US4895989A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for producing alkali metal alcoholates
Assignee: GEA Group AG
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Filing: 1988-07-11
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Granted: 1990-01-23
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Expires: 2008-07-11
Abstract
Abstract A process is described for the production of alcoholates from alkali metal hydroxides and aliphatic alcohol which in their molecule contain 1 to 6 carbon atoms. The alcoholates are produced in that alkali metal hydroxide is mixed with an alcohol and is reacted with said alcohol at a temperature from 80° to 110° C., preferably from 80° to 100° C., and under a pressure from 0.3 to 1.2 bars, the alcohol water mixture which evaporates during the reaction is separated into its components by at least one membrane, the alcohol vapor and the water vapor are condensed and the condensed alcohol is recycled to the reaction.
Inventors
- 👤 Ulrich Sander
- 👤 Pavel Soukup
- 👤 Harald Helmrich
- 👤 Wilfried Weiss
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 20:49
CPC Classifications
C; C07; C07C; C07C29/00; C07C29/68; C07C29/70; C07C29/74; C07C29/76; Y; Y10; Y10S; Y10S203/00; Y10S203/06; Y10S203/14
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
186 words
A process for producing an alkali metal alcoholate, comprising the steps of: (a) mixing an alkali metal hydroxide with an alcohol capable of reacting therewith to form an alcoholate and reacting the resulting mixture at a temperature of 50° to 110° C. under a pressure of 0.3 to 1.2 bar to produce an alkali metal alcoholate and a vapor-phase alcohol-water mixture and separating the alkali metal alcoholate from the vapor phase alcohol-water mixture; (a 1 ) heating said vapor-phase alcohol-water mixture to a temperature above the reaction temperature in step (a) but less than 120° C. prior to separation of the vapor-phase alcohol-water mixture; (b) separating the components of said vapor-phase alcohol-water mixture by pervaporation through at least one membrane with one of said components permeating said membrane while the other component is retained thereby to recover alcohol vapor and water vapor from said vapor-phase alcohol-water mixture; (c) separately condensing the recovered alcohol and water vapors of step (b); (d) recycling condensed alcohol from step (c) to step (a) for reaction with alkali metal hydroxide; and (e) recovering the alkali metal alcoholate produced in step (a).
Claim 2
Dependent Claim
186 words
A process for producing an alkali metal alcoholate, comprising the steps of: (a) mixing an alkali metal hydroxide with an alcohol capable of reacting therewith to form an alcoholate and reacting the resulting mixture at a temperature of 50° to 110° C. under a pressure of 0.3 to 1.2 bar to produce an alkali metal alcoholate and a vapor-phase alcohol-water mixture and separating the alkali metal alcoholate from the vapor phase alcohol-water mixture; (a 1 ) heating said vapor-phase alcohol-water mixture to a temperature above the reaction temperature in step (a) but less than 120° C. prior to separation of the vapor-phase alcohol-water mixture; (b) separating the components of said vapor-phase alcohol-water mixture by pervaporation through at least one membrane with one of said components permeating said membrane while the other component is retained thereby to recover alcohol vapor and water vapor from said vapor-phase alcohol-water mixture; (c) separately condensing the recovered alcohol and water vapors of step (b); (d) recycling condensed alcohol from step (c) to step (a) for reaction with alkali metal hydroxide; and (e) recovering the alkali metal alcoholate produced in step (a).
Claim 3
Dependent Claim
14 words
The process defined in claim 1 wherein said temperature is 80° to 100° C.
Claim 4
Dependent Claim
25 words
The process defined in claim 1 wherein said alkali metal hydroxide and said alcohol are mixed in a molar ratio of substantially 1:2 to 1:10.
Claim 5
Dependent Claim
65 words
The process defined in claim 1 wherein said membrane comprises a carrier having a thickness of substantially 50 to 300 μm, a porous supporting membrane layer on said carrier and of a thickness of substantially 50 to 500 μm, and a nonporous separating layer on a surface of said porous supporting membrane layer opposite said carrier of a thickness of substantially 0.2 to 0.5 μm.
Claim 6
Dependent Claim
54 words
The process defined in claim 4 wherein said carrier is a woven or nonwoven polyester fabric, said porous supporting membrane layer is composed of polyacrylonitrile or polysulfone, the separating layer is composed of polyvinylalcohol, and the pore diameter of pores of said porous supporting membrane layer decreases from the carrier to the separating layer.
Claim 7
Dependent Claim
30 words
The process defined in claim 1 wherein said membrane has a membrane exchange area of substantially 20 to 40 m 2 per kg of water vapor permeating therethrough per hour.
Claim 8
Dependent Claim
30 words
The process defined in claim 6 wherein said membrane has a membrane exchange area of substantially 25 to 35 m 2 per kg of water vapor permeating therethrough per hour.
Claim 9
Dependent Claim
28 words
The process defined in claim 1 wherein said vapor-phase alcohol-water mixture is heated to a temperature of at most 50° C. above the reaction temperature in step (a).
Claim 10
Dependent Claim
31 words
The process defined in claim 1, further comprising the step of passing said vapor-phase alcohol-water mixture through a droplet separator to remove entrained alcoholate therefrom prior to separation in step (b).
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1993-01-22 | 1993-07-24 | 1994-01-23 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1997-01-22 | 1997-07-24 | 1998-01-23 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2001-01-22 | 2001-07-24 | 2002-01-23 | $7700.00 | Window Closed / Lapsed |