AU1040283A - Monofilaments of low carboxyl content for use in fabricating a paper machine dryer fabric - Google Patents
Monofilaments of low carboxyl content for use in fabricating a paper machine dryer fabricInfo
- Publication number
- AU1040283A AU1040283A AU10402/83A AU1040283A AU1040283A AU 1040283 A AU1040283 A AU 1040283A AU 10402/83 A AU10402/83 A AU 10402/83A AU 1040283 A AU1040283 A AU 1040283A AU 1040283 A AU1040283 A AU 1040283A
- Authority
- AU
- Australia
- Prior art keywords
- polyester
- monofilament
- stabilizer
- percent
- weight
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 title claims description 15
- 239000004744 fabric Substances 0.000 title claims description 13
- 229920000728 polyester Polymers 0.000 claims description 41
- 239000003381 stabilizer Substances 0.000 claims description 22
- 238000005299 abrasion Methods 0.000 claims description 15
- 238000000034 method Methods 0.000 claims description 15
- 230000003301 hydrolyzing effect Effects 0.000 claims description 13
- 230000015556 catabolic process Effects 0.000 claims description 12
- 238000006731 degradation reaction Methods 0.000 claims description 12
- 239000012815 thermoplastic material Substances 0.000 claims description 12
- 239000000463 material Substances 0.000 claims description 11
- 150000002148 esters Chemical class 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 6
- -1 polyethylene terephthalate Polymers 0.000 claims description 6
- 239000004814 polyurethane Substances 0.000 claims description 6
- 150000001718 carbodiimides Chemical class 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 229920002635 polyurethane Polymers 0.000 claims description 5
- 229920001400 block copolymer Polymers 0.000 claims description 4
- 150000001875 compounds Chemical class 0.000 claims description 4
- GYZLOYUZLJXAJU-UHFFFAOYSA-N diglycidyl ether Chemical group C1OC1COCC1CO1 GYZLOYUZLJXAJU-UHFFFAOYSA-N 0.000 claims description 4
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims description 4
- 239000012948 isocyanate Substances 0.000 claims description 4
- 150000002513 isocyanates Chemical class 0.000 claims description 4
- 150000003932 ketenimines Chemical class 0.000 claims description 4
- KKEYFWRCBNTPAC-UHFFFAOYSA-L terephthalate(2-) Chemical compound [O-]C(=O)C1=CC=C(C([O-])=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-L 0.000 claims description 4
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 claims description 4
- 150000001541 aziridines Chemical class 0.000 claims description 3
- 238000013329 compounding Methods 0.000 claims description 3
- 229920000139 polyethylene terephthalate Polymers 0.000 claims description 3
- 239000005020 polyethylene terephthalate Substances 0.000 claims description 3
- 239000004033 plastic Substances 0.000 claims description 2
- 229920003023 plastic Polymers 0.000 claims description 2
- 241000517645 Abra Species 0.000 claims 1
- 229920000642 polymer Polymers 0.000 description 9
- 238000012360 testing method Methods 0.000 description 7
- 230000007062 hydrolysis Effects 0.000 description 6
- 238000006460 hydrolysis reaction Methods 0.000 description 6
- 239000000654 additive Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 3
- 238000012668 chain scission Methods 0.000 description 3
- 239000013065 commercial product Substances 0.000 description 3
- 239000011347 resin Substances 0.000 description 3
- 229920005989 resin Polymers 0.000 description 3
- 230000000996 additive effect Effects 0.000 description 2
- 238000002144 chemical decomposition reaction Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 150000002894 organic compounds Chemical class 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 230000004580 weight loss Effects 0.000 description 2
- JIABEENURMZTTI-UHFFFAOYSA-N 1-isocyanato-2-[(2-isocyanatophenyl)methyl]benzene Chemical compound O=C=NC1=CC=CC=C1CC1=CC=CC=C1N=C=O JIABEENURMZTTI-UHFFFAOYSA-N 0.000 description 1
- KKEBXNMGHUCPEZ-UHFFFAOYSA-N 4-phenyl-1-(2-sulfanylethyl)imidazolidin-2-one Chemical compound N1C(=O)N(CCS)CC1C1=CC=CC=C1 KKEBXNMGHUCPEZ-UHFFFAOYSA-N 0.000 description 1
- NOWKCMXCCJGMRR-UHFFFAOYSA-N Aziridine Chemical compound C1CN1 NOWKCMXCCJGMRR-UHFFFAOYSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 229920001131 Pulp (paper) Polymers 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- XNGIFLGASWRNHJ-UHFFFAOYSA-L phthalate(2-) Chemical compound [O-]C(=O)C1=CC=CC=C1C([O-])=O XNGIFLGASWRNHJ-UHFFFAOYSA-L 0.000 description 1
- 229920000233 poly(alkylene oxides) Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920000921 polyethylene adipate Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 239000013055 pulp slurry Substances 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- DVKJHBMWWAPEIU-UHFFFAOYSA-N toluene 2,4-diisocyanate Chemical compound CC1=CC=C(N=C=O)C=C1N=C=O DVKJHBMWWAPEIU-UHFFFAOYSA-N 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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
- D01F6/88—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polycondensation products as major constituent with other polymers or low-molecular-weight compounds
- D01F6/92—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polycondensation products as major constituent with other polymers or low-molecular-weight compounds of polyesters
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/0008—Organic ingredients according to more than one of the "one dot" groups of C08K5/01 - C08K5/59
- C08K5/005—Stabilisers against oxidation, heat, light, ozone
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/15—Heterocyclic compounds having oxygen in the ring
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/16—Nitrogen-containing compounds
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L67/00—Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
- C08L67/02—Polyesters derived from dicarboxylic acids and dihydroxy compounds
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L75/00—Compositions of polyureas or polyurethanes; Compositions of derivatives of such polymers
- C08L75/04—Polyurethanes
Description
MONOFILAMENTS OF LOW CARBOXYL CONTENT FOR USE IN FABRICATING A PAPER MACHINE DRYER FABRIC
Technical Field
This invention relates to a monofilament of low carboxyl content for use in fabricating a paper machine dryer fabric having improved resistance to hydrolytic degradation and abrasion. The invention also relates to a method of making this filament and to a composition therefor.
Background Art
Polyester monofilaments, when woven into fabrics, have many applications in industrial filtration processes and as belts for conveying certain industrial product's. Such fabrics are used extensively in the paper industry to filter the wood pulp slurry and convey the formed paper to dryer sections of the paper-making process. The dryer section also contains conveying belts made out of industrial fabrics.
In industrial applications such as those mentioned above, the onofilaments are subjected to considerable abrasion and heat in wet atmospheres. Most polyesters known to the art are easily abraded and degraded in such applications, thereby limiting the useful life of the fabric.
There are several patents relating to improving the hydrolytic and thermal stability of polyesters. A non- exhaustive list includes the following references:
FR 2,309,581
US 3,959,228
SUBSTITUTE SHEET f O PI
US 4, 071, 504 US 3 , 975 , 329 US 3 , 676 , 393 US 3, 853 , 821 US 3 , 716, 582
GER 2,020,330 US 3,193,522 Most methods are directed towards reacting the free carboxyl end-groups of the polyester molecules with a suitable additive in order to chemically deactivate these end-groups. The carboxyl end-groups in the presence of water and high temperatures catalyze chain-scission at the ester linkages of the polymer molecule. Each broken bond creates an additional carboxyl group in the polymer thereby accelerating the chain-scission process.
Most additives for end-capping are slow to react with the molten polymer, thereby causing increased expenditure in time and equipment for commercial produc¬ tion of hydrolytically stable products. Catalysts are available to accelerate the reaction for a few of the additives, such that the reaction is complete within the 1 to 6 minutes that the polymer resides in a commercial extruder. The point of addition of the catalyst is usually at the start of the polymerization reaction. This ensures a thorough dispersion of the catalyst and is also the most convenient. The additive is best added at the throat of the extruder by means of a wel1-metered controlled-volume pump. However, this obviously entails complicated and expensive modification of the production machinery. It is preferable to use a polyester that has as low a carboxyl content as possible as the feed resin. Values as low as 15 meq COOH per 106 gms of resin and preferably a value of 10 or lower is recommended.
Disclosure of the Invention
It is an object of the present invention to provide a monofilament of low carboxyl content for use in fabri¬ cating a paper machine dryer fabric having improved resistance to hydrolytic degradation and abrasion.
It is another object of the invention to provide a process whereby such monofilaments can be easily fabri¬ cated with conventional machinery known to the art.
It is another object of the present invention to provide a monofilament of low carboxy content for use in fabricating a paper machine dryer fabric having improved resistance to hydrolytic degradation and abrasion, the monofilament comprising: a) a polyester; b) a polyester stabilizer; and c) a thermoplastic material.
It is another object of the invention to provide a composition comprising: a) a polyester; b) a polyester stabilizer; and c) a thermoplastic material. Brief Description of the Drawings
The invention is illustrated by means of the follow¬ ing drawings and tabulations in which: FIGURE 1 is a graph of the % of residual tensile strength vs. time showing a comparison in resistance to hydrolytic degradation between a commercial monofilament and the monofilament according to the invention.
Best Mode for Carrying Out the Invention Preferably, the polyester comprises polyethylene terephthalate.
In accordance with a preferred embodiment of the invention, the thermoplastic material is selected from the group consisting of polyurethanes and polyetherester block copolymers. In accordance with another preferred embodiment of the invention, the polyester stabilizer is selected from the group consisting of glycidyl ethers, carbodiimides, ketenimines, hydroxyl containing compounds, aziridines and isocyanates. The preferred thermoplastic material consists of poly { butylene terephthalate-co-(multibutyleneoxy)tere- phthalate } . This is a Dupont material known as HYTREL.
The optimum .amount of thermoplastic material to be added depends on the balance between the degree of abra- sion resistance required and the deterioration in the physical properties of the monofilament due to addition of the thermoplastic material. Amounts ranging from 1 percent to 30 percent of the compatible polymer may be used in the blend with 5 to 15 percent being the optimum for most applications.
The preferred polyester stabilizer consists of a polycarbodiimide known under the trademark STABAXOL.
Preferably, there is added about 0.1 to 5 percent by weight of said polyester stabilizer, more preferably about 1 to 2 percent by weight.
As stated above, the abrasion resistance can be improved by blending the polyester with optimum amounts of a compatible polymer which has superior abrasion resistance. Examples of compatible polymers with good abrasion resistance are polyurethanes produced by the reaction of methylene diphenyl isocyanate or tolylene diisocyanate with polyethylene adipate or phthalate or polyalkylene oxides. Elastomeric polyesters such as
polyether-ester block copolymers are also compatible with good abrasion resistance. An example of elastomeric polyester is the commercial product marketed under the trademark of HYTREL which is poly { butylene tere- phthalate-co-(multibutyleneoxy)terephthalate } . The polymers mentioned above have melt points considerably lower than those of the polyesters into which they are incorporated.
The hydrolytic stability of the polyester is improved by the addition of organic compounds such as carbodiimides which act as acid scavengers. The carboxyl end-groups in the polyester molecules catalyze chain- scission at the ester linkages, thereby degrading the physical properties of the product. Several organic compounds with groups capable of reacting with the COOH end-groups are known to the prior art and may be used as stabilizers for polyesters. Examples of such groups known to the prior art are gly- cidyl ether, carbodiimide, ketenimine, hydroxyl, aziri- dine and isocyanate. The stabilizer is normally incor¬ porated in the molten resin immediately after polymeri¬ zation or in the extruder during the fabrication process .
Other properties required of the stabilizer are good stability to high temperatures, a melting point below normal processing temperatures and lower diffusivity through the polymer. Polycarbodiimide such as those available commercially under the trademark of STABAXOL meet all those requirements and is used extensively with polyurethane and polyester products. However, since the polycarbodiimide is not readily soluble in molten polyesters, and since it has a low viscosity, it cannot be processed in a conventional single screw extruder without creating erratic flow and conveying in the feed section of the screw. Expensive modifications of the
extruder would be necessary in order to overcome the feed problems. An alternative to modifying the extruder is to compound the stabilizer in an appropriate carrier prior to incorporating into the polyester. The carrier for a compounded concentrate can be any thermoplastic material.
It is preferably to use a material having a low melt point to prevent thermal degradation of the stabilizer during compounding. It is also preferable to use a carrier that is compatible with the polyester. Poly- urethanes and elastomeric polyesters are the most suit¬ able carriers and this invention relates to their use in producing polyester monofilaments with low carboxyl con¬ tent.
The method of making a monofilament of low carboxly content for use in fabricating a paper machine dryer fabric having improved resistance to hydrolytic degrada¬ tion and abrasion according to the invention comprises: a) compounding a polyester stabilizer in a thermo¬ plastic material; b) incorporating the compounded material obtained in step a) with a polyester; and c) extruding the mixture obtained in step b) in a screw extruder so as to obtain a monofilament.
When used throughout the specification and claims, the term resistance to hydrolytic degradation means resistance to chemical degradation from the reaction of steam with the polyester. The chemical degradation results in a loss in strength of the monofilament fiber.
While there is thermal degradation at the dry end of the dryer machine, we are only concerned, in the present case, with the hydrolytic degradation at the initial stages of drying under the influence of steam.
TABLE 1, which is given below, is a summary of the
results obtained from the hydrolysis testing .
TABLE 1
Results of Hydrolysis Testing
Commercial Product Present Invention
Time, % Residual % Residual
Hours Lb/Strand Strength Lb/Strand Strength
0 18.47 100.0 17.46 100.0
24 18.27 98.9 17.09 97.9
48 17.84 96.6 16.99 97.3
72 17.63 95.4 16.65 95.4
96 17.30 93.7 — —
120 16.30 88.2 16.10 92.2
144 14.85 80.4 16.50 94.5
168 11.47 62.1 16.08 92.1
192 8.71 47.2 15.87 90.9
216 6.38 34.5 — —
240 4.73 25.6 14.38 82.4
264 12.68 72.6
288 10.39 59.5
312 7.72 44.2
TABLE 2, hich is given below, shows the results of abrasion tests conducted on the same monofilaments.
OMP
TABLE 2
Results of Abrasion Testing
Relative i-ibrasion Sample Condition Resistance (RAR)*
Before Hydrolysis 1.493
After 120 hrs. of Hydrolysis 1.695
After 192 hrs. of Hydrolysis 2.130
*RAR = % Weight Loss of Commercial Product % Weight oss of Present Invention
The tests leading to the' results of FIGURE 1 and TABLE 1 were carried out as follows:
Several five-foot lengths of the monofilaments were wound into 2" coils, mounted on a wire rack and auto- claved at 250°F and 15 Psig steam pressure. The autoc- lave was sampled every 24 hours. After conditioning the steam treated coils at 80°F and 50% R.H., they were uncoiled and tested for breaking strength on an Ihstron Universal Tensile Tester. Each data point in TABLE 1 and FIGURE 1 represents the average from several breaks. The tests leading to the results of TABLE 2 were carried out as follows:
Monofilaments to be tested were wrapped around a tared polyethylene rod and reweighed to obtain the weight of monofilament used in the test. The rod with the mono- filament was spun in a sand slurry for 40 minutes . The
sa ple was then removed, dried and reweighed to determine the weight loss.
As it appears in the graph and tabulations, it is obvious that the monofilaments according to the invention is more satisfactory than the commercial filament as its properties will be retained longer in an atmosphere of simultaneous abrasion and hydrolysis.
OMPI
Claims (22)
1. A monofilament of low carboxyl content for use in fabricating a paper machine dryer fabric having improved resistance to hydrolytic degradation and abra-
5 sion, said monofilament comprising: a) a polyester; b) a polyester stabilizer; and c) a thermoplastic material.
2. A monofilament according to Claim 1, wherein 10 said polyester comprises polyethylene terephthalate.
3. A monofilament according to Claim 1, wherein said thermoplastic material is selected from the group consisting of polyurethanes and polyether-ester block copolymers.
15 4. A monofilament according to Claim 1, wherein said polyester stabilizer is selected from the group consisting of glycidyl ethers, carbodiimides, keten- imines, hydroxyl containing compounds, aziridines and isocyanates.
20 5. A monofilament according to Claim 3, wherein said thermosplastic material consists of poly { butylene terephthalate-co-(multibutyleneoxy) terephthalate } .
6. A monofilament according to Claims 1, 3, or 5, comprising about 1 to 30 percent by weight of said ther-
25 moplastic material.
7. A monofilament according to Claims 1, 3 or 5, comprising about 5 to 15 percent by weight of said ther¬ moplastic material.
8. A monofilament according to Claim 4, wherein
30 said polyester stabilizer consists of a polycarbodiimide known under the trademark STABAXOL.
9. A monofilament according to Claims 1, 4 or 8, comprising about 0.1 to 5 percent by weight of said poly¬ ester stabilizer.
10. A monofilament according to Claims 1, 4 or 8, comprising about 1 to 2 percent by weight of said poly¬ ester stabilizer.
11. A method of making a monofilament of low car¬ boxyl content or use in fabricating a paper machine dryer fabric having improved resistance to hydrolytic degrada- tion and abrasion which comprises: a) compounding a polyester stabilizer in a thermo¬ plastic material; b) incorporating the compounded material obtained in step a) with a polyester; and c) extruding the blend obtained in step b) in a screw extruder so as to obtain a monofilament.'
12. A method according to Claim 11, wherein said polyester comprises polyethylene terephthalate.
13. A method according to Claim 11 wherein said thermoplastic material is selected from the group con¬ sisting of polyurethanes and polyether-ester block copolymers.
14. A method according to Claim 11, wherein said polyester stabilizer is selected from the group consist- ing of glycidyl ethers, carbodiimides, ketenimines, hydroxyl containing compounds, aziridines and isocyanates.
15. A method according to Claim 13, wherein said thermoplastic material consists of poly { butylene tere- phthalate-co-(multibutyleneoxy) terephthalate } .
16. A method according to Claims 11, 13 or 15, comprising about 1 to 30 percent by weight of said ther-
OMPI * moplastic material.
17. A method according to Claims 11, 13 or 15, comprising about 5 to 15 percent by weight of said ther¬ moplastic material.
18. A method according to Claim 14, wherein said polyester stabilizer consists of a polycarbodiimide known under the trademark STABAXOL.
19. A method according to Claims 11, 14 or 18, comprising about 0.1 to 5 percent by weight of said poly- ester stabilizer.
20. A method according to Claims 11, 14 or 18, comprising about 1 to 2 percent by weight of said poly¬ ester stabilizer.
21. Monofilaments of low carboxyl content for use in fabricating a paper machine dryer fabric having improved resistance to hydrolytic degradation and abra¬ sion, obtained by the method of Claim 11.
22. A composition suitable for making monofilaments of low carboxyl content and improved resistance to hydrolytic degradation and abrasion which comprises: a) a polyester; b) a polyester stabilizer; and c) a thermoplastic material.
-£UR£A
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US31027881A | 1981-10-09 | 1981-10-09 | |
| US310278 | 1981-10-09 | ||
| PCT/US1982/001465 WO1983001253A1 (en) | 1981-10-09 | 1982-10-12 | Monofilaments of low carboxyl content for use in fabricating a paper machine dryer fabric |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| AU1040283A true AU1040283A (en) | 1983-04-27 |
Family
ID=23201772
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AU10402/83A Abandoned AU1040283A (en) | 1981-10-09 | 1982-10-12 | Monofilaments of low carboxyl content for use in fabricating a paper machine dryer fabric |
Country Status (9)
| Country | Link |
|---|---|
| EP (1) | EP0090862A4 (en) |
| JP (1) | JPS59500373A (en) |
| AU (1) | AU1040283A (en) |
| DE (1) | DE3249110T1 (en) |
| GB (1) | GB2123839A (en) |
| IT (1) | IT1148619B (en) |
| NL (1) | NL8220462A (en) |
| SE (1) | SE8303240D0 (en) |
| WO (1) | WO1983001253A1 (en) |
Families Citing this family (25)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5006162A (en) * | 1982-03-25 | 1991-04-09 | Ici Americas Inc. | Certain 2-(2-substituted benzoyl)-1,3,5-cyclohexanetriones |
| JPS60210659A (en) * | 1984-04-04 | 1985-10-23 | Polyplastics Co | Polyester composition having excellent resistance to boiling water |
| JPS616390A (en) * | 1984-05-01 | 1986-01-13 | ジエイダブリユ−アイ・リミテツド | Cloth for dryer having yarn strand prepared from melt extrudable polyphenylene sulfide |
| NL8700617A (en) * | 1987-03-16 | 1988-10-17 | Akzo Nv | PROCESS FOR MANUFACTURING YARNS BY MELTING SPINNING POLYETHYLENE TERPHALATE |
| US5502120A (en) * | 1988-08-05 | 1996-03-26 | Jwi Ltd. | Melt-extruded monofilament comprised of a blend of polyethylene terephthalate and a thermoplastic polyurethane |
| US5169711A (en) * | 1988-08-05 | 1992-12-08 | Jwi Ltd. | Paper makers forming fabric |
| ES2064400T5 (en) * | 1989-03-17 | 2001-03-01 | Jwi Ltd | POLYESTER FORMATION FABRIC MODIFIED BY STABILIZED POLYURETHANE. |
| DE69031037T3 (en) * | 1989-04-24 | 2008-05-21 | Albany International Corp. | papermaker |
| DE3930845A1 (en) * | 1989-09-15 | 1991-03-28 | Hoechst Ag | POLYESTER FIBERS MODIFIED WITH CARBODIIMIDES AND METHOD FOR THEIR PRODUCTION |
| JP3228977B2 (en) * | 1991-03-14 | 2001-11-12 | ジョーンズ・マンヴィル・インターナショナル・インコーポレーテッド | Carbodiimide-modified polyester fiber and method for producing the same |
| DE4307392C2 (en) * | 1993-03-10 | 2001-03-29 | Klaus Bloch | Monofilament with increased hydrolysis resistance based on polyester for use in technical fabrics and processes for its manufacture |
| JP3110633B2 (en) * | 1994-02-02 | 2000-11-20 | 東レ株式会社 | Polyester compositions, monofilaments and industrial textiles |
| DE4410399A1 (en) * | 1994-03-25 | 1995-09-28 | Hoechst Ag | Abrasion-resistant polyester blend with increased processing safety, monofilaments made of it and their production and use |
| DE19511852A1 (en) * | 1995-03-31 | 1996-10-02 | Hoechst Trevira Gmbh & Co Kg | Heavy-duty core / sheath monofilaments for technical applications |
| DE19511853A1 (en) * | 1995-03-31 | 1996-10-02 | Hoechst Trevira Gmbh & Co Kg | Heavy-duty core / sheath monofilaments for technical applications |
| DE19547028A1 (en) * | 1995-12-15 | 1997-07-17 | Hoechst Trevira Gmbh & Co Kg | Hydrolysis-resistant polyester fibers and filaments, masterbatches and processes for the production of polyester fibers and filaments |
| US5763538A (en) * | 1996-10-28 | 1998-06-09 | E. I. Du Pont De Nemours And Company | Process for making an oriented polyester article having improved hydrolytic stability |
| US6147128A (en) * | 1998-05-14 | 2000-11-14 | Astenjohnson, Inc. | Industrial fabric and yarn made from recycled polyester |
| DE19834008C2 (en) * | 1998-07-29 | 2000-11-30 | Johns Manville Int Inc | Monofilament bicomponent threads of the core sheath type, process for their production and their use |
| US6589392B1 (en) * | 2001-10-18 | 2003-07-08 | Shakespeare Company Llc | Multicomponent monofilament for papermaking forming fabric |
| WO2007089747A1 (en) | 2006-01-27 | 2007-08-09 | General Electric Company | Articles derived from compositions containing modified polybutylene terephthalate (pbt) random copolymers derived from polyethylene terephthalate (pet) |
| JP2009525358A (en) | 2006-01-27 | 2009-07-09 | ゼネラル・エレクトリック・カンパニイ | Molding composition comprising polyalkylene terephthalate and modified polybutylene terephthalate (PBT) derived from PET |
| US7799838B2 (en) | 2006-07-26 | 2010-09-21 | Sabic Innovative Plastics Ip B.V. | Elastomer blends of polyesters and copolyetheresters derived from polyethylene terephthalate, method of manufacture, and articles therefrom |
| US8309656B2 (en) | 2006-07-26 | 2012-11-13 | Sabic Innovative Plastics Ip B.V. | Elastomer blends containing polycarbonates and copolyetheresters derived from polyethylene terephthalate, method of manufacture, and articles therefrom |
| US8158710B2 (en) | 2006-11-27 | 2012-04-17 | Sabic Innovative Plastics Ip B.V. | Polyester blends, methods of making, and articles formed therefrom |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3652713A (en) * | 1969-02-18 | 1972-03-28 | Toray Industries | Polyester composition having improved antistatic properties and process for the preparation thereof |
| US3652714A (en) * | 1970-02-20 | 1972-03-28 | Phillips Petroleum Co | Dyeable blends of poly(ethylene terephthalate) and polyesterether polymers |
| US3904706A (en) * | 1973-03-15 | 1975-09-09 | Du Pont | Stabilization of polymers containing poly(alkylene oxide) units |
| US4156702A (en) * | 1973-10-29 | 1979-05-29 | E. I. Du Pont De Nemours And Company | Adhesion promoted block copolyester composition with multi-functional carboxylic compound |
| US4167541A (en) * | 1977-05-12 | 1979-09-11 | Fiber Industries, Inc. | Continuous carrierless dyeable polyesters |
| AU502933B2 (en) * | 1978-02-02 | 1979-08-16 | The Goodyear Tire & Rubber Company | Screen for papermaking apparatus |
-
1982
- 1982-10-11 IT IT49252/82A patent/IT1148619B/en active
- 1982-10-12 GB GB08315841A patent/GB2123839A/en not_active Withdrawn
- 1982-10-12 WO PCT/US1982/001465 patent/WO1983001253A1/en not_active Application Discontinuation
- 1982-10-12 DE DE19823249110 patent/DE3249110T1/en not_active Withdrawn
- 1982-10-12 EP EP19830900675 patent/EP0090862A4/en not_active Withdrawn
- 1982-10-12 AU AU10402/83A patent/AU1040283A/en not_active Abandoned
- 1982-10-12 NL NL8220462A patent/NL8220462A/en unknown
- 1982-10-12 JP JP58500145A patent/JPS59500373A/en active Pending
-
1983
- 1983-06-08 SE SE8303240A patent/SE8303240D0/en not_active Application Discontinuation
Also Published As
| Publication number | Publication date |
|---|---|
| GB2123839A (en) | 1984-02-08 |
| IT8249252A0 (en) | 1982-10-11 |
| GB8315841D0 (en) | 1983-07-13 |
| EP0090862A4 (en) | 1984-01-12 |
| IT1148619B (en) | 1986-12-03 |
| DE3249110T1 (en) | 1984-04-19 |
| SE8303240L (en) | 1983-06-08 |
| JPS59500373A (en) | 1984-03-08 |
| WO1983001253A1 (en) | 1983-04-14 |
| SE8303240D0 (en) | 1983-06-08 |
| NL8220462A (en) | 1983-09-01 |
| EP0090862A1 (en) | 1983-10-12 |
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