GB800847A - Process for the hydrogenation of aliphatic mono- and dicarboxylic acids - Google Patents
Process for the hydrogenation of aliphatic mono- and dicarboxylic acidsInfo
- Publication number
- GB800847A GB800847A GB21195/56A GB2119556A GB800847A GB 800847 A GB800847 A GB 800847A GB 21195/56 A GB21195/56 A GB 21195/56A GB 2119556 A GB2119556 A GB 2119556A GB 800847 A GB800847 A GB 800847A
- Authority
- GB
- United Kingdom
- Prior art keywords
- catalyst
- per cent
- hydrogenation
- aliphatic mono
- caustic
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/80—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with zinc, cadmium or mercury
Abstract
A catalyst for the hydrogenation of aliphatic mono- and di-carboxylic acids and esters thereof comprises a Zn-Cu-Al alloy surface-etched with caustic alkali, the Zn content being 5-40 per cent and the Al and Cu contents each 30-60 per cent. The preferred composition is Zn20, Cu40, Al40. The catalyst is made by melting the constituents together in an inert atmosphere, grinding to any desired size from lumps to powder, and heating to 50-100 DEG C. with caustic soda or caustic potash solution for 10-120 minutes. The activated catalyst is then washed with water and another solvent (e.g. methanol) and dried away from air. The catalyst becomes inactive in use and can be regenerated 10-20 times by the same process as above. Examples are given of the preparation of typical catalysts.ALSO:Aliphatic mono- and di-hydric alcohols are made by hydrogenating saturated monocarboxylic acids of 2-18 carbon atoms or dicarboxylic acids of 2-12 carbon atoms, or esters thereof, at 180-350 DEG C. and 100-500 atmos. in the presence of a Zn-Cu-Al alloy surfaceetched with caustic alkali; the Zn content of the alloy is 5-40 per cent and the Al and Cu contents are each 30-60 per cent, the preferred composition being Zn 20, Cu 40, Al 40. The process may be intermittent or continuous, the latter employing the catalyst in lump form. The preheated acid or ester is dissolved in e.g. methanol, passed with hydrogen over the heated catalyst, and the gaseous products separated and recycled. If the catalyst is in powder form it is separated by filtration or centrifuging before the product solidifies. When the catalyst becomes inactive it can be re-etched with caustic alkali. The products may be converted into the corresponding chlorinated hydrocarbons. Examples show the hydrogenation of (1) dimethyl adipate to hexanol-1 and hexanediol-1 : 6; (2) adipic acid to hexanediol-1 : 6; (3) sebacic acid to decanol-1 and decanediol; (4) dimethyl pimelate to heptanediol-1 : 7; (5) dimethyl succinate to butanediol-1 : 4; (6) methyl stearate to stearyl alcohol and octadecane; (7) beef tallow to a fatty alcohol mixture.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE800847X | 1955-07-08 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB800847A true GB800847A (en) | 1958-09-03 |
Family
ID=6714209
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB21195/56A Expired GB800847A (en) | 1955-07-08 | 1956-07-09 | Process for the hydrogenation of aliphatic mono- and dicarboxylic acids |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB800847A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3432560A (en) * | 1965-09-23 | 1969-03-11 | Celanese Corp | Method for preparation of alkanediols |
DE2845905A1 (en) * | 1978-10-21 | 1980-04-24 | Huels Chemische Werke Ag | METHOD FOR THE CONTINUOUS PRODUCTION OF BUTANDIOL-1,4 |
US5576467A (en) * | 1992-08-21 | 1996-11-19 | Japan Tobacco Inc. | Method of preparing an alcohol |
CN107774303A (en) * | 2016-08-30 | 2018-03-09 | 中国石油化工股份有限公司 | Porous metals/molecular sieve composite catalyst, its preparation method and the purposes in preparing low-carbon olefin |
-
1956
- 1956-07-09 GB GB21195/56A patent/GB800847A/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3432560A (en) * | 1965-09-23 | 1969-03-11 | Celanese Corp | Method for preparation of alkanediols |
DE2845905A1 (en) * | 1978-10-21 | 1980-04-24 | Huels Chemische Werke Ag | METHOD FOR THE CONTINUOUS PRODUCTION OF BUTANDIOL-1,4 |
US5576467A (en) * | 1992-08-21 | 1996-11-19 | Japan Tobacco Inc. | Method of preparing an alcohol |
CN107774303A (en) * | 2016-08-30 | 2018-03-09 | 中国石油化工股份有限公司 | Porous metals/molecular sieve composite catalyst, its preparation method and the purposes in preparing low-carbon olefin |
CN107774303B (en) * | 2016-08-30 | 2020-02-28 | 中国石油化工股份有限公司 | Porous metal/molecular sieve composite catalyst, preparation method thereof and application thereof in preparation of low-carbon olefin from synthesis gas |
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