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US4421936A Expired / Lapsed US ⏱️ 0.0 years remaining

Continuous alkoxidation process

Assignee: FMC Corp
•
Filing: 1983-03-31
•
Granted: 1983-12-20
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Expires: 2003-03-31
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Abstract

Abstract A continuous process for producing alkali metal alkoxides comprising continuously introducing an aqueous solution of an alkali metal hydroxide into an upper section of a column reactor; continuously vaporizing an alkanol or an alkoxyalkanol of 4 to 18 carbon atoms into a lower section of the reactor at a rate of at least about 2 to 4 moles of alcohol for each mole of alkali metal hydroxide introduced into the reaction zone; reacting the aliphatic alcohol with the alkali metal hydroxide in the reactor; concurrently removing water from the alkali metal hydroxide solution and the alkoxide formation from an upper section of the reactor as an azeotrope formed by excess alcohol and water; continuously condensing and separating the azeotrope into an alcohol phase and a water phase, the water phase being removed from the process and the alcohol phase being returned to the column reactor; and removing a substantially anhydrous reaction product consisting primarily of alkoxide product in excess alcohol from a bottom section of the reactor while simultaneously maintaining a nonoxidizing atmosphere while conducting the reaction.

Inventors

  • 👤 Harry M. Smith
  • 👤 Raymond D. Williams

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-02 01:33
CPC Classifications
C; C07; C07F; C07F9/00; C07F9/02; C07F9/06; C07F9/08; C07F9/09; C07F9/11; C07C; C07C41/00; C07C41/01; C07C41/18; C07C41/34; C07C41/40; C07C41/42; C07F9/091

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 210 words
A continuous process for producing alkali metal alkoxides comprising the steps: (a) Continuously introducing an aqueous solution of an alkali metal hydroxide into an upper section of a column-reactor; (b) Continuously vaporizing an aliphatic alcohol of the formula ##STR3## in which R 1 , R 2 and R 3 are selected from hydrogen, alkyl or alkoxyalkyl radicals, said aliphatic alcohol having 4 to 18 carbon atoms, and feeding the vaporized alcohol into a lower section of the column reactor at a rate of 2 to 4 moles of alcohol per mole of alkali metal hydroxide introduced into the column reactor; (c) Reacting the aliphatic alcohol with the alkali metal hydroxide in the column reactor; (d) Concurrently removing water from the alkali metal hydroxide solution and the alkoxide formation from an upper section of the column reactor in the form of an azeotrope; (e) Continuously condensing and separating the azeotrope into an alcohol phase and a water phase, the water phase being removed from the process and the alcohol phase being returned to the column reactor; (f) Recovering a substantially anhydrous reaction product comprising alkoxide product and aliphatic alcohol from a lower section of the column reactor while simultaneously maintaining a non-oxidizing atmosphere throughout the conduct of steps a through f.
Claim 2
Dependent Claim 210 words
A continuous process for producing alkali metal alkoxides comprising the steps: (a) Continuously introducing an aqueous solution of an alkali metal hydroxide into an upper section of a column-reactor; (b) Continuously vaporizing an aliphatic alcohol of the formula ##STR3## in which R 1 , R 2 and R 3 are selected from hydrogen, alkyl or alkoxyalkyl radicals, said aliphatic alcohol having 4 to 18 carbon atoms, and feeding the vaporized alcohol into a lower section of the column reactor at a rate of 2 to 4 moles of alcohol per mole of alkali metal hydroxide introduced into the column reactor; (c) Reacting the aliphatic alcohol with the alkali metal hydroxide in the column reactor; (d) Concurrently removing water from the alkali metal hydroxide solution and the alkoxide formation from an upper section of the column reactor in the form of an azeotrope; (e) Continuously condensing and separating the azeotrope into an alcohol phase and a water phase, the water phase being removed from the process and the alcohol phase being returned to the column reactor; (f) Recovering a substantially anhydrous reaction product comprising alkoxide product and aliphatic alcohol from a lower section of the column reactor while simultaneously maintaining a non-oxidizing atmosphere throughout the conduct of steps a through f.
Claim 3
Dependent Claim 56 words
The process of claim 1 wherein the aliphatic alcohol is selected from alkanols of the formula R--OH in which R contains 4 to 12 carbon atoms and alkoxy alkanols of the formula R 4 --O--R 5 --OH in which R 4 contains 1 to 6 carbon atoms and R 5 contains 1 to 4 carbon atoms.
Claim 4
Dependent Claim 20 words
The process of claim 1 wherein the alkali metal hydroxide is selected from sodium hydroxide, potassium hydroxide and lithium hydroxide.
Claim 5
Dependent Claim 34 words
The process of claim 1 wherein the reaction product removed from a lower section of the column reactor is distilled to recover part of the unreacted alcohol which is returned to the column reactor.
Claim 6
Dependent Claim 11 words
The process of claim 2 wherein the aliphatic alcohol is butanol.
Claim 7
Dependent Claim 11 words
The process of claim 2 wherein the aliphatic alcohol is 2-butoxyethanol.

References Cited (Backward Citations)

US1910331A Cited
GB490388A Cited
GB698282A Cited
US2877274A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-12-19 1987-06-20 1987-12-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-12-19 1991-06-20 1991-12-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-12-19 1995-06-20 1995-12-20 $7700.00 Window Closed / Lapsed

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