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    • 1. 发明专利
    • Apparatus and method for regenerating development waste liquid
    • 用于再生发展废水的装置和方法
    • JP2012210565A
    • 2012-11-01
    • JP2011077081
    • 2011-03-31
    • Kurita Water Ind LtdTama Kagaku Kogyo Kk多摩化学工業株式会社栗田工業株式会社
    • OSAWA KIMINOBUKOFUNE KEIRYOONODA SEIICHICHO TOSHITSURASATO TAKAHIRO
    • C02F1/44B01D61/02B01D61/10B01D61/12B01D61/14B01D61/58B01D65/02C02F1/28
    • PROBLEM TO BE SOLVED: To stably and efficiently carry out long-term regeneration treatment of a development waste liquid that contains resist exfoliation and tetraalkylammonium hydroxide (TAAH).SOLUTION: Acid is added to the development waste liquid containing resist exfoliation and TAAH to adjust the liquid to pH 8-9.5, and then membrane separation treatment is carried out by an MF membrane module 1. A permeated liquid is subjected to membrane separation treatment at a liquid permeation temperature of 40-80°C by a nanofiltration (NF) membrane module 2 with a molecular weight cutoff of 200-900 and treated in an activated carbon column 3. Setting the liquid permeation temperature of the NF membrane to 40-80°C lowers the viscosity of the treated liquid and suppresses an operating pressure to increase the amount of permeated liquid. When the amount of permeated liquid of the NF membrane is increased, the resist exfoliation leaks to the permeated liquid side of the NF membrane. However, since the resist exfoliation can be eliminated in the activated carbon treatment in a subsequent stage, a regenerated liquid of high TAAH purity can be obtained.
    • 要解决的问题:为了稳定有效地进行含有抗蚀剂剥离的显影废液和四烷基氢氧化铵(TAAH)的长期再生处理。

      解决方案:将酸加入到含抗蚀剂剥离的发泡废液和TAAH中以将液体调节至pH8-9.5,然后通过MF膜组件1进行膜分离处理。将渗透液体进行膜 通过分子量截留值为200-900的纳滤(NF)膜组件2在40-80℃的液体渗透温度下进行分离处理,并在活性炭柱中处理3.将NF膜的液体渗透温度设定为 40-80℃降低处理液体的粘度,并抑制操作压力以增加渗透液体的量。 当NF膜的渗透液量增加时,抗剥离层泄漏到NF膜的渗透液侧。 然而,由于在后续阶段的活性炭处理中可以消除抗蚀剂剥离,所以可以获得高TAAH纯度的再生液体。 版权所有(C)2013,JPO&INPIT

    • 2. 发明专利
    • Recovery method for water from aerobically and biologically treated water
    • 从生物和生物处理水中回收水的方法
    • JP2012206066A
    • 2012-10-25
    • JP2011075499
    • 2011-03-30
    • Kurita Water Ind Ltd栗田工業株式会社
    • IKEDA HIROYUKIKOFUNE KEIRYOOSAWA KIMINOBU
    • C02F1/44B01D61/58C02F1/52C02F1/56
    • Y02A20/131
    • PROBLEM TO BE SOLVED: To provide a recovery method for water from aerobically and biologically treated water that prevents a NF membrane or RO membrane from being clogged and efficiently recovers water from aerobically and biologically treated water.SOLUTION: The method is for recovering water by subjecting the aerobically and biologically treated water generated by aerobically and biologically treating organic wastewater to filtration in a MF membrane or UF membrane apparatus and then to desalination in a NF membrane or RO membrane apparatus, wherein the aerobically and biologically treated water contains a metabolite formed during biological treatment and has a Langelier index larger than 0. The recovery method for water from aerobically and biologically treated water is characterized in that the water to be supplied for treatment to the MF membrane or UF membrane apparatus has a pH of 5.5 or lower.
    • 要解决的问题:提供一种从有氧和生物处理水中提取水的回收方法,防止NF膜或RO膜被堵塞并有效地从有氧和生物处理的水中回收水。 解决方案:该方法用于通过对在MF膜或UF膜装置中有氧和生物处理有机废水产生的有氧生物处理水进行过滤,然后在NF膜或RO膜装置中脱盐, 其中有氧和生物处理的水含有在生物处理期间形成的代谢物,并且具有大于0的Langelier指数。来自有氧和生物处理水的水的回收方法的特征在于,供应给MF膜的水或 UF膜装置的pH为5.5以下。 版权所有(C)2013,JPO&INPIT
    • 3. 发明专利
    • Electric deionizer
    • 电动除尘器
    • JP2009233536A
    • 2009-10-15
    • JP2008081205
    • 2008-03-26
    • Kurita Water Ind Ltd栗田工業株式会社
    • KAKO HIRONORIOSAWA KIMINOBUDEGUCHI TOMOAKI
    • C02F1/469B01D61/48
    • Y02A20/134
    • PROBLEM TO BE SOLVED: To provide an electric deionizer which can promote movement of ion components in water to be treated to a concentration chamber without short-circuiting the water to be treated through a desalting chamber, and can obtain satisfactory treated water quality even when the passing amount of the water to be treated is small, and a pure water production system using the electric deionizer.
      SOLUTION: The electric deionizer 1 is made by forming desalting chambers 2 and concentration chambers 3 by arranging a plurality of anion exchange membranes 5 and cation exchange membranes 4 between the cathode 6 and the anode 7. The desalting chamber 2 is filled with a porous material having an ion-exchange group and installed with a rectifying member 9 for making the water to be treated supplied to the desalting member flow almost uniformly through the almost whole of the porous material.
      COPYRIGHT: (C)2010,JPO&INPIT
    • 要解决的问题:提供一种电去离子器,其可以促进待处理的水中的离子组分的移动到浓缩室,而不会通过脱盐室短路待处理的水,并且可以获得令人满意的处理水质 即使待处理水的通过量少,也可以使用使用电去离子的纯水生产系统。 解决方案:电去离子器1是通过在阴极6和阳极7之间布置多个阴离子交换膜5和阳离子交换膜4来形成脱盐室2和浓缩室3制成的。脱盐室2填充有 具有离子交换基团的多孔材料并且安装有用于使被供给到脱盐部件的被处理水的整流部件9几乎均匀地流过几乎全部的多孔材料。 版权所有(C)2010,JPO&INPIT
    • 4. 发明专利
    • Electro-deionization apparatus and method for operating electro-deionization apparatus
    • 电去离子装置和操作电解脱附装置的方法
    • JP2008296204A
    • 2008-12-11
    • JP2007148562
    • 2007-06-04
    • Kurita Water Ind Ltd栗田工業株式会社
    • KAKO HIRONORIOSAWA KIMINOBU
    • C02F1/469B01D61/44B01D61/46
    • Y02A20/134
    • PROBLEM TO BE SOLVED: To provide an electro-deionization apparatus which can prevent the occurrence of scale even when water, in which an inorganic carbonic acid and a hardness component remain, is diffused into and flows backward into a concentration chamber as a result of the stop of the electro-deionization apparatus for a long period of time. SOLUTION: An electro-deionization apparatus 1 comprises a plurality of desalination chambers 2 and a plurality of concentration chambers 3 each provided between a plurality of cation exchange membranes 4 and a plurality of anion exchange membranes 5. The concentration chamber 3 is divided by a bipolar membrane 10 into a cathode-side concentration chamber 3A and an anode-side concentration chamber 3B. A flow passage R1 for water W1 to be treated is connected to the desalination chamber 2. The outlet side of the desalination chamber 2 functions as a flow passage R2 for deionized water (treated water) W2. The flow passage R2 is branched, and a flow passage branch R3 and flow passages R3a to R3d communicate, for example, with the cathode-side concentration chamber 3A, the anode-side concentration chamber 3B etc., respectively. A part of the deionized water W2 in the desalination chamber 2 is introduced into the concentration chamber 3. In such a state that circulating water in the concentration chamber 3 has been diluted with deionized water, concentrated water W3 is discharged through each of discharge flow passages R4a to R4d each provided with a check valve 20 and a combined discharge passage R4. COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:提供一种电去离子装置,其即使在残留有无机碳酸和硬度成分的水被扩散入并流入浓缩室中的水时也能够防止水垢的发生,作为 电去离子装置长时间停止的结果。 电去离子装置1包括多个淡化室2和多个浓缩室3,每个浓缩室3设置在多个阳离子交换膜4和多个阴离子交换膜5之间。浓缩室3被分割 通过双极膜10进入阴极侧浓缩室3A和阳极侧浓缩室3B。 用于待处理水W1的流路R1连接到脱盐室2.脱盐室2的出口侧用作去离子水(处理水)W2的流路R2。 流路R2分支,流路分支R3和流路R3a〜R3d分别与阴极侧浓缩室3A,阳极侧浓缩室3B等连通。 脱盐室2中的去离子水W2的一部分被引入浓缩室3.在浓缩室3中的循环水已用去离子水稀释的状态下,浓缩水W3通过排出流路 R4a至R4d均设有止回阀20和组合排放通道R4。 版权所有(C)2009,JPO&INPIT
    • 5. 发明专利
    • Pure water making method and pure water making apparatus
    • 纯水制造方法和纯水制造设备
    • JP2008161761A
    • 2008-07-17
    • JP2006351565
    • 2006-12-27
    • Kurita Water Ind Ltd栗田工業株式会社
    • MISUMI YOSHITERUOSAWA KIMINOBUSATO SHIGEAKIIIZUKA HIROSHI
    • C02F1/469B01D61/48B01J39/04B01J41/04B01J47/12C02F1/42H01M8/06
    • Y02A20/131Y02A20/134Y02P70/56
    • PROBLEM TO BE SOLVED: To perform both the production of pure water due to electric deionization and the production of pure water due to ion exchange using an electric deionizing apparatus. SOLUTION: In a pure water making apparatus having the electric deionizing device constituted by providing a concentration chamber and cathode chamber 35, a desalting chamber 37 and an anode-side concentration chamber 40 by arranging ion exchange films 33', 34 and 33 between an anode 32 and a cathode 31 and filling the respective chambers with ion exchange resins, water to be treated is passed through the desalting chamber 37 in the state that the supply of a current is stopped or controlled so that current density becomes 1,000 mA/dm 2 or below and subjected to ion exchange by the ion exchange resins 38 and 39 in the desalting chamber 37 to allow pure water to flow out of the desalting chamber 37. COPYRIGHT: (C)2008,JPO&INPIT
    • 要解决的问题:由于电去离子而产生纯水,并且由于使用电去离子装置的离子交换而产生纯水。 解决方案:在具有通过设置浓缩室和阴极室35构成的电去离子装置的纯水制造装置中,通过配置离子交换膜33',34和33,设置脱盐室37和阳极侧浓缩室40 在阳极32和阴极31之间并用离子交换树脂填充各个室,待停止或控制电流供应的状态下,待处理水被通过脱盐室37,使电流密度成为1,000mA / dm 2或以下,并通过脱盐室37中的离子交换树脂38和39进行离子交换,以使纯水从脱盐室37流出。(C) 2008年,日本特许厅和INPIT
    • 6. 发明专利
    • Fungistatic treatment method of fuel cell system
    • 燃料电池系统的真菌治疗方法
    • JP2007234459A
    • 2007-09-13
    • JP2006056199
    • 2006-03-02
    • Kurita Water Ind Ltd栗田工業株式会社
    • CHUMA TAKAAKIOSAWA KIMINOBU
    • H01M8/04B01D19/00B01D61/44C02F1/20C02F1/46C02F1/469
    • Y02E60/50
    • PROBLEM TO BE SOLVED: To provide a fungistatic treatment method of a fuel cell system provided with an electric deionization device in which fungistatic treatment of treated water can be carried out without providing a special equipment for the fungistatic treatment of the treated water, and provide the fuel cell system which is provided with the electric deionization device capable of controlling fungus. SOLUTION: This fuel cell system 1 is provided with a fuel cell main body 2, the electric deionization device 31 which is installed at the front stage of the fuel cell main body 2 and which has a cathode room 31B and an anode room 31A segmented by ion exchange membranes, and a return pipe 9 in which exhaust water (cathode water) from the cathode room 31B of the electric deionization device 31 is made to flow into a fungistic target place in the fuel cell system 1. COPYRIGHT: (C)2007,JPO&INPIT
    • 解决问题的方案:提供一种具有电去离子装置的燃料电池系统的抑菌处理方法,其中可以进行处理水的抑菌处理而不设置用于处理水的抑菌处理的特殊设备, 并且提供具有能够控制真菌的电去离子装置的燃料电池系统。 解决方案:该燃料电池系统1设置有燃料电池主体2,该电去离子装置31安装在燃料电池主体2的前级,并具有阴极室31B和阳极室 31A,并且使来自电去离子装置31的阴极室31B的排出水(阴极水)流入燃料电池系统1中的真空目标位置的返回管9。 版权所有(C)2007,JPO&INPIT
    • 9. 发明专利
    • APPARATUS FOR SUPPLYING OZONE WATER
    • JP2000037695A
    • 2000-02-08
    • JP20940298
    • 1998-07-24
    • KURITA WATER IND LTD
    • OSAWA KIMINOBUMIWA RYOHEI
    • B08B5/00C02F1/78H01L21/304
    • PROBLEM TO BE SOLVED: To reduce the consumption of ozone by a process in which the self- decomposition of ozone is controlled, the decrease of ozone concentration is low even during long distance transportation, and ozone water of constant concentration can be supplied to a use point by dissolving carbon dioxide or an organic compound in pure water or ozone water. SOLUTION: Ozone-containing gas is produced by supplying a mixed gas of oxygen gas and a trace amount of nitrogen gas from an oxygen gas container 1 and a nitrogen gas container 2 to an ozone generator 3, and ozone is dissolved in pure water degassed in advance to produce ozone water. An addition means 10 is installed in the pre-stage, post stage, or apparatus itself of an ozone dissolving apparatus 4, ozone water in which carbon dioxide or an organic compound is dissolved is used in a use point 7 from a branch pipe 6 through supply piping 11, and ozone in excess ozone water which is not taken out is decomposed by an ozone decomposing apparatus 8. In this way, the self-decomposition of ozone in ozone water is controlled to reduce its consumption so that ozone water of constant concentration can be supplied to a use point after long distance transportation.