RU2003101340A - METHOD FOR PRODUCING HYDROGEN PEROXIDE AND COMPOSITION FOR ITS IMPLEMENTATION - Google Patents

METHOD FOR PRODUCING HYDROGEN PEROXIDE AND COMPOSITION FOR ITS IMPLEMENTATION

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Publication number
RU2003101340A
RU2003101340A RU2003101340/15A RU2003101340A RU2003101340A RU 2003101340 A RU2003101340 A RU 2003101340A RU 2003101340/15 A RU2003101340/15 A RU 2003101340/15A RU 2003101340 A RU2003101340 A RU 2003101340A RU 2003101340 A RU2003101340 A RU 2003101340A
Authority
RU
Russia
Prior art keywords
solvent
quinones
isodurol
working solution
amount
Prior art date
Application number
RU2003101340/15A
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Russian (ru)
Other versions
RU2235680C2 (en
Inventor
Матс НЮСТРЕМ
Кристина ЙЕРНВИК
Original Assignee
Акцо Нобель Н.В.
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Акцо Нобель Н.В. filed Critical Акцо Нобель Н.В.
Publication of RU2003101340A publication Critical patent/RU2003101340A/en
Application granted granted Critical
Publication of RU2235680C2 publication Critical patent/RU2235680C2/en

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Claims (9)

1. Способ получения пероксида водорода в соответствии с антрахиноновым способом, включающий поочередное гидрирование и окисление одного или более хинонов, выбранных из антрахинонов и/или тетрагидроантрахинонов, в рабочем растворе, содержащем, по меньшей мере, один растворитель для хинонов и, по меньшей мере, один растворитель для гидрохинонов, отличающийся тем, что, по меньшей мере, один растворитель для хинонов включает изодурол в количестве от 15 вес.% и дополнительно дурол в количестве, не превышающем около 25 вес.% от общего количества растворителей для хинонов.1. A method of producing hydrogen peroxide in accordance with the anthraquinone method, comprising alternately hydrogenating and oxidizing one or more quinones selected from anthraquinones and / or tetrahydroantraquinones, in a working solution containing at least one solvent for quinones and at least one solvent for hydroquinones, characterized in that at least one solvent for quinones includes isodurol in an amount of from 15 wt.% and additionally durene in an amount not exceeding about 25 wt.% of the total amount of diluents for quinones. 2. Способ по п.1, где, по меньшей мере, один растворитель для хинонов включает от около 20 до около 80 вес.% изодурола.2. The method according to claim 1, where at least one solvent for quinones includes from about 20 to about 80 wt.% Isodurol. 3. Способ по одному любому из пп.1 и 2, где рабочий раствор содержит от около 25 до около 70 вес.% изодурола.3. The method according to any one of claims 1 and 2, where the working solution contains from about 25 to about 70 wt.% Isodurol. 4. Способ по одному любому из пп.1-3, где общее количество изодурола и дурола в указанном, по меньшей мере, одном растворителе для хинонов составляет от около 30 до около 100 вес.% от содержания растворителей для хинонов.4. The method according to any one of claims 1 to 3, where the total amount of isodurol and durene in the specified at least one solvent for quinones is from about 30 to about 100 wt.% Of the content of solvents for quinones. 5. Способ по одному любому из пп.1-4, где весовое отношение изодурола к дуролу в рабочем растворе составляет от около 1,5:1 до 5:1.5. The method according to any one of claims 1 to 4, where the weight ratio of isodurol to durene in the working solution is from about 1.5: 1 to 5: 1. 6. Способ по одному любому из пп.1-5, где указанный, по меньшей мере, один растворитель для гидрохинонов включает один или более из ди-изобутилкарбинола или тетрабутилмочевины.6. The method according to any one of claims 1 to 5, wherein said at least one hydroquinone solvent comprises one or more of di-isobutylcarbinol or tetrabutylurea. 7. Способ по одному любому из пп.1-6, где молярное отношение тетрагидроантрахинонов к антрахинонам в рабочем растворе, подлежащем гидрированию, превышает 1:1.7. The method according to any one of claims 1 to 6, where the molar ratio of tetrahydroanthraquinones to anthraquinones in the working solution to be hydrogenated exceeds 1: 1. 8. Способ по одному любому из пп.1-7, где от около 50 до около 100 мол.% антрахинонов и тетрагидроантрахинонов замещены одной этильной группой.8. The method according to any one of claims 1 to 7, where from about 50 to about 100 mol.% Anthraquinones and tetrahydroantraquinones are substituted with one ethyl group. 9. Композиция, пригодная в качестве рабочего раствора при получении пероксида водорода антрахиноновым способом, содержащая один или более хинонов, выбранных из антрахинонов и/или тетрагидроантрахинонов, растворенных, по меньшей мере, в одном растворителе для хинонов и, по меньшей мере, одном растворителе для гидрохинонов, отличающаяся тем, что, по меньшей мере, один растворитель для хинонов включает изодурол в количестве от около 15 вес.% и дополнительно дурол в количестве, не превышающем 25 вес.% от общего количества растворителей для хинонов.9. A composition suitable as a working solution in the preparation of hydrogen peroxide by the anthraquinone method, containing one or more quinones selected from anthraquinones and / or tetrahydroanthraquinones dissolved in at least one quinone solvent and at least one solvent for hydroquinones, characterized in that at least one solvent for quinones includes isodurol in an amount of from about 15 wt.% and additionally durene in an amount not exceeding 25 wt.% of the total number of solvents for quinono in.
RU2003101340/15A 2000-06-19 2001-05-28 Hydrogen peroxide manufacture method and composition for realization of the method RU2235680C2 (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US21263300P 2000-06-19 2000-06-19
EP00850109.0 2000-06-19
EP00850109 2000-06-19
US60/212,633 2000-06-19

Publications (2)

Publication Number Publication Date
RU2003101340A true RU2003101340A (en) 2004-05-10
RU2235680C2 RU2235680C2 (en) 2004-09-10

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
RU2003101340/15A RU2235680C2 (en) 2000-06-19 2001-05-28 Hydrogen peroxide manufacture method and composition for realization of the method

Country Status (14)

Country Link
EP (1) EP1292533B1 (en)
JP (1) JP3992244B2 (en)
KR (1) KR100498786B1 (en)
CN (1) CN1233547C (en)
AT (1) ATE453602T1 (en)
AU (1) AU2001274712A1 (en)
BR (1) BR0111857B1 (en)
CA (1) CA2412956C (en)
CZ (1) CZ299805B6 (en)
ES (1) ES2338298T3 (en)
PL (1) PL200150B1 (en)
PT (1) PT1292533E (en)
RU (1) RU2235680C2 (en)
WO (1) WO2001098204A1 (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BRPI1013683A2 (en) * 2009-03-27 2016-04-26 Solvay process for the production of hydrogen peroxide
CN107539957B (en) * 2016-06-23 2020-10-27 中国石油化工股份有限公司 Solvent system for producing hydrogen peroxide by anthraquinone process, variable working solution and application
SE540100C2 (en) * 2016-12-29 2018-03-27 Eb Nuberg Ab Aromatic solvent for hydrogen peroxide production
FR3131292A1 (en) 2021-12-23 2023-06-30 Arkema France Hydrogen peroxide production process
FR3141158B1 (en) 2022-10-25 2024-10-04 Arkema France Process for the production of hydrogen peroxide
CN115924853B (en) * 2022-11-15 2024-01-05 黎明化工研究设计院有限责任公司 High-yield working liquid system for producing hydrogen peroxide by anthraquinone process

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB834154A (en) * 1957-02-25 1960-05-04 Columbia Southern Chem Corp Improvements in the preparation of hydrogen peroxide
DE1914739A1 (en) * 1969-03-22 1970-10-01 Degussa Process for the production of hydrogen peroxide
BE756015A (en) * 1969-09-10 1971-02-15 Degussa PROCESS FOR THE PREPARATION OF HYDROGEN PEROXIDE (E)
BE756013A (en) * 1969-09-10 1971-02-15 Degussa PROCESS FOR THE EXTRACTION OF HYDROGEN PEROXIDE FROM THE WORKING SOLUTIONS OF THE ANTHRAQUINONE PROCESS
DE2532819C3 (en) * 1975-07-23 1978-10-05 Deutsche Gold- Und Silber-Scheideanstalt Vormals Roessler, 6000 Frankfurt Process for the production of hydrogen peroxide

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