公开(公告)号：US20120042748A1

公开(公告)日：2012-02-23

申请号：US13212711

申请日：2011-08-18

Applicant: Amanda M. Johnsen ,  Chuck Z. Soderquist ,  Bruce K. McNamara ,  Darrell K. Fisher

Inventor： Amanda M. Johnsen ,  Chuck Z. Soderquist ,  Bruce K. McNamara ,  Darrell K. Fisher

IPC: C22B4/04 ,  C22B59/00

CPC classification number: C01F17/0068 ,  B01J39/05 ,  B01J49/53 ,  C01F17/00 ,  G21G1/06 ,  G21G2001/0094

Abstract: An alteration of the traditional zinc/zinc-amalgam reduction procedure which eliminates both the hazardous mercury and dangerous hydrogen gas generation. In order to avoid the presence of water and hydrated protons in the working solution, which can oxidize Eu2+ and cause hydrogen gas production, a process utilizing methanol as the process solvent is described. While methanol presents some flammability hazard in a radiological hot cell, it can be better managed and is less of a flammability hazard than hydrogen gas generation.

Abstract translation: 改变传统的锌/锌合金还原程序，消除了危险的汞和危险的氢气产生。 为了避免在工作溶液中存在水分和水合质子，其可以氧化Eu 2+并引起氢气产生，描述了使用甲醇作为加工溶剂的方法。 虽然甲醇在放射性热电池中存在一些可燃性危险，但可以更好地管理并且比氢气产生更易燃易燃危害。

公开(公告)号：US20120029233A1

公开(公告)日：2012-02-02

申请号：US13191163

申请日：2011-07-26

Applicant: In-Hyoung RHEE ,  Hyun-Jun JUNG

Inventor： In-Hyoung RHEE ,  Hyun-Jun JUNG

IPC: C07C209/86 ,  B01D15/04 ,  B01J19/00

CPC classification number: C02F1/42 ,  B01J39/05 ,  B01J49/06 ,  B01J49/53 ,  C02F1/20 ,  C02F2001/425 ,  C02F2101/38 ,  C02F2209/02 ,  C02F2301/063 ,  C02F2303/10 ,  C02F2303/16 ,  C07C209/86 ,  Y02W10/30

Abstract: Provided is an apparatus for recovering amines from amine-containing waste water generated in power stations, etc., and regenerating a cation exchange resin. The apparatus includes: a cation exchange resin layer capturing amines from amine-containing waste water and eluting the amines therefrom; a degassing tower degassing the eluted amines; a vacuum pump connected to the degassing tower; and a condensation and cooling tower condensing the degassed amines at a temperature of −33° C. or lower, wherein the amines captured in the cation exchange resin layer are eluted by injecting a strong acidic solution, while the resin is regenerated, and the amines eluted by the strong acidic solution is subjected to vacuum degassing and then recovered. Provided also is a method for recovering amines and regenerating a cation exchange resin using the apparatus. The apparatus and method for recovering amines and regenerating a cation exchange resin improve the quality of effluent water from power stations, etc., and increase the cost-efficiency through the recycle of amines.

Abstract translation: 提供了一种用于从在发电站等中产生的含胺废水中回收胺并且再生阳离子交换树脂的装置。 该装置包括：阳离子交换树脂层，其从含胺废水捕获胺并从其中洗脱出胺; 脱气塔脱气洗脱的胺; 连接到脱气塔的真空泵; 在-33℃以下冷凝脱气的胺的冷凝冷却塔，其中，在树脂再生时，通过注入强酸性溶液洗脱阳离子交换树脂层中捕集的胺，并且胺 用强酸溶液洗脱后进行真空脱气，然后回收。 还提供了使用该装置回收胺并再生阳离子交换树脂的方法。 用于回收胺和再生阳离子交换树脂的装置和方法提高了发电站等的排出水的质量，并且通过再循环胺提高了成本效率。

公开(公告)号：US08097068B2

公开(公告)日：2012-01-17

申请号：US12266012

申请日：2008-11-06

Applicant: Matthew Campbell ,  John Sarlis ,  Vijay Bhambhani Godhwani ,  Melina Infantino

Inventor： Matthew Campbell ,  John Sarlis ,  Vijay Bhambhani Godhwani ,  Melina Infantino

IPC: B01D53/14

CPC classification number: B01D53/1493 ,  B01D53/1425 ,  B01D53/1456 ,  B01D2252/2041 ,  B01D2252/20431 ,  B01D2257/302 ,  B01D2257/304 ,  B01D2257/404 ,  B01D2257/504 ,  B01J39/05 ,  B01J49/06 ,  B01J49/08 ,  C10L3/103 ,  C10L3/104 ,  B01J41/07

Abstract: A diamine absorbent that contains heat stable salts is regenerated using an ion exchange process wherein the concentration of heat stable salts in the feed stream provided to the cation exchange unit is limited.

Abstract translation: 含有热稳定盐的二胺吸收剂使用离子交换方法再生，其中提供给阳离子交换单元的进料流中的热稳定盐的浓度受到限制。

公开(公告)号：US20110315631A1

公开(公告)日：2011-12-29

申请号：US13116413

申请日：2011-05-26

Applicant: Riad A. Al-Samadi

Inventor： Riad A. Al-Samadi

IPC: C02F9/04 ,  C02F1/42 ,  C02F5/00 ,  C02F1/44 ,  C02F1/66 ,  C02F103/02 ,  C02F103/06 ,  C02F101/00

CPC classification number: C02F1/441 ,  B01D61/025 ,  B01D61/04 ,  B01D61/12 ,  B01D2311/04 ,  B01D2311/08 ,  B01D2313/50 ,  B01J39/05 ,  B01J39/07 ,  B01J45/00 ,  B01J47/02 ,  B01J49/06 ,  B01J49/53 ,  B01J49/75 ,  B01J49/80 ,  C02F1/001 ,  C02F1/42 ,  C02F1/442 ,  C02F2103/04 ,  B01D2311/2649 ,  B01D2311/12 ,  B01D2311/18 ,  B01D2311/2623 ,  B01D2311/2673 ,  B01D2311/2642

Abstract: Disclosed is a versatile multi-use high water recovery process that integrates the use of water purification membranes including reverse osmosis and nanofiltration with ion exchange water softening resins in a number of configurations that optimize operation and achieve maximum membrane permeate recoveries while eliminating the use of fresh water, sodium chloride and other chemicals needed to regenerate the IX resin. The invention provides process mobility and flexibility that enable selection of optimum process configurations and features to address variability in the Influent Water quality.

Abstract translation: 公开了一种通用的多用途高水回收方法，其将使用包括反渗透和纳滤的水净化膜与离子交换水软化树脂结合在一起，其优化操作并实现最大的膜渗透回收率，同时消除使用新鲜的 水，氯化钠和其他需要再生IX树脂的化学品。 本发明提供流程移动性和灵活性，使得能够选择最佳过程配置和特征来解决流入水质量的变异性。

公开(公告)号：US20110278225A1

公开(公告)日：2011-11-17

申请号：US13096406

申请日：2011-04-28

Applicant: Francis Boodoo

Inventor： Francis Boodoo

IPC: C02F1/42 ,  B01D61/14 ,  C02F1/44

CPC classification number: C02F9/00 ,  B01D61/04 ,  B01D2311/04 ,  B01D2311/08 ,  B01D2311/2623 ,  B01J39/05 ,  B01J47/02 ,  B01J49/06 ,  B01J49/53 ,  B01J49/75 ,  C02F1/008 ,  C02F1/42 ,  C02F1/441 ,  C02F1/442 ,  C02F2001/425 ,  C02F2103/08 ,  C02F2209/005 ,  C02F2209/055 ,  C02F2209/40 ,  C02F2303/16 ,  C02F2303/22 ,  Y02A20/131

Abstract: The present invention provides a method for purifying or softening water comprising: passing a specific volume of feedwater through at least one service column comprising a strong acid cationic exchange resin capable of binding divalent cations that are present in the feedwater, wherein the loading of the divalent cations on the resin is restricted to about 1 to 25% of the available ion exchange sites on the resin, and the total dissolved solids in the feedwater is greater than 100 mg/l; feeding the water exiting the service column to a reverse osmosis membrane or a nanofiltration membrane to produce permeate water stream and a reject water stream; and passing all or some of the volume of the reject stream corresponding the specific volume of feedwater through at least one off-line column capable of binding monovalent cations; wherein the chemical equivalent ratio of monovalent to divalent cations in the water exiting the service column is greater than 20 to 1; wherein no external source of regenerant salt is used. The inventive method allows for multiple softening/regeneration cycles so that steady state hardness leakage is achieved that is lower than obtainable with conventional ion exchange softening systems.

Abstract translation: 本发明提供了一种净化或软化水的方法，包括：使特定体积的给水通过至少一个包含能够结合给水中存在的二价阳离子的强酸阳离子交换树脂的服务塔，其中二价 树脂上的阳离子限制在树脂上可用的离子交换位点的约1至25％，给水中的总溶解固体量大于100mg / l; 将从服务塔排出的水送入反渗透膜或纳滤膜，以产生渗透水流和废水流; 并且使通过能够结合一价阳离子的至少一个离线柱相应于给定水体积的排出流的全部或一些体积; 其中离开所述使用塔的水中的一价二价阳离子的化学当量比大于20:1; 其中不使用外源再生盐。 本发明的方法允许多次软化/再生循环，使得达到低于常规离子交换软化系统可获得的稳态硬度泄漏。

公开(公告)号：US20110250696A1

公开(公告)日：2011-10-13

申请号：US13084746

申请日：2011-04-12

Applicant: Marcus RAJCHEL ,  Michael F. RAY

Inventor： Marcus RAJCHEL ,  Michael F. RAY

IPC: G01N33/44 ,  C01C3/10

CPC classification number: C01C3/10 ,  B01J39/05 ,  B01J49/06 ,  C01F11/24 ,  G01C3/10

Abstract: Provided is a method for high concentration cation exchange metathesis of divalent ions such as calcium with univalent ions such as sodium or potassium. Due to the difference between ionic valences between the exchanged ions, the provided process behavior is strongly dependent upon the selection of resin properties and to total solution normality. A combination of resin properties and solution normality is provided to achieve the cation exchange.

Abstract translation: 提供了一种二价离子（例如钙）与一价离子如钠或钾的高浓度阳离子交换复分解的方法。 由于交换的离子之间的离子价之间的差异，所提供的过程行为强烈地依赖于树脂性质的选择和总溶液的正常性。 提供树脂性质和溶液正常性的组合以实现阳离子交换。

公开(公告)号：US07846338B2

公开(公告)日：2010-12-07

申请号：US11986616

申请日：2007-11-21

Applicant: Michael M. Kearney ,  Lawrence Velasquez

Inventor： Michael M. Kearney ,  Lawrence Velasquez

IPC: B01J49/00

CPC classification number: C02F1/42 ,  B01J39/05 ,  B01J39/07 ,  B01J49/53 ,  C02F2001/425

Abstract: A method is described that relates to reducing amounts of regenerant waste or increasing the concentration of regenerant waste from ion exchange processes. A method is described that may allow a batch ion exchange process to compete on these factors with continuous or simulated continuous ion exchange processes, and/or to improve the efficiency in operation continuous or simulated continuous ion exchange processes. A specific application addressed is the treatment of water in the Coal Bed Methane Process.

Abstract translation: 描述了一种减少再生废物量或从离子交换过程增加再生废物浓度的方法。 描述了可以允许批次离子交换过程利用连续或模拟的连续离子交换过程在这些因素上竞争和/或提高连续或模拟连续离子交换过程的操作效率的方法。 一个具体的应用是煤层气过程中的水处理。

公开(公告)号：US20100240915A1

公开(公告)日：2010-09-23

申请号：US12696083

申请日：2010-01-29

Applicant: Robert Jansen ,  Anthony Baiada ,  John Kerr ,  Peter Lloyd-Jones

Inventor： Robert Jansen ,  Anthony Baiada ,  John Kerr ,  Peter Lloyd-Jones

IPC: C07D307/36 ,  C07C29/76

CPC classification number: C02F1/42 ,  B01D61/36 ,  B01D61/362 ,  B01D65/08 ,  B01D2311/04 ,  B01D2311/2623 ,  B01D2321/16 ,  B01J39/04 ,  B01J39/05 ,  B01J41/04 ,  C02F1/04 ,  C02F2001/422 ,  C02F2001/425 ,  C02F2101/34 ,  C02F2103/36 ,  C07C29/76 ,  C07C31/08 ,  C07C31/12 ,  B01J41/07

Abstract: We disclose a method of extracting an alcohol or furan from a predominantly liquid stream comprising the alcohol or furan, comprising removing cations from the predominantly liquid stream comprising the alcohol or furan, using a cation-exchange resin; removing anions from the predominantly liquid stream comprising the alcohol or furan, using an anion-exchange resin; and recovering alcohol or furan from the predominantly liquid stream comprising the alcohol or furan, using either a vapor permeation membrane, a perevaporation process, or both.

Abstract translation: 我们公开了从包含醇或呋喃的主要液体流中提取醇或呋喃的方法，其包括使用阳离子交换树脂从包含醇或呋喃的主要液体流中除去阳离子; 使用阴离子交换树脂从包含醇或呋喃的主要液体流中除去阴离子; 并使用蒸气渗透膜，蒸发蒸发法或二者从包含醇或呋喃的主要液体物流中回收醇或呋喃。

公开(公告)号：US20090130723A1

公开(公告)日：2009-05-21

申请号：US12282815

申请日：2007-03-15

Applicant: Hideki Murata ,  Noboru Fujii ,  Kenji Tajima

Inventor： Hideki Murata ,  Noboru Fujii ,  Kenji Tajima

IPC: C12P13/24

CPC classification number: C12P13/24 ,  B01J39/05

Abstract: In the method for separating and purifying histidine from a culture containing the amino acid, the culture containing histidine and microbial cells is charged onto the top of a column filled with a carrier particle whose particle size is 350 μm or more and which has an ability to adsorb histidine and then an eluent is passed through the column whereby accomplishing the separation and purification of histidine, and preferably in the step mentioned above, a strong acid cation exchange resin is employed as a carrier particle whereby accomplishing the separation and purification of histidine.

Abstract translation: 在从含有氨基酸的培养物分离和纯化组氨酸的方法中，将含有组氨酸和微生物细胞的培养物装入填充有粒度为350μm以上的载体颗粒的柱的顶部，并且具有 吸附组氨酸，然后使洗脱液通过柱，从而完成组氨酸的分离和纯化，优选在上述步骤中，使用强酸阳离子交换树脂作为载体颗粒，从而完成组氨酸的分离和纯化。

公开(公告)号：US07264678B2

公开(公告)日：2007-09-04

申请号：US09875311

申请日：2001-06-06

Applicant: Bruce Barger ,  Alan Scott Goldstein ,  Henry Cheng Na

Inventor： Bruce Barger ,  Alan Scott Goldstein ,  Henry Cheng Na

IPC: B08B3/02

CPC classification number: C11D11/0064 ,  B01J39/05 ,  B08B3/026 ,  C02F1/42 ,  C02F2001/422 ,  C02F2001/425 ,  C11D3/3776 ,  C11D11/0023 ,  B01J41/07

Abstract: A process is described wherein a surface, for example the exterior surface of a vehicle, is contacted with a cleaning composition capable of rendering the surface treated hydrophilic and then rinsed with purified rinse water. Preferably the process also involves a pre-wetting step, wherein the surface is rinsed with water prior to being contacted with the cleaning composition, and/or an additional rinsing step, wherein the surface is rinsed with unpurified water prior to rinsing with the purified rinse water.

Abstract translation: 描述了一种方法，其中表面，例如车辆的外表面与清洁组合物接触，所述清洁组合物能够使表面经过亲水处理，然后用净化的冲洗水冲洗。 优选地，该方法还涉及预润湿步骤，其中在与清洁组合物接触之前用水冲洗该表面和/或另外的冲洗步骤，其中在用净化的漂洗液漂洗之前用未纯化的水冲洗该表面 水。