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    • 31. 发明专利
    • Treatment method and treatment apparatus of water containing calcium and magnesium
    • 包含钙和镁的处理方法和处理装置
    • JP2013202582A
    • 2013-10-07
    • JP2012077251
    • 2012-03-29
    • Kurita Water Ind Ltd栗田工業株式会社
    • NAKAHARA TOSHIJIASADA HIROYUKI
    • C02F1/58B01D61/14C02F1/44C02F5/00C02F5/02
    • PROBLEM TO BE SOLVED: To obtain treated water of high water quality at high level by removing calcium and magnesium in wastewater forming scale components in post processes by using a relatively simple device without requiring any coagulation treatment with polymers.SOLUTION: Carbonate group is added to water containing calcium and magnesium to deposit calcium carbonate and magnesium hydroxide under the alkaline condition of ≥pH 11, and reaction liquid containing deposits is subjected to solid-liquid separation by an MF membrane separator. Condensed water of the MF membrane separator is circulated to the raw water side. Treated water of high water quality of SS concentration of ≤10 mg/L can be consistently obtained by performing the solid-liquid separation by the MF membrane without performing any coagulation treatment with polymers. By modifying deposited sludge by circulating the condensed water from the MF membrane separator, sludge of high concentration can be obtained, the treatment efficiency of discharged sludge can be improved, and the sludge treatment cost can be reduced.
    • 要解决的问题:通过使用相对简单的装置在聚酰胺中进行任何凝固处理,通过在后处理中除去废水形成垢成分中的钙和镁来获得高水质的处理水。解决方案:将碳酸盐基团加入 含有钙和镁的水在≥pH11的碱性条件下沉积碳酸钙和氢氧化镁,并且通过MF膜分离器将含有沉淀物的反应液体进行固液分离。 MF膜分离器的冷凝水循环到原水侧。 通过在不进行聚合物凝固处理的情况下,通过MF膜进行固液分离,可以一致地获得SS浓度≤10mg/ L的高水质处理水。 通过从MF膜分离器循环冷凝水来改性沉积污泥,可以获得高浓度的污泥,可以提高排污污泥的处理效率,降低污泥处理成本。
    • 33. 发明专利
    • Turbine facility, and water treatment method of heater drain water from turbine facility
    • 涡轮机设备的加热器水和水处理方法
    • JP2008025922A
    • 2008-02-07
    • JP2006199600
    • 2006-07-21
    • Kurita Water Ind LtdMitsubishi Heavy Ind Ltd三菱重工業株式会社栗田工業株式会社
    • MOTAI KENJITSUBAKISAKI SENICHIMIYAZAWA NORIYUKIASADA HIROYUKITSURUMI TAKESHIKONAGAI FUMIONAKAHARA TOSHIJI
    • F22B37/54B01D36/02C02F1/44F22D11/00
    • PROBLEM TO BE SOLVED: To provide a turbine facility and a water treatment method of heat drain water from the turbine facility, capable of reducing an iron concentration of a condensate supplied to a boiler to a reference value or smaller in a short time.
      SOLUTION: The turbine facility 10 comprises a boiler 118, a steam turbine 12, a condenser 106, a water supply system A for supplying water 107 to the boiler 118 side, and a low-pressure water heater 109 for heating the water 107. The turbine facility further comprises a low-pressure heater drain tank 116 for storing heater drain water 117; a filter device 15 for filtering an iron content in the heater drain water 117; a flow passage switching part 16 for discharging the heater drain water 117 out of the system when the iron content in the hater drain water 117 has a predetermined value or larger, and supplying the heat drain water 117 to the filter device 15 when the iron content therein is smaller than the predetermined value; and an iron concentration measurement part 17 for measuring the iron content in the heater drain water 117.
      COPYRIGHT: (C)2008,JPO&INPIT
    • 要解决的问题:为了提供来自涡轮机设备的排热水的涡轮机设备和水处理方法,能够将供应给锅炉的冷凝物的铁浓度在短时间内降低到参考值或更小 。 解决方案:涡轮机设备10包括锅炉118,蒸汽轮机12,冷凝器106,用于向锅炉118侧供水107的供水系统A和用于加热水的低压热水器109 涡轮机设备还包括用于存储加热器排水117的低压加热器排放罐116; 用于过滤加热器排水117中的铁含量的过滤装置15; 当加热器排水117中的铁含量具有预定值或更大值时,用于将加热器排水117排出系统的流路切换部分16,并且当铁含量 其中小于预定值; 以及用于测量加热器排水117中铁含量的铁浓度测量部件17。版权所有(C)2008,JPO&INPIT
    • 35. 发明专利
    • Boron-containing water treatment method
    • 含硼含水处理方法
    • JP2005329281A
    • 2005-12-02
    • JP2004147626
    • 2004-05-18
    • Kurita Water Ind Ltd栗田工業株式会社
    • ASADA HIROYUKITAKABAYASHI YASUHIKO
    • C02F1/52C02F1/28
    • PROBLEM TO BE SOLVED: To provide a boron-containing water treatment method by which boron in boron-containing water containing phosphorous and/or silica is removed by being adsorbed in a granulated body on which hydrated oxide of rare earth element is deposited, in a stable and efficient manner by preventing reduction in the boron adsorbing properties of the granulated body.
      SOLUTION: The boron-containing water treatment method is characterized in that when the boron-containing water containing phosphorous and/or silica is brought into contact with the granulated body on which the hydrated oxide of rare earth element is deposited and the boron is removed by being adsorbed in the granulated body, phosphorous and/or silica in the boron-containing water is removed beforehand, and the water is then brought into contact with the granulated body. By removing phosphorous and/or silica beforehand, the reduction in the boron adsorbing properties of the granulated body caused by phosphorous and/or silica can be securely prevented.
      COPYRIGHT: (C)2006,JPO&NCIPI
    • 待解决的问题:提供一种含硼水处理方法,其中通过吸附含有磷和/或二氧化硅的含硼水中的硼被吸附在稀土元素的水合氧化物沉积的粒状体中而被除去 通过防止粒状体的硼吸附性能的降低而稳定而有效地进行。 解决方案:含硼水处理方法的特征在于,当含有磷和/或二氧化硅的含硼水与沉积稀土元素的水合氧化物的颗粒体接触时,硼 通过吸附在造粒体中除去,预先除去含硼水中的磷和/或二氧化硅,然后与造粒体接触。 通过事先去除磷和/或二氧化硅,可以可靠地防止由磷和/或二氧化硅引起的造粒体的硼吸附性能的降低。 版权所有(C)2006,JPO&NCIPI
    • 37. 发明专利
    • BORON-CONTAINING WATER TREATMENT METHOD
    • JP2002346574A
    • 2002-12-03
    • JP2001153685
    • 2001-05-23
    • KURITA WATER IND LTD
    • SATO TAKESHIETO YOSHIHIROASADA HIROYUKI
    • C02F1/58
    • PROBLEM TO BE SOLVED: To provide a boron-containing water treatment method capable of efficiently removing boron in a high removal ratio by using a reduced amount of a chemical agent and reducing the generation amount of sludge. SOLUTION: Raw water 11 is introduced into an aluminum adding tank 1, and an aluminum compound 12, a pH control agent 13, or the like, are added to the raw water 11 to adjust the pH thereof to 8 or more and this raw water is held for 2 min or more while stirred by a stirrer 14. This aluminum compound 2-added water 15 is introduced into a reaction tank 2, and a calcium compound 16, a pH control agent 17, or the like, are injected in the aluminum compound-added water 15 to adjust the pH thereof to 9 or more and reacted with the aluminum compound-added water 15 while stirred and mixed by a stirrer 18 to form an insoluble precipitate. The reaction liquid 21 is sent to a solid-liquid separation tank 3 and, if necessary, a flocculant 22 such as a polymeric flocculant is added to the reaction liquid to form flocs at this time and the reaction liquid is allowed to stand in the slid-liquid separation tank 3 to be subjected to solid-liquid separation. The separated liquid separated in the solid-liquid separation tank 3 is discharged as treated water 23. The separated sludge 24 is introduced into a neutralization tank 4 in a neutralization process and neutralized with an acid 26 to be discharged as waste sludge 27.
    • 39. 发明专利
    • TREATMENT OF BORON-CONTAINING WATER
    • JPH11169864A
    • 1999-06-29
    • JP33912297
    • 1997-12-09
    • KURITA WATER IND LTD
    • ETO YOSHIHIROASADA HIROYUKI
    • C02F1/42B01J47/02B01J49/00C02F1/04C02F1/58C02F9/00
    • PROBLEM TO BE SOLVED: To obtain a high quality treated water by separating a boron-containing water into a condensed water and a concentrated material by evaporation concentration, bringing the condensed water into contact with an ion exchange resin to remove boron and returning a regeneration waste liquid generated by the regeneration of the ion exchange resin to an evaporation concentration process to efficiently remove boron. SOLUTION: The raw water from a raw water passage 5 and the regenerated waste liquid from a waste liquid supply passage 6 are introduced into an adjusting vessel 1, mixed with a stirrer 7 and adjusted pH to >= neutral by injecting a pH adjuster from a chemical injection passage 8. The mixed liquid in the adjusting vessel 1 is introduced into an evaporation condensation device 2, the condensed water is obtained by condensing the vapor and is sent to an ion exchange resin vessel 3. The ion exchange resin vessel 3 has a resin layer 12, boron is exchanged and adsorbed to be removed by passing the condensed water through the resin 12 in an ion exchange process and the treated water is taken out from a treated water passage 13. The resin layer 12 is regenerated by injecting a regenerating agent from the chemical injection passage 14 and the regenerated waste liquid is sent to a waste liquid storage vessel 4 from a line passage 15, mixed by a stirrer 16 and supplied to the adjusting vessel 1 from the waste liquid supply passage 6 at a homogenization flow rate.