WO1998025986A1 - Polyestercarbonate-polyurethaneurea fibers - Google Patents
Polyestercarbonate-polyurethaneurea fibers Download PDFInfo
- Publication number
- WO1998025986A1 WO1998025986A1 PCT/US1997/022568 US9722568W WO9825986A1 WO 1998025986 A1 WO1998025986 A1 WO 1998025986A1 US 9722568 W US9722568 W US 9722568W WO 9825986 A1 WO9825986 A1 WO 9825986A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- diol
- diisocyanate
- spandex
- poly
- diamine
- Prior art date
Links
Classifications
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
- D01F6/58—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
- D01F6/70—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyurethanes
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/42—Polycondensates having carboxylic or carbonic ester groups in the main chain
- C08G18/44—Polycarbonates
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/08—Processes
- C08G18/10—Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
- C08G18/72—Polyisocyanates or polyisothiocyanates
- C08G18/74—Polyisocyanates or polyisothiocyanates cyclic
- C08G18/75—Polyisocyanates or polyisothiocyanates cyclic cycloaliphatic
Definitions
- This invention relates to spandex comprising polyestercarbonate-urethaneureas and more specifically to spandex prepared from a polycarbonate diol made from poly (hexane-1, 6-carbonate) diol and poly ( ⁇ -capro- lactone) diol, a cyclic aliphatic diisocyanate, and a diamine chain extender.
- 4,837,292 discloses spandex prepared from the reaction product of polycarbonate diols with diisocyanates and diamine chain extenders .
- the polycarbonate diols disclosed are poly (pentane-1, 5-carbonate) diol, poly (hexane-1, 6-carbonate) diol, copolymers thereof and mixtures thereof.
- Italian Patent No. 710,940 discloses spandex made from hexamethylene glycol-based polycarbonate diols, aromatic diisocyanates, and aliphatic diamines . Although spandex based on ordinary polycarbonate diols can have superior environmental resistance, it often has low flexibility and elongation. As disclosed in Japanese Patent Application Publication No.
- the spandex of the present invention is a polyestercarbonate-polyurethaneurea which is the reaction product of: a modified polycarbonate prepared by reacting a mixture of poly (hexane-1 , 6-carbonate) diol and poly ( ⁇ -caprolactone) diol with a dialkylcarbonate; a cyclic aliphatic diisocyanate; and a diamine chain extender.
- spandex has its customary meaning: a manufactured fiber in which the fiber- forming substance is a long chain synthetic elastomer comprised of at least 85% by weight of a segmented polyurethane .
- the polyurethane can generally be prepared by "capping" a polymeric glycol with a diisocyanate and reacting the resulting "capped glycol” (sometimes called an "NCO-terminated prepolymer") with a diamine to form a polyurethaneurea .
- the chain extension and subsequent processing are preferably carried out in a suitable solvent.
- the polyurethane- urea-based spandex can then be prepared by dry or wet spinning the polymer solution; dry spinning is pre erred.
- the polymeric diol used in making the spandex of the present invention is a modified polycarbonate diol prepared by transesterifying a mixture of poly(hexane-
- Dialkylcarbonate is intended to include alkylene carbonates.
- minor amounts of another diol may also be added, for example 1,3- propanediol, neopentyl glycol, 2-methyl-l, 4-butanediol, cyclohexanediol, and low molecular weight oligomers of poly (tetramethyleneether) glycol such as dibutyleneether glycol and tributyleneether glycol.
- the weight ratio of poly (hexane-1 , 6-carbonate) diol to poly( ⁇ - caprolactone) diol in the modified polycarbonate diol is in the range of about 95:5 to 65:35, preferably in the range of about 90:10 to 70:30.
- the number-average molecular weight of the modified polycarbonate diol is preferably in the range of about 1000 to 8000, more preferably in the range of about 1000 to 5000, and most preferably in the range of about 1500 to 3000. Good strength and elongation can be obtained when the modified diol is in this range.
- the modified polycarbonate diol is reacted with a cyclic aliphatic diisocyanate to form a capped glycol .
- suitable alicyclic diisocyanates include 4,4 ' -methylenebis (cyclohexylisocyanate) , hereinafter, "H12MDI", isophorone diisocyanate, methylcyclohexane- 2, 4-diisocyanate, methylcyclohexane-2, 6-diisocyanate, cyclohexane-1, 4-diisocyanate, hexahydroxylylene diisocyanate, and octahydro-1 , 5-naphthalene diisocyanate and mixtures thereof.
- H12MDI 4,4 ' -methylenebis (cyclohexylisocyanate)
- H12MDI is preferred.
- the molar ratio of the modified polycarbonate diol to the alicyclic diisocyanate can be within a range of about 1:1.3 to 1:3.0.
- a molar ratio within a range of about 1:1.5 to 1:2.2 is preferable.
- Spandex having a high elongation-to-break and a high melting point can be obtained within this range.
- a chain extender can be reacted with the capped glycol in a suitable solvent .
- the chain extender used in the present invention is a diamine, preferably a low-molecular- weight diamine. If a low-molecular-weight glycol is used, the melting point of the resulting yarn is low, and problems such as a long reaction time arise, which is undesirable. However, minor amounts of low- molecular-weight glycols can be used, provided this is within a range that does not eliminate or diminish the effects of the present invention.
- low- molecular weight diamines examples include ethylenediamine, 1, 2-propanediamine, 1, 3-propanediamine, 1, 6-hexamethyl- ene diamine, 1, 4-cyclohexyldiamine, 1, 3-cyclohexyl- diamine and mixtures thereof. Ethylenediamine is preferred.
- the resulting solution of polymer can then be spun to prepare the spandex of this invention.
- the polyurethane fibers of this invention generally have a stress (load power) at 100% elongation of about 0.020-0.070 times the strength at break and a stress at 200% elongation of about 0.035-0.150 times the strength at break.
- Such fibers have a soft stretchability and a suitable tightening force.
- the diameter or the cross-sectional shape of the fibers of this invention can be circular or flat.
- the presence of various stabilizers, pigments and the like within the fibers of the present invention is permitted and poses no problem.
- light resistance agents and antioxidants can be incorporated with the polymer such as 2 , 6-di-t-butyl-4-methylphenol, benzotriazole stabilizers such as TINUVIN® stabilizers (Ciba Geigy) , phosphorus agents such as SUMILYZER® P-16 (Sumitomo Chemical) , and hindered amine stabilizers such as TINUVIN®.
- benzotriazole stabilizers such as TINUVIN® stabilizers (Ciba Geigy)
- phosphorus agents such as SUMILYZER® P-16 (Sumitomo Chemical)
- hindered amine stabilizers such as TINUVIN®.
- inorganic pigments such as titanium oxide, zinc oxide and carbon black; metal soaps such as magnesium stearate; germicides containing mercury, zinc, or compounds thereof; deodorizers; lubricants such as silicones or mineral oils; and various antistatic agents such as barium sulfate, cerium oxide, betaine and phosphorus -based compounds can also be spun into the spandex.
- nitrogen oxide scavengers such as HN-150 (an aromatic hydrazide manufactured by Nippon Hydrazine, Chiyoda-ku, Tokyo, Japan) ; heat and oxidation stabilizers such as SUMILYZER® GA-80 (a hindered phenol manufactured by Sumitomo Chemical, Osaka, Japan); and light stabilizers such as SUMISORB® 300#622 (manufactured by Sumitomo Chemical) can also be included.
- HN-150 an aromatic hydrazide manufactured by Nippon Hydrazine, Chiyoda-ku, Tokyo, Japan
- heat and oxidation stabilizers such as SUMILYZER® GA-80 (a hindered phenol manufactured by Sumitomo Chemical, Osaka, Japan)
- light stabilizers such as SUMISORB® 300#622 (manufactured by Sumitomo Chemical)
- the polyurethane of the present invention can be prepared as follows. Because the polyurethane of the present invention utilizes a diamine chain extender whose reactivity with diisocyanate compounds differs from that of modified polycarbonate diols, it is preferable that production be carried out by a prepolymer method in which a polymeric diol is reacted with a diisocyanate in the range of about room temperature to about 200°C, thereby synthesizing an NCO-terminated prepolymer, adding to this a solvent that is substantially inert to the isocyanate groups and a chain extender that has been diluted with this solvent, then carrying out chain extension polymerization at about room temperature to about 60°C.
- suitable solvents include dimethyl formamide, dimethyl acetamide ("DMAc”), dimethyl sulfone oxide, methyl ethyl ketone, toluene, xylene, dioxane, tetrahydrofuran, ethyl acetate and N-methyl pyrrolidone.
- DMAc dimethyl acetamide
- One or more of these solvents can be used, although it is preferable to use an amide-type solvent capable of achieving a high solute concentration, such as dimethyl formamide or DMAc.
- Monofunctional chain terminators such as diethylamine, butylamine, ethanol, propanol or butanol can be used to achieve the desired molecular weight or solution viscosity. Diethylamine is preferred.
- the solids concentration is preferably about 30-40%, the solution viscosity is about 1200-6500 poises, preferably about 2000-6000 poises.
- the high- side melting point of the fibers of the invention is approximately 200°C to 250°C. This can be measured by Differential Scanning Calorimetry of finely cut fibers; two measurements are carried out and the second value is reported.
- a 12-micron film can be prepared by casting the polyurethaneurea solution, drying the cast solution in a nitrogen atmosphere, and measuring the second run value of the melting point.
- the number average molecular weight of the polymer is approximately 40,000 to 150,000, as measured by Gel Permeation Chromatography based on a polystyrene standard.
- Spinning can be carried out conventionally by either a wet spinning method or a dry spinning method, although is preferable to carry out a dry spinning method.
- test methods used in the Examples of the present invention are described below.
- a polycarbonate diol (“Nipporan 982N", molecular weight of about 2000, Nippon Urethanes, Osaka, Japan) was used. This diol was prepared by reacting a 9:1 by weight mixture of 2000 molecular weight poly (hexane-1 , 6 -carbonate) diol and 2000 molecular weight poly ( ⁇ -caprolactone) diol with a dialkyl carbonate.
- stabilizing additives were mixed with the polymer solution before spinning.
- the additives and their amounts were: 1.7wt% HN-150, 0.9wt% SUMILYZER® GA-80, and 0.4wt% SUMISORB® 300#622.
- the total of these additives was 3.0wt% based on polymer.
- the Table (below) gives the test results for each of the spandex yarns in the Examples: stress (load power) at 100% elongation (grams per denier) , stress at 200% elongation (grams per denier) , elongation at break (%) , tensile strength at break (grams per denier) , ratio of (stress at 100% elongation) / (strength at break), ratio of (stress at 200% elongation) / (strength at break), durability and yellowing resistance.
- the viscosity of this polymer solution was measured with a falling ball-type viscometer, and was found to be 3540 poises at 40°C.
- the polymer solution (32% solids) was then conventionally dry-spun at a speed of 530 m/min with the speed ratio between the godet roller and the winder set at 1.45, and 18 -denier/filament yarn was wound onto a conventional cardboard tube.
- the viscosity of this polymer solution was measured with a falling ball-type viscometer, and was found to be 1986 poises at 40°C.
- the polymer solution (32% solids) was then conventionally dry-spun at a speed of 530 m/min with the speed ratio between the godet roller and the winder set at 1.45, and 18- denier/filament yarn was wound onto a conventional cardboard tube .
- the viscosity of this polymer solution was measured with a falling ball-type viscometer, and was found to be 2805 poises at 40°C.
- the polymer solution (32% solids) was then dry-spun at a speed of 530 m/min with the speed ratio between the godet roller and the take-up unit set at 1.45, and 18-denier/monofilament yarn was taken up onto a conventional cardboard tube.
- NCO-terminal urethane prepolymer was prepared by reacting a poly (tetramethyleneether) glycol having a molecular weight of 1800 with MDI at 90°C in the absence of solvent, and at a molar ratio of 1:1.58 for a period of 2 hours .
- This prepolymer was cooled to room temperature, after which 500 g was collected in a 2-liter flask, then dissolved in 1000 g of DMAc.
- a solution of a mixture of 7.80 g of ethylene diamine and 1.17 g of diethylamine diluted with 80.7 g of DMAc was then added, in this way carrying out the chain extension reaction and giving a viscous polymer solution.
- the viscosity of this polymer solution was measured with a falling-ball viscometer, and found to be 2800 poises at 40°C.
- the polymer solution (32% solids) was then conventionally dry-spun at a velocity of 733 m/min, and 20 denier, 2 -filament yarn was wound up on a cardboard tube .
- the polyurethane fibers of this invention have an unexpectedly, markedly enhanced durability and retention of strength when compared to prior art fibers and retain the good elongation properties of the prior art fibers. Because of these excellent properties, by using them alone or in combinations with various fibers, they can be utilized in various uses, such as a tightening material in a variety of textile products such as socks, stockings, circular knit fabrics, tricot fabrics, bathing suits, ski pants, work clothes, fire- resistant clothing, Western-style clothes, golf clothes, wet suits, brassieres, girdles and gloves. They can also be utilized as tightening material to prevent sanitary products such as disposable diapers from leaking and in waterproof materials; and such other uses as artificial bait, imitation flowers, wire insulation, wiping cloths, "copy cleaners," gaskets and the like.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Artificial Filaments (AREA)
- Polyurethanes Or Polyureas (AREA)
Abstract
Description
Claims
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP97951605A EP0944662A1 (en) | 1996-12-13 | 1997-12-10 | Polyestercarbonate-polyurethaneurea fibers |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8/352793 | 1996-12-13 | ||
JP35279396 | 1996-12-13 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1998025986A1 true WO1998025986A1 (en) | 1998-06-18 |
Family
ID=18426484
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US1997/022568 WO1998025986A1 (en) | 1996-12-13 | 1997-12-10 | Polyestercarbonate-polyurethaneurea fibers |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP0944662A1 (en) |
KR (1) | KR20000057560A (en) |
WO (1) | WO1998025986A1 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8029783B2 (en) | 2005-02-02 | 2011-10-04 | Genentech, Inc. | DR5 antibodies and articles of manufacture containing same |
WO2016000845A1 (en) * | 2014-07-02 | 2016-01-07 | Basf Coatings Gmbh | Two-component coating compositions and coatings made therefrom for increasing resistance against erosion |
CN111793342A (en) * | 2020-06-08 | 2020-10-20 | 金发科技股份有限公司 | Polycarbonate composition and preparation method thereof |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2006788A1 (en) * | 1968-04-23 | 1970-01-02 | Bayer Ag | |
US4837292A (en) * | 1987-12-17 | 1989-06-06 | E. I. Dupont De Nemours And Company | Article of spandex having polycarbonate soft segment |
EP0421217A2 (en) * | 1989-10-03 | 1991-04-10 | Bayer Ag | Elasthan fibres with high elasticity and tenacity and process for their preparation |
-
1997
- 1997-12-10 EP EP97951605A patent/EP0944662A1/en not_active Withdrawn
- 1997-12-10 KR KR1019990705287A patent/KR20000057560A/en not_active Application Discontinuation
- 1997-12-10 WO PCT/US1997/022568 patent/WO1998025986A1/en not_active Application Discontinuation
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2006788A1 (en) * | 1968-04-23 | 1970-01-02 | Bayer Ag | |
US4837292A (en) * | 1987-12-17 | 1989-06-06 | E. I. Dupont De Nemours And Company | Article of spandex having polycarbonate soft segment |
EP0321288A1 (en) * | 1987-12-17 | 1989-06-21 | E.I. Du Pont De Nemours And Company | Article of spandex having polycarbonate soft segment |
EP0421217A2 (en) * | 1989-10-03 | 1991-04-10 | Bayer Ag | Elasthan fibres with high elasticity and tenacity and process for their preparation |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8029783B2 (en) | 2005-02-02 | 2011-10-04 | Genentech, Inc. | DR5 antibodies and articles of manufacture containing same |
US8030023B2 (en) | 2005-02-02 | 2011-10-04 | Genentech, Inc. | Nucleic acid encoding DR5 antibodies and uses thereof |
US8409570B2 (en) | 2005-02-02 | 2013-04-02 | Genentech, Inc. | Method of inducing apoptosis using anti-DR5 antibodies |
WO2016000845A1 (en) * | 2014-07-02 | 2016-01-07 | Basf Coatings Gmbh | Two-component coating compositions and coatings made therefrom for increasing resistance against erosion |
US10519340B2 (en) | 2014-07-02 | 2019-12-31 | Basf Coatings Gmbh | Two-component coating compositions and coatings produced therefrom for improving erosion resistance |
CN111793342A (en) * | 2020-06-08 | 2020-10-20 | 金发科技股份有限公司 | Polycarbonate composition and preparation method thereof |
CN111793342B (en) * | 2020-06-08 | 2021-11-12 | 金发科技股份有限公司 | Polycarbonate composition and preparation method thereof |
Also Published As
Publication number | Publication date |
---|---|
EP0944662A1 (en) | 1999-09-29 |
KR20000057560A (en) | 2000-09-25 |
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