US4371684A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Thermoplastic polyurethanes for processing in extruders and/or on calenders
Assignee: Bayer AG
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Filing: 1981-05-29
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Granted: 1983-02-01
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Expires: 2001-05-29
Abstract
Abstract The invention is directed to a process extruding or melt roll calendering thermoplastic polyurethanes wherein the polyurethanes used are synthesized from p1 (a) one or more relatively high molecular weight substantially linear polyols having molecular weights in the range from 400 to 10,000 (b) diphenyl methane and/or hexamethylene diisocyanate and (c) a mixture of 85 to 99% by weight of 1,4-butane diol and 1 to 15% by weight of at least one co-extender selected from the group consisting of ethylene glycol, diethylene glycol, triethylene glycol, diethylene 1,2-propane diol, 1,3-butane diol, 1,6-hexane diol, 2-ethyl-1,3-hexane diol, 2,2-dimethyl-1,3-propane diol, 1,4-bis-hydroxymethyl cyclohexane, hydroquinone-bis-hydroxyethyl ether, and mixtures thereof, the equivalent ratio of NCO groups in component (B) to the Zerewitinoff-active hydrogen atoms in components (A) and (C) being from 0.9:1 to 1.2:1 and the molar ratio of component (A) to (C) being from 1:20 to 5:1.
Inventors
- 👤 Bernd Quiring
- 👤 Georg Niederdellmann
- 👤 Wilhelm Goyert
- 👤 Hans Wagner
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-24 00:00
CPC Classifications
C; C08; C08G; C08G18/00; C08G18/06; C08G18/28; C08G18/65; C08G18/6505; C08G18/6511; C08G18/08; C08G18/10; C08G18/40; C08G18/61
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
177 words
In the processing of thermoplastic polyurethanes in extruders and/or melt roll calenders, the improvement wherein the polyurethanes used are synthesized from (A) one or more relatively high molecular weight substantially linear polyols having molecular weights in the range from 400 to 10,000 selected from the group consisting of hydroxyl-group-containing polyesters of glycols and adipic acid, phthalic and/or terephthalic acid and their hydrogenation products, hydroxyl polycarbonates, polycaprolactones, polyethylene oxide and polypropylene oxide started with glycols, amines and/or water and polytetrahydrofuran, (B) diphenyl methane diisocyanate and/or hexamethylene diisocyanate and (C) a mixture of 85 to 99% by weight of 1,4-butane diol and 1 to 15% by weight of at least one co-extender selected from the group consisting of ethylene glycol, diethylene glycol, triethylene glycol, diethylene-1,2-propane diol, 1,3-butane diol, 1,6-hexane diol, 2-ethyl-1,3-hexane diol, 2,2-dimethyl-1,3-propane diol, 1,4-bis-hydroxymethyl cyclohexane, hydroquinone-bis-hydroxyethyl ether, and mixtures thereof, the equivalent ratio of NCO groups in component (B) to the Zerewitinoff-active hydrogen atoms in components (A) and (C) being from 0.9:1 to 1.2:1 and the molar ratio of component (A) to (C) being from 1:20 to 5:1.
Claim 2
Dependent Claim
177 words
In the processing of thermoplastic polyurethanes in extruders and/or melt roll calenders, the improvement wherein the polyurethanes used are synthesized from (A) one or more relatively high molecular weight substantially linear polyols having molecular weights in the range from 400 to 10,000 selected from the group consisting of hydroxyl-group-containing polyesters of glycols and adipic acid, phthalic and/or terephthalic acid and their hydrogenation products, hydroxyl polycarbonates, polycaprolactones, polyethylene oxide and polypropylene oxide started with glycols, amines and/or water and polytetrahydrofuran, (B) diphenyl methane diisocyanate and/or hexamethylene diisocyanate and (C) a mixture of 85 to 99% by weight of 1,4-butane diol and 1 to 15% by weight of at least one co-extender selected from the group consisting of ethylene glycol, diethylene glycol, triethylene glycol, diethylene-1,2-propane diol, 1,3-butane diol, 1,6-hexane diol, 2-ethyl-1,3-hexane diol, 2,2-dimethyl-1,3-propane diol, 1,4-bis-hydroxymethyl cyclohexane, hydroquinone-bis-hydroxyethyl ether, and mixtures thereof, the equivalent ratio of NCO groups in component (B) to the Zerewitinoff-active hydrogen atoms in components (A) and (C) being from 0.9:1 to 1.2:1 and the molar ratio of component (A) to (C) being from 1:20 to 5:1.
Claim 3
Dependent Claim
25 words
The process of claim 1, characterized in that the ratio of NCO-groups to Zerewitinoff-active groups in components (A) and (C) is from 0.93:1 to 1.04:1.
Claim 4
Dependent Claim
23 words
The process of claim 1, characterized in that the ratio by weight of butane diol to co-chain extender is from 98:2 to 90:10.
Claim 5
Dependent Claim
23 words
The process of claim 3, characterized in that the ratio by weight of butane diol to co-chain extender is from 95:5 to 92:8.
Claim 6
Dependent Claim
24 words
The process of claim 1, characterized in that component (A) is a polyol having average molecular weight in the range from 450 to 5000.
Claim 7
Dependent Claim
26 words
The process of claim 1, characterized in that the co-extender is selected from the group consisting of ethylene glycol, diethylene glycol, hexane diol, and mixtures thereof.
Claim 8
Dependent Claim
21 words
The process of claim 6, characterized in that the molar ratio of components (A) to (C) is from 1:15 to 1:1.
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) | 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 |