Patent US4053446A successfully refreshed from Google Patents.
US4053446A
Expired / Lapsed
US
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Process for preparing high tear-strength polydiene polyurethane
Assignee: Bridgestone Corp
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Filing: 1976-08-31
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Granted: 1977-10-11
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Expires: 1996-08-31
Abstract
Abstract Polydiene polyurethanes having high tear strength are obtained by using polydiene glycols, prepared with use of lithium-based catalyst, having a number average molecular weight of 1,000 to 5,000 and functionality of 1.8 - 2.1, diisocyanates and chain-extending agents, and by controlling chemical cross-link density being 4 × 10 -5 mole/cc and less. When the chemical cross-link density is within the above range, elongation and tensile strength in addition to tear strength of the polyurethane are improved significantly. Furthermore, when 10 - 50 parts by weight of the specified carbon black are added to 100 parts by weight of the mixture of the prepolymer, the chain-extending agent and the additive prior to curing the prepolymer, these mechanical properties of the polyurethane are improved further.
Inventors
- 👤 Yoji Watabe
- 👤 Michio Ishii
- 👤 Yutaka Iseda
- 👤 Kouei Komatsu
- 👤 Noboru Ohshima
- 👤 Yozo Nakata, deceased
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 18:12
CPC Classifications
C; C08; C08G; C08G18/00; C08G18/06; C08G18/28; C08G18/67; C08G18/69; C08K; C08K3/00; C08K3/02; C08K3/04
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
138 words
A process for preparing a polydiene polyurethane having high tear strength, which process comprises reacting a. a polydiene glycol prepared with use of a dilithio compound as a catalyst, and having a functionality of from 1.8 to 2.1 and a number average molecular weight of from 1,000 to 5,000, the residual lithium content being below 30 ppm, b. a diisocyanate compound, and c. a chain-extending agent selected from diamine and diol compounds by the prepolymer method, the equivalent ratio of the isocyanate groups in said polydiene glycol being 1.5 to 3.0, the equivalent ratio of active hydrogens in said chain-extending agent to isocyanate groups in said prepolymer being 0.8 to 1.1, and the curing temperature being 50 to 140° C. the polydiene polyurethane so obtained having a chemical cross-link density of 4 × 10 -5 mole/cc or less.
Claim 2
Dependent Claim
138 words
A process for preparing a polydiene polyurethane having high tear strength, which process comprises reacting a. a polydiene glycol prepared with use of a dilithio compound as a catalyst, and having a functionality of from 1.8 to 2.1 and a number average molecular weight of from 1,000 to 5,000, the residual lithium content being below 30 ppm, b. a diisocyanate compound, and c. a chain-extending agent selected from diamine and diol compounds by the prepolymer method, the equivalent ratio of the isocyanate groups in said polydiene glycol being 1.5 to 3.0, the equivalent ratio of active hydrogens in said chain-extending agent to isocyanate groups in said prepolymer being 0.8 to 1.1, and the curing temperature being 50 to 140° C. the polydiene polyurethane so obtained having a chemical cross-link density of 4 × 10 -5 mole/cc or less.
Claim 3
Dependent Claim
214 words
A process for preparing a polydiene polyurethane having high tear strength, which process comprises reacting a. a polydiene glycol prepared with use of dilithio compound as a catalyst, and having a functionality of from 1.8 to 2.1, a number average molecular weight of from 1,000 to 5,000 and a residual lithium content of less than 30 ppm after treatment with mineral acid other than sulfuric acid; b. a diisocyanate compound, and c. a chain extending agent selected from diamine and diol compounds by the prepolymer method, and compounding 10 to 50 parts by weight of carbon black per 100 parts by weight of the total amount of said polydiene glycol, said diisocyanate compound and said chain-extending agent before curing, the equivalent ratio of the isocyanate groups in said polydiene glycol being 1.5 to 3.0, the equivalent ratio of active hydrogens in said chain-extending agent to the isocyanate groups in said prepolymer being 0.8 to 1.1, and the curing temperature being 50° to 140° C., the ratio of chain length between physical cross-links in the corresponding non-loaded polyurethane to the particle size of said carbon black being established within the range of from 2.4 to 15, and the chemical crosslink density of said corresponding non-loaded polydiene polyurethane being 4 × 10 -5 mole/cc or less.
Claim 4
Dependent Claim
214 words
A process for preparing a polydiene polyurethane having high tear strength, which process comprises reacting a. a polydiene glycol prepared with use of dilithio compound as a catalyst, and having a functionality of from 1.8 to 2.1, a number average molecular weight of from 1,000 to 5,000 and a residual lithium content of less than 30 ppm after treatment with mineral acid other than sulfuric acid; b. a diisocyanate compound, and c. a chain extending agent selected from diamine and diol compounds by the prepolymer method, and compounding 10 to 50 parts by weight of carbon black per 100 parts by weight of the total amount of said polydiene glycol, said diisocyanate compound and said chain-extending agent before curing, the equivalent ratio of the isocyanate groups in said polydiene glycol being 1.5 to 3.0, the equivalent ratio of active hydrogens in said chain-extending agent to the isocyanate groups in said prepolymer being 0.8 to 1.1, and the curing temperature being 50° to 140° C., the ratio of chain length between physical cross-links in the corresponding non-loaded polyurethane to the particle size of said carbon black being established within the range of from 2.4 to 15, and the chemical crosslink density of said corresponding non-loaded polydiene polyurethane being 4 × 10 -5 mole/cc or less.
Claim 5
Dependent Claim
13 words
A high tear-strength polydiene polyurethane produced according to the process of claim 1.
Claim 6
Dependent Claim
20 words
The process of claim 1 wherein said number average molecular weight is within the range of from 1,300 to 3,500.
Claim 7
Dependent Claim
23 words
The process of claim 1 wherein said polydiene glycol is treated with sulfuric acid to remove residual lithium on preparing said polydiene glycol.
Claim 8
Dependent Claim
32 words
The process of claim 1 wherein said polydiene glycol is treated with mineral acid except sulfuric acid on preparing said polybutadiene glycol and the residual lithium content is less than 30 ppm.
Claim 9
Dependent Claim
12 words
The process of claim 1 wherein said mineral acid is hydrochloric acid.
Claim 10
Dependent Claim
12 words
The process of claim 1 wherein said polydiene glycol is polybutadiene glycol.
Claim 11
Dependent Claim
18 words
The process of claim 1 wherein said chemical cross-link density is 2.0 × 10 -5 mole/cc and less.
Claim 12
Dependent Claim
13 words
The process of claim 2 wherein said carbon black is neutral carbon black.
Claim 13
Dependent Claim
26 words
The process of claim 2 wherein said carbon black is selected from super abrasion furnace (SAF) carbon black and neutralized high color channel (HCC) carbon black.
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) | 1980-10-10 | 1981-04-11 | 1981-10-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-10-10 | 1985-04-11 | 1985-10-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-10-10 | 1989-04-11 | 1989-10-11 | $7700.00 | Window Closed / Lapsed |