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    • 1. 发明专利
    • Liquid treatment apparatus
    • 液体处理设备
    • JP2010063954A
    • 2010-03-25
    • JP2008230400
    • 2008-09-09
    • Hitachi Ltd株式会社日立製作所
    • SUMIKURA MISAKIHIDAKA MASATAKATAKEMOTO TAKESHIWATANABE SHOJIENBUTSU ICHIRONOBUTOMO YOSHIHIROTADOKORO HIDEYUKIHARA NAOKI
    • C02F1/78C02F1/24C02F1/32C02F1/50C02F1/76
    • PROBLEM TO BE SOLVED: To reduce operating cost for the whole processes by separating objects into objects to be removed suitable for an ozone treatment process and objects to be removed suitable for a sterilization process and achieving target water quality by the processes. SOLUTION: A liquid treatment apparatus includes an ozone generator 3 for injecting ozone gas which reacts with water to be treated in an ozone contact tank 2, a colorimeter 8 in a passage connected to the ozone contact tank 2, a chlorine injector 11 for injecting a chlorine agent into an ultraviolet irradiation tank 6 equipped with an ultraviolet lamp and connected to the passage or into the passage, and an input means 10 for performing input into a controller 9 controlling the ozone generator 3, the ultraviolet lamp, or the chlorine injector 11. The output of the ozone generator 3 is controlled from a deviation between the target value of a first water quality item from the input means 10 and a value of the first water quality item measured by a water quality measuring meter. The output of the ultraviolet lamp or the injection rate of the chlorine agent of the chlorine injector 11 is controlled from the target value of a second water quality item from the input means 10 by a relationship between the first water quality item and ultraviolet irradiation or a relationship between the first water quality item and the injection rate of the chlorine agent. COPYRIGHT: (C)2010,JPO&INPIT
    • 要解决的问题:通过将物体分离成适合于臭氧处理过程的待去除物体和适于灭菌过程的待去除物体并通过该过程实现目标水质来降低整个过程的操作成本。 解决方案:液体处理装置包括臭氧发生器3,其用于在臭氧接触罐2中喷射与待处理的水反应的臭氧气体,连接到臭氧接触罐2的通道中的色度计8,氯喷射器11 用于将氯剂注入装有紫外线灯并连接到通道或通道的紫外线照射罐6中,以及输入装置10,用于输入到控制臭氧发生器3,紫外线灯或 氯喷射器11.臭氧发生器3的输出由来自输入装置10的第一水质物品的目标值与由水质量测量计测量的第一水质物品的值之间的偏差控制。 通过第一水质项目和紫外线照射之间的关系,从输入装置10的第二水质项目的目标值控制氯注射器11的氯剂的输出或氯气喷射量的输出,或 第一个水质项目与氯剂的喷射率之间的关系。 版权所有(C)2010,JPO&INPIT
    • 2. 发明专利
    • Water treatment device
    • 水处理设备
    • JP2009233622A
    • 2009-10-15
    • JP2008085588
    • 2008-03-28
    • Hitachi Ltd株式会社日立製作所
    • YAMANOI ICHIROENBUTSU ICHIROKAGEYAMA KOJIHARA NAOKIWATANABE SHOJITAKEMOTO TAKESHI
    • B01D65/08B01D65/02C02F1/44C02F3/12
    • Y02W10/15
    • PROBLEM TO BE SOLVED: To suppress the formation of an instable main stream part by minute turbulence to obtain an excellent cleaning effect of a membrane element. SOLUTION: In a biological treatment tank 1 filled with an active sludge mixture liquid 11, a membrane unit 2 composed of a plurality of membrane elements 21 having a filtration action is immersed, and an aeration tube 4 is provided below it. Air supplied from an aeration blower 5 is discharged as bubbles 12 from the aeration tube 4, and the discharged bubbles 12 form an elevating flow, pass through a flow speed adjuster 3 and flow into the inter-membrane flow path 22 of the membrane unit 2. A recessed part in an inverse chevron shape or a chevron shape is provided on the upper side or lower side of the flow speed adjuster 3, and the flow path resistance of a center part is small. Thus, a flow speed at the center part of the inter-membrane flow path 22 becomes high, and a stable main stream part is formed at the center part of the inter-membrane flow path 22. Since the bubbles 12 of the stable main stream part act on the membrane elements 21, the deposition of active sludge is prevented, and the formation of the instable main stream part is suppressed. COPYRIGHT: (C)2010,JPO&INPIT
    • 要解决的问题:为了通过微小的湍流抑制不稳定主流部分的形成,以获得优异的膜元件清洁效果。 解决方案:在填充有活性污泥混合液11的生物处理槽1中,浸渍由具有过滤作用的多个膜元件21构成的膜单元2,在其下方设置曝气管4。 从曝气鼓风机5供给的空气从曝气管4排出为气泡12,排出的气泡12形成升降流,通过流量调节器3流入膜单元2的膜间流路22 在流速调节器3的上侧或下侧设置有倒V形或V形形状的凹部,中心部的流路阻力小。 因此,膜间流路22的中央部的流速变高,在膜间流路22的中心部形成稳定的主流部。由于稳定主流的气泡12 部分作用在膜元件21上,防止了活性污泥的沉积,并且抑制了不稳定主流部分的形成。 版权所有(C)2010,JPO&INPIT
    • 3. 发明专利
    • Operation method of water purification membrane filtration system
    • 水净化膜过滤系统的运行方法
    • JP2009195893A
    • 2009-09-03
    • JP2008180861
    • 2008-07-11
    • Hitachi Ltd株式会社日立製作所
    • TAKEMOTO TAKESHIKAGEYAMA KOJIWATANABE SHOJIHARA NAOKI
    • C02F1/44B01D65/02
    • PROBLEM TO BE SOLVED: To provide an operation method of a water purification membrane filtration system which can optimize the operating condition of the membrane filtration system proper according to raw water and the operating state of the membrane filtration system, and enables easy grasping of the operating state of the membrane filtration system.
      SOLUTION: In the operation method of a water purification membrane filtration system which comprises the membrane filtration means including a plurality of membrane modules for filtering raw water, and the membrane filtration control means 8 controlling a filtration time, a filtration flow rate, the backwashing time, and a backwashing flow rate of the membrane modules, and sequentially backwashes the membrane modules, the lower limit of the filtration time is defined as the product of the number of the membrane modules in operation and the backwashing time.
      COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:提供一种水净化膜过滤系统的操作方法,其可以根据原水和膜过滤系统的操作状态优化膜过滤系统的工作状态,并且能够容易地抓握 的膜过滤系统的运行状态。 解决方案:在水净化膜过滤系统的操作方法中,其包括膜过滤装置,该膜过滤装置包括用于过滤原水的多个膜组件,以及膜过滤控制装置8,其控制过滤时间,过滤流速, 反冲洗时间和膜组件的反冲洗流量,顺序地反洗膜组件,将过滤时间的下限定义为操作中的膜组件的数量与反冲洗时间的乘积。 版权所有(C)2009,JPO&INPIT
    • 4. 发明专利
    • Operation method of water purification membrane filtration system
    • 水净化膜过滤系统的运行方法
    • JP2009195818A
    • 2009-09-03
    • JP2008039500
    • 2008-02-21
    • Hitachi Ltd株式会社日立製作所
    • TAKEMOTO TAKESHIKAGEYAMA KOJIWATANABE SHOJIHARA NAOKI
    • C02F1/44B01D65/02
    • PROBLEM TO BE SOLVED: To provide an operation method of a water purification membrane filtration system which can optimize the operating condition of the membrane filtration system proper according to raw water and the operating state of the membrane filtration system, and enables easy grasping of the operating state of the membrane filtration system.
      SOLUTION: A membrane filtration control means 8 sets a filtration time from a raw water turbidity 1 measured by a raw water quality measuring meter 5 and a measured value of a transmembrane pressure difference measured by a primary side pressure measuring means 6 and a secondary side pressure measuring means 7 from a preset relation of the transmembrane pressure difference and a filtration time for each raw water turbidity, displays the relation of the transmembrane pressure difference and the filtration time for each raw water turbidity on a display means 9, and plots the present value and the past values of the filtration time.
      COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:提供一种水净化膜过滤系统的操作方法,其可以根据原水和膜过滤系统的操作状态优化膜过滤系统的工作状态,并且能够容易地抓握 的膜过滤系统的运行状态。 解决方案:膜过滤控制装置8设定由原水质量测量仪5测量的原水浊度1和通过初级侧压力测量装置6测量的跨膜压差的测量值和 将二次侧压力测量装置7从跨膜压差的预设关系和每个原水浊度的过滤时间显示出来,显示装置9上的每个原水浊度的跨膜压力差和过滤时间的关系,以及图 过滤时间的当前值和过去值。 版权所有(C)2009,JPO&INPIT
    • 5. 发明专利
    • Solid-liquid separation treatment apparatus and solid-liquid separation treatment system
    • 固液分离处理装置和固液分离处理系统
    • JP2009018237A
    • 2009-01-29
    • JP2007181621
    • 2007-07-11
    • Hitachi Ltd株式会社日立製作所
    • KAGEYAMA KOJIWATANABE SHOJITAKEMOTO TAKESHIHARA NAOKI
    • C02F1/44B01D63/08B01D65/08C02F3/08C02F3/10C02F3/12
    • Y02W10/15
    • PROBLEM TO BE SOLVED: To provide a solid-liquid separation treatment apparatus which effectively peels the adherend on the surface of a membrane to suppress a fall in the flux density of a membrane filtering speed or a rise in membrane difference pressure and reducing the work labor such as lifting labor or the like required when the membrane is washed with chemicals or replaced, and a solid-liquid separation treatment system. SOLUTION: The solid-liquid separation treatment apparatus is equipped with a casing 12 having an inflow port 20 of water to be treated, an outflow port 10 of concentrated water and an outflow port 14 of filtered water, an ascending flow producing part for converting the inflow water to be treated to an ascending flow in the casing 12, flat membrane modules 24 arranged so as to allow the ascending flow to flow through the gap between the flat membrane modules 24, sedimentary carriers 18 sealed in the casing 12, smaller than the distance between the membrane modules 24 and having a specific gravity of 1.2-3.0 and a sedimentation flow channel 28 for sedimenting the sendimentary carriers 18 rising the gap between the flat membrane modules 24 by the ascending flow. COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:提供一种固体分离处理装置,其有效地将膜的表面上的被粘物剥离,以抑制膜过滤速度的通量密度的下降或膜差压的上升,并降低 当用化学品或更换膜洗涤膜时所需的劳动力等劳动力等,以及固液分离处理系统。 解决方案:固液分离处理装置配备有具有被处理水的流入口20,浓缩水的流出口10和过滤水的流出口14的壳体12,上升流产生部 为了将待处理的流入水转换成壳体12中的上升流,平面膜组件24被布置成允许上升流动通过平膜组件24之间的间隙,密封在壳体12中的沉积载体18, 小于膜模块24之间的距离并且具有1.2-3.0的比重,以及沉降流路28,用于沉积通过上升流动使平板组件24之间的间隙上升的缓冲载体18。 版权所有(C)2009,JPO&INPIT
    • 6. 发明专利
    • Fine-particulate detector and fine-particulate detection method
    • 微分检测器和微细检测方法
    • JP2009014740A
    • 2009-01-22
    • JP2008257035
    • 2008-10-02
    • Hitachi Ltd株式会社日立製作所
    • MICHIGUCHI YOSHIHIROTAKEMOTO TAKESHIENBUTSU ICHIROKAGEYAMA KOJIWATANABE SHOJITADOKORO HIDEYUKI
    • G01N15/14
    • PROBLEM TO BE SOLVED: To provide a fine-particulate detector and a fine-particulate detection method, capable of reducing a detector cost while securing detection sensitivity of a fine particulate in a specimen.
      SOLUTION: This fine-particulate detector for detecting the fine particulate in the specimen by detecting fluctuation of a detection light intensity generated by a light shielding, diffraction or interference effect of an inspection light due to the fine particulate crossing a detection area within an irradiation area irradiated with the inspection light is provided with a light emitting element 12 for emitting the inspection light to the specimen, a photoreception element 14 for receiving the inspection light getting incident transmitted through the specimen, a porous plate 17 having a light transmission hole 17-1 provided between the specimen and the photoreception element 14 to contract the detection area, and a signal processor 16 for detecting the fine particulate in the specimen by detecting fluctuation of the detection light intensity generated by the light shielding, diffraction or interference effect of the inspection light due to the fine particulate moving in the detection area, based on a signal from the photoreception element 14.
      COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:提供一种细小颗粒检测器和微粒检测方法,其能够在确保样品中微粒的检测灵敏度的同时降低检测器成本。 解决方案:该微粒检测器用于通过检测由于穿过检测区域的细颗粒而导致的检查光的遮光,衍射或干涉效应产生的检测光强度的波动来检测样品中的细颗粒 用检查光照射的照射区域设置有用于向检体发射检查光的发光元件12,用于接收通过检体透射的检查光的光接收元件14,具有透光孔的多孔板17 17-1设置在样本和光接收元件14之间以收缩检测区域;以及信号处理器16,用于通过检测由遮光,衍射或干涉效应产生的检测光强度的波动来检测样本中的细颗粒 检测光由于微粒在检测中移动 区域,基于来自光接收元件14的信号。版权所有(C)2009,JPO&INPIT
    • 7. 发明专利
    • Method for detecting damage in membrane, and membrane filter device
    • 用于检测膜损伤的方法和膜过滤装置
    • JP2008296087A
    • 2008-12-11
    • JP2007142030
    • 2007-05-29
    • Hitachi Ltd株式会社日立製作所
    • WATANABE SHOJITAKEMOTO TAKESHIKAGEYAMA KOJIENBUTSU ICHIROMICHIGUCHI YOSHIHIROHARA NAOKI
    • B01D65/10C02F1/44G01N15/06G01N15/08
    • PROBLEM TO BE SOLVED: To provide a highly accurate method of detecting damage in a membrane at a low cost with improved detection sensitivity, and to provide a membrane filter device. SOLUTION: The method of detecting damage in a membrane for use in a membrane filter device constituted of a raw water supply means 20 for supplying raw water, a membrane filter means for obtaining filtrate water from raw water supplied thereto, and a back-washing water supply means 40 for supplying the membrane filter means with a portion of filtered water as water for back-washing is characterized by comprising the process of preparing microbubble-containing water as a source of suspended matters by injecting a gas into a liquid flow path to admix the gas with a liquid flowing into the raw water supply means 20 or into the back-washing water supply means 40 via the liquid flow path, the process of measuring the state of the suspended matters in effluent discharged out of the membrane filter means from the microbubble-containing water supplied thereto via the liquid supply path, and the process of detecting a presence or an absence of damage in the membrane filter means from the above measured value. COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:提供以更低的检测灵敏度以低成本检测膜中的损伤的高精度方法,并提供膜过滤装置。 检测用于由用于供给原水的原水供给装置20构成的膜过滤装置中的膜的损伤的方法,从供给原料的水中得到滤液的膜过滤装置和背面 用于向膜过滤装置供给过滤水的一部分作为反洗用水的洗涤水供给装置40的特征在于包括通过将气体注入液体流中来制备含微泡水的水作为悬浮物质源的方法 通过液体流路将气体与流入原水供给装置20的液体或回洗水供给装置40混合的流路,测定从膜过滤器排出的流出物中的悬浮物的状态的处理 来自通过液体供给路供给到其中的含微泡水的装置,以及从上述的膜过滤装置中检测有无损伤的处理 ve测量值。 版权所有(C)2009,JPO&INPIT
    • 9. 发明专利
    • Membrane filtration apparatus and membrane module contamination detecting method
    • 膜过滤装置和膜模块污染检测方法
    • JP2007136300A
    • 2007-06-07
    • JP2005331676
    • 2005-11-16
    • Hitachi Ltd株式会社日立製作所
    • IMAI MIKIHARA NAOKIKAGEYAMA KOJIWATANABE SHOJI
    • B01D65/10B01D65/02C02F1/44G01N33/18
    • PROBLEM TO BE SOLVED: To surely detect trace of contaminant attached to a membrane module at an early stage.
      SOLUTION: The membrane filtration apparatus comprising multiple external pressure type membrane modules removing contaminants in supplied raw water and a bubble supply means supplying bubbles to the raw water supply side of the external pressure type membrane modules, is provided with a bubble floating-up means provided connectedly to the raw water outlet side of the membrane module and floating up bubbles flowing in together with the raw water; a contaminant measuring means measuring contaminants floating up to the water surface by the bubble floating-up means; a contamination determining means determining the contamination degree of the membrane module based on the measured values outputted from the contaminant measuring means; and an output means displaying the determination results.
      COPYRIGHT: (C)2007,JPO&INPIT
    • 要解决的问题:在早期阶段确实检测附着在膜组件上的污染物。 解决方案:包括多个外部压力型膜组件的膜过滤装置,其将所供给的原水中的污染物除去,以及向外部压力型膜组件的原水供给侧供给气泡的气泡供给装置, 连接到膜组件的原水出口侧的浮起装置,浮起与原水一起流动的气泡; 污染物测量装置测量通过气泡浮起装置漂浮到水面的污染物; 污染确定装置,根据从污染物测量装置输出的测量值,确定膜组件的污染程度; 以及显示确定结果的输出装置。 版权所有(C)2007,JPO&INPIT
    • 10. 发明专利
    • Method and apparatus for injecting flocculant in water clarifying process
    • 用于注射水中澄清过程的方法和装置
    • JP2007098236A
    • 2007-04-19
    • JP2005289496
    • 2005-10-03
    • Hitachi Ltd株式会社日立製作所
    • WATANABE SHOJIENBUTSU ICHIROHAGA TETSUROKAGEYAMA KOJITAKEMOTO TAKESHIHARA NAOKI
    • C02F1/52B01D21/01B01D21/30
    • PROBLEM TO BE SOLVED: To provide a method and an apparatus for injecting a flocculant in a water clarifying process by which the flocculant can be properly injected even in high turbidity raw water and good flocculation precipitation treatment liquid can be stably maintained. SOLUTION: Two kinds of quantities of suspensoid in raw water, turbidity and suspensoid concentration, and particle size distribution of the suspensoid are measured and property coefficients and average or medium particle size of the suspensoid are obtained from these measured values. From pattern information on measured particle size distribution, a relational formula between two kinds of property coefficients input in advance or suspensoid particle size and flocculant injection coefficient per unit suspensoid quantity is selected. By using the selected relational formula, the flocculant injection coefficient per unit suspensoid quantity corresponding to property coefficient arithmetic value or suspensoid particle size arithmetic value is calculated. By using the flocculant injection coefficient and the suspensoid quantity, a flocculant injection ratio per unit volume is obtained and flocculant injection quantity corresponding to a raw water flow rate is operated. COPYRIGHT: (C)2007,JPO&INPIT
    • 要解决的问题:提供一种在絮凝剂注入絮凝剂的方法和装置中,即使在高浊度原水中也可以适当地注入絮凝剂,并且可以稳定地保持良好的絮凝沉淀处理液。

      解决方案:测量原水中的两种悬浮液,浊度和悬浮液浓度,以及悬浮液的粒径分布,并从这些测量值获得悬浮体的性能系数和平均或中等粒径。 从测量粒度分布的模式信息中,选择预先输入的两种属性系数或悬浮粒度和每单位悬浮液量的絮凝剂注入系数之间的关系式。 通过使用选定的关系式,计算与属性系数算术值或悬浮粒度算术值对应的每单位悬浮液量的絮凝剂注入系数。 通过使用絮凝剂注入系数和悬浮液量,获得每单位体积的絮凝剂注入量,并且操作对应于原水流量的絮凝剂注入量。 版权所有(C)2007,JPO&INPIT