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公开(公告)号:CN101939068A
公开(公告)日:2011-01-05
申请号:CN200980104513.4
申请日:2009-02-06
Applicant: 美国达拉斯集团公司
Inventor: 詹姆斯·R·芒森 , 布莱恩·S·库克 , 布莱恩·L·贝特拉姆
IPC: B01D15/00
CPC classification number: B01D15/00 , B01D15/361 , B01J20/10 , B01J20/12 , B01J20/3433 , B01J20/3475 , B01J39/04 , B01J41/04 , B01J49/05 , B01J2220/58 , C07C67/56 , C10G2300/1014 , C10G2300/205 , C10G2300/4081 , C10G2300/44 , C10L1/026 , Y02E50/13 , Y02P30/20 , C07C69/52 , C07C69/24 , B01D15/265
Abstract: 描述了使用粉末状、粒状或挤压的吸附剂的快速、经济环保、绿色的连续纯化生物柴油(脂肪酸烷酯(FAAE))的方法。所述吸附剂被包含在柱系统中并可再生重复利用多次。所述方法利用包含在柱中的吸附剂诸如但不限于碳、二氧化硅、粘土、沸石或金属硅酸盐以连续的工艺从脂肪酸烷酯(FAAE)或原生物柴油除去杂质。该方法使用吸附柱系统来纯化生物柴油,而非用水或过滤来纯化,将存在于生物柴油中的皂类和其它杂质除去。原生物柴油与填充到柱中或串联的多个柱中的吸附剂接触足够长的时间,除去杂质,诸如但不限于皂类、金属、游离的甘油、甾醇糖苷和许多其它的降低生物柴油稳定性的杂质。得到的成品生物柴油从柱排出,准备进行甲醇回收工艺。一旦吸附剂不再除去期望量的杂质,将其再生以重复利用。通过将用于再生方法的溶剂循环回酯交换反应来再生和再利用。
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公开(公告)号:CN101213021A
公开(公告)日:2008-07-02
申请号:CN200680020974.X
申请日:2006-03-07
Applicant: 西门子水处理技术控股公司
CPC classification number: B01D61/48 , B01D61/52 , B01D2321/16 , B01J47/08 , B01J49/05 , C02F1/4602 , C02F1/4695 , C02F2303/16
Abstract: 本公开总的涉及电净化含物类如矿物、盐、离子、有机物等的液体的方法、系统和装置。本发明的一方面提供了在电净化装置内再生介质的方法,例如使介质暴露于一种或多种洗脱溶液中和/或通过使介质暴露于一定的洗脱条件下而从介质选择性地脱附离子、有机物和/或其他物类。另一方面,本发明提供了从待净化的液体中选择性地除去一种或多种离子、有机物和/或其他物类的方法,例如通过选择性地从溶液中除去能易于沉淀和/或引起结垢或污染发生的一种或多种离子或有机物等。再另一方面,本发明提供了用电净化装置以连续或半连续方式处理含离子、有机物和/或其他物类的溶液并同时也进行装置内所含介质的再生的方法。
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公开(公告)号:CN1177649C
公开(公告)日:2004-12-01
申请号:CN01815261.9
申请日:2001-10-10
Applicant: 普里泰克有限责任公司
Inventor: 菲利普·罗谢特
CPC classification number: F16K11/085 , B01J47/00 , B01J47/11 , B01J49/05
Abstract: 本发明涉及一种流体处理装置,该流体处理装置包含布料装置(2),它具有在固定壳体(13)内的旋转盘(12);以及马达(15),用于旋转旋转盘(12)。进料和排出管(3、5、6;4、7、8)连接至壳(13)的端壁,并通至旋转盘(12)。固定容器(1)通过连接管(10、11)连接至所述壳(13)。在旋转盘(12)中设置有通道(44-49),它们通至盘(12)的圆形外侧面。对于此盘(12)的若干位置,每条通道(44-49)均连至一条上述连接管(10、11),而进料管(3、5、6)和排出管(4、7、8)则通过孔道(24、29、30、50-52和37-38、53-55)通入不同的通道(44-49)。
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公开(公告)号:WO02038254A1
公开(公告)日:2002-05-16
申请号:PCT/US2001/043657
申请日:2001-11-09
CPC classification number: B01D65/08 , B01D61/00 , B01D61/145 , B01D61/147 , B01D61/16 , B01D2311/04 , B01D2311/2607 , B01D2311/2623 , B01D2315/06 , B01D2321/185 , B01J20/28009 , B01J49/00 , B01J49/05 , C02F1/42 , C02F1/444
Abstract: An apparatus and method for the treatment and purification of drinking water combines the use of ion-exchange resin and a membrane filter (12) in a single process tank (14). The ion-exchange resin is removed from the process tank (14) and regenerated in column (24) for reuse.
Abstract translation: 用于处理和净化饮用水的装置和方法将离子交换树脂和膜过滤器(12)的使用结合在一个处理罐(14)中。 将离子交换树脂从处理罐(14)中取出并在柱(24)中再生以再利用。
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公开(公告)号:JP2010022923A
公开(公告)日:2010-02-04
申请号:JP2008186235
申请日:2008-07-17
Applicant: Mitsubishi Chemicals Corp , 三菱化学株式会社
Inventor: SUMI YOSHIYUKI , FUKUI KATSUHIKO , MIYAMOTO TETSUJI , MINEMOTO KOKI
CPC classification number: B01J31/403 , B01J31/2239 , B01J45/00 , B01J49/05 , B01J49/50 , B01J2231/70 , B01J2531/72 , B01J2531/845 , C02F1/28 , C02F1/42 , C02F1/683 , C02F2101/20 , C02F2209/02 , C02F2303/16
Abstract: PROBLEM TO BE SOLVED: To provide a wastewater treatment method which enables the efficient recovery of heavy metal compounds derived from an aromatic carboxylic acid production process from wastewater containing the heavy compounds. SOLUTION: In the wastewater treatment method, the wastewater derived from the aromatic carboxylic acid production process is brought into contact with a chelate resin to recover the heavy metal compounds contained in the wastewater into the chelate resin, and the chelate resin comprises particles having a uniform coefficient of 1.4 or less. COPYRIGHT: (C)2010,JPO&INPIT
Abstract translation: 要解决的问题:提供一种废水处理方法,其能够从含有重质化合物的废水中有效地回收由芳族羧酸生产方法衍生的重金属化合物。 解决方案:在废水处理方法中,将来自芳族羧酸生产过程的废水与螯合树脂接触以将废水中所含的重金属化合物回收到螯合树脂中,并且螯合树脂包含颗粒 具有1.4或更小的均匀系数。 版权所有(C)2010,JPO&INPIT
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公开(公告)号:KR1020110051235A
公开(公告)日:2011-05-17
申请号:KR1020117005369
申请日:2009-07-28
Applicant: 오르가노 코포레이션
IPC: C02F1/44 , C02F1/42 , B01D65/02 , C02F103/08
CPC classification number: B01D63/02 , B01D65/02 , B01D2313/20 , B01D2313/90 , B01D2321/04 , B01D2321/18 , B01D2325/12 , B01J47/022 , B01J49/05 , B01J49/60 , C02F1/001 , C02F1/42 , C02F1/44 , C02F2001/422 , C02F2001/425 , C02F2001/427 , C02F2101/006 , C02F2101/203 , C02F2201/003 , C02F2303/16 , Y02A20/131
Abstract: 높이가 제한된 장치를 사용함으로써 장치의 가격과 건설 비용을 줄일 수 있고 또한 양호한 작업성은 물론 충분한 처리 용량을 보장할 수 있는 여과 및 탈염 장치가 제공된다. 본 여과 및 탈염 장치 (10) 는, 회전체 형태로 된 용기 (20); 상기 용기(20) 의 내부 공간에 배치되는 중공 주상체 (40) 로서, 이의 일단부 (40a) 는 그의 전체 둘레를 따라 용기 (20) 의 내면에 연결되고, 타 단부 (40b) 는 개구를 형성하는 중공 주상체; 및 상기 중공 주상체의 타 단부 (40b) 의 전체 둘레를 따라 그 타 단부에 연결되는 격판 (44) 으로서, 중공 주상체 (40) 의 내부 공간 또는 외부 공간을 용기내의 독립적인 공간으로 분리하는 격판을 포함한다. 상기 격판 (44) 은 처리될 물이 통과할 수 있는 순환 포트 (43) 를 갖는다. 상기 격판에 의해 분리되는 용기내의 상기 독립적인 공간은 필터 요소가 설치되는 여과 챔버 (41) 로서 기능하며, 격판에 의해 독립적인 공간으로서 분리되어 있지 않은 중공 주상체의 내부 공간 또는 외부 공간은 탈염 챔버 (22) 로서 기능하고, 여과 챔버에서 처리된 물은 상기 순환 포트 (43) 를 통해 탈염 챔버에 들어가게 된다.
Abstract translation: 提供一种能够通过使用高度受限制的装置并且还能够确保足够的处理能力以及良好的可操作性的装置来降低装置的成本和建筑成本的过滤和脱矿质装置。 过滤和脱矿质装置10包括旋转体形式的容器20; 位于容器20的内部空间的中空柱状体40,柱状体的一端40a沿着端部的整个圆周与容器20的内表面连接,柱状体的另一端40b 身体形成开口; 以及分隔板44,其沿着另一端部40b的整个圆周连接到中空柱状体的另一端部40b,隔板构造成将中空柱状体40的内部空间或外部空间分离为 船上独立空间。 分隔板44具有允许待处理水通过的循环口43。 由分隔板隔开的容器中的独立空间用作过滤器元件被装载的过滤室41,并且中空柱状体的内部空间或外部空间作为独立空间被隔板分隔开 板作为脱盐室22起作用,在过滤室中处理的水适于通过循环端口43进入脱盐室。
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公开(公告)号:JP5425079B2
公开(公告)日:2014-02-26
申请号:JP2010523832
申请日:2009-07-28
Applicant: オルガノ株式会社
CPC classification number: B01D63/02 , B01D65/02 , B01D2313/20 , B01D2313/90 , B01D2321/04 , B01D2321/18 , B01D2325/12 , B01J47/022 , B01J49/05 , B01J49/60 , C02F1/001 , C02F1/42 , C02F1/44 , C02F2001/422 , C02F2001/425 , C02F2001/427 , C02F2101/006 , C02F2101/203 , C02F2201/003 , C02F2303/16 , Y02A20/131
Abstract: A filtration and demineralization apparatus that is capable of reducing the cost of the apparatus and building cost by using an apparatus whose height is limited, and that is also capable of ensuring sufficient treatment capacity, as well as good operability, is provided. A filtration and demineralization apparatus 10 comprises a vessel 20 in a form of a body of revolution; a hollow columnar body 40 that is located in an internal space of the vessel 20, one end 40a of the columnar body being connected to an inner surface of the vessel 20 along an entire circumference of the end, and the other end 40b of the columnar body forming an opening; and a partition plate 44 that is connected to the other end 40b of the hollow columnar body along an entire circumference of the other end 40b, the partition plate being configured to separate an inside space or an outside space of the hollow columnar body 40 as an independent space in the vessel. The partition plate 44 has a circulation port 43 that allows water that is to be treated to pass therethrough. The independent space in the vessel that is separated by the partition plate functions as a filtration chamber 41 in which filter elements are loaded, and the inside space or the outside space of the hollow columnar body that is not separated as the independent space by the partition plate functions as a demineralization chamber 22, the water that was treated in the filtration chamber being adapted to enter the demineralization chamber through the circulation port 43.
Abstract translation: 提供一种能够通过使用高度受限制的装置并且还能够确保足够的处理能力以及良好的可操作性的装置来降低装置的成本和建筑成本的过滤和脱矿质装置。 过滤和脱矿质装置10包括旋转体形式的容器20; 位于容器20的内部空间的中空柱状体40,柱状体的一端40a沿着端部的整个圆周与容器20的内表面连接,柱状体的另一端40b 身体形成开口; 以及分隔板44,其沿着另一端部40b的整个圆周连接到中空柱状体的另一端部40b,隔板构造成将中空柱状体40的内部空间或外部空间分离为 船上独立空间。 分隔板44具有允许待处理水通过的循环口43。 由分隔板隔开的容器中的独立空间用作过滤器元件被装载的过滤室41,并且中空柱状体的内部空间或外部空间作为独立空间被隔板分隔开 板作为脱盐室22起作用,在过滤室中处理的水适于通过循环端口43进入脱盐室。
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公开(公告)号:JPS5161485A
公开(公告)日:1976-05-28
申请号:JP11900275
申请日:1975-10-03
Applicant: Hoogovens Ijmuiden Bv
Inventor: SHERUDON EUANSU
Abstract: A regenerative base ion exchange process involving the step of passing a liquid upwardly through a bed of particulate solid base ion exchange resin in a chamber of a two-phase reactor to regenerate said resin, wherein the rate of liquid flow is such that the solid resin is compacted and held by the liquid as a compact bed against a barrier located above it and is prevented by the liquid from sinking.
Abstract translation: 一种再生式基础离子交换方法,其包括将液体向上通过两相反应器的室中的颗粒状固体基离子交换树脂床以再生所述树脂的步骤,其中液体流动速率使得固体树脂 被压实并被液体保持为紧凑的床抵靠位于其上的阻挡物,并被液体吸收所阻止。
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公开(公告)号:KR101649398B1
公开(公告)日:2016-08-30
申请号:KR1020137030624
申请日:2012-05-01
Applicant: 오르가노 가부시키가이샤
CPC classification number: B01D15/22 , B01D24/12 , B01D24/4631 , B01J47/022 , B01J47/04 , B01J49/05 , B01J49/70 , C02F1/42 , C02F1/44 , C02F2103/34
Abstract: 본발명은압력손실을낮게억제하여, 이온교환체에의해처리된물을원활하게장치밖으로배출하는것을과제로한다. 이온교환장치 (1) 는, 내부공간 (2) 을갖는외측용기 (3) 와, 내부공간 (2) 중적어도일부를상측공간 (2a) 과하측공간 (2b) 으로나누고, 상측공간 (2a) 에충전되도록된 이온교환체를유지할수 있는이온교환체유지부 (4) 를갖고있다. 이온교환체유지부 (4) 의상면중 적어도일부는, 이온교환체를유지함과함께이온교환체에의해처리된물을하측공간 (2b) 으로유통시키는유로를구비한적어도 1 개의스크린으로구성되어있다.
Abstract translation: 本发明的目的在于限制压力损失并且将由离子交换剂处理的水平稳地排放到设备的外部。 离子交换装置1具有内部空间2的外部容器3; 以及将内部空间2的至少一部分分离成上部空间2a和下部空间2b的离子交换器支撑体4,并且能够将离子交换器支撑在上部空间2a中。 离子交换器支撑体的上表面的至少一部分由至少一个支撑离子交换器的筛网制成,并且具有允许由离子交换剂处理的水流入下部空间2b的流路。
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公开(公告)号:KR101851387B1
公开(公告)日:2018-04-23
申请号:KR1020147000911
申请日:2011-08-10
Applicant: 다이헤이요 세멘토 가부시키가이샤
CPC classification number: B08B17/00 , B01J43/00 , B01J49/05 , C02F1/001 , C02F1/42 , C02F2001/007 , C02F2101/101 , C02F2101/103 , C02F2101/105 , C02F2101/106 , C02F2101/108 , C02F2101/14 , C02F2101/20 , C02F2101/363 , C02F2103/06 , C02F2103/12 , C02F2103/18 , C02F2209/05 , C02F2209/08 , C02F2209/29 , C02F2301/043 , C02F2303/22
Abstract: [과제] 약제비용을저감하고, 운전비용을낮게억제할수 있는칼슘스케일의방지방법을제공한다. [해결수단] 칼슘스케일의발생을유인하는배수를, 양쪽성이온교환수지(4)를사용하여, 칼슘이온농도가낮고, 유해물질의농도가높은제 1 용액(L4)과, 칼슘이온농도가높고유해물질의농도가낮은제 2 용액(L3)으로분리하고, 제 1 및제 2 용액을별도로처리한다. 양쪽성이온교환수지로부터배출되는제 1 용액과, 제 2 용액과의전환타이밍을, 양쪽성이온교환수지로부터배출되는용액의 COD 농도, 칼슘이온농도, 염소이온농도및 전기전도도로부터선택되는 1 이상에기초하여제어할수 있다. 칼슘스케일의발생을유인하는배수를, 최종처분장의침출수(W1), 소각재를수세하여얻어진여과액, 염소바이패스더스트를수세하여얻어진여과액으로할 수있다.
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