GB646497A - Improvements in and relating to the production of alcohols - Google Patents
Improvements in and relating to the production of alcoholsInfo
- Publication number
- GB646497A GB646497A GB2445246A GB2445246A GB646497A GB 646497 A GB646497 A GB 646497A GB 2445246 A GB2445246 A GB 2445246A GB 2445246 A GB2445246 A GB 2445246A GB 646497 A GB646497 A GB 646497A
- Authority
- GB
- United Kingdom
- Prior art keywords
- prepared
- catalyst
- water
- temperature
- per cent
- 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
- 150000001298 alcohols Chemical class 0.000 title abstract 2
- ZNOKGRXACCSDPY-UHFFFAOYSA-N tungsten trioxide Chemical compound O=[W](=O)=O ZNOKGRXACCSDPY-UHFFFAOYSA-N 0.000 abstract 8
- 239000003054 catalyst Substances 0.000 abstract 7
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical compound CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 abstract 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract 4
- 229910002804 graphite Inorganic materials 0.000 abstract 4
- 239000010439 graphite Substances 0.000 abstract 4
- 239000000203 mixture Substances 0.000 abstract 4
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 abstract 3
- DKGAVHZHDRPRBM-UHFFFAOYSA-N Tert-Butanol Chemical compound CC(C)(C)O DKGAVHZHDRPRBM-UHFFFAOYSA-N 0.000 abstract 3
- 238000006243 chemical reaction Methods 0.000 abstract 3
- XAYGUHUYDMLJJV-UHFFFAOYSA-Z decaazanium;dioxido(dioxo)tungsten;hydron;trioxotungsten Chemical compound [H+].[H+].[NH4+].[NH4+].[NH4+].[NH4+].[NH4+].[NH4+].[NH4+].[NH4+].[NH4+].[NH4+].O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.[O-][W]([O-])(=O)=O.[O-][W]([O-])(=O)=O.[O-][W]([O-])(=O)=O.[O-][W]([O-])(=O)=O.[O-][W]([O-])(=O)=O.[O-][W]([O-])(=O)=O XAYGUHUYDMLJJV-UHFFFAOYSA-Z 0.000 abstract 3
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 abstract 3
- 229910052721 tungsten Inorganic materials 0.000 abstract 3
- 239000010937 tungsten Substances 0.000 abstract 3
- CMPGARWFYBADJI-UHFFFAOYSA-L tungstic acid Chemical compound O[W](O)(=O)=O CMPGARWFYBADJI-UHFFFAOYSA-L 0.000 abstract 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract 2
- BTANRVKWQNVYAZ-UHFFFAOYSA-N butan-2-ol Chemical compound CCC(C)O BTANRVKWQNVYAZ-UHFFFAOYSA-N 0.000 abstract 2
- IAQRGUVFOMOMEM-UHFFFAOYSA-N butene Natural products CC=CC IAQRGUVFOMOMEM-UHFFFAOYSA-N 0.000 abstract 2
- 229910002091 carbon monoxide Inorganic materials 0.000 abstract 2
- 239000007789 gas Substances 0.000 abstract 2
- 229910052739 hydrogen Inorganic materials 0.000 abstract 2
- 239000001257 hydrogen Substances 0.000 abstract 2
- 125000004435 hydrogen atom Chemical class [H]* 0.000 abstract 2
- 239000000376 reactant Substances 0.000 abstract 2
- IAQRGUVFOMOMEM-ONEGZZNKSA-N trans-but-2-ene Chemical compound C\C=C\C IAQRGUVFOMOMEM-ONEGZZNKSA-N 0.000 abstract 2
- DNIAPMSPPWPWGF-GSVOUGTGSA-N (R)-(-)-Propylene glycol Chemical compound C[C@@H](O)CO DNIAPMSPPWPWGF-GSVOUGTGSA-N 0.000 abstract 1
- -1 aliphatic alcohols Chemical class 0.000 abstract 1
- 230000036571 hydration Effects 0.000 abstract 1
- 238000006703 hydration reaction Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
- 239000008188 pellet Substances 0.000 abstract 1
- 239000011541 reaction mixture Substances 0.000 abstract 1
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 abstract 1
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
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/24—Chromium, molybdenum or tungsten
- B01J23/30—Tungsten
-
- 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
- C07C29/03—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by addition of hydroxy groups to unsaturated carbon-to-carbon bonds, e.g. with the aid of H2O2
- C07C29/04—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by addition of hydroxy groups to unsaturated carbon-to-carbon bonds, e.g. with the aid of H2O2 by hydration of carbon-to-carbon double bonds
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
Abstract
Tertiary butanol is prepared by reacting isobutene and water at elevated pressure and at a temperature within the range of from 160 DEG to 220 DEG C. in the presence of an unsupported pelleted catalyst consisting of the blue oxide of tungsten having a formula approximating to W2O5 and prepared by reducing a hydrated tungsten trioxide or ammonium paratungstate at elevated temperatures. Secondary butanol is prepared in the same manner from butene-1 and/or butene-2 but at a temperature in the range of from 230 DEG to 270 DEG C. Water-to-olefine molecular ratios may vary from 1 : 1 up to as high as 20 : 1, the higher ratios being preferred. The process may be operated continuously, any unreacted olefine being recycled. A mixture of isobutene and either or both n-butenes and water may be passed over the catalyst at a temperature within the range of from 160 DEG to 220 DEG C., the resulting t-butanol separated from the reaction mixture and the residue, with more water, if necessary or desired, then passed over a second blue oxide of tungsten catalyst at a temperature in the higher range to form secondary butanol. Suitable catalysts are prepared by pelleting a mixture of powdered tungstic acid and 2 per cent graphite which is then reduced, for example, by treatment at an elevated temperature with hydrogen, carbon monoxide, mixtures containing these gases, or with a lower aliphatic alcohol, or it may be placed in the reaction vessel and treated at elevated temperature with the reactants; the tungstic acid may be replaced by ammonium para-tungstate. Examples describe the conversion of isobutene and butene-2 into the corresponding alcohols at 250 atmospheres pressure, the catalyst used being prepared by pelleting tungstic acid containing 2 per cent graphite and treating with ethanol for 3 hours at 250 DEG C., and then similarly treating with water. Specification 622,937 is referred to. According to the Provisional Specification the catalyst may be prepared by the reduction of WO3 containing 2 per cent of graphite.ALSO:Blue oxide of tungsten, for use as catalyst in the hydration of butenes to sec.- and tertiary-butanols, is prepared in unsupported pelleted form by reducing ammonium paratungstate or a hydrated tungsten trioxide, or WO3 according to the Provisional Specification, at elevated temperature. Hydrogen, carbon monoxide, or mixtures containing these gases, or lower aliphatic alcohols, may be used for the reduction; alternatively the pellets may be reduced in the reaction vessel by means of the reactants themselves. In an example, hydrated tungsten trioxide containing 2 per cent graphite is pelleted and then treated at 250 DEG C. with ethanol for 3 hours and then with water for three hours.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2445246A GB646497A (en) | 1946-08-16 | 1946-08-16 | Improvements in and relating to the production of alcohols |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2445246A GB646497A (en) | 1946-08-16 | 1946-08-16 | Improvements in and relating to the production of alcohols |
Publications (1)
Publication Number | Publication Date |
---|---|
GB646497A true GB646497A (en) | 1950-11-22 |
Family
ID=10211928
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2445246A Expired GB646497A (en) | 1946-08-16 | 1946-08-16 | Improvements in and relating to the production of alcohols |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB646497A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8558036B2 (en) | 2010-11-15 | 2013-10-15 | Saudi Arabian Oil Company | Dual phase catalysts system for mixed olefin hydrations |
-
1946
- 1946-08-16 GB GB2445246A patent/GB646497A/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8558036B2 (en) | 2010-11-15 | 2013-10-15 | Saudi Arabian Oil Company | Dual phase catalysts system for mixed olefin hydrations |
US8865951B2 (en) | 2010-11-15 | 2014-10-21 | Saudi Arabian Oil Company | Dual phase catalysts system for mixed olefin hydrations |
US9056315B2 (en) | 2010-11-15 | 2015-06-16 | Saudi Arabian Oil Company | Dual phase catalysts system for mixed olefin hydrations |
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