会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 1. 发明专利
    • Biological treatment tank for waste water and biologically treating method
    • 生物处理罐用于废水和生物处理方法
    • JP2006007033A
    • 2006-01-12
    • JP2004185350
    • 2004-06-23
    • Kobe Steel LtdKobelco Eco-Solutions Co Ltd株式会社神戸製鋼所株式会社神鋼環境ソリューション
    • ODA TAKESHIISHIYAMA AKIRAMIZUGUCHI HIROYUKIWATANABE SHOZO
    • C02F3/08B01F5/04C02F3/34
    • Y02W10/15
    • PROBLEM TO BE SOLVED: To provide a biological treatment tank for waste water, in which a circulating flow is formed without necessitating the supply of the power other than the power for prevention of the sedimentation of a microbe-fixed carrier and that for aeration from the outside and the microbe-fixed carrier or a suspended microbe is returned excellently and to provide a biologically treating method. SOLUTION: A screen 12 for separating the microbe-fixed carrier and carrier intakes 13, 13a are arranged on the outflow side of the biological treatment tank in which the microbe-fixed carrier of a suspended state is incorporated. Circulation ducts are arranged for communicating these carrier intakes with the inflow side of the biological treatment tank. Ejector pipes 18, 18a are arranged on the inflow side of the biological treatment tank so that a flow of the microbe-fixed carrier from the outflow side to the inflow side is formed in each of circulation ducts 17, 17a by utilizing a water level difference between the biological treatment tank and a waste water tank arranged on the upstream side of the biological treatment tank, namely, by transforming the positional energy into the kinetic energy. As a result, since a sucking flow is formed on the inflow side even when external energy is not supplied, the water to be treated is mixed with the microbe-fixed carrier by the ejector effect and the circulating flow is formed, and the biological treatment can be effectively performed. COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题:为了提供一种废水生物处理槽,其中形成循环流而不需要除了用于防止微生物固定载体沉降的动力之外的动力供应,并且对于 从外部通气和微生物固定载体或悬浮微生物得到良好的返回并提供生物处理方法。 解决方案:用于分离微生物固定载体和载体进入口13,131的筛网12布置在生物处理槽的流出侧,其中结合悬浮状态的微生物固定载体。 循环管道布置成将这些载体进口与生物处理槽的流入侧连通。 喷射管18,18a布置在生物处理槽的流入侧,从而通过利用水位差,在每个循环管道17,17a中形成从流出侧到流入侧的微生物固定载体的流动 在生物处理槽和布置在生物处理槽的上游侧的废水槽之间,即通过将位置能转换成动能。 结果,由于即使在不供给外部能量的情况下也在流入侧形成吸入流,所以被处理水通过喷射器作用与微生物固定载体混合,形成循环流,生物处理 可以有效地执行。 版权所有(C)2006,JPO&NCIPI
    • 2. 发明专利
    • Wastewater treatment method and wastewater treatment apparatus
    • 废水处理方法和废水处理装置
    • JP2006043563A
    • 2006-02-16
    • JP2004226966
    • 2004-08-03
    • Kobe Steel LtdKobelco Eco-Solutions Co Ltd株式会社神戸製鋼所株式会社神鋼環境ソリューション
    • MATSUBARA MASAAKIISHIYAMA AKIRAFUTABOSHI YUKIHIRO
    • C02F3/12C02F1/52
    • Y02W10/15
    • PROBLEM TO BE SOLVED: To provide a wastewater treatment method and apparatus which can prevent the flow out of activated sludge from a final settling basin due to the deterioration of activated sludge settling properties when wastewater is treated with the activated sludge. SOLUTION: (1) In the waste water treatment method using the activated sludge, the kinds and number of protozoa in the activated sludge are measured, a diversity index is calculated from the results, and the settling properties of the activated sludge are predicted based on the value of the diversity index to judge whether prevention of flow out of the activated sludge from the final settling basin is necessary or not. (2) In the above waste water treatment method, the calculation of the diversity index is performed with Shannon's equation for obtaining a diversity index. (3) In the above waste water treatment method, preventative measures against the flow out of the activated sludge from the final settling basin are taken when the value of the diversity index calculated with the above equation is below the predetermined value (for example, 0.4-0.6). (4) The wastewater treatment apparatus is used for such a wastewater treatment method. COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题:提供一种废水处理方法和装置,其可以防止活性污泥从最终沉降池流出,这是由于当用活性污泥处理废水时活性污泥沉淀性能的劣化。 (1)在使用活性污泥的废水处理方法中,测定活性污泥中原生动物的种类和数量,从结果计算出多样性指数,活性污泥的沉降特性 根据多样性指数的价值预测,判断是否需要预防流出最终沉降池的活性污泥。 (2)在上述废水处理方法中,利用香农获得多样性指数的方程式进行多样性指标的计算。 (3)在上述废水处理方法中,当用上述方程计算出的多样性指数的值低于预定值(例如,0.4)时,采取从最终沉降池流出活性污泥的预防措施 -0.6)。 (4)废水处理装置用于这种废水处理方法。 版权所有(C)2006,JPO&NCIPI
    • 4. 发明专利
    • Gas diffuser, membrane module, membrane separator, gas diffusion method and membrane separation method
    • 气体扩散器,膜模块,膜分离器,气体扩散方法和膜分离方法
    • JP2010188278A
    • 2010-09-02
    • JP2009035138
    • 2009-02-18
    • Kobelco Eco-Solutions Co Ltd株式会社神鋼環境ソリューション
    • ISHIYAMA AKIRAKAWASHIMA ATSUSHI
    • C02F3/20B01D65/00B01D65/02C02F1/44
    • B01F3/04262B01D63/02B01D2313/26B01D2321/185B01F2003/04312B01F2003/0439C02F3/1273C02F3/20Y02W10/15
    • PROBLEM TO BE SOLVED: To reduce the scale of a space in which a gas diffuser is arranged while diffusing bubbles substantially uniformly from each through hole. SOLUTION: The gas diffuser includes a porous plate having a plurality of through holes, and a diffuser pipe arranged in such a manner that a discharge port for discharging bubbles into a sludge mixture liquid is located below the porous plate. In the diffuser, the center of the opening plane of the discharge port is located substantially directly under the center of the smallest circle surrounding the through holes of the porous plate, and the opening direction of the discharge port is set to be any one of the horizontal direction, vertical downward direction, and the direction between the horizontal direction and vertical downward direction. The inner diameter of the discharge port is 16 mm or above, and the ratio (L/D) of the distance L between the lower surface of the porous plate and the center of the opening plane of the discharge port to the diameter D of the circle is 0.8-1.2. COPYRIGHT: (C)2010,JPO&INPIT
    • 要解决的问题:为了减小气体扩散器布置的空间的尺度,同时从每个通孔大致均匀地扩散气泡。 解决方案:气体扩散器包括具有多个通孔的多孔板和扩散管,其布置成使得用于将气泡排放到污泥混合液中的排出口位于多孔板下方。 在扩散器中,排出口的开口面的中心基本上位于围绕多孔板的通孔的最小的圆的中心附近,排出口的打开方向被设定为 水平方向,垂直向下方向,以及水平方向和垂直向下方向之间的方向。 排出口的内径为16mm以上,多孔板的下表面与排出口的开口面的中心的距离L的比(L / D)相对于 圈数为0.8-1.2。 版权所有(C)2010,JPO&INPIT
    • 5. 发明专利
    • Aeration method and aeration device
    • 航空方法与航空装置
    • JP2010172792A
    • 2010-08-12
    • JP2009015715
    • 2009-01-27
    • Kobelco Eco-Solutions Co Ltd株式会社神鋼環境ソリューション
    • ISHIYAMA AKIRAKAWASHIMA ATSUSHI
    • C02F3/20
    • Y02W10/15
    • PROBLEM TO BE SOLVED: To reduce the time and labor for the maintenance of an air diffusing pipe, and make a space, in which the air diffusing pipe in disposed, small by inhibiting sludge mixed liquor from entering into the air diffusing pipe, disposed in the sludge mixed liquor, of activated sludge process equipment or the like to inhibit the clogging of the air diffusing pipe. SOLUTION: In an aeration method where the air diffusing pipe is disposed in the sludge mixed liquor and gas is discharged from the diffusing pipe to perform aeration, the air diffusing pipe having an internal diameter of discharge port for discharging the gas of 20 mm or more is arranged in the sludge mixed liquor so that the opening direction of the discharge port may be a horizontal direction, and the gas is discharged so that the linear velocity of the gas at the opening end of the discharge port may be 4 m/s or more and 15 m/s or less, thereby performing aeration. COPYRIGHT: (C)2010,JPO&INPIT
    • 要解决的问题:为了减少空气扩散管的维护的时间和人力,并且通过抑制污泥混合液进入空气扩散管而使其中放置的空气扩散管的空间小 处理污泥混合液,活性污泥处理设备等,以抑制空气扩散管的堵塞。 解决方案:在空气扩散管设置在污泥混合液中并从扩散管排出气体进行曝气的曝气方法中,具有用于排出气体的排出口内径的空气扩散管20 在污泥混合液中配置mm以上,排出口的开口方向为水平方向,排出气体,排出口的开口端的气体的线速度为4m s以上且15m / s以下,进行曝气。 版权所有(C)2010,JPO&INPIT
    • 7. 发明专利
    • Membrane separation type sewage treatment apparatus and operating method therefor
    • 膜分离式污水处理装置及其操作方法
    • JP2006007103A
    • 2006-01-12
    • JP2004188118
    • 2004-06-25
    • Kobelco Eco-Solutions Co Ltd株式会社神鋼環境ソリューション
    • HASEGAWA SUSUMUISHIYAMA AKIRANAKAJIMA YUICHI
    • C02F3/12C02F1/44C02F3/34
    • Y02W10/15
    • PROBLEM TO BE SOLVED: To provide a membrane separation type sewage treatment apparatus with which sewage can be treated while dispensing with a flow rate adjusting tank even when the amount of the sewage to be treated exceeds the throughput capacity of an immersed membrane separation unit temporarily and to provide a method for operating this sewage treatment apparatus. SOLUTION: The membrane separation type sewage treatment apparatus is characterized in that a partition 4 is arranged in a bio-reaction tank 1 to divide the inside of the bio-reaction tank 1 into the first reaction tank 2 in which sewage is made to flow and the second reaction tank 3 which is communicated with the first reaction tank 2 and in which the immersed membrane separation unit 9 is housed, a first diffuser 7 and a second diffuser 8 are arranged respectively in the first reaction tank 2 and the second reaction tank 3, a supernatant liquid discharging means 21 is arranged in the first reaction tank 2 for discharging a supernatant liquid, and sewage supply destination changing-over means 19, 20 for changing-over a supply destination of sewage from the first reaction tank 2 to the second reaction tank 3 are provided. COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题:为了提供一种膜分离型污水处理装置,即使在待处理污水的量超过浸入的膜分离的通过量时,也可以在分配流量调节罐的同时处理污水 并且提供操作该污水处理装置的方法。 解决方案:膜分离型污水处理装置的特征在于,在生物反应罐1中配置隔板4,以将生物反应罐1的内部分解成制造污水的第一反应槽2 与第一反应槽2连通并且其中容纳浸入的膜分离单元9的第二反应槽3分别布置在第一反应罐2中,第二扩散器7和第二扩散器8分别布置在第一反应罐2中, 反应容器3,在第一反应槽2内设置上清液排放装置21,用于排出上清液;以及用于从第一反应罐2转换污水的供给目的地的污水供给目的地转换装置19,20 到第二反应槽3。 版权所有(C)2006,JPO&NCIPI
    • 8. 发明专利
    • Water treatment apparatus
    • 水处理设备
    • JP2011020018A
    • 2011-02-03
    • JP2009165372
    • 2009-07-14
    • Kobelco Eco-Solutions Co Ltd株式会社神鋼環境ソリューション
    • ISHIYAMA AKIRA
    • C02F3/12C02F3/00
    • Y02W10/15
    • PROBLEM TO BE SOLVED: To provide a water treatment apparatus capable of suppressing a deterioration in purifying effect of activated sludge by preventing extinction of microorganisms in the activated sludge without requiring a huge storage tank beyond necessity even when the amount of BOD fluctuates that is introduced to an aerobic treatment tank per unit time. SOLUTION: The water treatment apparatus equipped with the aerobic treatment tank for an aerobic treatment by bringing the activated sludge into contact with water to be treated containing an organic substance is characterized by having an organic substance supply means for supplying the aerobic treatment tank with a biodegradable organic substance when the ratio of the amount of the BOD in the water to be treated introduced to the aerobic treatment tank per unit time to the amount of the activated sludge in the aerobic treatment tank comes down below the prescribed value. COPYRIGHT: (C)2011,JPO&INPIT
    • 要解决的问题:提供一种水处理装置,其能够通过防止活性污泥中的微生物的灭绝而抑制活性污泥的净化效果的劣化,而不需要巨大的储存罐,即使当BOD的量波动时, 每单位时间引进好氧处理槽。 解决方案:通过使活性污泥与含有机物质的待处理水接触,配备有好氧处理槽的水处理装置的特征在于,具有供给有氧处理槽的有机物质供给单元 当待处理的待处理水中的BOD的量与单位时间的需氧处理槽的比例相对于需氧处理槽中的活性污泥的量的比例低于规定值时,具有生物降解性有机物质。 版权所有(C)2011,JPO&INPIT
    • 9. 发明专利
    • Operation method of combined filtration equipment
    • 组合过滤设备的操作方法
    • JP2010000475A
    • 2010-01-07
    • JP2008162952
    • 2008-06-23
    • Kobelco Eco-Solutions Co Ltd株式会社神鋼環境ソリューション
    • TANIZAWA KENHIRAI YUKIKOISHIYAMA AKIRA
    • C02F1/44B01D36/00B01D61/16B01D63/02C02F1/52
    • PROBLEM TO BE SOLVED: To provide an operation method of adding a coagulant to water to be treated of an immersion type membrane separation device and water to be treated of a media filtration device so as to provide the optimal concentration for both of the immersion type membrane separation device and the media filtration device, in combined filtration equipment in which the membrane permeated water and media filtrated water are obtained at the same time by jointly using the immersion type membrane separation device and the media filtration device.
      SOLUTION: The operation method of combined filtration equipment is characterized in that the coagulant is added so as to provide a concentration range of 0.3 mg/L to 0.55 mg/L for raw water to be supplied to the immersion type membrane separation device, having a turbidity of 1 degree to 15 degree and the coagulant is added so as to provide a concentration range of 0.55 mg/L to 0.8 mg/L for concentrated water to be supplied to the media filtration device, in the combined filtration equipment in which the raw water such as river water and water of lake and marsh is membrane-separated by the immersion type membrane separation device to provide membrane permeated water and concentrated water of the immersion type membrane separation device is filtrated by the media filtration device to provide filtrated water, and both of the permeated water and filtrated water are supplied as treated water.
      COPYRIGHT: (C)2010,JPO&INPIT
    • 要解决的问题:提供一种将浸渍型膜分离装置的待处理水和絮凝剂添加到介质过滤装置的被处理水中的操作方法,以提供两者的最佳浓度 浸渍式膜分离装置和介质过滤装置,通过联合使用浸渍型膜分离装置和介质过滤装置,同时获得膜渗透水和介质过滤水的组合过滤装置。 组合式过滤设备的操作方法的特征在于,对浸入式膜分离装置的原水提供浓度范围为0.3mg / L至0.55mg / L的凝结剂 ,浊度为1〜15度,加入絮凝剂,浓缩范围为0.55mg / L〜0.8mg / L,浓缩水供给到介质过滤装置中,在组合过滤设备中 其中浸入式膜分离装置将浸入式膜分离装置的膜透过水和浓缩水用水和水和沼泽水等原水进行膜分离,通过介质过滤装置过滤, 水,并且作为处理水供给渗透水和过滤水。 版权所有(C)2010,JPO&INPIT
    • 10. 发明专利
    • Operation method of combined filtration equipment
    • 组合过滤设备的操作方法
    • JP2010000474A
    • 2010-01-07
    • JP2008162951
    • 2008-06-23
    • Kobelco Eco-Solutions Co Ltd株式会社神鋼環境ソリューション
    • TANIZAWA KENHIRAI YUKIKOISHIYAMA AKIRA
    • C02F1/44B01D36/00B01D61/16B01D63/02C02F1/52
    • PROBLEM TO BE SOLVED: To provide an operation method of adding a coagulant only to water to be treated (raw water such as river water and water of lake and marsh) of an immersion type membrane separation device so as to provide the optimal concentration for both of the immersion type membrane separation device and a media filtration device, in combined filtration equipment in which the membrane permeated water and media filtrated water are obtained at the same time by jointly using the immersion type membrane separation device and the media filtration device.
      SOLUTION: The operation method of combined filtration equipment is characterized in that the coagulant is added so as to provide a concentration range of 0.4 mg/L to 1.2 mg/L for raw water to be supplied to the immersion type membrane separation device, having a turbidity of 4 degree to 15 degree and the coagulant is not added to concentrated water to be supplied to the media filtration device, in the combined filtration equipment in which the raw water such as river water and water of lake and marsh is membrane-separated by the immersion type membrane separation device to provide membrane permeated water and concentrated water of the immersion type membrane separation device is filtrated by the media filtration device to provide filtrated water, and both of the permeated water and filtrated water are supplied as treated water.
      COPYRIGHT: (C)2010,JPO&INPIT
    • 要解决的问题:提供一种仅将浸渍型膜分离装置中的絮凝剂添加到浸渍型膜分离装置的待处理水(如河水,湖泊,沼泽的水等原水)中的操作方法,以提供最佳 通过联合使用浸渍型膜分离装置和介质过滤装置,同时获得膜渗透水和介质过滤水的组合过滤设备中浸渍型膜分离装置和介质过滤装置的浓度 。 解决方案:组合过滤设备的操作方法的特征在于加入凝结剂以提供浓度范围为0.4mg / L至1.2mg / L,以供给浸入式膜分离装置的原水 在河流水和湖泊和沼泽水等原水为膜的组合过滤设备中,浊度为4度〜15度,凝结剂不加入到供给到介质过滤装置的浓缩水中 通过浸渍式膜分离装置分离浸渍型膜分离装置的膜透过水和浓缩水,通过介质过滤装置过滤,提供过滤水,并将渗透水和过滤水两者作为处理水供给 。 版权所有(C)2010,JPO&INPIT