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    • 6. 发明专利
    • Method for condensing sea water
    • 冷凝海水的方法
    • JP2006167533A
    • 2006-06-29
    • JP2004360985
    • 2004-12-14
    • Nippon Steel CorpToyama Prefecture富山県新日本製鐵株式会社
    • KIMURA HARUOTAKAHASHI NAOYAKUYO HIDEOKATO HATSUICHI
    • C02F1/44B01D61/02B01D61/04B01D61/14B01D61/58
    • PROBLEM TO BE SOLVED: To provide a method for efficiently producing condensed sea water of 100 g/L or higher by reverse osmosis membrane treatment.
      SOLUTION: In the method for producing the condensed sea water by the reverse osmosis membrane treatment, RO membranes are placed in series, a recovery rate of the condensed sea water in the first step of the reverse osmosis membrane treatment is 40% or lower, a row water supply amount per unit membrane area in the second step of the reverse osmosis membrane treatment is 40% or lower of a row water supply amount per a unit membrane area in the first step of the reverse osmosis membrane treatment, and also an operation pressure in the second step of the reverse osmosis membrane treatment is 8 MPa or higher.
      COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题:提供通过反渗透膜处理有效地生产100g / L以上的凝结海水的方法。 解决方案:在通过反渗透膜处理制造冷凝海水的方法中,反渗透膜被串联放置,反渗透膜处理的第一步骤中的冷凝海水的回收率为40% 在反渗透膜处理的第一步骤中,反渗透膜处理的第二步骤中每单位膜面积的排水量为单位膜面积的排水量的40%以下, 反渗透膜处理的第二工序中的操作压力为8MPa以上。 版权所有(C)2006,JPO&NCIPI
    • 7. 发明专利
    • Removal method of nitrogen and phosphorus from sewage, and removal apparatus
    • 硝酸和磷的去除方法和除去装置
    • JP2007136298A
    • 2007-06-07
    • JP2005331462
    • 2005-11-16
    • Nippon Steel Corp新日本製鐵株式会社
    • MIKI OSAMUKATO TOSHIROTAKAHASHI NAOYA
    • C02F3/34C02F3/30
    • PROBLEM TO BE SOLVED: To provide a new removal method of nitrogen and phosphorus, and a removal apparatus.
      SOLUTION: The biological nitrogen and phosphorus removal process (A
      2 O method) comprises a primary settling tank, an anaerobic tank, anoxic tanks (denitrification tank), an aerobic tank, and a final settling tank, and circulates active sludge of a terminal part of the aerobic tank to the anoxic tank (denitrification tank). A second anoxic tank is provided at a rear stage of the aerobic tank, and the activated sludge of the terminal part of the second anoxic tank is circulated to the preceding anoxic tank (denitrification tank), and circulation of the activated sludge from the aerobic tank to the preceding anoxic tank (denitrification tank) is stopped.
      COPYRIGHT: (C)2007,JPO&INPIT
    • 要解决的问题:提供氮和磷的新的去除方法以及去除装置。 解决方案:生物除氮和除磷工艺(A 2 O方法)包括初级沉淀池,厌氧池,缺氧罐(脱氮罐),需氧罐和最终沉降 并将需氧罐的末端部分的活性污泥循环到缺氧罐(脱氮罐)。 在需氧罐的后段设有第二个缺氧罐,第二个缺氧罐的末端部分的活性污泥循环到前一个缺氧罐(脱氮罐),并将活性污泥从需氧罐中循环 到脱水槽(脱氮槽)停止。 版权所有(C)2007,JPO&INPIT
    • 8. 发明专利
    • Circulating water reuse apparatus and reuse method in cooling system for open circulating system
    • 开放式循环系统冷却系统循环水再利用装置与再利用方法
    • JP2009195808A
    • 2009-09-03
    • JP2008039082
    • 2008-02-20
    • Nippon Steel Corp新日本製鐵株式会社
    • TSUJIMOTO WATARUNIEKAWA HIROSHITAKAHASHI NAOYA
    • C02F1/46B01D61/02C02F1/44
    • PROBLEM TO BE SOLVED: To provide a method in a circulating water cooling system of an open circulating system in which salt crystallization and development of organisms are prevented, a stable circulating water quality is maintained, sticking of polluting matters including oil is prevented, the development of microorganism is restrained and which is cheap and easy for maintenance control.
      SOLUTION: Part of the circulating water of an open circulating system in the steel industry is branched at a bypass tube, filtered and separated at a reverse osmosis membrane. The filtered water is reused as a water for steel process which carries out cooling of a roll or a hydraulic apparatus at the steel facilities, and carries out dilution of a rolling oil or a chemical. Part of the enriched drain is flowed into an electrolyte tank which is separated by a diaphragm having an ion permeability. An acid electrolytic water generated at the anode side of the electrolyte tank and an alkali electrolyte water generated at the cathode side are mixed into the circulating water alternately, and injected into a cooling tower intermittently. By doing this, sticking of polluting matters including oil to the cooling tower cell or the circulation piping is prevented and the development of microorganisms is restrained.
      COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:为了提供一种开放循环系统的循环水冷却系统的方法,其中防止了盐结晶和生物的发育,保持了稳定的循环水质,防止了含油污染物质的粘附 微生物的发育受到限制,便于维护控制。

      解决方案:钢铁工业中开放循环系统的一部分循环水在旁通管分支,在反渗透膜处过滤分离。 过滤后的水被再次用作在钢铁厂进行冷却辊或液压装置的炼钢工艺,进行轧制油或化学品的稀释。 富集排水管的一部分流入电解槽,隔膜由具有离子渗透性的隔膜分开。 在电解槽的阳极侧产生的酸性电解水和在阴极侧产生的碱性电解水交替地混入循环水中,并间歇地注入冷却塔。 通过这样做,可以防止将污染物质(包括油)粘附在冷却塔池或循环管道上,从而抑制微生物的发育。 版权所有(C)2009,JPO&INPIT

    • 9. 发明专利
    • Method for concentrating sludge
    • 浓缩污泥的方法
    • JP2005193222A
    • 2005-07-21
    • JP2004076122
    • 2004-03-17
    • Nippon Steel Corp新日本製鐵株式会社
    • ONO NOBUYUKITAKAHASHI NAOYATAKAHASHI KENJI
    • C02F11/12B01D37/02C25D21/16
    • PROBLEM TO BE SOLVED: To provide a method capable of stably and effectively treating sludge of metal compounds continuously for a long time, the sludge of metal compounds being produced via a neutralizing treatment of acidic waste water containing metal ions.
      SOLUTION: The metal compound sludge is produced via the neutralizing treatment of the acidic waste water containing the metal ions and concentrated via a cake filtration in which the cake thickness is not less than 1 mm and not more than 50 mm, and the average diameter of a grain composing the cake is not less than 4 μm or the average specific resistance of the cake is not more than 6×10
      8 cm/g.
      COPYRIGHT: (C)2005,JPO&NCIPI
    • 要解决的问题:为了提供能够长时间连续地稳定和有效地处理金属化合物的污泥的方法,通过中和处理含有金属离子的酸性废水来生产金属化合物的污泥。 解决方案:金属化合物污泥是通过中和处理含有金属离子的酸性废水生成的,并通过滤饼过滤浓缩,其中滤饼厚度不小于1mm且不大于50mm,并且 构成滤饼的颗粒的平均直径不小于4μm,或者滤饼的平均电阻率不大于6×10 SP / cm 3 / g。 版权所有(C)2005,JPO&NCIPI