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公开(公告)号:KR1020100075839A
公开(公告)日:2010-07-05
申请号:KR1020107005808
申请日:2008-10-23
申请人: 가부시키가이샤 신꼬오 간쿄우 솔루션
CPC分类号: B01D61/025 , B01D61/12 , B01D2311/24 , C02F1/008 , C02F1/441 , C02F9/00 , C02F2103/002 , C02F2103/08 , C02F2209/001 , C02F2209/003 , C02F2209/04 , C02F2209/05 , C02F2209/06 , C02F2209/40 , C02F2301/043 , Y02A20/131
摘要: This invention provides a water treatment method which can produce a treated water having a given level of quality. The water treatment method comprises allowing a raw water to flow into a membrane separation module using a reverse osmosis membrane to separate the water into a treated water and a concentrated water. The water treatment method is characterized in that the impurities of the raw water, the treated water or the concentrated water are measured and the quality of the treated water is regulated based on the measured impurity value.
摘要翻译: 本发明提供一种水处理方法,其可以产生具有给定质量水平的处理水。 水处理方法包括使用反渗透膜将原水流入膜分离组件,将水分离成处理水和浓缩水。 水处理方法的特征在于,测量原水,处理水或浓缩水的杂质,并根据测得的杂质值调节处理水的质量。
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公开(公告)号:KR1020120002522A
公开(公告)日:2012-01-05
申请号:KR1020117019458
申请日:2010-03-26
申请人: 쿠리타 고교 가부시키가이샤
IPC分类号: H01L21/67 , H01L21/306 , B01D61/12 , B01D61/22 , B01D61/58 , H01L31/0236 , B01D61/02 , B01D61/14 , C02F1/66 , C02F11/12
CPC分类号: H01L21/30604 , B01D61/027 , B01D61/12 , B01D61/145 , B01D61/22 , B01D61/58 , B01D2311/06 , C02F1/52 , C02F1/66 , C02F11/12 , C02F2001/5218 , C02F2103/346 , Y02W10/37 , H01L21/67075 , H01L31/0236 , B01D2311/12 , B01D2311/24 , B01D2311/18 , B01D2311/243 , B01D2311/10
摘要: 에칭액의 교환 빈도를 감소시킬 수 있음과 함께, 처리된 에칭액 중에 불순물이 혼입되는 것도 방지되는 에칭액의 처리 장치 및 에칭액의 처리 방법. 실리콘을 에칭 처리한 에칭액을 순환 재이용하기 위한 에칭액의 처리 장치로서, 에칭조 (2) 로부터의 에칭액을 막 처리하는 막 분리 수단 (3) 과, 그 막 분리 수단 (3) 의 막 투과액을 그 에칭조에 순환시키는 순환 수단 (6) 을 구비한다. 상기 막 분리 수단 (3) 은 UF 막 모듈 (4) 과 NF 막 모듈 (5) 을 갖는다. 막 투과액에 알칼리 및 유기물을 첨가해도 된다.
摘要翻译: 一种用于处理蚀刻溶液的设备和方法,其中蚀刻溶液的替换频率降低,同时防止在处理的蚀刻溶液中包含杂质。 一种用于处理蚀刻溶液的装置,以便重新利用硅蚀刻处理中使用的蚀刻溶液,其中该装置包括:对从蚀刻浴2供应的蚀刻溶液进行膜分离处理的膜分离装置3; 以及将从膜分离装置3供给的渗透液循环到蚀刻槽2的循环装置6.膜分离装置3包括UF膜组件4和NF膜组件5.碱性和有机物质可以添加到蚀刻 从膜分离装置3供应的溶液。
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公开(公告)号:KR100766885B1
公开(公告)日:2007-10-18
申请号:KR1020060034151
申请日:2006-04-14
申请人: 신윤호
发明人: 신윤호
IPC分类号: G06F19/00
CPC分类号: B01D63/02 , B01D61/145 , B01D61/18 , B01D61/22 , B01D2311/24 , B01D2315/06 , C02F1/444 , G01N33/18
摘要: An ultra filtration system for an online analyzer is provided to enable the online analyzer to stably perform a quantitative analysis of a sample containing lots of suspended solids by filtrating the solid contents with an absorption mode using a hollow fiber filter. A single way first value(31) is formed to a first pipe(21) connected to a first pump(11) for pumping the sample(1). A hollow fiber filter module(70) is formed to another end of the first pipe. A second/third pipe(83,22) is connected to an upper part of a module housing. A pipe(103) penetrating a lower part of the module housing is connected to the second pipe and value(85). The third pipe is connected to a single way third value(32). A fourth pipe(23) connected to a lower tank(73) of the module is connected to a two-way fourth/fifth valve(33,34) through the fifth/ninth pipe(104). The fifth pipe is connected to a first flow meter(61) and a second pump, and a two-way fifth valve is connected to an end part of the fifth pipe. An eighth pipe(82) is connected to a lower end of a sample tank(40) connected to a seventh pipe(24), which is connected to another end of the fifth valve, through a third pump(12). The analyzer(50) precisely measures the sample through the module by pumping up the sample through a tenth pipe(81) connected to the sample tank.
摘要翻译: 提供一种用于在线分析仪的超滤系统,使在线分析仪能够通过使用中空纤维过滤器以吸收模式过滤固体内容物来稳定地对含有大量悬浮固体的样品进行定量分析。 单向第一值(31)形成于与第一泵(11)连接的用于泵送样品(1)的第一管(21)。 中空纤维过滤器模块(70)形成在第一管的另一端。 第二/第三管(83,22)连接到模块外壳的上部。 穿过模块壳体的下部的管道(103)连接到第二管道和值(85)。 第三管连接到单向第三值(32)。 连接到模块的下箱(73)的第四管(23)通过第五/第九管(104)连接到双向第四/第五阀(33,34)。 第五管连接到第一流量计(61)和第二泵,并且二通第五阀连接到第五管的端部。 第八管(82)连接到通过第三泵(12)连接到与第五阀的另一端连接的第七管(24)的样品罐(40)的下端。 分析器(50)通过将样品泵送通过连接到样品罐的第十管(81)来精确地测量样品通过模块。
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公开(公告)号:KR1020140054670A
公开(公告)日:2014-05-09
申请号:KR1020120120432
申请日:2012-10-29
申请人: 도레이케미칼 주식회사 , 한국수자원공사
CPC分类号: B01D65/02 , B01D2311/24 , B01D2321/16 , B01D2321/185 , B01D2321/40 , C02F1/44
摘要: A membrane filtration process system using a membrane fouling index according to the present invention is a system that is configured to include a mixing tank and a flocculation tank, a sedimentation tank, and a membrane filtration tank and controls chemical cleaning by measuring a membrane fouling index of the membrane filtration tank. The system includes a measuring unit that performs real-time monitoring and measurement of the resistance and trans-membrane pressure of the membrane filtration tank; a calculation unit that calculates a momentary rate of change of the trans-membrane pressure measured by the measuring unit, and calculates a membrane fouling index of the membrane filtration tank corresponding thereto; a control unit that analyzes the momentary rate of change of the trans-membrane pressure calculated in real time and the membrane fouling index so as to set a cleaning mode corresponding thereto; and a CIP tank portion that injects a chemical into treated water and pumps the treated water and transports the treated water to the membrane filtration tank in a case where the cleaning mode which is set in the control unit is a chemical cleaning mode. According to the present invention, the membrane fouling index is calculated in real time by using the momentary rate of change of the trans-membrane pressure, and the optimal chemical cleaning (clean in place, CIP) can be selectively performed according to the calculated membrane fouling index.
摘要翻译: 根据本发明的使用膜污染指数的膜过滤系统是一种被配置为包括混合槽和絮凝罐,沉淀池和膜过滤罐的系统,并通过测量膜污染指数来控制化学清洗 的膜过滤罐。 该系统包括一个测量单元,对膜过滤罐的电阻和跨膜压力进行实时监测和测量; 计算单元,计算由测量单元测量的跨膜压力的瞬时变化率,并计算与其对应的膜过滤罐的膜污染指数; 控制单元,其分析实时计算的跨膜压力的瞬时变化率和膜污染指数,以设定与其对应的清洁模式; 以及在设置在控制单元中的清洁模式是化学清洁模式的情况下,将处理过的水喷射到处理过的水并将处理过的水输送到膜过滤罐的CIP罐部分。 根据本发明,通过使用跨膜压力的瞬时变化率实时计算膜污染指数,并且可以根据计算的膜选择性地进行最佳化学清洁(就地清洁,CIP) 污染指数
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公开(公告)号:KR101354403B1
公开(公告)日:2014-01-22
申请号:KR1020117024505
申请日:2009-06-26
申请人: 아사히 가세이 케미칼즈 가부시키가이샤
CPC分类号: B01D61/22 , B01D61/14 , B01D65/02 , B01D2311/14 , B01D2311/16 , B01D2311/24 , B01D2321/04 , C02F1/444 , C02F2209/001 , C02F2209/005 , C02F2209/03 , C02F2209/11 , C02F2209/20 , C02F2209/40
摘要: 막모듈에 대하여 압력을 구동력으로 하는 여과 운전을 실행함으로써, 원수를 여과하여 여과수를 얻는 여과 방법으로서, 상기 여과 운전은, 원수측 가압 여과와, 여과수측 감압 여과와, 상기 원수측 가압 여과 및 상기 여과수측 감압 여과를 조합한 복합 여과의 3가지 양태를 포함하고, 원수측 수질, 막여과 유속, 막차압의 하나 이상을 측정하고, 측정치에 따라서, 상기 3가지 양태 중 어느 하나의 여과로부터 다른 여과로 전환하는 것을 특징으로 하는 여과 방법.
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公开(公告)号:KR101333243B1
公开(公告)日:2013-11-26
申请号:KR1020087010854
申请日:2006-10-06
申请人: 파이오네틱스 코포레이션
发明人: 니버그,에릭데이비드 , 보그데스,크리스틴엘렌 , 홀메스,제임스크로포드 , 자나흐,아쇼크쿠마르
CPC分类号: C02F1/4695 , B01D61/44 , B01D61/54 , B01D2311/24 , C02F1/001 , C02F1/283 , C02F1/32 , C02F1/441 , C02F1/4602 , C02F1/46109 , C02F1/4672 , C02F1/469 , C02F1/4693 , C02F2001/422 , C02F2001/425 , C02F2001/46152 , C02F2201/003 , C02F2201/46115 , C02F2201/46125 , C02F2201/4613 , C02F2201/46145 , C02F2201/4616 , C02F2209/02 , C02F2209/03 , C02F2209/05 , C02F2209/40 , C02F2301/026 , C02F2301/043 , C02F2303/04 , C02F2303/16 , Y02A20/131 , Y02A20/134
摘要: 유체를 처리하기 위한 유체 처리 장치(100)는 유체를 수용하고 배출하기 위한 유체 오리피스를 갖는 전기화학적 셀(102)을 포함하며, 물-분해 이온교환막(110)과 오리피스를 연결하는 유체 통로는 통로에서 유체에 노출된다. 제 1 전극 및 제 2 전극(106,108)은 막(110) 주변에 위치된다. 장치는 또한 전력공급원(114) 및 밸브 시스템(118)을 제어하고 작동시키기 위한 제어기(170)를 포함한다. 전력공급원(114)은 유체 중의 미생물의 세균발육억제, 비활성화 또는 감소를 초래하기에 충분히 높은 전류 밀도에서 제 1 전극 및 제 2 전극(106,108)에 전류를 공급한다. 제어기(170)는 또한 유체를 탈이온화시키고 셀을 재생하기 위해 셀의 세트를 작동시킬 수 있다.
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公开(公告)号:KR1020100007873A
公开(公告)日:2010-01-22
申请号:KR1020097023283
申请日:2008-04-04
申请人: 닛토덴코 가부시키가이샤
CPC分类号: B01D61/025 , B01D61/12 , B01D65/02 , B01D65/10 , B01D2311/04 , B01D2317/04 , B01D2321/162 , C02F1/441 , B01D2311/24
摘要: A method of membrane separation and membrane separation apparatus, with which not only a supply liquid can be evaluated but also the problems, such as scale, occurring on reverse osmosis membrane can be monitored in a highly straightforward fashion. There is provided a membrane separation apparatus equipped with reverse osmosis membrane module (3) so as to be adapted for feeding of a supply liquid and obtaining of a permeated liquid and a concentrated liquid, characterized by comprising a feeding-side membrane separation means (10) which includes a separation membrane (11) of which the membrane face (11a) can be monitored and guides the supply liquid so as to separate the membrane, and a concentrating-side membrane separation means (20) which includes a separation membrane (21) of which the membrane face (21a) can be monitored and guides the concentrated liquid so as to separate the membrane separation thereof.
摘要翻译: 一种膜分离和膜分离装置的方法,不仅可以评估供应液体,而且可以以非常直接的方式监测反渗透膜上发生的尺度等问题。 提供一种装有反渗透膜组件(3)的膜分离装置,以适于供给供给液体并获得渗透液体和浓缩液体,其特征在于,包括进料侧膜分离装置(10 ),其包括可以监测所述膜面(11a)的分离膜(11)并引导所述供给液体以分离所述膜;以及浓缩侧膜分离装置(20),其包括分离膜(21) ),其中可以监测膜面(21a)并引导浓缩液体以分离其膜分离。
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公开(公告)号:KR1020080056284A
公开(公告)日:2008-06-20
申请号:KR1020087010854
申请日:2006-10-06
申请人: 파이오네틱스 코포레이션
发明人: 니버그,에릭데이비드 , 보그데스,크리스틴엘렌 , 홀메스,제임스크로포드 , 자나흐,아쇼크쿠마르
CPC分类号: C02F1/4695 , B01D61/44 , B01D61/54 , B01D2311/24 , C02F1/001 , C02F1/283 , C02F1/32 , C02F1/441 , C02F1/4602 , C02F1/46109 , C02F1/4672 , C02F1/469 , C02F1/4693 , C02F2001/422 , C02F2001/425 , C02F2001/46152 , C02F2201/003 , C02F2201/46115 , C02F2201/46125 , C02F2201/4613 , C02F2201/46145 , C02F2201/4616 , C02F2209/02 , C02F2209/03 , C02F2209/05 , C02F2209/40 , C02F2301/026 , C02F2301/043 , C02F2303/04 , C02F2303/16 , Y02A20/131 , Y02A20/134
摘要: A fluid treatment apparatus (100) for treating a fluid comprises an electrochemical cell (102) having fluid orifices (124, 125) to receive and release fluid, and a fluid passageway connecting the orifices with a water-splitting ion exchange membrane (110) is exposed to the fluid in the passageway. First and second electrodes (106, 108) are positioned about the membrane (110). The apparatus also comprises a controller (170) to control and operate a power supply (114) and valve system (118). The power supply (114) supplies a current to the first and second electrodes (106, 108) at sufficiently high current density to result in bacteriostasis, deactivation, or a reduction in the microorganisms in the fluid. The controller (170) can also operate a set of cells to deionize fluid and regenerate the cells.
摘要翻译: 用于处理流体的流体处理装置(100)包括具有用于接收和释放流体的流体孔(124,125)的电化学电池(102),以及将孔与水分解离子交换膜(110)连接的流体通道, 暴露于通道中的流体。 第一和第二电极(106,108)围绕膜(110)定位。 该装置还包括用于控制和操作电源(114)和阀门系统(118)的控制器(170)。 电源(114)以足够高的电流密度向第一和第二电极(106,108)提供电流,以导致流体中微生物的抑菌,失活或减少。 控制器(170)还可以操作一组细胞以使流体去离子并再生细胞。
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公开(公告)号:KR1020180092586A
公开(公告)日:2018-08-20
申请号:KR1020170018467
申请日:2017-02-10
申请人: 한국과학기술원
CPC分类号: B01D65/10 , B01D61/002 , B01D61/005 , B01D65/08 , B01D2311/24 , C02F1/445
摘要: 본발명은하수처리를위한삼투가진행됨에따라바이오파울링이형성되는분리막의오염정도를모니터링하는장치의동작방법으로써, 빛이조사된상기분리막표면을촬영한영상데이터를수신하는단계, 그리고상기영상데이터에서상기바이오파울링으로인해가시광을발하는면적을계산하고, 상기분리막의전체면적대비상기계산된형광면적의변화정보를이용하여막 오염정도를모니터링하는단계를포함한다.
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公开(公告)号:KR101704376B1
公开(公告)日:2017-02-08
申请号:KR1020117019458
申请日:2010-03-26
申请人: 쿠리타 고교 가부시키가이샤
IPC分类号: H01L21/67 , H01L21/306 , B01D61/12 , B01D61/22 , B01D61/58 , H01L31/0236 , B01D61/02 , B01D61/14 , C02F1/66 , C02F11/12
CPC分类号: H01L21/30604 , B01D61/027 , B01D61/12 , B01D61/145 , B01D61/22 , B01D61/58 , B01D2311/06 , C02F1/52 , C02F1/66 , C02F11/12 , C02F2001/5218 , C02F2103/346 , Y02W10/37 , B01D2311/12 , B01D2311/24 , B01D2311/18 , B01D2311/243 , B01D2311/10
摘要: 에칭액의교환빈도를감소시킬수 있음과함께, 처리된에칭액중에불순물이혼입되는것도방지되는에칭액의처리장치및 에칭액의처리방법. 실리콘을에칭처리한에칭액을순환재이용하기위한에칭액의처리장치로서, 에칭조 (2) 로부터의에칭액을막 처리하는막 분리수단 (3) 과, 그막 분리수단 (3) 의막 투과액을그 에칭조에순환시키는순환수단 (6) 을구비한다. 상기막 분리수단 (3) 은 UF 막모듈 (4) 과 NF 막모듈 (5) 을갖는다. 막투과액에알칼리및 유기물을첨가해도된다.
摘要翻译: 一种用于处理蚀刻溶液的设备和方法,其中蚀刻溶液的替换频率降低,同时防止在处理的蚀刻溶液中包含杂质。 一种用于处理蚀刻溶液的装置,以便重新利用硅蚀刻处理中使用的蚀刻溶液,其中该装置包括:对从蚀刻浴2供应的蚀刻溶液进行膜分离处理的膜分离装置3; 以及将从膜分离装置3供给的渗透液循环到蚀刻槽2的循环装置6.膜分离装置3包括UF膜组件4和NF膜组件5.碱性和有机物质可以添加到蚀刻 从膜分离装置3供应的溶液。
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