Patent US4359128A successfully refreshed from Google Patents.
Patent US4533729A successfully refreshed from Google Patents.
US4533729A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the preparation of polycarbonate polyols
Assignee: Eastman Chemical Co
•
Filing: 1983-11-14
•
Granted: 1985-08-06
•
Expires: 2003-11-14
Abstract
Abstract The present invention provides a novel process for preparing specified amorphous polycarbonate polyols. The process comprises reacting phosgene, a branched-chain polyhydric alcohol, and a straight chain polyhydric alcohol in the presence of a solvent and in the absence of a catalyst at a temperature of about 60° to 100° C., and then contacting the amorphous polycarbonate product in the reaction mixture with a catalytic amount of a tertiary amine at reflux temperature for a period of time of at least about 30 minutes. The straight chain polyhydric alcohol is employed in an amount of about 3 to 40 mole percent, based upon the total amount of polyhydric alcohol present in the reaction system. A preferred branched-chain polyhydric alcohol is neopentyl glycol, and a preferred straight chain polyhydric alcohol is 1,6-hexanediol. Preferred solvents are xylene and toluene, and preferred tertiary amines are triethylamine and pyridine.
Inventors
- 👤 Gordon C. Newland
- 👤 William R. Darnell
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 11:02
CPC Classifications
C; C08; C08G; C08G18/00; C08G18/06; C08G18/28; C08G18/40; C08G18/42; C08G18/44; C08G64/00; C08G64/02; C08G64/0208; C08G64/20; C08G64/22; C08G64/226
Claims Analysis
Total Claims: 22
Claim 1
Independent Claim
111 words
A process for preparing amorphous polycarbonate polyols comprising the steps of: (A) reacting (i) phosgene, (ii) a branched-chain polyhydric alcohol having about 4 to 12 carbon atoms, and (iii) about 3 to 40 mole percent, based upon the total amount of polyhydric alcohol, of a straight chain polyhydric alcohol having about 5 to 20 carbon atoms in the presence of a solvent and in the absence of a catalyst at a temperature of about 60° to 100° C., and (B) contacting the amorphous polycarbonate product in the reaction mixture with a catalytic amount of a tertiary amine at reflux temperature for a period of time of at least about 30 minutes.
Claim 2
Dependent Claim
111 words
A process for preparing amorphous polycarbonate polyols comprising the steps of: (A) reacting (i) phosgene, (ii) a branched-chain polyhydric alcohol having about 4 to 12 carbon atoms, and (iii) about 3 to 40 mole percent, based upon the total amount of polyhydric alcohol, of a straight chain polyhydric alcohol having about 5 to 20 carbon atoms in the presence of a solvent and in the absence of a catalyst at a temperature of about 60° to 100° C., and (B) contacting the amorphous polycarbonate product in the reaction mixture with a catalytic amount of a tertiary amine at reflux temperature for a period of time of at least about 30 minutes.
Claim 3
Dependent Claim
22 words
The process of claim 1 wherein said reacting step is conducted for a period of time of at least about 15 minutes.
Claim 4
Dependent Claim
11 words
The process of claim 1 wherein said polyhydric alcohols are diols.
Claim 5
Dependent Claim
18 words
The process of claim 1 wherein said branched-chain polyhydric alcohol comprises neopentyl glycol, pentaerythritol, or a mixture thereof.
Claim 6
Dependent Claim
21 words
The process of claim 3 wherein said straight chain diol comprises 1,6-hexanediol, 1,8-octanediol, 1,10-decanediol, 1,12-dodecanediol, tetraethylene glycol, or a mixture thereof.
Claim 7
Dependent Claim
22 words
The process of claim 1 wherein the molar ratio of total alcohol:phosgene present in the reaction system is about 1.25:1 to 1:1.
Claim 8
Dependent Claim
19 words
The process of claim 1 wherein said solvent comprises xylene, toluene, benzene, chlorobenzene, methylene chloride, or a mixture thereof.
Claim 9
Dependent Claim
15 words
The process of claim 1 wherein said solvent comprises xylene, toluene, or a mixture thereof.
Claim 10
Dependent Claim
20 words
The process of claim 1 wherein said reacting step is conducted at a temperature of about 80° to 90° C.
Claim 11
Dependent Claim
16 words
The process of claim 1 wherein said tertiary amine comprises triethylamine, pyridine, or a mixture thereof.
Claim 12
Dependent Claim
24 words
The process of claim 1 wherein said tertiary amine is employed in an amount of at least about 0.01 mole per mole of phosgene.
Claim 13
Dependent Claim
24 words
The process of claim 1 wherein said tertiary amine is employed in an amount of about 0.01 to 0.2 mole per mole of phosgene.
Claim 14
Dependent Claim
30 words
The process of claim 1 wherein said straight chain polyhydric alcohol is employed in an amount of about 10 to 20 mole percent, based upon the total amount of alcohol.
Claim 15
Dependent Claim
20 words
The process of claim 1 wherein said contacting step is conducted at a temperature of about 100° to 150° C.
Claim 16
Dependent Claim
155 words
A process for preparing amorphous polycarbonate polyols comprising the steps of: (A) reacting for a period of time of at least about 15 minutes (i) phosgene, (ii) a branched-chain diol comprising neopentyl glycol, and (iii) about 10 to 20 mole percent, based upon the total amount of diol, of a straight chain diol comprising 1,6-hexanediol, 1,8-octanediol, 1,10-decanediol, 1,12-dodecanediol, tetraethylene glycol, or a mixture thereof in the absence of a catalyst and in the presence of a solvent comprising xylene toluene, or a mixture thereof at a temperature of about 80° to 90° C., wherein the molar ratio of total diol:phosgene present in the reaction mixture is about 1.25:1 to 1:1, and (B) contacting the amorphous polycarbonate product in the reaction mixture at a temperature of about 100° to 150° C. with about 0.01 to 0.2 mole of a tertiary amine per mole of phosgene for a period of time of at least about 30 minutes.
Claim 17
Dependent Claim
155 words
A process for preparing amorphous polycarbonate polyols comprising the steps of: (A) reacting for a period of time of at least about 15 minutes (i) phosgene, (ii) a branched-chain diol comprising neopentyl glycol, and (iii) about 10 to 20 mole percent, based upon the total amount of diol, of a straight chain diol comprising 1,6-hexanediol, 1,8-octanediol, 1,10-decanediol, 1,12-dodecanediol, tetraethylene glycol, or a mixture thereof in the absence of a catalyst and in the presence of a solvent comprising xylene toluene, or a mixture thereof at a temperature of about 80° to 90° C., wherein the molar ratio of total diol:phosgene present in the reaction mixture is about 1.25:1 to 1:1, and (B) contacting the amorphous polycarbonate product in the reaction mixture at a temperature of about 100° to 150° C. with about 0.01 to 0.2 mole of a tertiary amine per mole of phosgene for a period of time of at least about 30 minutes.
Claim 18
Dependent Claim
16 words
The process of claim 15 wherein said tertiary amine comprises triethylamine, pyridine, or a mixture thereof.
Claim 19
Dependent Claim
24 words
The process of claim 15 wherein said tertiary amine is employed in an amount of about 0.03 to 0.18 mole per mole of phosgene.
Claim 20
Dependent Claim
12 words
The process of claim 15 wherein said straight chain diol comprises 1,6-hexanediol.
Claim 21
Dependent Claim
15 words
The process of claim 15 wherein the molar ratio of total diol:phosgene is about 1.1:1.
Claim 22
Dependent Claim
11 words
An amorphous polycarbonate polyol made by the process of claim 1.
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) | 1988-08-05 | 1989-02-04 | 1989-08-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-08-05 | 1993-02-04 | 1993-08-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-08-05 | 1997-02-04 | 1997-08-06 | $7700.00 | Window Closed / Lapsed |