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    • 1. 发明专利
    • 紫外線処理装置
    • 超紫外线处理装置
    • JP2014223583A
    • 2014-12-04
    • JP2013103717
    • 2013-05-16
    • 株式会社東芝Toshiba Corp東芝プラントシステム株式会社Toshiba Plant Systems & Services Corp国立大学法人お茶の水女子大学Ochanomizu Univ
    • NAKANO SOICHIROUMIGA NOBUYOSHIHATANO AKINORIOTAKI MASAHIRO
    • C02F1/32C02F1/50C02F1/78G01N21/64
    • Y02W10/37
    • 【課題】紫外線処理の際に被処理水に必要量以上の紫外線の照射を防止する紫外線処理装置を提供する。【解決手段】被処理水の蛍光強度である被処理水蛍光強度を測定する少なくとも1つの被処理水蛍光分析計11と、被処理水の溶存酸素濃度を測定する溶存酸素計12と、紫外線照射槽13内に配置され、被処理水に紫外線を照射する紫外線照射装置14と、紫外線処理された紫外線照射処理水の蛍光強度である処理水蛍光強度を測定する少なくとも1つの処理水蛍光分析計15と、予め定められるルールにしたがって、測定された被処理水蛍光強度、溶存酸素濃度及び処理水蛍光強度をパラメータとして被処理水の紫外線処理に必要な紫外線量を求め、求められた必要な紫外線量の紫外線を照射するように紫外線照射装置14を制御する紫外線照射量制御装置16aとを備える。【選択図】図1
    • 要解决的问题:提供一种紫外线处理装置,其防止被处理水在紫外线处理中暴露于过量的紫外线。溶液:紫外线处理装置包括:至少一个待处理水的荧光分析仪11 ,其测量待处理的水的荧光强度; 溶解氧分析仪12,其测量待处理的水中的溶解氧浓度; 设置在紫外线照射容器13中的紫外线照射单元14,其对被处理水进行紫外线照射,至少一个用于待处理水的荧光分析仪15,其测量用紫外线处理的水的荧光强度; 以及紫外线照射量控制部16a,使用所测定的被处理水的荧光强度,溶解氧浓度,处理水的荧光强度等作为参数,对紫外线进行紫外线处理,得到紫外线。 按照规定的规定,控制紫外线照射单元14,使紫外线照射所需的量。
    • 3. 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
    • 6. 发明专利
    • WATER TREATMENT APPARATUS
    • JPH06198290A
    • 1994-07-19
    • JP34870392
    • 1992-12-28
    • TOSHIBA CORP
    • UMIGA NOBUYOSHI
    • C02F1/78C02F3/20G05D21/00G05D21/02
    • PURPOSE:To realize stable plant operation by utilizing unreacted ozone gas in water treatment by providing a valve closing a branch pipe from the atmosphere and a control part controlling an ozone generator so as to make the injection amt. of ozonized gas less than the suction amt. of the gas of an ejector. CONSTITUTION:Ozone supplied from an ozone generator 8 is reacted in an ozone reaction tower 7 to treat raw water to be treated with ozone. Unreacted ozone is supplied to an ejector 3 by the exhaust gas piping 5 connected to the upper part of the tower 7 to be introduced into the raw water. Since a control part 12 performs control so that the injection amt. of ozonized gas is always made less than the suction amt. of the gas of the ejector 3, the supply amt. of the gas to the ejector 3 becomes insufficient but the atmosphere is sucked from the branch pipe 10 of the exhaust gas piping 5 in the amt. corresponding to the insufficient amt. When the suction amt. of the gas of the ejector 3 is lowered because of the abnormality of a raw water pump 1, the unreacted gas is discharged to the atmosphere from the branch pipe 10 but, since the valve 11 closed by the abnormality of the raw water pump 1 is provided to the branch pipe 10, the discharge of unreacted ozone is prevented.
    • 7. 发明专利
    • FLOCCULATING AND SETTLING TANK
    • JPH04305205A
    • 1992-10-28
    • JP6967091
    • 1991-04-02
    • TOSHIBA CORP
    • UMIGA NOBUYOSHI
    • B01D21/08B01D21/00C02F1/52
    • PURPOSE:To remove an obstacle due to algae and to keep safety in working environment maintaining constant brightness even if flocculating and settling is performed without the use of chlorine by installing a green transparent or translucent window or skylight using glass or plastic in a building where a flocculating and settling tank is installed. CONSTITUTION:Raw water is introduced from a conduit tube 1 and a flocculant, a pH conditioner, etc., are added from a chemical tank 2. The mixture is agitating in a rapid agitating tank 4 and then agitated in a slow agitated tank 6 to flocculate turbid components in the raw water as floc which is settled and separated in a settling tank 7 as sludge 8. The whole settling tank 7 is installed within a building 10 and sunlight is taken in through a window 11 from the outside. The window 11 consists of green transparent or translucent glass or plastic and shuts out the light of complementary color of green which is necessary for the growth of plankton in the sunlight.
    • 8. 发明专利
    • PURIFICATION SYSTEM OF GOLF COURSE
    • JPH03275186A
    • 1991-12-05
    • JP7551390
    • 1990-03-27
    • TOSHIBA CORP
    • TAMURA HIROSHIUMIGA NOBUYOSHIOKAWA MASAYUKI
    • C02F1/00
    • PURPOSE:To prevent generation of algae in an appreciation pond and to efficiently purify this appreciation pond by introducing the water of this pond in a golf course and purifying it and thereafter returning the purified water to the appreciation pond and forming the region of the purified water in the prescribed part of the appreciation pond. CONSTITUTION:The purification system of a golf course is constituted by providing a purifier 1 and two valves 2, 3. In this system, the water of an appreciation pond 4 is introduced and also purified and algae are removed. Thereafter, the purified water is reintroduced into the appreciation pond 4 and region 5 of the purified water is formed in one part thereof. Thereby, even when agricultural chemicals of high concn. are introduced, a fish 6 is run into the region 5 of purified water and the fish 6 is prevented from dying by the agricultural chemicals. The purifier 1 is equipped with a sand filter part packed with fine sand and an adsorption part packed with a fine activator.
    • 9. 发明专利
    • OZONIZER
    • JPH03164405A
    • 1991-07-16
    • JP30090289
    • 1989-11-21
    • TOSHIBA CORP
    • HOSHINA FUMIOUMIGA NOBUYOSHI
    • C01B13/11
    • PURPOSE:To remove NOx generated on the inner surface of a discharge tube and to prevent the deterioration of a conductive film by stopping the cooling of an ozonizer by an operation stop command, stopping the discharge of the ozonizer and stopping the supply of raw air based on the detected gas outlet temp. CONSTITUTION:Cooling water is supplied to the discharge tube in the ozonizer 1 when operation is commanded, and the supply of cooling water is stopped by an operation stop command. The temp. of the ozonized air is detected by a temp. sensor 10 provided at the outlet of the ozonizer 1. Discharge is continued until a specified temp. is detected. When the specified temp. is detected, the discharge of the ozonizer 1 is stopped after a fixed time. Raw air is supplied after a fixed time to discharge all the ozonized air. Consequently, the NOX generated on the inner surface of the discharge tube is opportunely removed, and the discharge tube is not broken.
    • 10. 发明专利
    • WATER TREATING DEVICE
    • JPH0326393A
    • 1991-02-04
    • JP16011389
    • 1989-06-22
    • TOSHIBA CORP
    • SHIBATA KATSUHIROTAKAHASHI IKUOUMIGA NOBUYOSHI
    • C02F1/78
    • PURPOSE:To oxidize org. matter having no unsaturated bonds with ozone by providing a pipe for introducing water to be treated, an ozone diffuser pipe, a catalyst diffuser pipe and a mechanism for circulating the catalyst settled on the bottom in an ozone reaction vessel. CONSTITUTION:Water A to be treated is introduced into the ozone reaction vessel 1 through an inlet pipe 2, and an ozone-contg. gas B is injected into the water A as bubbles from the diffuser pipe 5 through an inlet pipe 4. The gas B is subjected to a gas-liq. catalytic reaction with the water A and sent upward to the upper part of the vessel 1, and the ozone is dissolved in the water to oxidize the org. matter in the water. Meanwhile, ferric oxide C as catalyst is uniformly injected into the water A from the diffuser pipe 7 at the upper part and gravitated in the water, and the ozone oxidation reaction is accelerated. The catalyst settled on the bottom of the vessel is returned to the diffuser pipe by a circulating mechanism and effective used.