US4439546A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Scrap rim polyurethane modified extender polyols
Assignee: Dow Chemical Co
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Filing: 1983-08-05
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Granted: 1984-03-27
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Expires: 2003-08-05
Abstract
Abstract Mixtures of aromatic polyols containing ester functionalities suitable for use as polyol extenders in polyurethane foams prepared by reacting dibasic acid residues with an alkylene glycol residue, the reaction product of which is reacted with recycled polyethylene terephthalate into which scrap RIM is dissolved, are described. Scrap RIM is recycled reaction injection molded polyurethane material which has been chopped or pulverized. From about 10 to 50 wt. % of the resulting modified extender polyol mixture may be scrap RIM. Surprisingly, the process is non-catalytic. These novel polyols may be blended with conventional polyols to yield excellent rigid foams, thus serving as useful polyol extenders.
Inventors
- 👤 Michael E. Brennan
- 👤 Doris M. Rice
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 15:34
CPC Classifications
C; C08; C08G; C08G63/00; C08G63/02; C08G63/12; C08G63/16; C08G63/18; B; B29; B29B; B29B17/00; C08G18/00; C08G18/06; C08G18/28; C08G18/40; C08G18/42; C08G18/4205; C08G18/4208; C08G18/4211; C08G18/4213; C08G18/4216; B29C; B29C67/00; B29C67/24; B29C67/246; C08G2110/00; C08G2110/0025; C08G2110/0041; C08G2110/005; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/582; Y02W; Y02W30/00; Y02W30/50; Y02W30/62
Claims Analysis
Total Claims: 23
Claim 1
Independent Claim
35 words
A mixture of scrap reaction injection molded polyurethane modified extender polyols, being produced by reacting a dibasic acid with an aklylene glycol and recycled polyethylene terephthalate in the presence of scrap reaction injection molded polyurethane.
Claim 2
Dependent Claim
35 words
A mixture of scrap reaction injection molded polyurethane modified extender polyols, being produced by reacting a dibasic acid with an aklylene glycol and recycled polyethylene terephthalate in the presence of scrap reaction injection molded polyurethane.
Claim 3
Dependent Claim
25 words
The mixture of modified extender polyols of claim 1 in which the scrap injection molded polyurethane comprises 10 to 50 wt.% of the reaction components.
Claim 4
Dependent Claim
32 words
The mixture of modified extender polyols of claim 1 in which the reaction is conducted at a temperature in the range of 170° to 250° C. in the absence of a catalyst.
Claim 5
Dependent Claim
36 words
The mixture of modified extender polyols of claim 1 in which the dibasic acid is a waste stream which comprises one or more acids from the group consisting of glutaric acid, succinic acid and adipic acid.
Claim 6
Dependent Claim
38 words
The mixture of modified extender polyols of claim 1 in which the alkylene glycol has the formula ##STR5## where R is hydrogen or lower alkyl of 1 to 4 carbon atoms and n is from 1 to 3.
Claim 7
Dependent Claim
27 words
The mixture of modified extender polyols of claim 1 in which the approximate mole ratio of the reactants polyethylene terephthalate scrap: dibasic acid: aklylene glycol is 1:1:2.
Claim 8
Dependent Claim
24 words
The mixture of modified extender polyols of claim 1 in which the average hydroxyl number of the resultant mixture is between 100 and 400.
Claim 9
Dependent Claim
97 words
A mixture of scrap reaction injection molded polyurethane modified extender polyols having hydroxyl, aromatic and ester functionalities for use in preparing rigid foams, being produced by the process comprising a. esterifying, in the absence of a catalyst, a dibasic acid with an alkylene glycol to produce a polyester polyol, b. transesterifying, in the absence of a catalyst, recycled polyethylene terephthalate with the polyester polyol reaction product from the previous step to produce a mixture of aromatic polyester polyols, and c. dissolving scrap reaction injection molded polyurethane in the mixture of aromatic polyester polyols of the previous step.
Claim 10
Dependent Claim
97 words
A mixture of scrap reaction injection molded polyurethane modified extender polyols having hydroxyl, aromatic and ester functionalities for use in preparing rigid foams, being produced by the process comprising a. esterifying, in the absence of a catalyst, a dibasic acid with an alkylene glycol to produce a polyester polyol, b. transesterifying, in the absence of a catalyst, recycled polyethylene terephthalate with the polyester polyol reaction product from the previous step to produce a mixture of aromatic polyester polyols, and c. dissolving scrap reaction injection molded polyurethane in the mixture of aromatic polyester polyols of the previous step.
Claim 11
Dependent Claim
26 words
The mixture of modified extender polyols of claim 8 in which the scrap reaction injection molded polyurethane comprises 10 to 50 wt.% of the total mixture.
Claim 12
Dependent Claim
27 words
The mixture of modified extender polyols of claim 8 in which the mixture is formed at a temperature in the range of from 170° to 250° C.
Claim 13
Dependent Claim
36 words
The mixture of modified extender polyols of claim 8 in which the dibasic acid is a waste stream which comprises one or more acids from the group consisting of glutaric acid, succinic acid and adipic acid.
Claim 14
Dependent Claim
38 words
The mixture of modified extender polyols of claim 8 in which the alkylene glycol has the formula ##STR6## where R is hydrogen or lower alkyl of 1 to 4 carbon atoms and n is from 1 to 3.
Claim 15
Dependent Claim
26 words
The mixture of modified extender polyols of claim 8 in which the approximate mole ratio of the reactants polyethylene terephthalate scrap:dibasic acid waste:alkylene glycol is 1:1:2.
Claim 16
Dependent Claim
24 words
The mixture of modified extender polyols of claim 8 in which the average hydroxyl number of the resultant mixture is between 100 and 400.
Claim 17
Dependent Claim
100 words
A mixture of scrap reaction injection molded polyurethane modified extender polyols having hydroxyl, aromatic and ester functionalities for use in preparing rigid foams, being produced by the process comprising a. esterifying, in the absence of a catalyst, a dibasic acid with an alkylene glycol to produce a polyester polyol, b. dissolving scrap reaction injection molded polyurethane in the polyester polyol, and c. transesterifying, in the absence of a catalyst, recycled polyethylene terephthalate with the polyester polyol reaction product from the previous step, such that the average hydroxyl number of the resultant modified extender polyol mixture is between 100 and 400.
Claim 18
Dependent Claim
100 words
A mixture of scrap reaction injection molded polyurethane modified extender polyols having hydroxyl, aromatic and ester functionalities for use in preparing rigid foams, being produced by the process comprising a. esterifying, in the absence of a catalyst, a dibasic acid with an alkylene glycol to produce a polyester polyol, b. dissolving scrap reaction injection molded polyurethane in the polyester polyol, and c. transesterifying, in the absence of a catalyst, recycled polyethylene terephthalate with the polyester polyol reaction product from the previous step, such that the average hydroxyl number of the resultant modified extender polyol mixture is between 100 and 400.
Claim 19
Dependent Claim
26 words
The mixture of modified extender polyols of claim 15 in which the scrap reaction injection molded polyurethane comprises 10 to 50 wt.% of the reaction components.
Claim 20
Dependent Claim
26 words
The mixture of modified extender polyols of claim 15 in which the reaction is conducted at a temperature in the range of 170° to 250° C.
Claim 21
Dependent Claim
36 words
The mixture of modified extender polyols of claim 15 in which the dibasic acid is a waste stream which comprises one or more acids from the group consisting of glutaric acid, succinic acid and adipic acid.
Claim 22
Dependent Claim
47 words
The mixture of modified extender polyols of claim 15 in which the alkylene glycol is a glycol waste stream comprising alkylene glycols of the formula ##STR7## where R is hydrogen or lower alkyl of 1 to 4 carbon atoms and n is from 1 to 3, and
Claim 23
Dependent Claim
25 words
The mixture of modified extender polyols of claim 15 in which the approximate mole ratio of the reactants recycled polyethylene terephthalate:dibasic acid:alkylene glycol is 1:1:2.
References Cited (Backward Citations)
US4166896A
Cited
US4159972A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-03-27 | 1987-09-26 | 1988-03-27 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-03-27 | 1991-09-26 | 1992-03-27 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-03-27 | 1995-09-26 | 1996-03-27 | $7700.00 | Window Closed / Lapsed |