GB867152A - Method of oxygen recycle in ozonization - Google Patents
Method of oxygen recycle in ozonizationInfo
- Publication number
- GB867152A GB867152A GB11435/59A GB1143559A GB867152A GB 867152 A GB867152 A GB 867152A GB 11435/59 A GB11435/59 A GB 11435/59A GB 1143559 A GB1143559 A GB 1143559A GB 867152 A GB867152 A GB 867152A
- Authority
- GB
- United Kingdom
- Prior art keywords
- oxygen
- oxide
- solid absorbent
- ozone
- ozonide
- 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.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
- C11C3/00—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
- C11C3/006—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by oxidation
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
- C01B13/10—Preparation of ozone
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Inorganic Chemistry (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Treating Waste Gases (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
<PICT:0867152/IV (b)/1> <PICT:0867152/IV (b)/2> In the production of an ozonide by reacting ozonised oxygen e.g. containing 2% of ozone, with an unsaturated carboxylic acid, removing entrained organic substances from the used oxygen by contracting with a solid absorbent, reozonising the purified oxygen, and recycling to the ozonide production step, residual ozone in the oxygen is decomposed before the contact with the solid absorbent by contacting with a catalyst comprising one or more of an iron oxide, cupric oxide, silver oxide, nickelous oxide, and barium peroxide. The oxygen may e.g. be passed through a rusted mild steel tube or a glass tube containing rusted mild steel turnings or an iron oxide produced by the interaction of ferrous sulphate or ferric nitrate and sodium carbonate. The catalyst may alternatively be prepared by pelleting and calcining a mixture of diatomaceous earth and a saturated solution of cupric nitrate. The temperature of decomposition may be 15-100 DEG C. The solid absorbent may be active silica, alumina, or carbon. The carboxylic acid may be commercial oleic acid or rice bran fatty acid, and may be mixed with a solvent consisting of caproic and pelargonic acid. As shown oxygen is passed round a cycle comprising an ozoniser 1, a reactor 2, a cyclone 3, a water wash tower 4, an ozone decomposer 5, an absorber 6, and a blower 7.ALSO:In the production of an ozonide by reacting ozonised oxygen, e.g. containing 2% of <PICT:0867152/III/1> <PICT:0867152/III/2> ozone, with an unsaturated carboxylic acid, removing entrained organic substances from the used oxygen by contacting with a solid absorbent, reozonising the purified oxygen, and recycling to the ozonide production step, residual ozone in the oxygen is decomposed before the contact with the solid absorbent by contacting with a catalyst comprising one or more of an iron oxide, cupric oxide, silver oxide, nickelous oxide, and barium peroxide. The oxygen may, e.g. be passed through a rusted mild steel tube or a glass tube containing rusted mild steel turnings or an iron oxide produced by the interaction of ferrous sulphate or ferric nitrate and sodium carbonate. The catalyst may alternatively be prepared by pelleting and calcining a mixture of diatomaceous earth and a saturated solution of cupric nitrate. The temperature of decomposition may be 15-100 DEG C. The solid absorbent may be active silica, alumina, or carbon. The carboxylic acid may be commercial oleic acid or rice bran fatty acid, and may be mixed with a solvent consisting of caproic and pelargonic acid. As shown oxygen is passed round a cycle comprising an ozoniser 1, a reactor 2, a cyclone 3, a water wash tower 4, an ozone decomposer 5, an absorber 6, and a blower 7.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP867152X | 1958-04-07 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB867152A true GB867152A (en) | 1961-05-03 |
Family
ID=13894577
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB11435/59A Expired GB867152A (en) | 1958-04-07 | 1959-04-03 | Method of oxygen recycle in ozonization |
Country Status (2)
Country | Link |
---|---|
DE (1) | DE1103308B (en) |
GB (1) | GB867152A (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4343776A (en) * | 1980-12-22 | 1982-08-10 | Engelhard Corporation | Ozone abatement catalyst having improved durability and low temperature performance |
DE3632937A1 (en) * | 1986-09-27 | 1988-03-31 | Bbc Brown Boveri & Cie | METHOD FOR PRODUCING OZONE |
DE102006021438A1 (en) | 2006-05-09 | 2007-11-15 | Cognis Ip Management Gmbh | Ozonolysis of unsaturated compound comprises carrying out the reaction in a structured reactor |
-
1959
- 1959-04-03 GB GB11435/59A patent/GB867152A/en not_active Expired
- 1959-04-06 DE DET16502A patent/DE1103308B/en active Pending
Also Published As
Publication number | Publication date |
---|---|
DE1103308B (en) | 1961-03-30 |
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