CA2612545A1 - Process for the production of hydrogen peroxide and chlorate - Google Patents
Process for the production of hydrogen peroxide and chlorate Download PDFInfo
- Publication number
- CA2612545A1 CA2612545A1 CA002612545A CA2612545A CA2612545A1 CA 2612545 A1 CA2612545 A1 CA 2612545A1 CA 002612545 A CA002612545 A CA 002612545A CA 2612545 A CA2612545 A CA 2612545A CA 2612545 A1 CA2612545 A1 CA 2612545A1
- Authority
- CA
- Canada
- Prior art keywords
- mediator
- organic
- group
- organic salt
- anode
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/24—Halogens or compounds thereof
- C25B1/26—Chlorine; Compounds thereof
- C25B1/265—Chlorates
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/28—Per-compounds
- C25B1/30—Peroxides
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- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Cosmetics (AREA)
- Saccharide Compounds (AREA)
Abstract
The invention relates to a process for the production of alkali metal chlorate comprising: providing an electrochemical cell comprising an anode and a cathode in separate anode and cathode compartments; contacting the cathode with an electrolyte comprising at least one organic mediator and one or more organic or mineral acids; reacting the organic mediator at the cathode to form at least one reduced form of the mediator; reacting the at least one reduced form of the mediator with oxygen to form hydrogen peroxide; contacting the anode with an anolyte comprising alkali metal chloride; reacting chloride at the anode to form chlorine that is hydrolysed; and, reacting the hydrolysed chlorine to form chlorate.
Claims (19)
1. ~Process for the production of alkali metal chlorate comprising:
providing an electrochemical cell comprising an anode and a cathode in separate anode and cathode compartments;
contacting the cathode with an electrolyte comprising at least one organic mediator and one or more organic or mineral acids;
reacting the organic mediator at the cathode to form at least one reduced form of the mediator;
reacting the at least one reduced form of the mediator with oxygen to form hydrogen peroxide;
contacting the anode with an anolyte comprising alkali metal chloride;
reacting chloride at the anode to form chlorine that is hydrolysed; and, reacting the hydrolysed chlorine to form chlorate.
providing an electrochemical cell comprising an anode and a cathode in separate anode and cathode compartments;
contacting the cathode with an electrolyte comprising at least one organic mediator and one or more organic or mineral acids;
reacting the organic mediator at the cathode to form at least one reduced form of the mediator;
reacting the at least one reduced form of the mediator with oxygen to form hydrogen peroxide;
contacting the anode with an anolyte comprising alkali metal chloride;
reacting chloride at the anode to form chlorine that is hydrolysed; and, reacting the hydrolysed chlorine to form chlorate.
2. ~Process as claimed in claim 1, wherein the concentration of chloride ions in the anolyte is from about 30 to about 300 g/l, calculated as sodium chloride.
3. ~Process as claimed in any one of the claims 1-2, wherein the pH in the bulk of the anolyte is from about 4 to about 10.
4. ~Process as claimed in any one of the claims 1-3, wherein the electrochemical cell comprises at least one compartment between the anode- and cathode compartments.
5. ~Process as claimed in any one of the claims 1-4, wherein the organic mediator is selected from the group consisting of quinones, flavoquinones, pyridine derivates, and ketones.
6. ~Process as claimed in claim 5, wherein the organic mediator is selected from the group consisting of quinones containing a (benzo)quinone-moiety.
7. ~Process as claimed in claim 6, wherein the organic mediator is selected from the group consisting of anthraquinones, tetrahydro anthraquinones, naphtoquinones, benzoquinones and derivates thereof.
8. ~Process as claimed in any one of the claims 1-7, wherein the content of organic mediator, including the reduced forms, in the catholyte is at least about 1 wt%.
9. ~Process as claimed in any one of the claims 1-8, wherein the catholyte comprises an at least partially organic salt, comprising at least one kind of organic cation and/or organic anion.
10. ~Process as claimed in claim 9, wherein the content of the at least partially organic salt in the catholyte is from about 20 wt% to about 99 wt%.
11. Process as claimed in any one of the claims 9-10, wherein the at least partially organic salt is present together with a neutral co-solvent and the weight ratio salt to co-solvent is from about 1:1 to about 1000:1.
12. Process as claimed in any one of the claims 9-11, wherein a neutral co-solvent is present in the catholyte in an amount up to about 50 wt%.
13. Process as claimed in any one of the claims 9-12, wherein the at least partially organic salt that in itself or in combination with a neutral co-solvent forms a liquid phase at atmospheric pressure below about 130°C.
14. Process as claimed in any one of the claims 9-13, wherein the at least partially organic salt at 100°C has a partial pressure below about 10 kPa.
15. Process as claimed in any one of the claims 9-14, wherein the at least partially organic salt comprises a cation selected from the group consisting of 1-alkyl-3-methyl imidiazolium, 1-butyl-3-methyl imidazolium [BMIM], 1-ethyl-3-methyl imidazolium [EMIM], 1,2,3-trimethyl imidazolium, N-alkylpyridinium, N-butyl pyridinium [BPY], pyrrolidinium, guanidinium and alkyl guanidinium, isouronium, PR4+, NR4+, SR3+, tetramethylammonium, choline, cocomonium, and mixtures thereof, R being, independently of each other, optionally substituted alkyl, alkenyl or aryl, or hydrogen.
16. Process as claimed in any one of the claims 9-15, wherein the at least partially organic salt comprises a cation selected from the group consisting of substituted quinones.
17. Process as claimed in any one of the claims 9-16, wherein the at least partially organic salt comprises an anion selected from the group consisting of hexafluorophosphate [HFP], tetrafluoroborate [TFB], fluorosulfonate, hexafluoroantimonate hexafluoroarsenate, chloroaluminate, bromoaluminate, bis(trifluoromethylsulfonyl)imide, tris(trifluoromethylsulfonyl)methide, tricyanomethide, dicyanamide, nonafluorobutanesulfonate, trifluoromethane sulfonate, 2,2,2-trifluororethanesulfonate, nitrate, sulphate, phosphate, RPO42-, R2PO4 , R2PO2 (e.g. a dialkylphosphinate), perchlorate, actetate, alkylsul phonate, bis(2-ethylhexyl)sodium sulfosuccinate, diethyleneglycolmonomethylethersulfate, alkyloligoethersulfate, pivalate, tetraalkylborate, propionate, succinate, saccharinate, glycolate, stearate, lactate, malate, tartrate, citrate, ascorbate, glutamate, benzoate, salicylate, methanesulfonate, toluenesulfonate, and mixtures thereof, R being, independently of each other, optionally substituted alkyl, alkenyl or aryl, or hydrogen.
18. Process as claimed in any one of the claims 9-17, wherein the at least partially organic salt comprises an anion selected from the group consisting of substituted quinones.
19. ~Process as claimed in any one of the claims 9-18, wherein the at least partially organic salt comprises a cation selected from the group consisting of [1,3-dialkyl imidazolium], [trialkylammonium], [tetraalkylammonium], [trialkylphosphonium], [tetraalkylphosphonium], [alkylpyridinium], [choline], [Q-NR3+] and [Q-PR3+]
and an anion selected from the group consisting of [sulphate], [phosphate], [alkyl sulphate], [alkyl sulphonate], [dialkyl phosphate], [alkyl phosphonate], [Q-(O)-S03] and [Q-(O)-PO3R-], where Q is a quinone, (0) is an optional oxygen and R is, independently of each other, optionally substituted alkyl, alkenyl or aryl, or hydrogen.
and an anion selected from the group consisting of [sulphate], [phosphate], [alkyl sulphate], [alkyl sulphonate], [dialkyl phosphate], [alkyl phosphonate], [Q-(O)-S03] and [Q-(O)-PO3R-], where Q is a quinone, (0) is an optional oxygen and R is, independently of each other, optionally substituted alkyl, alkenyl or aryl, or hydrogen.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP05105885.7 | 2005-06-30 | ||
EP05105885 | 2005-06-30 | ||
PCT/SE2006/050183 WO2007004971A1 (en) | 2005-06-30 | 2006-06-02 | Process for the production of hydrogen peroxide and chlorate |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2612545A1 true CA2612545A1 (en) | 2007-01-11 |
CA2612545C CA2612545C (en) | 2010-04-06 |
Family
ID=35385846
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA2612545A Expired - Fee Related CA2612545C (en) | 2005-06-30 | 2006-06-02 | Process for the production of hydrogen peroxide and chlorate |
Country Status (8)
Country | Link |
---|---|
EP (1) | EP1896632B1 (en) |
CN (1) | CN101213324B (en) |
AT (1) | ATE423861T1 (en) |
BR (1) | BRPI0612885B1 (en) |
CA (1) | CA2612545C (en) |
DE (1) | DE602006005363D1 (en) |
RU (1) | RU2375500C2 (en) |
WO (1) | WO2007004971A1 (en) |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA2760094C (en) * | 2009-05-15 | 2018-03-20 | Akzo Nobel Chemicals International B.V. | Activation of cathode |
RU2494960C2 (en) * | 2010-09-16 | 2013-10-10 | Российская Федерация, от имени которой выступает Министерство образования и науки РФ (Минобрнаука РФ) | Method of obtaining hydrogen peroxide |
US8562810B2 (en) | 2011-07-26 | 2013-10-22 | Ecolab Usa Inc. | On site generation of alkalinity boost for ware washing applications |
US10011549B2 (en) * | 2015-07-06 | 2018-07-03 | Robert Bosch Gmbh | Electrochemically active agents for pH modulation in biological buffers |
KR20240035640A (en) * | 2015-10-27 | 2024-03-15 | 메사추세츠 인스티튜트 오브 테크놀로지 | Electrochemical process for gas separation |
EP3323779B1 (en) * | 2016-11-18 | 2020-06-03 | Diehl Aviation Gilching GmbH | Method for generating oxygen using ionic liquids for decomposing peroxides |
CN109055966A (en) * | 2018-09-13 | 2018-12-21 | 北京化工大学 | A kind of chemical combined method for preparing chlorine dioxide of electrochemistry- |
CN113149063A (en) * | 2020-01-22 | 2021-07-23 | 付冬 | Method for preparing calcium stannate nano particles and method for preparing corresponding electrode |
EP4283018A1 (en) * | 2022-05-24 | 2023-11-29 | Siemens Energy Global GmbH & Co. KG | Method of producing a concentrated hydrogen peroxide solution |
Family Cites Families (3)
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 |
JPS61284591A (en) * | 1985-06-10 | 1986-12-15 | Japan Carlit Co Ltd:The | Production of hydrogen peroxide |
US6712949B2 (en) * | 2001-07-22 | 2004-03-30 | The Electrosynthesis Company, Inc. | Electrochemical synthesis of hydrogen peroxide |
-
2006
- 2006-06-02 EP EP06748023A patent/EP1896632B1/en not_active Not-in-force
- 2006-06-02 CN CN2006800237190A patent/CN101213324B/en not_active Expired - Fee Related
- 2006-06-02 BR BRPI0612885A patent/BRPI0612885B1/en not_active IP Right Cessation
- 2006-06-02 WO PCT/SE2006/050183 patent/WO2007004971A1/en active Application Filing
- 2006-06-02 RU RU2008103350/15A patent/RU2375500C2/en not_active IP Right Cessation
- 2006-06-02 AT AT06748023T patent/ATE423861T1/en not_active IP Right Cessation
- 2006-06-02 CA CA2612545A patent/CA2612545C/en not_active Expired - Fee Related
- 2006-06-02 DE DE602006005363T patent/DE602006005363D1/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
ATE423861T1 (en) | 2009-03-15 |
CA2612545C (en) | 2010-04-06 |
CN101213324B (en) | 2011-09-07 |
BRPI0612885B1 (en) | 2017-03-07 |
CN101213324A (en) | 2008-07-02 |
WO2007004971A1 (en) | 2007-01-11 |
DE602006005363D1 (en) | 2009-04-09 |
BRPI0612885A2 (en) | 2010-12-07 |
RU2375500C2 (en) | 2009-12-10 |
EP1896632A1 (en) | 2008-03-12 |
EP1896632B1 (en) | 2009-02-25 |
RU2008103350A (en) | 2009-08-10 |
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EEER | Examination request | ||
MKLA | Lapsed |
Effective date: 20160602 |