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    • 1. 发明专利
    • Ultrapure water production method and apparatus, and washing method and apparatus for electronic component members
    • 超声波水生产方法和装置,以及电子元件成员的洗涤方法和装置
    • JP2009112945A
    • 2009-05-28
    • JP2007288734
    • 2007-11-06
    • Kurita Water Ind Ltd栗田工業株式会社
    • HOTTA HITOSHIFUKUI NAGAOMORITA HIROSHI
    • C02F1/42H01L21/304
    • PROBLEM TO BE SOLVED: To provide an ultrapure water production apparatus which can stably produce ultrapure water having a boron concentration of 1 ng/L or less, and an ultrapure water production method and a washing method and apparatus for electronic component members using the ultrapure water production apparatus. SOLUTION: In the ultrapure water production apparatus where a mixed bed deionizer 16 with an anion exchange resin and a cation exchange resin is installed as the last-stage deionizer, an anion exchange resin the boron content of which has been confirmed to be equal to or less than the prescribed value is used as the anion exchange resin. Preferably the prescribed value is 50 μg/L-anion exchange resin (in a wet state). COPYRIGHT: (C)2009,JPO&INPIT
    • 解决的问题:提供一种能够稳定地制造硼浓度为1ng / L以下的超纯水的超纯水制造装置,以及超纯水制造方法以及使用电子部件的洗涤方法和装置 超纯水生产设备。 解决方案:在具有阴离子交换树脂和阳离子交换树脂的混合床去离子器16作为最后阶段的去离子器的超纯水生产装置中,其中硼含量已被确认为的阴离子交换树脂 等于或小于规定值用作阴离子交换树脂。 优选规定值为50μg/ L-阴离子交换树脂(处于湿态)。 版权所有(C)2009,JPO&INPIT
    • 3. 发明专利
    • Breakthrough time prediction method of non-regenerative ion-exchange resin device and maintenance method
    • 非再生离子交换树脂装置的延迟时间预测方法及维护方法
    • JP2012154634A
    • 2012-08-16
    • JP2011011063
    • 2011-01-21
    • Kurita Water Ind Ltd栗田工業株式会社
    • ISHIZUKA SATOSHIFUKUI NAGAOHORII SHIGEKIMIYAMOTO SHINGO
    • G01N30/00C02F1/42G01N30/64G01N30/88
    • PROBLEM TO BE SOLVED: To provide a breakthrough time prediction method of non-regenerative ion-exchange resin device with high prediction accuracy, and a maintenance method for an ion-exchange resin device based on the method.SOLUTION: A method to predict breakthrough time of a non-regenerative ion-exchange resin device 2 with a column filled with an ion-exchange resin includes: a step for arranging the non-regenerative ion-exchange resin device 2 in parallel with small-sized resin columns 3A and 3B with smaller columns than the column filled with ion-exchange resins identical to the ion-exchange resin; a step for running processed water through the small-sized resin columns 3A and 3B; and a step for predicting the breakthrough time of the non-regenerative ion-exchange resin device 2 based on data of the processed water of the small-sized resin columns.
    • 要解决的问题:提供一种具有高预测精度的非再生离子交换树脂装置的突破性时间预测方法,以及基于该方法的离子交换树脂装置的维护方法。 解决方案:用填充有离子交换树脂的柱来预测非再生离子交换树脂装置2的穿透时间的方法包括:并行地布置非再生离子交换树脂装置2的步骤 具有比填充有与离子交换树脂相同的离子交换树脂的柱更小的柱的小尺寸树脂柱3A和3B; 通过小型树脂柱3A和3B运行加工水的步骤; 以及基于小型树脂柱的处理水的数据来预测非再生离子交换树脂装置2的突破时间的步骤。 版权所有(C)2012,JPO&INPIT
    • 4. 发明专利
    • Washing method for ultrapure water production system
    • 超声波水生产系统的洗涤方法
    • JP2011161418A
    • 2011-08-25
    • JP2010030286
    • 2010-02-15
    • Kurita Water Ind Ltd栗田工業株式会社
    • FUKUI NAGAOMORITA HIROSHI
    • C02F1/44B01D65/00B08B3/08B08B9/027C02F1/20C02F1/42C02F9/00
    • PROBLEM TO BE SOLVED: To provide a washing method for ultrapure water production system, removing metal impurities from an ultrapure water production system with high efficiency and shortening washing time. SOLUTION: Hydrochloric acid is added into a primary pure water tank 21, circulated in a heat exchanger 23, an ultraviolet ray oxidation treatment apparatus 24, bypass lines 30, 31, 32, a flow path 6a, a use point 4 and a flow path 6b by a pump 22 in the order and then placed under an immersed state. Subsequently, the inside of the tank 21 is filled with primary pure water. Next, the primary pure water is passed in the same order, and washing liquid is discharged from the terminal of the flow path 6b to the system outside. In performing pickling, a degassing apparatus 25, an ion exchange resin tower 26, and a UF apparatus 27 are bypassed. By bypassing the UF apparatus 27, extrusion washing time of hydrochloric acid-containing liquid is shortened. COPYRIGHT: (C)2011,JPO&INPIT
    • 要解决的问题:为了提供超纯水生产系统的洗涤方法,从超纯水生产系统中以高效率和缩短洗涤时间去除金属杂质。 解决方案:将盐酸加入初级纯水槽21中,在热交换器23中循环,紫外线氧化处理装置24,旁通管线30,31,32,流路6a,使用点4和 通过泵22按顺序流过流路6b,然后放置在浸没状态。 随后,罐21的内部填充有初级纯水。 接下来,一次纯水以相同的顺序通过,洗涤液从流路6b的端子排出到系统外部。 在进行酸洗时,旁路脱气装置25,离子交换树脂塔26和UF装置27。 通过绕开UF装置27,含盐酸液体的挤出洗涤时间缩短。 版权所有(C)2011,JPO&INPIT
    • 6. 发明专利
    • Ion exchanger
    • 离子交换器
    • JP2012205994A
    • 2012-10-25
    • JP2011072519
    • 2011-03-29
    • Kurita Water Ind Ltd栗田工業株式会社
    • FUKUI NAGAOISHIZUKA SATOSHIMIYAZAKI YOICHI
    • C02F1/42B01J49/00
    • PROBLEM TO BE SOLVED: To provide an ion exchanger which can surely prevent an anion exchange resin and a cation exchange resin from being reversely regenerated and can produce deionized water of high water quality even immediately after regeneration.SOLUTION: During regeneration, a valve 12 is closed and valves 7, 10 are opened and an alkaline solution is supplied from an upper supply/discharge pipe 3 and further an acid solution is supplied from a third communication pipe 8. The alkaline solution flows through a water collection/delivery member 4, an inactive resin 22, an anion exchange resin 21, a glass bead 23, a water collection/delivery member 6, a communication pipe 5 and a valve 7 in order to regenerate the anion exchange resin 21. The acid solution flows through a water collection/delivery member 9, an inactive resin 32, an alkali exchange resin 31, a water collection/delivery member 14, a glass bead 33 and a lower supply/discharge pipe 13 in order to regenerate the cation exchange resin 31.
    • 要解决的问题:提供一种离子交换剂,其可以确实地防止阴离子交换树脂和阳离子交换树脂反向再生,并且即使在再生之后立即也能够产生高水质的去离子水。 解决方案:在再生期间,关闭阀12并打开阀门7,10,并且从上部供给/排出管3供给碱性溶液,并且还从第三连通管8供给酸溶液。碱性 溶液流过收集/释放构件4,惰性树脂22,阴离子交换树脂21,玻璃珠23,集水/排出构件6,连通管5和阀7,以便再生阴离子交换 树脂21。酸溶液流过收集/输送构件9,非活性树脂32,碱交换树脂31,收水/输送构件14,玻璃珠33和下供排管13,以便 再生阳离子交换树脂31.版权所有(C)2013,JPO&INPIT
    • 7. 发明专利
    • Ion exchange apparatus and column body thereof
    • 离子交换装置及其柱体
    • JP2012205993A
    • 2012-10-25
    • JP2011072518
    • 2011-03-29
    • Kurita Water Ind Ltd栗田工業株式会社
    • FUKUI NAGAOISHIZUKA SATOSHIMIYAZAKI YOICHI
    • B01J47/02B01J49/00C02F1/42
    • PROBLEM TO BE SOLVED: To provide an ion exchange apparatus, in the column body of which an anion exchange resin and a cation exchange resin can surely be prevented from being regenerated reversely and high-quality deionized water can be produced even immediately after the regeneration is performed and to provide the column body of the ion exchange apparatus.SOLUTION: When the regeneration is performed, valves 12, 17 are closed, valves 7, 10 are opened, an alkaline solution is supplied through an upper supply/discharge pipeline 3 and an acidic solution is supplied through a third communication pipeline 8. The alkaline solution is made to flow through a collection/delivery water member 4, an inactive resin 22, the anion exchange resin 21, a collection/delivery water member 6, a communication pipeline 5 and the valve 7 in this order to regenerate the anion exchange resin 21. The acidic solution is made to flow through a collection/delivery water member 9, an inactive resin 32, the cation exchange resin 31, a collection/delivery water member 14 and a lower supply/discharge pipeline 13 in this order to regenerate the cation exchange resin 31. When a rinsing is performed after the regeneration is performed, water is supplied through the pipelines 5, 13, waste cleaning water is discharged through the pipelines 3, 8 and simultaneously the valve 17 is opened and the waste cleaning water is also discharged through a withdrawal pipe 18 at the top of the column body to promote the withdrawal of a chemical in the top thereof.
    • 要解决的问题:为了提供一种离子交换装置,可以确定地防止阴离子交换树脂和阳离子交换树脂反向再生的柱体中,甚至可以立即产生高品质的去离子水 进行再生并提供离子交换装置的柱体。 解决方案:当进行再生时,关闭阀12,17,打开阀门7,10,通过上部供给/排放管线3供给碱性溶液,通过第三连通配管8供给酸性溶液 使碱性溶液依次流过收集/输送水构件4,惰性树脂22,阴离子交换树脂21,收集/输送水构件6,连通管线5和阀7,以再生 阴离子交换树脂21.使酸性溶液依次流过收集/输送水部件9,非活性树脂32,阳离子交换树脂31,收集/输送水部件14和下部供应/排出管线13 以再生阳离子交换树脂31.当进行再生后进行漂洗时,通过管线5,13供给水,废水通过管道3,8排出,同时阀 e 17打开,废水清洗水也通过柱体顶部的抽出管18排出,以促进化学品在其顶部的排出。 版权所有(C)2013,JPO&INPIT
    • 8. 发明专利
    • Ion exchange device
    • 离子交换装置
    • JP2011189317A
    • 2011-09-29
    • JP2010059390
    • 2010-03-16
    • Kurita Water Ind Ltd栗田工業株式会社
    • FUKUI NAGAOMIYAZAKI YOICHIKITAMI KATSUNOBU
    • C02F1/42
    • PROBLEM TO BE SOLVED: To provide an ion exchange device which can prevent scale deposition onto an anion exchange resin in a column, can surely prevent an anion-exchange resin and a cation-exchange resin from being reversely regenerated, and can stably produce deionized water of high water quality even immediately after regeneration, and a column for the ion exchange device. SOLUTION: After raw water containing hardness components is passed through a hardness component removing means 1 to remove the hardness components, the water is supplied to an ion exchange column 2 to be brought into contact with the anion-exchange resin 31, then to be brought into contact with the cation-exchange resin 21. The inside of the ion exchange column 2 is divided into upper and lower two chambers by an impervious partition plate 2a, and the water brought into contact with the anion-exchange resin 31 in the lower chamber is passed through external piping and then introduced into the upper chamber. COPYRIGHT: (C)2011,JPO&INPIT
    • 要解决的问题:为了提供能够防止在柱中的阴离子交换树脂上的结垢的离子交换装置,可以可靠地防止阴离子交换树脂和阳离子交换树脂的反向再生,并且可以稳定地 即使在再生后立即生成高水质的去离子水,也可以生成离子交换装置用的柱。 解决方案:将含有硬度成分的原水通过硬度成分除去装置1以除去硬度成分后,将水供给到离子交换柱2以与阴离子交换树脂31接触,然后 与阳离子交换树脂21接触。离子交换柱2的内部由不透水隔板2a分成上下两个室,水与阴离子交换树脂31接触 下腔通过外部管道,然后引入上腔室。 版权所有(C)2011,JPO&INPIT
    • 9. 发明专利
    • Method and apparatus for supplying ozone water
    • 供应臭氧水的方法和装置
    • JP2005294377A
    • 2005-10-20
    • JP2004104505
    • 2004-03-31
    • Kurita Water Ind Ltd栗田工業株式会社
    • FUKUI NAGAOIDA JUNICHIMORITA HIROSHI
    • C02F1/02B08B3/08C01B13/10C02F1/32C02F1/34C02F1/36C02F1/70C02F1/72C02F1/78C03C23/00H01L21/027H01L21/304
    • C02F1/78B08B3/08B08B2203/005C01B13/10C02F1/02C02F1/32C02F1/34C02F1/36C02F1/70C02F1/722C02F2201/782C02F2209/23C03C23/0075
    • PROBLEM TO BE SOLVED: To provide an ozone water supplying method and an ozone water supplying apparatus for stably supplying the ozone water of the predetermined ozone concentration to use points in a wet cleaning process for electronic materials such as a semiconductor and liquid crystal and in a surface processing process.
      SOLUTION: The ozone water including ozone decomposition control substance is supplied to use points, and ozone concentration is lowered to the predetermined concentration with a concentration adjusting means at the areas near the use points. The ozone water supplying apparatus comprises an ozone dissolving apparatus for adjusting the ozone water by dissolving the ozone gas into the pure water, a means for supplying the ozone decomposition control substance to the pure water or ozone water, an ozone water transferring pipe for transferring the ozone water adjusted by the ozone dissolving apparatus to the use points, and a concentration adjusting means provided to the area near the use points to lower the concentration of the ozone water transferred with the ozone water transferring pipe to the predetermined ozone concentration.
      COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题:为了提供臭氧水供应方法和臭氧供水装置,用于将预定臭氧浓度的臭氧水稳定地供给到用于诸如半导体和液晶的电子材料的湿式清洗工艺中的使用点 并在表面处理过程中。 解决方案:将含臭氧分解控制物质的臭氧水供应到使用点,并且在使用点附近的区域用浓度调节装置将臭氧浓度降低至预定浓度。 臭氧水供给装置包括臭氧溶解装置,用于通过将臭氧气体溶解到纯水中来调节臭氧水,将臭氧分解控制物质供应到纯水或臭氧水的装置,用于将臭氧水输送到纯水或臭氧水的臭氧水输送管 通过臭氧溶解装置调节的臭氧水到使用点,以及设置在使用点附近的区域的浓度调节装置,以将臭氧水输送管转移的臭氧水的浓度降低到预定的臭氧浓度。 版权所有(C)2006,JPO&NCIPI