US4371713A
Expired / Lapsed
US
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Process for the preparation of polyether glycol
Assignee: JSR Corp
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Filing: 1981-10-29
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Granted: 1983-02-01
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Expires: 2001-10-29
Abstract
Abstract In the process for preparing polyether glycol comprising (A) polymerizing tetrahydrofuran or a mixture of tetrahydrofuran and other copolymerizable cyclic ether(s) in the presence of a ring-opening polymerization catalyst comprising fuming sulfuric acid and/or fluorosulfuric acid as principal component, (B) adding water or an aqueous alkali solution to the polymerization product, and heating said reaction product under the strongly acidic condition to hydrolyze the same and (C) washing the hydrolysis product comprising polytetramethylene glycol and polyether glycol having oxytetramethylene groups as principal constituent, the polymerization of the tetrahydrofuran or the mixture of tetrahydrofuran and other copolymerizable cyclic ether(s) in the (A) step is carried out by (1) contacting the same with a ring-opening polymerization catalyst at a temperature within the range of -30° C. to 10° C. in the first stage, and (2) elevating the reaction temperature, when the conversion of said monomer into the polymer has reached 5% or more, to a temperature which falls within the range of 0° C. to 40° C. and is at least 10° C. higher than the reaction temperature in the first stage and continuing the polymerization at this temperature. This process enables the effective and easy preparation of a highly functional polyether glycol having a relatively low molecular weight of about 500 to 5,000 and comprising oxytetramethylene groups as principal constituent, said polyether glycol being useful as a starting material for the preparation of polyurethanes, elastomeric polyesters, elastomeric polyamides and the like.
Inventors
- 👤 Shuichi Matsumoto
- 👤 Kenji Yasuda
- 👤 Masayuki Endoh
- 👤 Kunihiro Harada
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-23 07:55
CPC Classifications
C; C08; C08G; C08G65/00; C08G65/02; C08G65/04; C08G65/06; C08G65/16; C08G65/20; C08G18/00; C08G18/06; C08G18/28; C08G18/40; C08G18/48; C08G18/4854
Claims Analysis
Total Claims: 15
Claim 1
Independent Claim
168 words
A process for preparing polyether glycol, comprising (A) polymerizing tetrahydrofuran or a mixture of tetrahydrofuran and other copolymerizable cyclic ether(s) in the presence of a ring-opening polymerization catalyst comprising as principal components fuming sulfuric acid and/or fluorosulfuric acid, (B) adding water or an aqueous alkali solution to the polymerization product, hydrolyzing the said product under the strongly acidic condition, and (C) washing the hydrolysis product, characterized in that the polymerization of tetrahydrofuran or a mixture of tetrahydrofuran and other copolymerizable cyclic ether(s) is conducted by (1) contacting the monomer with the ring-opening polymerization catalyst at a temperature within the range of -30° C. to 10° C. at the first stage and (2) elevating the reaction temperature, when the conversion of said monomer into the polymer has reached 5% or more, to a temperature which falls within the range of 0° C. to 40° C. and is at least 10° C. higher than the reaction temperature at the first stage and continuing the polymerization reaction at the elevated temperature.
Claim 2
Dependent Claim
168 words
A process for preparing polyether glycol, comprising (A) polymerizing tetrahydrofuran or a mixture of tetrahydrofuran and other copolymerizable cyclic ether(s) in the presence of a ring-opening polymerization catalyst comprising as principal components fuming sulfuric acid and/or fluorosulfuric acid, (B) adding water or an aqueous alkali solution to the polymerization product, hydrolyzing the said product under the strongly acidic condition, and (C) washing the hydrolysis product, characterized in that the polymerization of tetrahydrofuran or a mixture of tetrahydrofuran and other copolymerizable cyclic ether(s) is conducted by (1) contacting the monomer with the ring-opening polymerization catalyst at a temperature within the range of -30° C. to 10° C. at the first stage and (2) elevating the reaction temperature, when the conversion of said monomer into the polymer has reached 5% or more, to a temperature which falls within the range of 0° C. to 40° C. and is at least 10° C. higher than the reaction temperature at the first stage and continuing the polymerization reaction at the elevated temperature.
Claim 3
Dependent Claim
21 words
The process according to claim 1, wherein the reaction temperature at the first stage is from -30° C. to 0° C.
Claim 4
Dependent Claim
52 words
The process according to claim 1 or 2, wherein when the conversion has reached 10% or more, the reaction temperature is elevated to a temperature which falls within the range of from 10° C. to 40° C. and is at least 15° C. higher than the reaction temperature at the first stage.
Claim 5
Dependent Claim
75 words
The process according to claim 1, wherein the hydrolysis in the step (B) is conducted under the addition of an alkali to the hydrolysis reaction system in an amount which is 1/4 or more of the amount necessary for neutralizing the amount of the mixture of water and fuming sulfuric acid and/or fluorosulfuric acid used in the polymerization and which is sufficient to keep the pH of the hydrolysis reaction system at 3 or less.
Claim 6
Dependent Claim
31 words
The process according to claim 4, wherein the alkali is added in its entire amount prior to the hydrolysis treatment or it is added stepwise or continuously during the hydrolysis treatment.
Claim 7
Dependent Claim
23 words
The process according to claim 1 or 4, wherein the hydrolysis temperature in the step (B) is from 50° C. to 150° C.
Claim 8
Dependent Claim
40 words
The process according to claim 1 or 4, wherein the hydrolysis product, that is, polytetramethylene glycol or polyether glycol having oxytetramethylene groups as principal constituent is washed with an aqueous neutral sulfate solution or an aqueous basic magnesium salt solution.
Claim 9
Dependent Claim
24 words
The process according to claim 7, wherein the aqueous neutral sulfate solution is an aqueous solution of sodium sulfate, potassium sulfate or magnesium sulfate.
Claim 10
Dependent Claim
37 words
The process according to claim 7, wherein the amount of the aqueous neutral sulfate solution is 20-200 parts by weight per 100 parts by weight of polytetramethylene glycol or polyether glycol having oxytetramethylene groups as principal constituent.
Claim 11
Dependent Claim
30 words
The process according to claim 7, wherein washing with the aqueous neutral sulfate solution is performed while heating the system at a temperature of from 50° C. to 150° C.
Claim 12
Dependent Claim
31 words
The process according to claim 7, wherein the aqueous basic magnesium salt solution is an aqueous solution of magnesium hydroxide, magnesium oxide, magnesium carbonate, basic magnesium carbonate or a mixture thereof.
Claim 13
Dependent Claim
38 words
The process according to claim 11, wherein the amount of the aqueous basic magnesium salt solution is 10-500 parts by weight per 100 parts by weight of polytetramethylene glycol or polyether glycol having oxytetramethylene groups as principal constituent.
Claim 14
Dependent Claim
38 words
The process according to claim 1, wherein said other copolymerizable cyclic ether to be mixed with tetrahydrofuran is selected from the group consisting of ethylene oxide, propylene oxide, epichlorohydrin, oxacyclobutane, 3,3-dimethyloxacyclobutane, 3,3-bis(chloromethyl)oxacyclobutane, 2-methyltetrahydrofuran, 3-methyltetrahydrofuran, 2,5-dihydrofuran, tetrahydropyran and oxacycloheptane.
Claim 15
Dependent Claim
28 words
The process according to claim 13, wherein the amount of the cyclic ether used is 100 parts by weight or less per 100 parts by weight of tetrahydrofuran.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1986-01-31 | 1986-08-02 | 1987-02-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-01-31 | 1990-08-02 | 1991-02-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-01-31 | 1994-08-02 | 1995-02-01 | $7700.00 | Window Closed / Lapsed |