JPWO2021025991A5 - - Google Patents

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JPWO2021025991A5
JPWO2021025991A5 JP2022502916A JP2022502916A JPWO2021025991A5 JP WO2021025991 A5 JPWO2021025991 A5 JP WO2021025991A5 JP 2022502916 A JP2022502916 A JP 2022502916A JP 2022502916 A JP2022502916 A JP 2022502916A JP WO2021025991 A5 JPWO2021025991 A5 JP WO2021025991A5
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electrochemical cell
actinic radiation
outlet
electrolyte
reactor
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JP2022502916A
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Japanese (ja)
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JP2022542227A (en
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Priority claimed from PCT/US2020/044476 external-priority patent/WO2021025991A1/en
Publication of JP2022542227A publication Critical patent/JP2022542227A/en
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Claims (21)

化学線放射反応器、
過酸化水素を生成するように構成され、電解液源と化学線放射反応器との間に流体連通する出口を有する電気化学セル、および
電気化学セルの入口と連通する酸素源を含む、水処理システム。
actinic radiation reactor,
Water treatment comprising: an electrochemical cell configured to produce hydrogen peroxide and having an outlet in fluid communication between an electrolyte source and an actinic radiation reactor; and an oxygen source in communication with the electrochemical cell inlet. system.
電解液源を電気化学セルの入口に流体的に結合する第1の導管、および、
電気化学セルの出口と化学線放射反応器の入口とを流体的に結合する第2の導管をさらに含む、請求項1に記載のシステム。
a first conduit fluidly coupling the electrolyte source to the inlet of the electrochemical cell; and
2. The system of claim 1, further comprising a second conduit fluidly coupling the outlet of the electrochemical cell and the inlet of the actinic radiation reactor.
電気化学セルの出口が、電解液源を電気化学セルの入口に流体的に結合する導管の導入点に流体的に結合される、請求項1に記載のシステム。 2. The system of claim 1, wherein the outlet of the electrochemical cell is fluidly coupled to an entry point of a conduit that fluidly couples the electrolyte source to the inlet of the electrochemical cell. 前記化学線放射反応器が、紫外線促進酸化プロセス反応器である、請求項1に記載のシステム。 2. The system of claim 1, wherein said actinic radiation reactor is an ultraviolet-enhanced oxidation process reactor. 電解液が水を含む、請求項1に記載のシステム。 2. The system of claim 1, wherein the electrolyte comprises water. 電気化学セルの出口に結合された貯蔵タンクをさらに含む、請求項1に記載のシステム。 3. The system of claim 1, further comprising a storage tank coupled to the outlet of the electrochemical cell. 前記化学線放射反応器の出口に流体的に結合された導管、および、
前記化学線放射反応器の出口の下流で前記導管と流体連通している出口を有する第2の電気化学セルであって、前記導管内の処理水溶液中に存在する過酸化水素をクエンチする化学薬剤を生成するように構成された前記第2の電気化学セルをさらに含む、請求項1に記載のシステム。
a conduit fluidly coupled to the outlet of the actinic radiation reactor; and
A second electrochemical cell having an outlet in fluid communication with the conduit downstream of the outlet of the actinic radiation reactor, the chemical agent for quenching hydrogen peroxide present in the aqueous treatment solution within the conduit. 2. The system of claim 1, further comprising said second electrochemical cell configured to generate a .
前記第2の電気化学セルの出口に結合された貯蔵タンクをさらに含む、請求項7に記載のシステム。 8. The system of claim 7, further comprising a storage tank coupled to the outlet of said second electrochemical cell. 前記化学薬剤が、次亜塩素酸ナトリウムを含む、請求項7に記載のシステム。 8. The system of Claim 7, wherein the chemical agent comprises sodium hypochlorite. 前記導管が、前記化学線放射反応器の前記出口を前記第2の電気化学セルの入口に流体的に連結している、請求項7に記載のシステム。 8. The system of claim 7, wherein said conduit fluidly connects said outlet of said actinic radiation reactor to an inlet of said second electrochemical cell. 前記第2の電気化学セルの前記出口が、前記化学線放射反応器の前記出口の下流にある前記導管の導入点に流体的に結合されている、請求項7に記載のシステム。 8. The system of claim 7, wherein said outlet of said second electrochemical cell is fluidly coupled to an introduction point of said conduit downstream of said outlet of said actinic radiation reactor. 水溶液中の1つ以上の汚染物質の濃度を測定するように構成されたセンサをさらに含み、前記センサは、前記化学線放射反応器の上流または前記化学線放射反応器の下流のいずれかに配置される、請求項1から11のいずれかに記載のシステム。 Further comprising a sensor configured to measure the concentration of one or more contaminants in an aqueous solution, said sensor positioned either upstream of said actinic radiation reactor or downstream of said actinic radiation reactor. 12. The system of any of claims 1-11, wherein the system is 前記センサと通信し、前記1つ以上の汚染物質の測定された濃度に応答して、前記システムの1つ以上の動作パラメータを調整するように構成されたコントローラをさらに含む、請求項12に記載のシステム。 13. The method of claim 12, further comprising a controller in communication with the sensor and configured to adjust one or more operating parameters of the system in response to the measured concentration of the one or more contaminants. system. 前記1つ以上の動作パラメータは、前記電気化学セルに加えられる電力、前記第2の電気化学セルに加えられる電力、前記化学線放射反応器に加えられる電力、および前記電気化学セル、前記第2の電気化学セル、もしくは前記化学線放射反応器のうちの1つを通る電解液または水溶液の流量のうちの1つを含む、請求項13に記載のシステム。 The one or more operating parameters include power applied to the electrochemical cell, power applied to the second electrochemical cell, power applied to the actinic radiation reactor, and power applied to the electrochemical cell, the second or flow of an electrolyte or aqueous solution through one of said actinic radiation reactors. 前記酸素源は、前記電気化学セルの上流で前記電解液に前記酸素を導入するように構成される、請求項13に記載のシステム。 14. The system of claim 13, wherein the oxygen source is configured to introduce the oxygen to the electrolyte upstream of the electrochemical cell. 前記コントローラは、前記1つ以上の汚染物質の前記測定された濃度に応答して、前記電解液への前記酸素の導入速度を調節するようにさらに構成される、請求項15に記載のシステム。 16. The system of Claim 15, wherein the controller is further configured to adjust the introduction rate of the oxygen to the electrolyte in response to the measured concentration of the one or more contaminants. 前記電解液源からの電解液の1つ以上の測定された特徴または前記化学線放射反応器で生成される処理水溶液の1つ以上の測定された特徴に基づいて、前記貯蔵タンクから前記化学線放射反応器への過酸化水素の流量を調整するように構成されたコントローラをさらに含む、請求項6に記載のシステム。 actinic radiation from the storage tank based on one or more measured characteristics of the electrolyte from the electrolyte source or one or more measured characteristics of the aqueous treatment solution produced in the actinic radiation reactor; 7. The system of Claim 6, further comprising a controller configured to regulate the flow rate of hydrogen peroxide to the radiative reactor. 前記電解液源からの電解液の1つ以上の測定された特徴または前記化学線放射反応器で生成された処理水溶液の1つ以上の測定された特徴に基づいて、前記貯蔵タンクから前記化学線放射反応器の前記出口の下流の前記導管への次亜塩素酸ナトリウムの流量を調整するように構成されたコントローラをさらに含む、請求項8に記載のシステム。 actinic radiation from the storage tank based on one or more measured characteristics of the electrolyte from the electrolyte source or one or more measured characteristics of the process aqueous solution produced in the actinic radiation reactor; 9. The system of claim 8, further comprising a controller configured to regulate a flow rate of sodium hypochlorite into the conduit downstream of the outlet of the radiative reactor. 前記化学線放射反応器の下流に、処理水溶液中の過酸化水素の濃度を測定するように構成されたセンサをさらに含む、請求項1から11のいずれかに記載のシステム。 12. The system of any of claims 1-11, further comprising a sensor downstream of the actinic radiation reactor configured to measure the concentration of hydrogen peroxide in the aqueous treatment solution. 前記センサと通信し、前記過酸化水素の測定濃度に基づいて前記第2の電気化学セルの1つ以上の動作パラメータを調整するように構成されたコントローラをさらに含む、請求項19に記載のシステム。 20. The system of Claim 19, further comprising a controller in communication with said sensor and configured to adjust one or more operating parameters of said second electrochemical cell based on said measured concentration of hydrogen peroxide. . 前記第2の電気化学セルの前記1つ以上の動作パラメータは、前記第2の電気化学セルに加えられる電力、前記第2の電気化学セルへの電解液の流量、前記第2の電気化学セルからの次亜塩素酸ナトリウムの流量、または前記第2の電気化学セルで生成される次亜塩素酸ナトリウムの濃度のうちの1つ以上を含む、請求項20に記載のシステム。 The one or more operating parameters of the second electrochemical cell are electrical power applied to the second electrochemical cell, electrolyte flow rate to the second electrochemical cell, 21. The system of claim 20, comprising one or more of a flow rate of sodium hypochlorite from, or a concentration of sodium hypochlorite produced in the second electrochemical cell.
JP2022502916A 2019-08-02 2020-07-31 Control of on-site electrochemical generation of hydrogen peroxide for UV-enhanced oxidation process control Pending JP2022542227A (en)

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US201962882244P 2019-08-02 2019-08-02
US62/882,244 2019-08-02
US202063058528P 2020-07-30 2020-07-30
US63/058,528 2020-07-30
PCT/US2020/044476 WO2021025991A1 (en) 2019-08-02 2020-07-31 Regulation of on-site electrochemical generation of hydrogen peroxide for ultraviolet advanced oxidation process control

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Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20240010529A1 (en) * 2020-10-19 2024-01-11 Evoqua Water Technologies Llc Combined electrochemical advanced oxidation process for removal of organic contamination in water
WO2023173037A2 (en) * 2022-03-11 2023-09-14 Aecom Systems and methods for destroying per- and polyfluoroalkyl substances (pfas) using an electrochemical (ec) reactor

Family Cites Families (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2453739C3 (en) * 1974-11-13 1980-03-27 Kernforschungsanlage Juelich Gmbh, 5170 Juelich Process for the production of hydrogen peroxide
SE412577B (en) * 1976-09-06 1980-03-10 Licento Ag APPARATUS FOR WATER CHLORIZATION
US5770033A (en) * 1993-07-13 1998-06-23 Lynntech, Inc. Methods and apparatus for using gas and liquid phase cathodic depolarizers
JPH09279377A (en) * 1996-04-11 1997-10-28 Takuma Co Ltd Producing device of hydrogen peroxide and its production
JP3909957B2 (en) * 1998-06-04 2007-04-25 クロリンエンジニアズ株式会社 Electrolyzer for hydrogen peroxide production
JP2001079544A (en) * 1999-09-16 2001-03-27 Chlorine Eng Corp Ltd Water treatment by ultraviolet-irradiation
WO2005038091A2 (en) * 2003-10-11 2005-04-28 Niksa Marilyn J Use of electrochemical cell to produce hydrogen peroxide and dissolved oxygen
WO2005084720A1 (en) * 2004-03-10 2005-09-15 Trojan Technologies Inc. System for predicting reduction in concentration of a target material in a flow of fluid
CN100453472C (en) * 2004-12-15 2009-01-21 中国科学院生态环境研究中心 Method and apparatus for highly efficient removal of water organisms by utilizing photoelectric Fenton reaction
GB2437956A (en) * 2006-04-11 2007-11-14 Dyson Technology Ltd Production of hydrogen peroxide
CA2689646A1 (en) 2007-06-04 2008-12-11 David T. Schwartzel Aqueous treatment apparatus utilizing precursor materials and ultrasonics to generate customized oxidation-reduction-reactant chemistry environments in electrochemical cells and/or similar devices
CN101250738B (en) * 2007-12-04 2011-09-14 东南大学 Photoelectrocatalysis oxidization preparation method for titanium alloy surface anticoagulant titanium white film
FR2994174B1 (en) * 2012-08-01 2015-08-07 Degremont METHOD AND INSTALLATION FOR PROCESSING SHIP BALLAST WATER
US9630863B2 (en) * 2014-03-28 2017-04-25 Neptune-Benson, Llc Advanced oxidation system and method in a UV reactor with electrode
AU2016220179B2 (en) 2015-02-17 2021-05-06 Evoqua Water Technologies Llc Reduced volume electrochlorination cells and methods of manufacturing same
US10961143B2 (en) 2015-05-04 2021-03-30 Evoqua Water Technologies Llc Method and system for providing ultrapure water with flexible lamp configuration
KR101713932B1 (en) * 2015-07-31 2017-03-10 주식회사 럭키산업 Method of preparing alginate having low molecular weight using hydrogen peroxide and ultrasonic wave
EP3350130A4 (en) * 2015-09-18 2019-03-13 Evoqua Water Technologies LLC In-situ delivery systems for reaction product abatement in electrochemical cells
CN106631760B (en) * 2015-10-29 2019-05-28 上海医药工业研究院 The preparation process of cis- 1- hydroxyl-[1,1 '-bis- (hexamethylenes)] -2- carboxylic acid
GB201604397D0 (en) * 2016-03-15 2016-04-27 Kp2M Ltd Treatment of fluids
CN108545804A (en) * 2018-05-08 2018-09-18 凡邸(天津)环保科技有限公司 A method of bacterium is killed based on bioelectrochemistry, advanced oxidation Fourier Series expansion technique
CN109621701A (en) * 2018-11-08 2019-04-16 天津大学 A kind of device of biology dystopy degradation of organic substances
CN110054326A (en) * 2019-04-30 2019-07-26 宁波神同环境科技有限公司 Pressurized fluid electric flocculation sewage treatment process and system

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