576A
    • 1995-07-25
    • JP33088893
    • 1993-12-27
    • TOSHIBA CORP
    • UMIGA NOBUYOSHIKANAMARU KOJI
    • C02F1/24C02F1/32C02F1/52C02F1/78C02F9/00
    • PURPOSE:To decolor sewage disposal water and to exhance sterilization effect by preventing ultraviolet rays(UV) from being absorbed in colored substance when the UV irradiates by applying ozone treatment to sewage disposal water at a stage before UV irradiation is applied in equipment in the case the sterilization of the sewage disposal water before discharge is performed by the irradiation of the UV. CONSTITUTION:After sludge 3 is sedimented in a sedimentation basin 2, the supernatant liquid of activated sludge 1 is sent to a UV sterilization tank 4, and it is sterilized by applying the UV irradiation by a UV lamp 5. Displosal water is discharged to a river, etc., as discharge water 6. In such a case, an ozone reaction tank 7 is installed at the front stage of the UV sterilization tank 4. The ozone reaction tank 7 performs the ozone treatment of the disposal water by discharging ozonized air generated by an ozone generator 7A to the disposal water by a duffuser pipe 7B and an unreacting ozone is discharged to the air after being decomposed by an exhaust ozone decomposing tower 7C. The following UV sterilization can be effectively performed by performing the decoloring by the ozone treatment in such way.