US4142042A
Expired / Lapsed
US
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Alkenyl ethers from high molecular weight polyols
Assignee: Diamond Shamrock Corp
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Filing: 1977-10-06
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Granted: 1979-02-27
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Expires: 1997-10-06
Abstract
Abstract Disclosed is a process for preparing alkenyl ethers from high molecular weight polyols in a liquid phase system containing concentrated alkali metal hydroxide, water, water immiscible hydrocarbon solvent and high molecular weight polyol such that the addition of an alkenyl halide results in a reaction which yields an alkenyl ether product which is not readily distillable from the reaction solution at slightly elevated temperatures and atmospheric pressures.
Inventors
- 👤 Paul H. Goble
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-06 16:11
CPC Classifications
C; C07; C07C; C07C41/00; C07C41/01; C07C41/16; C08; C08G; C08G65/00; C08G65/02; C08G65/32; C08G65/329; C08G65/337
Claims Analysis
Total Claims: 20
Claim 1
Independent Claim
231 words
A process for preparing alkenyl ethers from polyols having more than 15 carbon atoms and a molecular weight less than 6,000 wherein the resultant alkenyl ethers are not readily distillable from the reaction mixture and the process facilitates ether product recovery, comprising the steps of: establishing a substantially uniform mixture, by stirring at elevated temperatures, the mixture consisting of alkali metal hydroxide, sufficient water as to dissolve the alkali metal hydroxide, water immiscible hydrocarbon solvent, and a polyol having more than 15 carbon atoms and a molecular weight less than 6,000 in which 3 to 6 or 10 hydroxyl groups are the sole functional groups and is free from aliphatic unsaturation; azeotropically distilling water and water immiscible hydrocarbon solvent from the system and returning the water immiscible hydrocarbon solvent to the reaction mixture to result in a uniform suspension of finely divided solids in a viscous phase; adding an alkenyl chloride, containing a chlorine atom bound directly to a saturated aliphatic carbon atom, after removal of water is near completion, in a dropwise fashion, at a rate to maintain the temperature of reaction; removing most of the water of reaction; cooling the reaction mixture; washing the reaction mixture with water; separating the organic phase; and stripping the water immiscible hyhydrocarbon solvent from the organic phase to obtain the alkenyl ether; wherein the entire process is conducted at atmospheric or subatmospheric pressures.
Claim 2
Dependent Claim
231 words
A process for preparing alkenyl ethers from polyols having more than 15 carbon atoms and a molecular weight less than 6,000 wherein the resultant alkenyl ethers are not readily distillable from the reaction mixture and the process facilitates ether product recovery, comprising the steps of: establishing a substantially uniform mixture, by stirring at elevated temperatures, the mixture consisting of alkali metal hydroxide, sufficient water as to dissolve the alkali metal hydroxide, water immiscible hydrocarbon solvent, and a polyol having more than 15 carbon atoms and a molecular weight less than 6,000 in which 3 to 6 or 10 hydroxyl groups are the sole functional groups and is free from aliphatic unsaturation; azeotropically distilling water and water immiscible hydrocarbon solvent from the system and returning the water immiscible hydrocarbon solvent to the reaction mixture to result in a uniform suspension of finely divided solids in a viscous phase; adding an alkenyl chloride, containing a chlorine atom bound directly to a saturated aliphatic carbon atom, after removal of water is near completion, in a dropwise fashion, at a rate to maintain the temperature of reaction; removing most of the water of reaction; cooling the reaction mixture; washing the reaction mixture with water; separating the organic phase; and stripping the water immiscible hyhydrocarbon solvent from the organic phase to obtain the alkenyl ether; wherein the entire process is conducted at atmospheric or subatmospheric pressures.
Claim 3
Dependent Claim
31 words
A process according to claim 1 wherein the water immiscible hydrocarbon solvent forms an azeotrope with water and has a boiling point in the range of 70 to 150 degrees centigrade.
Claim 4
Dependent Claim
14 words
A process according to claim 2 wherein the water immiscible hydrocarbon solvent is toluene.
Claim 5
Dependent Claim
25 words
A process according to claim 1 wherein the alkali metal hydroxide is a flaked material selected from the group of sodium hydroxide or potassium hydroxide.
Claim 6
Dependent Claim
28 words
A process according to claim 1 wherein upon allowing the two phases to separate the phases are neutralized to a pH of about seven with an acidic substance.
Claim 7
Dependent Claim
49 words
A process according to claim 1 wherein the water immiscible hydrocarbon solvent is stripped from the alkenyl ether product by means of vacuum distillation at a temperature in the range of 50 to 150 degrees centigrade with a vacuum in the range of atmospheric to 0.001 millimeters of mercury.
Claim 8
Dependent Claim
12 words
A process according to claim 1 wherein the alkenyl chloride is 3-chloropropene.
Claim 9
Dependent Claim
192 words
A process for preparing allyl ethers from polyols having more than 15 carbon atoms and a molecular weight less than 6,000 in high yields comprising the steps of: establishing a substantially uniform mixture, by stirring at elevated temperatures the mixture, consisting of alkali metal hydroxide, sufficient water to dissolve the alkali metal hydroxide, toluene so as to form an azeotrope with the water and a polyol having more than 15 carbon atoms and a molecular weight less than 6,000 in which 3 to 6 or 10 hydroxyl groups are the sole functional groups and is free from aliphatic unsaturation; azeotropically distilling water and toluene from the system at nearly atmospheric pressure, and returning the toluene to the mixture, to result in a uniform suspension of finely divided solids in a viscous phase; adding allyl chloride after removal of water is near completion, in a dropwise fashion, at a rate to maintain the temperature of reaction, removing most of the water of reaction; cooling the reaction mixture; washing the reaction mixture with water; and recovering the allyl ether from the reaction mixture; wherein the entire process is conducted at atmospheric or subatmospheric pressures.
Claim 10
Dependent Claim
192 words
A process for preparing allyl ethers from polyols having more than 15 carbon atoms and a molecular weight less than 6,000 in high yields comprising the steps of: establishing a substantially uniform mixture, by stirring at elevated temperatures the mixture, consisting of alkali metal hydroxide, sufficient water to dissolve the alkali metal hydroxide, toluene so as to form an azeotrope with the water and a polyol having more than 15 carbon atoms and a molecular weight less than 6,000 in which 3 to 6 or 10 hydroxyl groups are the sole functional groups and is free from aliphatic unsaturation; azeotropically distilling water and toluene from the system at nearly atmospheric pressure, and returning the toluene to the mixture, to result in a uniform suspension of finely divided solids in a viscous phase; adding allyl chloride after removal of water is near completion, in a dropwise fashion, at a rate to maintain the temperature of reaction, removing most of the water of reaction; cooling the reaction mixture; washing the reaction mixture with water; and recovering the allyl ether from the reaction mixture; wherein the entire process is conducted at atmospheric or subatmospheric pressures.
Claim 11
Dependent Claim
77 words
A process according to claim 8 wherein the polyol is selected from the group of oxypropylated glycerol, oxypropylated trimethylolpropane, oxypropylated trimethylolethane, oxypropylated pentraerythritol, oxypropylated sorbitol, oxypropylated mannitol, oxypropylated sucrose, oxypropylated 1,2,5 hexantriol and oxypropylated 1,2,6 hexantriol, oxyethylated glycerol, oxyethylated trimethylolpropane, oxyethylated trimethylolethane, oxyethylated pentraerythritol, oxyethylated sorbitol, oxyethylated mannitol, oxyethylated sucrose, oxyethylated 1,2,5 hexantriol, oxyethylated 1,2,6 hexantriol, oxybutylated glycerol, oxybutylated trimethylolpropane, oxybutylated trimethylolethane, oxybutylated pentraerythritol, oxybutylated sorbitol, oxybutylated mannitol, oxybutylated sucrose, oxybutylated 1,2,5 hexantriol and oxybutylated 1,2,6 hexantriol.
Claim 12
Dependent Claim
12 words
A process according to claim 8 wherein the polyol is oxypropylated glyerol.
Claim 13
Dependent Claim
12 words
A process according to claim 8 wherein the polyol is oxypropylated trimethylolpropane.
Claim 14
Dependent Claim
12 words
A process according to claim 8 wherein the polyol is oxypropylated trimethylolethane.
Claim 15
Dependent Claim
12 words
A process according to claim 8 wherein the polyol is oxypropylated pentraerythritol.
Claim 16
Dependent Claim
12 words
A process according to claim 8 wherein the polyol is oxypropylated sorbitol.
Claim 17
Dependent Claim
12 words
A process according to claim 8 wherein the polyol is oxypropylated mannitol.
Claim 18
Dependent Claim
12 words
A process according to claim 8 wherein the polyol is oxypropylated sucrose.
Claim 19
Dependent Claim
13 words
A process according to claim 8 wherein the polyol is oxypropylated 1,2,5 hexantriol.
Claim 20
Dependent Claim
13 words
A process according to claim 8 wherein the polyol is oxypropylated 1,2,6 hexantriol.
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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) | 1982-02-26 | 1982-08-28 | 1983-02-27 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-02-26 | 1986-08-28 | 1987-02-27 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-02-26 | 1990-08-28 | 1991-02-27 | $7700.00 | Window Closed / Lapsed |