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    • 23. 发明专利
    • INTERMITTENT AERATION TYPE ACTIVATED SLUDGE TREATMENT APPARATUS
    • JPH11226594A
    • 1999-08-24
    • JP3334898
    • 1998-02-16
    • KURITA WATER IND LTD
    • HORI AKISHIMURAKAMI TAKAFUMI
    • C02F1/44C02F3/34
    • PROBLEM TO BE SOLVED: To obtain an intermittent aeration type activated sludge treatment apparatus wherein a liq. to be treated contg. high concn. nitrogen is treated at high load by using an intermittent aeration tank with a small vol. and a treated liq. with high water quality can be obtd. by elevating nitrogen removing rate. SOLUTION: A liq. to be treated is continuously fed into an intermittent aeration tank and aeration is intermittently performed in the presence of activated sludge to repeat an aerobic process and an anaerobic process and in the aerobic process, removal of BOD and nitrification of nitrogen are performed and in the anaerobic process, denitrification is performed and the denitrification treated liq. is introduced into a finishing nitrification tank 2 with a vol. of 0.3-2 times in vol. of the effluent in the anaerobic process in the intermittent aeration tank to perform finishing nitrification and finishing denitrification is performed in a finishing denitrification tank 3 with a vol. of 0.3-2 times in vol. of the effluent in one cycle of the aerobic process and the anaerobic process in the intermittent aeration tank and solid-liq. separation is performed in a membrane separation device 5 in a solid-liq. separation tank 4 and conc. sludge with 2-7 times in vol. of the treated liq. is returned to the intermittent aeration tank.
    • 24. 发明专利
    • TREATING DEVICE FOR LEACHED WATER FROM RECLAMATION
    • JPH10137779A
    • 1998-05-26
    • JP30214996
    • 1996-11-13
    • KURITA WATER IND LTD
    • HORI AKISHIMURAKAMI TAKAFUMI
    • C02F3/12C02F1/44
    • PROBLEM TO BE SOLVED: To improve treated water quality and also to enable a highly loaded operation by arranging a flocculating and separating device at the upstream side of an aeration tank. SOLUTION: The flocculating and separating device C consisting of a mixing tank C1 having an agitating means 1i and a liq. chemical feed means 1j, a similar flocculating tank C2 and a flocculating and settling tank C3 is disposed at the upstream side of a membrane separation type activated sludge treating device A having the aeration tank A1 . A settled sludge at the flocculating and settling tank C3 is returned to the mixing tank C1 with a piping P2 . An SS component in a raw water W1 is flocculated and removed, and an SS concn. is reduced till an order of about 20mg/L. An accumulation of the SS component at the post stage aeration tank A1 is prevented by attaining this residual SS concn. A floculant such as aluminum sulfate and a pH adjusting agent such as sodium hydroxide are used at the mixing tank C1 of the flocculating and separating device C. A high-molecular floculant such as nonionic floculant is used at the flocculating tank C2 . In this way, the SS concn. is reduced and BOD components are removed sufficiently.
    • 26. 发明专利
    • WATER TREATMENT
    • JPH01304096A
    • 1989-12-07
    • JP13634788
    • 1988-06-02
    • KURITA WATER IND LTD
    • MURAKAMI TAKAFUMI
    • C02F1/58
    • PURPOSE:To effectively prevent the generation of scales, by removing calcium from the filtrate resulting from solid-liquid separation after the addition of calcium compound to the water to be treated and sending at least a portion of the treated water back to the addition process for the calcium compound. CONSTITUTION:The method of treating the water containing fluoride ion and sulfate ion such as the waste water resulting from flue gas desulfurization comprises the steps of adding thereto calcium compound such as calcium hydroxide, adjusting the pH to cause a predipitate as required, obtaining filtrate by conventionally effecting solid-liquid separation, removing the precipitate from the water treating device, supplying a carbon dioxide containing gas to at least a portion of the filtrate for calcium removal therefrom and returning at least a portion of the filtrate resulting from the solid-liquid separation to the addition process for the aforesaid calcium compound. This method is effective in preventing the generation of scales.
    • 27. 发明专利
    • METHOD FOR BIOLOGICAL-REMOVEMENT OF NITROGEN
    • JPS62234596A
    • 1987-10-14
    • JP7789086
    • 1986-04-04
    • KURITA WATER IND LTD
    • TAKADOI TADASHIMURAKAMI TAKAFUMI
    • C02F3/28C02F3/34
    • PURPOSE:To enable stable denitriding treatment and also to simplify driving operation by detecting nitrogen removing velocity in a denitriding treatment tank and regulating amount of nitrogen load to be introduced into the denitriding treatment tank. CONSTITUTION:Pipelines 17, 18 for taking out liquid which are respectively provided with pumps 15, 16 are connected to a nitration tank 1 and a denitriding tank 2, and both nitrated liquid and denitrified liquid are respectively fed to a nitration velocity measuring device 19 and a denitriding velocity measuring device 20. The detection signals output from these devices 19, 20 are introduced into a controller 21 via signal lines 19a, 20a. The controller 21 treats these detection signals, and outputs a signal controlling amount of raw water to be introduced into a denitriding treatment tank A to a valve 5a via a signal line 21a. In other words, operation is performed in nitrogen load within the range of treatment capacity of microorganism and stable denitriding treatment can be performed even if the fluctuation of nitrogen load is caused. Further complicated driving operation for corresponding to the load fluctuation is not necessitated and the driving operation can be simplified.
    • 28. 发明专利
    • METHOD FOR TREATING BORON-CONTAINING WATER
    • JPS62121689A
    • 1987-06-02
    • JP25938785
    • 1985-11-19
    • KURITA WATER IND LTD
    • ETO YOSHIHIROITO YUKIOMURAKAMI TAKAFUMI
    • C02F1/04B01D11/04C02F1/26C02F1/42
    • PURPOSE:To efficiently remove boron, by a method wherein boron-containing water is treated by contact with an anion exchange resin and the used anion exchange resin is contacted with an acid to be regenerated while the waste liquid after regeneration is contacted with an extractant to extract boron. CONSTITUTION:Boron-containing water is supplied to an ion exchange tower 1 from a piping 11 to be treated by contact with an anion exchange resin and treated water is discharged out of the system from piping 12. At a stage wherein the anion exchange resin in the ion exchange tower 1 is saturated with boron, the supply of raw water is stopped and a regeneration liquid is passed through the anion exchange resin to elute boron exchanged and adsorbed by said resin. The waste liquid after regeneration is supplied into an extraction tower 2 from a piping 14 and contacted with an extractant to extract and remove boron. The extractant after the extraction of boron is treated with a counter extractant. The residual extractant is drawn out from a piping 15 to be reutilized. By this method, the effective utilization of a boron compound can be attained.
    • 30. 发明专利
    • Treatment method of copper-containing solution
    • 含铜溶液的处理方法
    • JP2006122817A
    • 2006-05-18
    • JP2004314615
    • 2004-10-28
    • Kurita Water Ind Ltd栗田工業株式会社
    • MURAKAMI TAKAFUMIKATO ISAMU
    • C02F1/62C02F1/52
    • PROBLEM TO BE SOLVED: To provide a treatment method of a copper-containing solution capable of removing copper from a copper-containing solution in a high removal ratio to obtain a treated liquid low in the concentration of copper, capable of obtaining dehydrated sludge high in the concentration of formed sludge, having good dehydration properties and a high sludge dehydration speed and low content of a cake even if the concentration of sulfate ions is high and capable of reducing the production amount of sludge, and a treatment apparatus therefor.
      SOLUTION: The copper-containing solution L1 is introduced into a first reaction tank 1 and mixture sludge L8 of alkali and return sludge is supplied to the reaction tank 1 to react with the copper-containing solution L1 at a pH of 6-7.5 while the reaction liquid of the first reaction tank 1 is introduced into a second reaction tank 2 and adjusted to a pH of 8-11 to further react with the copper-containing solution L1. The reaction liquid of the second reaction tank 2 is introduced into a flocculation tank 3 to be flocculated and the flocculated treated liquid is subjected to solid-liquid separation treatment in a solid-liquid separation tank 4 and a part L11 of the separated sludge is returned to a mixer 5 to be mixed with alkali L6 while the obtained alkali mixed sludge L8 is supplied to the first reaction tank 1.
      COPYRIGHT: (C)2006,JPO&NCIPI
    • 解决方案:提供一种能够以高脱除率从含铜溶液中除去铜的含铜溶液的处理方法,得到铜浓度低的处理液,能够得到脱水 即使硫酸根离子的浓度高,能够降低污泥的产生量,也可以具有良好的脱水性,污泥脱水速度快,滤饼含量低的污泥及其处理装置。 解决方案:将含铜溶液L1引入第一反应槽1中,将碱和返回污泥的混合污泥L8供给到反应罐1中,使其与含铜溶液L1反应,pH为6- 7.5,同时将第一反应槽1的反应液引入第二反应槽2中并调节至pH8-11,以进一步与含铜溶液L1反应。 将第二反应槽2的反应液引入絮凝槽3中进行絮凝,将固体分离槽4中的絮凝处理液进行固液分离处理,返回分离后的污泥的部分L11 将混合物5与碱L6混合,同时将所得的碱性混合污泥L8供给到第一反应槽1.版权所有(C)2006,JPO&NCIPI