GB867152A - Method of oxygen recycle in ozonization - Google Patents

Method of oxygen recycle in ozonization

Info

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
Application number
GB11435/59A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toyo Koatsu Industries Inc
Original Assignee
Toyo Koatsu Industries Inc
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 Toyo Koatsu Industries Inc filed Critical Toyo Koatsu Industries Inc
Publication of GB867152A publication Critical patent/GB867152A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11CFATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
    • C11C3/00Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
    • C11C3/006Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by oxidation
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B13/00Oxygen; Ozone; Oxides or hydroxides in general
    • C01B13/10Preparation 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.
GB11435/59A 1958-04-07 1959-04-03 Method of oxygen recycle in ozonization Expired GB867152A (en)

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)

* Cited by examiner, † Cited by third party
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

Also Published As

Publication number Publication date
DE1103308B (en) 1961-03-30

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