公开(公告)号：US20240157354A1

公开(公告)日：2024-05-16

申请号：US18284351

申请日：2022-01-27

Applicant: ORGANO CORPORATION

Inventor： Noriko TAKADA ,  Kaoru NUKUI

IPC: B01J47/016 ,  B01J39/05 ,  B01J39/07 ,  B01J45/00

CPC classification number: B01J47/016 ,  B01J39/05 ,  B01J39/07 ,  B01J45/00

Abstract: A dry ion exchange resin manufacturing method includes: obtaining a purified cation exchange resin by bringing a cation exchange resin to be purified into contact with a mineral acid solution having a metal impurity content of 1 mg/L, or less and a concentration of 5% by weight or more, to purify the cation exchange resin, wherein a total metal impurity elution amount eluted when hydrochloric acid having a concentration of 3% by weight is passed through the purified cation exchange resin with a volume ratio of 25 times is at most equal to 5 μg/mL-R; and a drying step of drying the purified cation exchange resin under reduced pressure at 80° C. or lower until the moisture content is at most equal to 5% by weight.

公开(公告)号：US20240002263A1

公开(公告)日：2024-01-04

申请号：US18254114

申请日：2021-11-10

Applicant: Panasonic Intellectual Property Management Co., Ltd.

Inventor： Hiroki ISHIKAWA ,  Ayaka NAGATA ,  Risako KOIKE ,  Yui MATSUMOTO ,  Hiroki MURASE ,  Minato KATO ,  Yohsuke HAMADA ,  Yuko MARUO ,  Hiroshi YANO ,  Yoshihiro SAKAGUCHI

IPC: C02F1/42 ,  C02F1/461 ,  C02F1/00 ,  B01J39/07 ,  B01J39/18 ,  B01J41/07 ,  B01J41/12 ,  B01J47/028 ,  B01J47/14 ,  B01J49/75 ,  B01J49/53 ,  B01J49/57 ,  B01J49/85 ,  B01J49/06 ,  B01J49/07 ,  B01J49/08

CPC classification number: C02F1/42 ,  C02F1/4618 ,  C02F1/008 ,  B01J39/07 ,  B01J39/18 ,  B01J41/07 ,  B01J41/12 ,  B01J47/028 ,  B01J47/14 ,  B01J49/75 ,  B01J49/53 ,  B01J49/57 ,  B01J49/85 ,  B01J49/06 ,  B01J49/07 ,  B01J49/08 ,  C02F2001/425 ,  C02F2001/422 ,  C02F2303/16 ,  C02F2301/08 ,  C02F2201/4613 ,  C02F2201/46145 ,  C02F2303/14 ,  C02F2301/043 ,  C02F2209/42

Abstract: Water softening device includes water softening tank and neutralizing tank. Water softening tank softens raw water containing a hardness component by weakly acidic cation exchange resin. Water softening tank includes first water softening tank and second water softening tank. Neutralizing tank neutralizes the pH of softened water that has passed through water softening tank by weakly basic anion exchange resin. Neutralizing tank includes first neutralizing tank and second neutralizing tank. Water softening device is configured to cause raw water containing a hardness component to flow through first water softening tank, first neutralizing tank, second water softening tank, and second neutralizing tank in this order.

公开(公告)号：US11707068B2

公开(公告)日：2023-07-25

申请号：US16823697

申请日：2020-03-19

Applicant: SONY CORPORATION

Inventor： Hironori Iida ,  Shun Yamanoi ,  Machiko Minatoya ,  Seiichiro Tabata ,  Shinichiro Yamada

IPC: A01N59/16 ,  B01J21/06 ,  B01J21/18 ,  C02F1/28 ,  B01J20/28 ,  B01J20/32 ,  B01J35/10 ,  B01J35/00 ,  B01J23/745 ,  B01J39/07 ,  B01J23/89 ,  B01J27/188 ,  B01J39/02 ,  C02F1/50

CPC classification number: A01N59/16 ,  B01J20/28057 ,  B01J20/28069 ,  B01J20/3204 ,  B01J20/3246 ,  B01J21/063 ,  B01J21/18 ,  B01J23/745 ,  B01J23/8993 ,  B01J27/188 ,  B01J35/002 ,  B01J35/004 ,  B01J35/108 ,  B01J35/1023 ,  B01J35/1028 ,  B01J35/1038 ,  B01J35/1042 ,  B01J39/02 ,  B01J39/07 ,  C02F1/281 ,  C02F1/285 ,  C02F1/288 ,  C02F1/505 ,  C02F2305/10 ,  Y10T428/249967 ,  A01N59/16 ,  A01N2300/00

Abstract: Disclosed herein is a fungicide, including a porous carbon material and a silver member adhered to the porous carbon material, wherein a value of a specific surface area based on a nitrogen BET, namely Brunauer, Emmett, and Teller method is equal to or larger than 10 m2/g, and a volume of a fine pore based on a BJH, namely Barrett, Joyner, and Halenda method and an MP, namely Micro Pore method is equal to or larger than 0.1 cm3/g.

公开(公告)号：US20220371887A1

公开(公告)日：2022-11-24

申请号：US17755613

申请日：2020-11-06

Applicant: Minoru TERADA ,  EVATEC CO., LTD.

Inventor： Minoru TERADA

IPC: C01B11/04 ,  B01J39/07 ,  B01J49/53

Abstract: Provided is a method for preparing a hypochlorous acid aqueous solution by which a weakly acidic hypochlorous acid aqueous solution having a pH of about 3.5-7 can be obtained without substantially generating chlorine gas even immediately after regeneration or even with a new weakly acidic cation exchange resin. In a method for preparing a hypochlorous acid aqueous solution wherein an aqueous solution of hypochlorite is brought into contact with a weakly acidic cation exchanger to exchange a cation constituting the hypochlorite with hydrogen ions to increase the concentration of hypochlorous acid in the aqueous solution, a neutral salt solution of a strong acid and a strong base in an amount that may obtain the hypochlorous acid aqueous solution having a pH of at least 3.5 when the hypochlorite aqueous solution is brought into contact with the weakly acidic cation exchanger is brought into contact, prior to the contact between the hypochlorite aqueous solution and the weakly acidic cation exchanger, with a weakly acidic cation exchanger that has been regenerated or has not been substantially subjected to cation exchange.

公开(公告)号：US20220016615A1

公开(公告)日：2022-01-20

申请号：US17324814

申请日：2021-05-19

Applicant: MICROCOSM TECHNOLOGY CO., LTD.

Inventor： Chun-Ting Yeh ,  Sih-Ci Jheng ,  Bo-Hung Lai

IPC: B01J39/19 ,  C08J5/22 ,  C08L63/00 ,  C08L79/08 ,  C08K5/3492 ,  B01J39/12 ,  B01J39/07 ,  B01J39/02

Abstract: A proton-conductive membrane includes a hydrophobic organic polymer and a hydrophilic proton-conductive component. The hydrophilic proton-conductive component includes one of an urea-containing material and a complex formed from an acidic substance and a basic substance, and a combination thereof. The hydrophilic proton-conductive component is present in an amount ranging from 23 parts by weight to 70 parts by weight based on 100 parts by weight of the proton-conductive membrane.

公开(公告)号：US20210386083A1

公开(公告)日：2021-12-16

申请号：US17282704

申请日：2019-10-03

Applicant: EUROSERUM

Inventor： Charlotte Bastian ,  Lydie Laurens ,  David Girardot

IPC: A23C9/146 ,  A23C9/142 ,  A23C17/00 ,  B01D61/14 ,  B01D61/16 ,  B01D71/02 ,  B01D69/02 ,  B01J39/07 ,  B01J39/20 ,  B01J47/02

Abstract: The method for producing a phospholipid concentrate derived from a liquid dairy composition comprising at least caseins and phospholipids, includes at least the steps of: —passing the dairy composition into an ion-exchange column on a cationic resin, —concentrating the phospholipids of the calcium-depleted dairy composition by means of controlled transmembrane pressure gradient microfiltration, and —recovering the retentate from the microfiltration and obtaining a phospholipid concentrate.

公开(公告)号：US11066751B2

公开(公告)日：2021-07-20

申请号：US16156360

申请日：2018-10-10

Applicant: AGC Inc.

Inventor： Yasushi Yamaki ,  Takayuki Kaneko ,  Hiromitsu Kusano ,  Takuo Nishio

IPC: C25B13/08 ,  B01J39/20 ,  B01J47/12 ,  C25B1/46 ,  B01J39/05 ,  B01J39/07 ,  C25B9/23

Abstract: To provide an ion exchange membrane for alkali chloride electrolysis which is a membrane having a high water permeability and being capable of maintaining a low electrolysis voltage while suppressing the amount of water supplied to a cathode chamber to be minimum, and which is capable of forming an aqueous alkali hydroxide solution having a high caustic alkali quality. The ion exchange membrane for alkali chloride electrolysis comprises a layer 12 made of a fluorinated polymer having carboxylic acid functional groups, and a layer 14A and a layer 14B made of a fluorinated polymer having sulfonic acid functional groups, wherein a reinforcing material 20 containing reinforcing threads 22 is disposed between the layer 14A and the layer 14B, the thickness when dried, of the layer 12 is from 9 to 28 μm, the layer 14B includes a layer having an ion exchange capacity of from 1.3 to 2.5 meq/g, the thickness when dried, of the layer 14B is from 6 to 100 μm, the layer 14A includes a layer having an ion exchange capacity of from 0.9 to 1.25 meq/g, and the thickness when dried, of the layer 14A is from 40 to 110 μm.

公开(公告)号：US10947268B2

公开(公告)日：2021-03-16

申请号：US16324595

申请日：2017-08-10

Applicant: BRISTOL-MYERS SQUIBB COMPANY

Inventor： Zhengjian Li ,  Xuankuo Xu ,  Chao Huang ,  Zhiqiang Chen

IPC: C07K1/18 ,  C07K16/00 ,  B01J39/07 ,  B01J39/20 ,  B01J39/22 ,  C07K1/22

Abstract: In some embodiments, the present invention provides a method of purifying a protein of interest with a reduced level of aggregation formation in cation exchange (CEX) chromatography, comprising: (a) providing a mixture comprising the protein of interest and one or more contaminants; (b) loading the mixture onto a CEX resin coupled with arginine; and (c) eluting the protein of interest from the resin, thereby purifying the protein of interest with a reduced level of aggregation formation in CEX chromatography.

公开(公告)号：US10919032B2

公开(公告)日：2021-02-16

申请号：US16252614

申请日：2019-01-19

Applicant: Florida State University Research Foundation, Inc.

Inventor： Joseph Schlenoff ,  Yara Ghoussoub

IPC: B01J47/014 ,  B01J41/14 ,  C02F1/42 ,  B01J41/07 ,  B01J39/05 ,  B01J41/05 ,  B01J39/07 ,  B01J43/00 ,  B01J47/016 ,  C02F101/30

Abstract: Compositions that include an ion exchange resin and a polyelectrolyte. The polyelectrolyte may be adsorbed to at least a portion of a surface of the ion exchange resin. Methods of treating a liquid with a composition, and methods of forming a composition that includes an ion exchange resin and a polyelectrolyte.

公开(公告)号：US10913058B2

公开(公告)日：2021-02-09

申请号：US16067041

申请日：2016-12-16

Applicant: Dow Global Technologies LLC

Inventor： Kaoru Ohba ,  Kenji Takano ,  Masonori Iida ,  Shinnosuke Abe ,  Takashi Masudo ,  Osamu Kishizaki ,  Ryo Ishibashi ,  Yusuke Yamashita

IPC: C07C67/56 ,  B01J47/04 ,  B01J41/07 ,  B01D15/00 ,  B01J39/05 ,  B01J39/07 ,  B01D15/36 ,  B01J39/18 ,  B01J41/12

Abstract: Methods for the removal of ionic contaminants from hydrolysable organic solvent by ion exchange resins are described. A mixed bed of ion exchange resin with cationic ion exchange resin and weak-base anionic ion exchange resin is used in such methods.