Patent US4440664A successfully refreshed from Google Patents.
US4440664A
Expired / Lapsed
US
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Process for the dispersion of chain extender in polyol
Assignee: Eastman Chemical Co
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Filing: 1982-11-01
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Granted: 1984-04-03
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Expires: 2002-11-01
Abstract
Abstract The present invention provides a process for preparing stable, uniform dispersions of chain extenders in polyurethane-forming polyol. The preferred chain extender is hydroquinone di(β-hydroxyethyl)ether. The process comprises an adiabatic quenching step in combination with an annealing step. The inventive process avoids the need for slow, carefully controlled cooling schemes.
Inventors
- 👤 Mark A. Pollock
- 👤 Jimmie D. Fleenor
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 14:05
CPC Classifications
C; C08; C08G; C08G18/00; C08G18/06; C08G18/28; C08G18/65; C08G18/66; C08G18/6666; C08G18/667; C08G18/6674; C08G2130/00
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
189 words
A process for preparing dispersions of hydroquinone di(β-hydroxyethyl)ether in polyurethane-forming polyol comprising the steps of: (a) heating and blending an initial mixture of about 5 to 30 parts by weight of said ether and about 10 to 50 parts by weight of said polyol until a condensed phase is formed by the melting of said ether at a temperature of at least about 90° C.; (b) combining with said initial mixture an additional quantity of polyol sufficient to bring the total amount of polyol in the resulting dispersion to about 100 parts by weight, the additional polyol being at a temperature substantially below that of said initial mixture so that the addition thereof to said initial mixture results in adiabatic quenching of the resulting dispersion to a temperature in the range of about 70° to 85° C.; (c) annealing said dispersion by heating said dispersion to a temperature which is at least about 5° C. greater than the quenching temperature and which is in the range of about 84° to 90° C.; and (d) cooling said dispersion to a desired handling temperature which is less than about 60° C.
Claim 2
Dependent Claim
189 words
A process for preparing dispersions of hydroquinone di(β-hydroxyethyl)ether in polyurethane-forming polyol comprising the steps of: (a) heating and blending an initial mixture of about 5 to 30 parts by weight of said ether and about 10 to 50 parts by weight of said polyol until a condensed phase is formed by the melting of said ether at a temperature of at least about 90° C.; (b) combining with said initial mixture an additional quantity of polyol sufficient to bring the total amount of polyol in the resulting dispersion to about 100 parts by weight, the additional polyol being at a temperature substantially below that of said initial mixture so that the addition thereof to said initial mixture results in adiabatic quenching of the resulting dispersion to a temperature in the range of about 70° to 85° C.; (c) annealing said dispersion by heating said dispersion to a temperature which is at least about 5° C. greater than the quenching temperature and which is in the range of about 84° to 90° C.; and (d) cooling said dispersion to a desired handling temperature which is less than about 60° C.
Claim 3
Dependent Claim
17 words
The process of claim 1 wherein said dispersion comprises about 20 parts by weight of said ether.
Claim 4
Dependent Claim
26 words
The process of claim 1 wherein said initial mixture is heated to a temperature of about 90° to 105° C. until a condensed phase is formed.
Claim 5
Dependent Claim
31 words
The process of claim 1 wherein said initial mixture comprises about 5 to 30 parts by weight of said ether and about 40 to 50 parts by weight of said polyol.
Claim 6
Dependent Claim
20 words
The process of claim 1 wherein said dispersion after annealing is cooled to a temperature less than about 50° C.
Claim 7
Dependent Claim
189 words
A process for preparing dispersions of hydroquinone di(β-hydroxyethyl)ether in polyurethane-forming polyol comprising the steps of: (a) heating and blending an initial mixture of about 5 to 30 parts by weight of said ether and about 40 to 50 parts by weight of said polyol until a condensed phase is formed by the melting of said ether at a temperature of about 90° to 105° C.; (b) combining with said initial mixture an additional quantity of polyol sufficient to bring the total amount of polyol in the resulting dispersion to about 100 parts by weight, the additional polyol being at a temperature substantially below that of said initial mixture so that the addition thereof to said initial mixture results in adiabatic quenching of the resulting dispersion to a temperature in the range of about 70° to 85° C.; (c) annealing said dispersion by heating said dispersion to a temperature which is at least about 5° C. greater than the quenching temperature and which is in the range of about 84° to 90° C.; and (d) cooling said dispersion to a desired handling temperature which is less than about 50° C.
Claim 8
Dependent Claim
189 words
A process for preparing dispersions of hydroquinone di(β-hydroxyethyl)ether in polyurethane-forming polyol comprising the steps of: (a) heating and blending an initial mixture of about 5 to 30 parts by weight of said ether and about 40 to 50 parts by weight of said polyol until a condensed phase is formed by the melting of said ether at a temperature of about 90° to 105° C.; (b) combining with said initial mixture an additional quantity of polyol sufficient to bring the total amount of polyol in the resulting dispersion to about 100 parts by weight, the additional polyol being at a temperature substantially below that of said initial mixture so that the addition thereof to said initial mixture results in adiabatic quenching of the resulting dispersion to a temperature in the range of about 70° to 85° C.; (c) annealing said dispersion by heating said dispersion to a temperature which is at least about 5° C. greater than the quenching temperature and which is in the range of about 84° to 90° C.; and (d) cooling said dispersion to a desired handling temperature which is less than about 50° C.
Claim 9
Dependent Claim
17 words
The process of claim 6 wherein said dispersion comprises about 20 parts by weight of said ether.
Claim 10
Dependent Claim
13 words
The process of claim 6 wherein said handling temperature is about 40° C.
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) | 1987-04-03 | 1987-10-03 | 1988-04-03 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-04-03 | 1991-10-03 | 1992-04-03 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-04-03 | 1995-10-03 | 1996-04-03 | $7700.00 | Window Closed / Lapsed |