GB977496A - Process for preparing acetic acid by catalytic oxidation of propylene - Google Patents
Process for preparing acetic acid by catalytic oxidation of propyleneInfo
- Publication number
- GB977496A GB977496A GB2527563A GB2527563A GB977496A GB 977496 A GB977496 A GB 977496A GB 2527563 A GB2527563 A GB 2527563A GB 2527563 A GB2527563 A GB 2527563A GB 977496 A GB977496 A GB 977496A
- Authority
- GB
- United Kingdom
- Prior art keywords
- catalyst
- molybdenum
- mixture
- acetic acid
- tin
- 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
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
- C07C51/25—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of unsaturated compounds containing no six-membered aromatic ring
- C07C51/252—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of unsaturated compounds containing no six-membered aromatic ring of propene, butenes, acrolein or methacrolein
Abstract
Acetic acid is obtained by reacting oxygen or an oxygen-containing gas with propylene in the gaseous phase at elevated temperature in the presence of a catalyst comprising both molybdenum and tin in the form of an oxide or oxides. In addition to acetic acid an appreciable amount of acrolein is obtained as well as small amounts of other products including acetaldehyde, acrylic acid, formic acid and formaldehyde. The catalyst may comprise a mixture of one or more molybdenum oxides with one or more tin oxides or may comprise an oxidic compound of molybdenum and tin, either alone or together with another oxide of one or both of the said metals. The oxidation is preferably carried out at between 250 and 400 DEG C. although higher or lower temperatures e.g. 200 DEG to 250 DEG C. or 400 DEG to 600 DEG C. may be used. It is preferred to operate under normal pressure but higher or lower pressures may be used. The process is preferably effected by leading a mixture of propylene and oxygen-containing gas e.g. air if desired in the presence of an inert gas or vapour, preferably steam, through a fixed bed of the catalysts mass but oxidation may also be effected in a fluidized catalyst bed or in successive fluidized and fixed catalyst beds. When air is used as the oxygen-containing gas good results are obtained by using 0.1 to 2.5 moles of oxygen and from 0.5 to 15 moles of steam per mole of propylene. The catalyst may be prepared by intimately mixing the constituents either alone or together with a carrier material and granulating or tabletting the mixture or by suspending the constituents either alone or together with a carrier material in water, evaporating the suspension with stirring and catalytically activating the resulting mass by drying and heating, e.g., to 400 DEG to 600 DEG C. Alternatively, the catalyst may be obtained by impregnating carrier material with an aqueous solution of a readily decomposable molybdenum salt, e.g. ammonium molybdate, and then adding the other component either as such or in the form of an aqueous solution of a salt of a volatile acid, e.g. stannic chloride, evaporating the suspension and then drying and heating. Suitable carrier materials are silica gel, clay, pumice stone, aluminium phosphate, aluminium oxide, boron phosphate and carborundum. The catalyst used may suitably correspond to the composition Sn-(MoO4)2 or to a mixture of one mole of the latter with one mole of SnO2 or MoO3. The recovery of the oxidation products may be effected by contacting the gas mixture with water at a temperature above the boiling point of acrolein to absorb the acetic acid and then contacting all or part of the gas stream issuing from the acetic acid absorber with water at a temperature below the boiling point of acrolein to absorb the latter. Specification 839,808 is referredALSO:A catalyst used for the oxidation of propylene to form acetic acid (see Division C2) comprises both molybdenum and tin in the form of an oxide or oxides. The catalyst may comprise a mixture of one or more molybdenum oxides with one or more tin oxides or may comprise an oxidic compound of molybdenum and tin either alone or mixed with another oxide of one or both of the said metals. It may be obtained by either (a) intimately mixing the constituents, e.g. MoO3 and SnO2, either alone or with a carrier material and granulating or tableting the mixture, (b) by suspending the constituents, e.g. MoO3 and SnO2, (with or without a carrier) in water, evaporating the suspension with stirring and finally drying and heating the resulting mass, e.g. at 400-600 DEG C., or (c) by impregnating a carrier with an aqueous solution of a readily decomposable molybdenum salt, e.g. ammonium molybdate, adding the other component either as such or in the form of an aqueous solution of a salt of a volatile acid, e.g. stannic chloride, evaporating the suspension and then drying and heating, e.g. at 400-600 DEG C. Specified carriers are silica gel, clay, pumice stone, aluminium phosphate, aluminium oxide, boron phosphate or carborundum. Specification 839,808 is referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL280186 | 1962-06-26 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB977496A true GB977496A (en) | 1964-12-09 |
Family
ID=19753926
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2527563A Expired GB977496A (en) | 1962-06-26 | 1963-06-25 | Process for preparing acetic acid by catalytic oxidation of propylene |
Country Status (5)
Country | Link |
---|---|
AT (1) | AT240347B (en) |
BE (1) | BE634086A (en) |
CH (1) | CH436247A (en) |
ES (1) | ES289307A1 (en) |
GB (1) | GB977496A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0294845A1 (en) * | 1987-06-12 | 1988-12-14 | Union Carbide Corporation | Acetic acid from ethane, ethylene and oxygen |
CN109894127A (en) * | 2017-12-07 | 2019-06-18 | 中国科学院大连化学物理研究所 | A kind of preparation of rare earth phosphate catalyst and its prepare application in acrylic acid (methyl esters) |
CN114425379A (en) * | 2020-10-15 | 2022-05-03 | 中国石油化工股份有限公司 | Catalyst for preparing acrolein by propylene oxidation and preparation method and application thereof |
-
1963
- 1963-06-21 CH CH776463A patent/CH436247A/en unknown
- 1963-06-24 ES ES289307A patent/ES289307A1/en not_active Expired
- 1963-06-25 GB GB2527563A patent/GB977496A/en not_active Expired
- 1963-06-26 AT AT512663A patent/AT240347B/en active
- 1963-06-29 BE BE634086A patent/BE634086A/en unknown
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0294845A1 (en) * | 1987-06-12 | 1988-12-14 | Union Carbide Corporation | Acetic acid from ethane, ethylene and oxygen |
CN109894127A (en) * | 2017-12-07 | 2019-06-18 | 中国科学院大连化学物理研究所 | A kind of preparation of rare earth phosphate catalyst and its prepare application in acrylic acid (methyl esters) |
CN109894127B (en) * | 2017-12-07 | 2021-10-29 | 中国科学院大连化学物理研究所 | Preparation of rare earth phosphate catalyst and application thereof in preparation of acrylic acid or methyl acrylate |
CN114425379A (en) * | 2020-10-15 | 2022-05-03 | 中国石油化工股份有限公司 | Catalyst for preparing acrolein by propylene oxidation and preparation method and application thereof |
CN114425379B (en) * | 2020-10-15 | 2024-01-26 | 中国石油化工股份有限公司 | Catalyst for preparing acrolein by propylene oxidation and preparation method and application thereof |
Also Published As
Publication number | Publication date |
---|---|
CH436247A (en) | 1967-05-31 |
AT240347B (en) | 1965-05-25 |
ES289307A1 (en) | 1963-11-16 |
BE634086A (en) | 1963-12-27 |
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