GB807581A - Production of alkynols and alkynediols - Google Patents
Production of alkynols and alkynediolsInfo
- Publication number
- GB807581A GB807581A GB33534/55A GB3353455A GB807581A GB 807581 A GB807581 A GB 807581A GB 33534/55 A GB33534/55 A GB 33534/55A GB 3353455 A GB3353455 A GB 3353455A GB 807581 A GB807581 A GB 807581A
- Authority
- GB
- United Kingdom
- Prior art keywords
- carrier
- heated
- acetylene
- per cent
- kaolin
- 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
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/36—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring increasing the number of carbon atoms by reactions with formation of hydroxy groups, which may occur via intermediates being derivatives of hydroxy, e.g. O-metal
- C07C29/38—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring increasing the number of carbon atoms by reactions with formation of hydroxy groups, which may occur via intermediates being derivatives of hydroxy, e.g. O-metal by reaction with aldehydes or ketones
- C07C29/42—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring increasing the number of carbon atoms by reactions with formation of hydroxy groups, which may occur via intermediates being derivatives of hydroxy, e.g. O-metal by reaction with aldehydes or ketones with compounds containing triple carbon-to-carbon bonds, e.g. with metal-alkynes
-
- 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
- B01J23/72—Copper
-
- 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
- B01J23/84—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 arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/843—Arsenic, antimony or bismuth
- B01J23/8437—Bismuth
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Alkynols (including alkyndiols) are made by reacting aldehydes or ketones with acetylene (see Group IV (b)) in the presence of a catalyst made by depositing copper oxide on a siliceous carrier which is then heated to a temperature of 400 DEG to 800 DEG C., by which a surface layer of copper silicate is formed. Preferably a little bismuth oxide is present with the copper oxide. The metal silicate prevents the formation of cuprene. Kaolin, silica gel, or fuller's earth may be used as the carrier, but preferably kaolin is mixed with an organic binder, formed into shapes and roasted at 800 DEG to 850 DEG C. to burn out the binder, and finally heated at 1000 DEG to 1200 DEG C. to impart a mullite-like structure. Binders specified are, polyacrylic acid, alginic or pectic acid, polyvinyl methyl ether or methyl cellulose. In examples, the calcined carrier is impregnated with a solution containing copper nitrate or nitrite, bismuth nitrate and dilute nitric acid. The pulp is extruded, and the shaped pieces dried and finally heated at 400 DEG to 800 DEG C. for 5 to 34 hours. The bismuth compound may be replaced by compounds of Au, Hg, Pb, Se, Ce, or of halogens. U.S.A. Specifications 2,232,867 and 2,300,969 are referred to.ALSO:Alkynols (including alkyndiols) are made by reacting aldehydes or ketones with acetylene in the presence of a catalyst made by depositing copper oxide on a siliceous carrier which is then heated to a temperature of 400 DEG to 800 DEG C., by which a surface coating of copper silicate is formed, thus preventing the formation of cuprene. Preferably, there is also present a small amount of an oxide of Bi, Au, Hg, Pb, Se or Ce. Kaolin, silica gel, or fuller's earth are used as carrier, but preferably kaolin is mixed with a polymeric organic binder, the mixture formed into shapes, dried, calcined and then impregnated with solutions of the metal salts and re-ignited (see Group III). In examples, a long tubular reactor column packed with the catalyst is first flushed with nitrogen, and then heated to 90 DEG C., while a 6 per cent formaldehyde solution trickles downwards through the column. Acetylene is bled into the nitrogen feed increasing to a concentration of 70 per cent acetylene, and also the temperature is raised to 120 DEG C. The concentration of formaldehyde is also raised to 18.5 per cent. The gases produced are condensed, surplus gases recycled, and water removed from the condensate, which is then submitted to azeotropic distillation. In a 600 hour operation, 80 per cent of the formaldehyde is converted to alkyne diol. U.S.A. Specifications 2,232,867, 2,300,969 and 2,527,358 are referred to.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB33534/55A GB807581A (en) | 1955-11-23 | 1955-11-23 | Production of alkynols and alkynediols |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB33534/55A GB807581A (en) | 1955-11-23 | 1955-11-23 | Production of alkynols and alkynediols |
Publications (1)
Publication Number | Publication Date |
---|---|
GB807581A true GB807581A (en) | 1959-01-21 |
Family
ID=10354201
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB33534/55A Expired GB807581A (en) | 1955-11-23 | 1955-11-23 | Production of alkynols and alkynediols |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB807581A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4085151A (en) * | 1977-06-29 | 1978-04-18 | E. I. Du Pont De Nemours And Company | Butynediol production |
CN113751039A (en) * | 2021-09-17 | 2021-12-07 | 山西大学 | Alkynylation catalyst for synthesizing propiolic alcohol, preparation method and application |
CN113813973A (en) * | 2021-09-17 | 2021-12-21 | 山西大学 | Nano gold confinement copper-based core-shell structure catalyst and preparation method and application thereof |
CN117205934A (en) * | 2023-11-09 | 2023-12-12 | 山东嘉虹化工有限公司 | Copper bismuth catalyst and preparation method thereof |
-
1955
- 1955-11-23 GB GB33534/55A patent/GB807581A/en not_active Expired
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4085151A (en) * | 1977-06-29 | 1978-04-18 | E. I. Du Pont De Nemours And Company | Butynediol production |
CN113751039A (en) * | 2021-09-17 | 2021-12-07 | 山西大学 | Alkynylation catalyst for synthesizing propiolic alcohol, preparation method and application |
CN113813973A (en) * | 2021-09-17 | 2021-12-21 | 山西大学 | Nano gold confinement copper-based core-shell structure catalyst and preparation method and application thereof |
CN113751039B (en) * | 2021-09-17 | 2022-07-19 | 山西大学 | Alkynylation catalyst for synthesizing propiolic alcohol, preparation method and application |
CN113813973B (en) * | 2021-09-17 | 2023-03-10 | 山西大学 | Nano gold confinement copper-based core-shell structure catalyst and preparation method and application thereof |
CN117205934A (en) * | 2023-11-09 | 2023-12-12 | 山东嘉虹化工有限公司 | Copper bismuth catalyst and preparation method thereof |
CN117205934B (en) * | 2023-11-09 | 2024-01-02 | 山东嘉虹化工有限公司 | Copper bismuth catalyst and preparation method thereof |
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