公开(公告)号：US5851372A

公开(公告)日：1998-12-22

申请号：US732216

申请日：1996-10-24

Applicant: Roland Noel

Inventor： Roland Noel

IPC: A23C9/144 ,  A23C9/146 ,  B01D61/42 ,  B01D61/58 ,  B01J39/04 ,  B01J49/00 ,  C02F1/42 ,  C02F1/469 ,  B01D61/44

CPC classification number: C02F1/4693 ,  A23C9/144 ,  A23C9/146 ,  B01J39/043 ,  B01J49/0069 ,  C02F1/42 ,  C02F2201/46115

Abstract: A process of demineralizing a liquid containing organic matter and inorganic salts in solution, in which the treatment of the liquid comprises the following steps: the liquid is percolated over a strong cationic ion exchange resin for monovalent ions; both a batch of liquid from the preceding step and a brine for receiving ions from that liquid are caused to circulate in loops through at least one "two-compartment" electrodialyzer comprising a plurality of anionic membranes interposed between a plurality of cationic membranes; and the brine whose salt concentration lies in the range 90 grams per liter (g/l) to 110 g/l is used to regenerate the ion exchange resin.

Abstract translation: PCT No.PCT / FR95 / 00595 Sec。 371日期：1996年10月24日 102（e）日期1996年10月24日PCT提交1995年5月9日PCT公布。 WO95 / 30482 PCT出版物 日期：1995年11月16日一种将含有机物的液体和溶液中的无机盐脱矿质的方法，其中处理液体包括以下步骤：将液体渗透在强阳离子交换树脂上用于一价离子; 使来自前述步骤的一批液体和用于从该液体接收离子的盐水通过至少一个“两室”电渗析器循环循环，所述“双室”电渗析器包括插入在多个阳离子膜之间的多个阴离子膜; 并且使用盐浓度在90克/升（g / l）至110g / l范围内的盐水来再生离子交换树脂。

公开(公告)号：US5518626A

公开(公告)日：1996-05-21

申请号：US173634

申请日：1993-12-23

Applicant: Philip J. Birbara ,  Timothy A. Nalette ,  Douglas A. Snowdon

Inventor： Philip J. Birbara ,  Timothy A. Nalette ,  Douglas A. Snowdon

IPC: B01J39/04 ,  B01J47/06 ,  B01J49/00 ,  C02F9/00

CPC classification number: B01J49/0078 ,  B01J39/043 ,  B01J47/06 ,  B01J49/0056

Abstract: The present invention provides a system and a process for removing contaminants such as CO.sub.2 and mobile cations and anions from aqueous solutions. The system and the process contemplate the use of thermally sterilizable aqueous polishing agents such as thermally sterilizable ion exchange resins and as a result, the need for chemical and/or mechanical microbial control or inhibition techniques is obviated. Therefore, the present invention will be especially useful in submarine and spacecraft applications where the need exists for reduced weight and volume water processing systems.

Abstract translation: 本发明提供一种用于从水溶液中去除污染物如CO 2和可移动阳离子和阴离子的系统和方法。 该系统和方法考虑使用可热灭菌的水性抛光剂如热灭菌的离子交换树脂，结果是免除了对化学和/或机械微生物控制或抑制技术的需要。 因此，本发明对于需要减轻重量和体积的水处理系统的潜艇和航天器应用尤其有用。

公开(公告)号：US5378366A

公开(公告)日：1995-01-03

申请号：US052025

申请日：1993-04-22

Applicant: Jeffrey H.-G. Yen

Inventor： Jeffrey H.-G. Yen

IPC: B01J39/04 ,  C02F1/52 ,  C02F9/00

CPC classification number: C02F9/00 ,  B01J39/043 ,  C02F1/5236 ,  C02F2101/20 ,  Y10S210/911

Abstract: A process is disclosed wherein arsenic dissolved in wastewater or groundwater is removed from solution by precipitation thereof as calcium arsenate formed by the reaction of the arsenic with lime or hydrated lime in a heated solution at a pH of about 11 to about 13. It is preferred that the arsenic is first converted by oxidation to its pentavalent form.

Abstract translation: 公开了一种方法，其中将溶解在废水或地下水中的砷通过其沉淀作为砷酸钙而从溶液中除去，所述砷酸钙是通过砷与石灰或熟石灰在pH为约11至约13的加热溶液中反应形成的。 砷首先通过氧化转化成其五价形式。

公开(公告)号：US5116512A

公开(公告)日：1992-05-26

申请号：US718320

申请日：1991-06-17

Applicant: Philip W. Bartram ,  Noel C. DiBona

Inventor： Philip W. Bartram ,  Noel C. DiBona

IPC: B01J39/04 ,  B01J47/00

CPC classification number: B01J47/003 ,  B01J39/043 ,  Y10S210/908 ,  Y10S210/911

Abstract: An absorption process of using polydivinylbenzene to remove nerve agents h as GD from a conventional solvent such as chlorofluorocarbon which itself is used to decontaminate a surface such as armament.

Abstract translation: 使用聚二乙烯基苯从诸如氯氟烃的常规溶剂中去除诸如GD的神经毒素的吸收方法，其本身用于去除诸如军备的表面。

公开(公告)号：US5108615A

公开(公告)日：1992-04-28

申请号：US442744

申请日：1989-11-28

Applicant: J. Michael Hosea ,  Michael D. Mayne ,  Dennis W. Darnall

Inventor： J. Michael Hosea ,  Michael D. Mayne ,  Dennis W. Darnall

IPC: B01J39/04 ,  B01J45/00 ,  C23C18/16

CPC classification number: B01J45/00 ,  B01J39/043 ,  C23C18/1617 ,  Y10S423/14

Abstract: A new process for removal of a metal ion from an anionic complex, including a first chelating agent and a metal ion, such as copper, nickel or cobalt ion, in electroless plating bath rinse streams utilizes a cation exchange resin to extract the metal ion from the rinse stream after the metal ion has been removed from the anionic complex and complexed with a second chelating agent.In another embodiment, a competing chelating agent is not added to the electroless plating bath waste stream, but rather, another metal ion (B), which has a higher affinity for the chelating agent than the metal ion (A) of interest and which is nontoxic, is added to the waste stream. Metal ion B is selected so that under predetermined conditions, metal ion B forms a stronger complex with the chelating agent than does metal ion A. Also, the complex of the chelating agent and nontoxic metal ion B is anionic. A cation exchange resin is used to extract metal ion A from the treated waste stream.

Abstract translation: 在化学镀浴冲洗流中，从阴离子配合物（包括第一螯合剂和金属离子）如铜，镍或钴离子中去除金属离子的新方法利用阳离子交换树脂从 金属离子从阴离子络合物中除去并与第二螯合剂络合后的漂洗流。 在另一个实施方案中，竞争性螯合剂不被添加到化学镀浴废料流中，而是加入对螯合剂具有比感兴趣的金属离子（A）更高的亲和性的另一种金属离子（B） 无毒，被添加到废物流中。 选择金属离子B，使得在预定条件下，金属离子B与金属离子A形成比螯合剂更强的络合物。此外，螯合剂和无毒金属离子B的络合物是阴离子的。 使用阳离子交换树脂从经处理的废物流中提取金属离​​子A.

公开(公告)号：US4542015A

公开(公告)日：1985-09-17

申请号：US409513

申请日：1982-08-19

Applicant: Robert Smakman ,  Gerrit H. van den Berg

Inventor： Robert Smakman ,  Gerrit H. van den Berg

IPC: A61M1/22 ,  A61K33/00 ,  A61K47/48 ,  A61M1/14 ,  A61M1/16 ,  A61M1/36 ,  B01J20/32 ,  B01J39/04 ,  B01J39/20 ,  A61K31/74

CPC classification number: A61K33/00 ,  A61K47/48184 ,  A61M1/1696 ,  A61M1/3679 ,  B01J39/04 ,  B01J39/043 ,  B01J39/046 ,  B01J39/20 ,  B01J41/043

Abstract: An apparatus for purifying blood has a blood compartment and a clearance compartment separated by a semi-permeable membrane. The apparatus includes a device containing a cation exchange resin charged with metal ions whose phosphates are insoluble in water. Metal salts of iron, aluminum, zirconium, lanthanum, thorium and tin are deposited on a cation exchange material and the charged cation exchange resin is contacted with dialysis liquid. The process of treating blood with the dialysis liquid is also contemplated.

Abstract translation: 用于净化血液的装置具有由半透膜隔开的血液隔室和间隙室。 该装置包括装有磷酸盐不溶于水的金属离子的阳离子交换树脂的装置。 将铁，铝，锆，镧，钍和锡的金属盐沉积在阳离子交换材料上，并将带电阳离子交换树脂与透析液接触。 也可以考虑用透析液处理血液的过程。

公开(公告)号：US4269705A

公开(公告)日：1981-05-26

申请号：US031157

申请日：1979-04-18

Applicant: Teruhiko Yoshioka ,  Hideo Matsuzawa ,  Kazuya Okada ,  Minoru Ikeda

Inventor： Teruhiko Yoshioka ,  Hideo Matsuzawa ,  Kazuya Okada ,  Minoru Ikeda

IPC: B01J39/04 ,  C01G37/00 ,  C07C51/47 ,  B01D15/04

CPC classification number: C07C51/47 ,  B01J39/043 ,  C01G37/003 ,  C22B3/42 ,  Y02P10/234

Abstract: A method of removing chromium ion from an aqueous solution of an organic acid of an acid concentration of up to 95% which comprises treating the solution with a cation exchange resin at a temperature higher than 55.degree. C.

Abstract translation: 从酸浓度高达95％的有机酸的水溶液中除去铬离子的方法，该方法包括在高于55℃的温度下用阳离子交换树脂处理该溶液。

公开(公告)号：US4160675A

公开(公告)日：1979-07-10

申请号：US832126

申请日：1977-09-12

Applicant: Wilhelmus Pannekeet ,  Robert Smakman

Inventor： Wilhelmus Pannekeet ,  Robert Smakman

IPC: C02F1/42 ,  B01D15/04 ,  B01J19/00 ,  B01J20/22 ,  B01J45/00 ,  C02F1/28 ,  C07B31/00 ,  C07B63/00 ,  C07B63/02 ,  C07C67/00 ,  C07H1/06 ,  C13B20/14 ,  C13D3/12 ,  C13D3/14

CPC classification number: B01J20/265 ,  B01J39/043 ,  C02F1/285 ,  Y10S210/917

Abstract: A process for removing an organic impurity from an aqueous solution is disclosed, said process comprising contacting the aqueous solution with an acid cation exchanger and subsequently with a polymer or polycondensate, which contains sulfur in the form of thiol groups bonded to carbon atoms.

Abstract translation: 公开了一种从水溶液中除去有机杂质的方法，所述方法包括使水溶液与酸性阳离子交换剂接触，随后与聚合物或缩聚物接触，所述聚合物或缩聚物含有与碳原子键合的巯基形式的硫。

公开(公告)号：US4012318A

公开(公告)日：1977-03-15

申请号：US563729

申请日：1975-03-31

Applicant: Toshio Hayashi

Inventor： Toshio Hayashi

IPC: B01J39/04 ,  B01J49/00 ,  C02F1/28 ,  C02F1/66 ,  C02F9/00 ,  C25D21/22 ,  C02B1/20 ,  C02B1/42 ,  C02B1/56

CPC classification number: C25D21/22 ,  B01J39/043 ,  B01J49/0017 ,  C02F1/285 ,  C02F1/66 ,  C02F2101/22 ,  C02F2103/16

Abstract: A method for the recycle treatment of chromium plating waste water, in the process of treating chromium plating waste water obtained by washing the chromium plated products with ion exchange resins, wherein, for the purposes of improving the rate of recovery of chromic acid, of extending the life of the ion exchange resins, and of preventing the formation of sludge, the chromium plating waste water is adjusted almost to neutrality by the addition of an alkaline substance so as to precipitate the metal components contained therein in the form of hydroxides, which are then removed by filtration; the filtrate so obtained is kept neutral during the subsequent treatment for the removal of alkaline components by adsorption in a pretreatment tower packed with cation exchange resins; the dilute dichromic acid solution so obtained is similarly treated for concentration in an adsorption tower packed with anion exchange resins and a purification tower packed with cation exchange resins so as to recover pure dichromic acid solution, whereas the above pretreatment tower and purification tower are regenerated by treatment with sulfuric acid.

Abstract translation: 在用离子交换树脂洗涤镀铬产品得到的镀铬废水的处理过程中，对镀铬废水进行再循环处理的方法，其中为了提高铬酸的回收率，延伸 离子交换树脂的寿命，并且防止污泥形成，通过添加碱性物质将镀铬废水几乎调节为中性，以使氢氧化物的形式沉淀其中所含的金属组分，其为 然后通过过滤除去; 所得到的滤液在随后的处理中保持中性，通过在填充有阳离子交换树脂的预处理塔中吸附除去碱性组分; 将如此获得的稀二重铬酸溶液类似地处理在装有阴离子交换树脂的吸附塔和填充有阳离子交换树脂的净化塔中的浓度，以回收纯二重铬酸溶液，而上述预处理塔和净化塔由 用硫酸处理。

公开(公告)号：US5985152A

公开(公告)日：1999-11-16

申请号：US840

申请日：1997-12-30

Applicant: Hideo Otaka ,  Nobuhiro Matsushita

Inventor： Hideo Otaka ,  Nobuhiro Matsushita

IPC: C02F1/00 ,  B01J39/04 ,  B01J41/04 ,  C02F1/42 ,  C02F5/00 ,  C23F11/173 ,  C23F14/00

CPC classification number: B01J41/043 ,  B01J39/04 ,  B01J39/043 ,  C02F2001/422 ,  C02F2001/425 ,  C02F2103/023

Abstract: Ca ion is removed by a cation exchange resin and silica and corrosive ions are removed by an anion exchange resin. Even after the anion exchange resin reaches the silica break through point or after the cation exchange resin reaches the Ca ion break through point, the supply of water is continued until the average of silica concentration or Ca ion concentration reaches a predetermined value. By supplying both treated water before the break through point and treated water after the break through point, water containing silica or Ca ion of suitable concentration can be supplied to the water system with only one anion exchange column or cation exchange column.

Abstract translation: 通过阳离子交换树脂和二氧化硅除去Ca离子，通过阴离子交换树脂除去腐蚀性离子。 即使在阴离子交换树脂达到二氧化硅破裂点之后或者在阳离子交换树脂达到Ca离子穿透点之后，继续供水直到二氧化硅浓度或Ca离子浓度的平均值达到预定值。 通过在通过点之前提供经处理的水和经过处理的水之后，可以仅使用一个阴离子交换柱或阳离子交换柱向水系统供应含有适当浓度的二氧化硅或Ca离子的水。