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    • 3. 发明专利
    • Apparatus and method for treating water
    • 装置和处理水的方法
    • JP2006218361A
    • 2006-08-24
    • JP2005032531
    • 2005-02-09
    • Kurita Water Ind Ltd栗田工業株式会社
    • IMAI KAZUO
    • C02F1/32B01D63/02B01D65/10C02F1/44C02F1/50C02F1/76
    • PROBLEM TO BE SOLVED: To provide an apparatus for treating water capable of supplying safe water while reducing a running cost, and an administrative and maintenance expense.
      SOLUTION: The apparatus for treating water comprising a raw water tank 1, a hollow fiber membrane filter 2, an ultraviolet irradiation device 11 and a chloride agent loading device 15 includes membrane break sensing means 10 at the latter step of the hollow fiber membrane filter 2 and a controller (control means) 12 for changing an ultraviolet irradiation amount of the ultraviolet irradiation device 11 corresponding to the sensed result of the membrane break of the hollow fiber membrane filter 2 by the membrane break sensing means 10. For, example, the controller 12 terminates a drive of the ultraviolet irradiation device 11 when the membrane break is not sensed by the membrane break sensing means 10 and drives the ultraviolet irradiation device 11 when the membrane break is detected.
      COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题:提供一种处理能够提供安全水的水的装置,同时降低运行成本,以及管理和维护费用。 解决方案:包含原水槽1,中空纤维膜过滤器2,紫外线照射装置11和氯化剂装载装置15的处理水的装置包括在中空纤维的后一步骤的膜断裂传感装置10 膜过滤器2和用于通过膜断裂检测装置10改变与中空纤维膜过滤器2的膜破裂的感测结果相对应的紫外线照射装置11的紫外线照射量的控制器(控制装置)12。 当膜断裂检测装置10未检测到膜断裂并且当检测到膜断裂时驱动紫外线照射装置11,控制器12终止紫外线照射装置11的驱动。 版权所有(C)2006,JPO&NCIPI
    • 4. 发明专利
    • Membrane filtration method of organic matter- containing water
    • 含有机含水的膜过滤方法
    • JP2006167582A
    • 2006-06-29
    • JP2004363110
    • 2004-12-15
    • Kurita Water Ind Ltd栗田工業株式会社
    • IMAI KAZUOSAWADA SHIGEKI
    • C02F1/44B01D65/06
    • PROBLEM TO BE SOLVED: To prevent increase of membrane pressure difference and to keep filtration flux density of the membrane stable over a long period in membrane filtration of organic matter-containing water, by suppressing chemical washing frequency and amount of chemical use, and preventing deterioration of the membrane.
      SOLUTION: This membrane filtration method of organic matter-containing water comprises a water-passing process for treating organic matter-containing water by passing the water through a membrane filtration apparatus, and a chemical washing process for washing the membrane of the membrane filtration apparatus. The chemical washing process comprises a first chemical washing process after the water-passing process for a given period (a), and a second chemical washing process using a chemical with different components and/or concentration from that for the first chemical washing. The second chemical washing process is performed when a period b longer than the given period (a) has passed from the previous second washing, or the membrane pressure difference has increased higher than a given value.
      COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题为了防止膜压差的增加,并且通过抑制化学洗涤频率和化学品使用量,通过长期将膜的过滤通量密度长期保持在含有机物的水的膜过滤中, 并防止膜的劣化。 解决方案:含有机物的水的膜过滤方法包括通过使水通过膜过滤装置来处理含有有机物的水的通水方法,以及用于洗涤膜的膜的化学洗涤方法 过滤装置。 化学洗涤方法包括在给定时间段(a)的通水过程之后的第一次化学洗涤过程,以及使用与第一次化学洗涤不同成分和/或浓度的化学品的第二次化学洗涤过程。 当比前一次第二次洗涤时间长于给定时间(a)的时间b或膜压力差已经增加到高于给定值时,进行第二次化学洗涤过程。 版权所有(C)2006,JPO&NCIPI
    • 5. 发明专利
    • Method for washing membrane module
    • 洗涤膜模块的方法
    • JP2005288442A
    • 2005-10-20
    • JP2005199075
    • 2005-07-07
    • Kurita Water Ind Ltd栗田工業株式会社
    • SAWADA SHIGEKITAKEUCHI OSAMUIMAI KAZUO
    • B01D65/06C02F1/44C02F1/52
    • PROBLEM TO BE SOLVED: To provide a method for washing membrane module capable of efficiently washing membrane separation equipment and unnecessitating treatment of washing waste liquid. SOLUTION: Acid and alkali are alternately injected into a membrane module 4 and, thereafter, the injected acid and alkali are respectively drawn out of a raw water chamber 4a. In accordance with water quality of raw water in the membrane separation equipment, alkali washing after acid washing or acid washing after alkali washing is properly selected, at the same time, respective concentrations of chemicals are adjusted to perform washing, thereby, the effective washing can be performed, a high washing effect can be obtained with chemicals of a dilute concentration and the membrane performance can be effectively restored. By using the acid and alkali by an equivalent quantity, waste water disposal of the washing waste liquid is made unnecessary and it is made possible to mix and neutralize acid washing waste liquid and alkali washing waste liquid and discharge the mixed and neutralized waste liquid without providing a separate waste water processing apparatus. Because the injected acid and alkali is drawn out from the raw water chamber side, the contamination of the permeate water chamber side can be prevented. COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题:提供一种能够有效洗涤膜分离设备并且不需要处理洗涤废液的洗涤膜组件的方法。 解决方案:将酸和碱交替地注入膜组件4中,然后将注入的酸和碱分别从原水室4a中抽出。 根据膜分离设备中原水的水质,碱洗后酸洗或酸洗后碱洗,同时调整各浓度的化学品进行洗涤,从而有效洗涤 可以通过稀释浓度的化学品获得高洗涤效果,并且可以有效地恢复膜的性能。 通过使用相当量的酸和碱,不需要废水处理,可以将酸洗废液和碱洗涤废液进行混合和中和,并排出混合和中和的废液,而不提供 单独的废水处理设备。 由于注入的酸和碱从原水室侧被抽出,所以可以防止渗透水室侧的污染。 版权所有(C)2006,JPO&NCIPI
    • 6. 发明专利
    • METHOD FOR CLEANING MEMBRANE
    • JPH1015365A
    • 1998-01-20
    • JP17500996
    • 1996-07-04
    • KURITA WATER IND LTD
    • SAWADA SHIGEKIIMAI KAZUO
    • B01D65/06B01D65/02
    • PROBLEM TO BE SOLVED: To carry out a process in which pollutants adherent to and are deposited on the surface of a membrane are washed out and removed efficiently with a small amount of backwashing water by a method in which when chlorine water is made to backflow through a membrane module from the secondary side of the membrane to the primary side to wash the membrane, after the passage of a prescribed time from the backflow of chlorine water, retained water on the primary side of the membrane is discharged outside a system. SOLUTION: Filtrate which is obtained by passing raw water in a raw water tank 1 through a membrane module 2 from the primary side 2A of the module 2 to the secondary side 2B and passed through a filtrate tank 3 is taken out as treated water. Besides, when the membrane is backwashed, pumps P1, P2 are stopped, valves V1-V3 are closed, and pumps P3, P4 are actuated. In this way, a sodium hypochlorite aqueous solution is injected into the filtrate from the tank 3 to prepare chlorine water, which is made to backflow from the secondary side 2B to the primary side 2A. The primary side 2A is filled with chlorine water, the pumps P3, P4 are stopped, after the elapse of a prescribed length of time, the pump P1 is actuated, the valve V1 is opened, raw water in the tank 1 is introduced to the primary side 2A, and chlorine water is discharged outside a system.
    • 9. 发明专利
    • WATER TREATMENT APPARATUS
    • JPH08117747A
    • 1996-05-14
    • JP25519094
    • 1994-10-20
    • KURITA WATER IND LTD
    • IMAI KAZUOSAWADA SHIGEKITAKEUCHI OSAMU
    • B01D21/30C02F1/44C02F1/52
    • PURPOSE: To control the addition amt. of a flocculant to the optimum amt. while keeping membrane separation capacity high to perform stable treatment by measuring the ultraviolet absorbancy of membrane filtered water from which a suspended substance is removed and performing feedback control on the basis of the measured value of ultraviolet absorbancy. CONSTITUTION: The flocculant in a flocculant storage tank 4 is injected into the raw water of piping 11 from piping 15 equipped with a pump P2. At this time, an ultraviolet absorptiometer 6 measuring the ultraviolet absorbancy of the membrane filtered water discharged from a membrane separation part 3 is provided to piping 14 and the operation of a flocculant injection pump P2 is adjusted on the basis of the measured value of the ultraviolet absorptiometer 6 by a control part 7 to control the injection amt. of the flocculant. The ultraviolet absorptiometer 6 measuring the ultraviolet absorbancy of the membrane filtered water from the membrane separation part 3 measures the ultraviolet absorbancy within a wavelength range of 200-500nm of the membrane filtered water.