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    • 11. 发明专利
    • Method for assembling electric deionizer
    • 装配电除尘器的方法
    • JP2003275769A
    • 2003-09-30
    • JP2002085822
    • 2002-03-26
    • Kurita Water Ind Ltd栗田工業株式会社
    • OSAWA KIMINOBUKATO OSAMUMORIBE TAKAYUKI
    • B01D61/48B01D12/00B01J47/06C02F1/469
    • Y02A20/134
    • PROBLEM TO BE SOLVED: To provide a method for assembling an electric deionizer which permits sure packing of a regulated amount of ion exchange resins into the electric deionizer, eliminates the deterioration of and damage to ion exchange membranes and ion exchange resins and eliminates the need for using the special high-strength ion exchange membranes.
      SOLUTION: The method for assembling the electric deionizer constructed by arraying the cation exchange membranes 6 and the anion exchange membranes 4 between a cathode plate 2 and an anode plate 9 to form concentrating chambers and desalting chambers and packing the ion exchange resins 5R into at least the desalting chambers comprises performing the packing of the ion exchange resins after removing 5 to 40% of the moisture included in the ion exchange resins in shipping the products of these resins on the occasion of packing the ion exchange resins therein.
      COPYRIGHT: (C)2003,JPO
    • 要解决的问题:提供一种组装电去离子的方法,其允许将规定量的离子交换树脂确实包装到电去离子中,消除离子交换膜和离子交换树脂的劣化和损坏,并消除 需要使用特殊的高强度离子交换膜。 解决方案:通过将阳离子交换膜6和阴离子交换膜4排列在阴极板2和阳极板9之间而构成的电去离子器的方法,以形成浓缩室和脱盐室,并将离子交换树脂5R 至少脱盐室包括在将离子交换树脂包装在其中的情况下,在运送这些树脂的产品之后,除去离子交换树脂中包含的5〜40%的水分后进行离子交换树脂的包装。 版权所有(C)2003,JPO
    • 12. 发明专利
    • Electric deionizing apparatus
    • 电动除尘装置
    • JP2003071456A
    • 2003-03-11
    • JP2001261708
    • 2001-08-30
    • Kurita Water Ind Ltd栗田工業株式会社
    • MORIBE TAKAYUKI
    • B01D61/48C02F1/469
    • PROBLEM TO BE SOLVED: To provide an electric deionizing apparatus enabling an increase in treatment flow rate and the reduction of manufacturing cost and capable of being also constituted so as to enhance durability.
      SOLUTION: A frame 20 has a rectangular shape, and a first desalting chamber 21 and a second desalting chamber 22 are formed on one half side and other half side in the long side direction of the frame. Introducing ports 31 and 32 of water to be treated are respectively arranged to the upper part of the desalting chamber 21 and the upper part of the desalting chamber 22 and outflow ports 41 and 42 of desalted water prepared by desalting water to be treated are respectively provided to the lower part of the desalting chamber 21 and the upper part of the desalting chamber 22. Openings 51 and 52 for forming water channels for guiding concentrated water to respective concentration chambers are provided to the upper part of the desalting chamber 21 and the lower part of the desalting chamber 22. An opening 53 for forming a water channel for taking out concentrated water from the respective concentration chambers is provided to a crossbeam part 54. A large number of the cation exchange membranes, the frames for forming the desalting chambers, anion exchange membranes and frames for forming the concentration chambers are laminated in this order.
      COPYRIGHT: (C)2003,JPO
    • 要解决的问题:提供能够提高处理流量和降低制造成本并且还可以构造以提高耐久性的电去离子装置。 解决方案:框架20具有矩形形状,并且第一脱盐室21和第二脱盐室22形成在框架的长边方向的一个半侧和另一半侧上。 引入待处理水的端口31和32分别设置在脱盐室21的上部,脱盐室22的上部和脱盐水的脱水口41和42分别设置在脱盐水处理 到脱盐室21的下部和脱盐室22的上部。用于形成用于将浓缩水引导到各浓缩室的水通道的开口51和52设置在脱盐室21的上部,下部 。用于形成用于从各浓缩室取出浓缩水的水通道的开口53设置在横梁部分54上。大量的阳离子交换膜,用于形成脱盐室的框架,阴离子 交换膜和用于形成浓缩室的框架按顺序层压。
    • 13. 发明专利
    • ELECTROLYTICALLY DEIONIZING DEVICE AND ITS OPERATION
    • JP2000229223A
    • 2000-08-22
    • JP2895599
    • 1999-02-05
    • KURITA WATER IND LTD
    • MORIBE TAKAYUKISATO SHIN
    • B01D61/46B01D61/52B01D61/54C02F1/469
    • PROBLEM TO BE SOLVED: To effectively suppress the deposition of scale in a concentration chamber by providing a means for controlling the temp. of water supplied to the concentration chamber to equal to or above a specific value in an electrolytically deionizing device constituted so as to alternately form the concentration chamber and a desalination chamber by alternately arranging plural anion exchange membranes and plural cation exchange membranes. SOLUTION: A part of raw water successively pretreated in an activated carbon column 1 and an RO membrane separation device 2 is supplied to a concentration chamber 3B of the electrolytically deionizing device 3, the remainder is supplied to the desalination chamber 3A and treated and the flow-out water from the desalination chamber 3A is taken out as a treated water (product water). On the other hand, a part of the flow-out water from the concentration chamber 3B is discharged out of the system and the remainder is circulated to the supply side of the concentration chamber 3B by a pump 6. The feed water, composed of the raw water and the circulated water, to the concentration chamber 3B is heated to >=25 deg.C by a heat exchanger 4, in which a hot water valve is opened and closed by being linked with a thermometer 5. As a result, the deposition of the scale in the concentration chamber 3B is effectively suppressed and stable operation is continued over a long period.
    • 18. 发明专利
    • PRODUCTION OF VEGETABLE JUICE
    • JPH11290041A
    • 1999-10-26
    • JP9635898
    • 1998-04-08
    • FUKUOKA PREFECTURE NOGYO KYODOKURITA WATER IND LTD
    • EJIMA HIROSHIMUTO YUKIMITSUMORIBE TAKAYUKIKATSUMATA TAKUYA
    • A23L2/02A23L2/78B01J41/04B01J49/00
    • PROBLEM TO BE SOLVED: To provide a method for efficiently carrying out the regeneration of an anion exchange resin, efficiently removing nitrate ions from a vegetable juice and producing the vegetable juice with a low content of the nitrate ions. SOLUTION: A stock solution (a pressed liquid) in a stock solution tank 6 is introduced from a gas-liquid inlet 28 into the upper part of a denitrating column 1 and passed through a resin bed 2 formed of a Cl-form strong basic anion exchange resin to remove nitrate ions. When the regeneration of the resin 2 is required, wash water is introduced from a gas-liquid introduction device 42 to backwash the resin 2 and feed the ion exchange resin into a regeneration column 3. A warm aqueous solution of sodium hydroxide in a downward stream is then passed from a water supply device 57 through the formed resin bed 56 to remove organic impurities sticking to the resin. An aqueous solution of sodium chloride is subsequently introduced from a tank 5 of the aqueous solution of sodium chloride into the regeneration column 3 and in a downward stream is passed from the water supply device 57 therethough to convert the resin into the Cl form. The regenerated resin is returned to the denitrating column 1 to repeat the denitrating treatment.