WO2009158293A2 - Method of making monofilament fishing lines of high tenacity polyolefin fibers - Google Patents
Method of making monofilament fishing lines of high tenacity polyolefin fibers Download PDFInfo
- Publication number
- WO2009158293A2 WO2009158293A2 PCT/US2009/048078 US2009048078W WO2009158293A2 WO 2009158293 A2 WO2009158293 A2 WO 2009158293A2 US 2009048078 W US2009048078 W US 2009048078W WO 2009158293 A2 WO2009158293 A2 WO 2009158293A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- yarn
- multifilament
- molecular weight
- yarns
- fishing line
- Prior art date
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Classifications
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06P—DYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
- D06P3/00—Special processes of dyeing or printing textiles, or dyeing leather, furs, or solid macromolecular substances in any form, classified according to the material treated
- D06P3/79—Polyolefins
-
- D—TEXTILES; PAPER
- D02—YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
- D02G—CRIMPING OR CURLING FIBRES, FILAMENTS, THREADS, OR YARNS; YARNS OR THREADS
- D02G3/00—Yarns or threads, e.g. fancy yarns; Processes or apparatus for the production thereof, not otherwise provided for
- D02G3/02—Yarns or threads characterised by the material or by the materials from which they are made
-
- 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
- D01F6/44—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds as major constituent with other polymers or low-molecular-weight compounds
- D01F6/46—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds as major constituent with other polymers or low-molecular-weight compounds of polyolefins
-
- D—TEXTILES; PAPER
- D02—YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
- D02G—CRIMPING OR CURLING FIBRES, FILAMENTS, THREADS, OR YARNS; YARNS OR THREADS
- D02G3/00—Yarns or threads, e.g. fancy yarns; Processes or apparatus for the production thereof, not otherwise provided for
- D02G3/22—Yarns or threads characterised by constructional features, e.g. blending, filament/fibre
- D02G3/36—Cored or coated yarns or threads
-
- D—TEXTILES; PAPER
- D02—YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
- D02G—CRIMPING OR CURLING FIBRES, FILAMENTS, THREADS, OR YARNS; YARNS OR THREADS
- D02G3/00—Yarns or threads, e.g. fancy yarns; Processes or apparatus for the production thereof, not otherwise provided for
- D02G3/22—Yarns or threads characterised by constructional features, e.g. blending, filament/fibre
- D02G3/40—Yarns in which fibres are united by adhesives; Impregnated yarns or threads
- D02G3/404—Yarns or threads coated with polymeric solutions
-
- D—TEXTILES; PAPER
- D02—YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
- D02G—CRIMPING OR CURLING FIBRES, FILAMENTS, THREADS, OR YARNS; YARNS OR THREADS
- D02G3/00—Yarns or threads, e.g. fancy yarns; Processes or apparatus for the production thereof, not otherwise provided for
- D02G3/44—Yarns or threads characterised by the purpose for which they are designed
- D02G3/444—Yarns or threads for use in sports applications
-
- D—TEXTILES; PAPER
- D02—YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
- D02J—FINISHING OR DRESSING OF FILAMENTS, YARNS, THREADS, CORDS, ROPES OR THE LIKE
- D02J1/00—Modifying the structure or properties resulting from a particular structure; Modifying, retaining, or restoring the physical form or cross-sectional shape, e.g. by use of dies or squeeze rollers
- D02J1/22—Stretching or tensioning, shrinking or relaxing, e.g. by use of overfeed and underfeed apparatus, or preventing stretch
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06P—DYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
- D06P1/00—General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed
- D06P1/14—General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed using phthalocyanine dyes without vatting
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06P—DYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
- D06P1/00—General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed
- D06P1/44—General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed using insoluble pigments or auxiliary substances, e.g. binders
- D06P1/52—General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed using insoluble pigments or auxiliary substances, e.g. binders using compositions containing synthetic macromolecular substances
- D06P1/5207—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds
- D06P1/5214—Polymers of unsaturated compounds containing no COOH groups or functional derivatives thereof
- D06P1/5221—Polymers of unsaturated hydrocarbons, e.g. polystyrene polyalkylene
-
- D—TEXTILES; PAPER
- D10—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B2321/00—Fibres made from polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D10B2321/02—Fibres made from polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds polyolefins
- D10B2321/021—Fibres made from polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds polyolefins polyethylene
- D10B2321/0211—Fibres made from polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds polyolefins polyethylene high-strength or high-molecular-weight polyethylene, e.g. ultra-high molecular weight polyethylene [UHMWPE]
Definitions
- This invention relates to improvements in fishing lines formed from high tenacity polyolefin fibers.
- This patent suggests forming braided or twisted yarns and then heating the yarns so that they fuse together. Certain coating materials are suggested to aid in the fusing of the multifilament yarns.
- the yarns are also subject to a drawing step, with draw ratios of between 1.01 and 2.5 being disclosed.
- the feeder yarn is a relatively low tenacity, heavy denier yarn.
- the colorant is introduced in a carrier of a thermoplastic resin. This invention thus provides colored fishing line from ultrahigh molecular weight polyolefins that have the feel of monofilament lines and in which the color resists abrading off and fading.
- the multifilament yarns used herein are formed from high tenacity polyolefin filaments.
- high tenacity fibers or filaments means fibers or filaments which have tenacities equal to or greater than about 7 g/d.
- these fibers have initial tensile moduli of at least about 150 g/d and energies-to-break of at least about 8 J/g as measured by ASTM D2256.
- initial tensile modulus means the modulus of elasticity as measured by ASTM 2256 for a yarn.
- a filament is an elongate body the length dimension of which is much greater that the transverse dimensions of width and thickness. Accordingly, the term filament includes fiber, ribbon, strip, staple and other forms of chopped, cut or discontinuous fiber or continuous fiber.
- the term "fiber” or “filament” includes a plurality of any of the foregoing or a combination thereof.
- a yarn is a continuous strand comprised of many fibers or filaments. Preferred are continuous multifilament yarns.
- the high tenacity fibers have tenacities equal to or greater than about 10 g/d, more preferably equal to or greater than about 15 g/d, even more preferably equal to or greater than about 20 g/d, and most preferably equal to or greater than about 25 g/d.
- U.S. Patent 4,457,985 generally discusses such high molecular weight polyethylene and polypropylene fibers, and the disclosure of this patent is hereby incorporated by reference to the extent that it is not inconsistent herewith.
- suitable fibers are those of weight average molecular weight of at least about 150,000, preferably at least about one million and more preferably between about two million and about five million.
- Such high molecular weight polyethylene fibers may be spun in solution (see U.S. Patent 4,137,394 and U.S. Patent 4,356,138), or a filament spun from a solution to form a gel structure (see U.S. Patent 4,413,1 10, German Off. No.
- High tenacity polyethylene multifilament yarns are preferred, and these are available, for example, under the trademark SPECTRA® fibers and yarns from Honeywell International Inc. of Morristown, New Jersey, U.S.A Depending upon the formation technique, the draw ratio and temperatures, and other conditions, a variety of properties can be imparted to these precursor fibers.
- the tenacity of the polyethylene fibers are at least about 7 g/d, preferably at least about 15 g/d, more preferably at least about 20 g/d, still more preferably at least about 25 g/d and most preferably at least about 30 g/d.
- the initial tensile modulus of the fibers is preferably at least about 300 g/d, more preferably at least about 500 g/d, still more preferably at least about 1 ,000 g/d and most preferably at least about 1 ,200 g/d.
- These highest values for initial tensile modulus and tenacity are generally obtainable only by employing solution grown or gel spinning processes.
- Many of the filaments have melting points higher than the melting point of the polymer from which they were formed.
- high molecular weight polyethylene of about 150,000, about one million and about two million molecular weight generally have melting points in the bulk of 138 0 C.
- the highly oriented polyethylene filaments made of these materials have melting points of from about 7 0 C to about 13 0 C higher.
- a slight increase in melting point reflects the crystalline perfection and higher crystalline orientation of the filaments as compared to the bulk polymer.
- the polyethylene employed is a polyethylene having fewer than about one methyl group per thousand carbon atoms, more preferably fewer than about 0.5 methyl groups per thousand carbon atoms, and less than about 1 wt. % of other constituents.
- polypropylene fibers of weight average molecular weight at least about 200,000, preferably at least about one million and more preferably at least about two million may be used.
- extended chain polypropylene may be formed into reasonably well oriented filaments by the techniques prescribed in the various references referred to above, and especially by the technique of U.S. Patent 4,413,1 10. Since polypropylene is a much less crystalline material than polyethylene and contains pendant methyl groups, tenacity values achievable with polypropylene are generally substantially lower than the corresponding values for polyethylene. Accordingly, a suitable tenacity is preferably at least about 8 g/d, more preferably at least about 11 g/d.
- the initial tensile modulus for polypropylene is preferably at least about 160 g/d, more preferably at least about 200 g/d.
- the melting point of the polypropylene is generally raised several degrees by the orientation process, such that the polypropylene filament preferably has a main melting point of at least 168 0 C, more preferably at least 17O 0 C.
- the particularly preferred ranges for the above described parameters can advantageously provide improved performance in the final article.
- Employing fibers having a weight average molecular weight of at least about 200,000 coupled with the preferred ranges for the above-described parameters (modulus and tenacity) can provide advantageously improved performance in the final article.
- the fishing lines of this invention comprise the high tenacity polyolefin fibers, or consist essentially of the high tenacity polyolefin fibers, or consist of the high tenacity polyolefin fibers, and the polyolefin fibers preferably are high tenacity polyethylene fibers.
- the multifilament yarns may be formed by any suitable technique, including melt extrusion.
- the multifilament yarns are preferably aligned in a substantially uniaxial direction along the length of the line.
- substantially uniaxial direction is meant that all or almost all (for example, at least about 95%, more preferably at least about 99%) of the yarns extend in a single direction.
- the multifilament feeder yarns are substantially untwisted.
- the yarns of the high tenacity fibers used herein may be of any suitable denier, such as, for example, about 100 to about 10,000 denier, more preferably from about 1000 to about 8,000 denier, still more preferably from about 650 to about 6000 denier, and most preferably from about 1200 to about 4800 denier.
- the number of filaments forming the multifilament feeder yarns used in this invention may vary widely depending on the desired properties.
- the number of filaments in a yarn may range from about 10 to about 3000, more preferably from about 30 to about 1500, and most preferably from about 60 to about 1200.
- the number of filaments in each multifilament precursor yarn preferably is substantially the same.
- the number of multifilament yarns or tows forming the fishing line of this invention may vary widely.
- the number of multifilament yarns may range from about 1 to about 16, more preferably from about 1 to about 8.
- the substantially untwisted multifilament yarn or yarns are coated with a colorant prior to twisting.
- Any suitable coating technique may be employed.
- coating apparatus that are useful in the method of this invention include, without limitation: lube rolls, kiss rolls, dip baths, spray coaters, etc.
- extrusion coaters may be employed.
- the colorant is preferably supplied in a carrier and may be in the form of a solution, dispersion or an emulsion using any suitable solvent, such as water or an organic solvent (such as methyl ethyl ketone, acetone, ethanol, methanol, isopropyl alcohol, cyclohexane, ethyl acetone, etc. and combinations thereof).
- the colorant is preferably applied as a continuous coating, although a discontinuous coating may be employed if desired.
- the yarn or yarns are dipped into a bath containing the colorant coating composition.
- excess coating composition may be removed by any one or more suitable means, such as being squeezed out, blown off or drained off, or air dried or dried in a heating device.
- any suitable coloring agent may be employed.
- Examples are dyes and pigments, both aqueous and organic.
- Non-limiting examples of such colorants are copper phthalocyanine and the like.
- the preferred colors are blue, green, yellow and black.
- the colorant is preferably carried in a carrier material.
- a carrier material is preferably a thermoplastic resin.
- thermoplastic resins include, without limitation, polyolefin resins such as low density polyethylene, linear low density polyethylene, polyolefin copolymers, e.g., ethylene copolymers such as ethylene-acrylic acid copolymer, ethylene- ethyl acrylate copolymer, ethylene-vinyl acetate copolymer, and the like, and blends of one or more of the foregoing.
- the thermoplastic resin preferably has a lower melting point than the specific polyolefin fiber that is utilized, and is a drawable material.
- the amount of the colored coating on the yarns may vary widely.
- the coating may comprise from about 1 to about 40 percent by weight of the total weight of the yarns after drying, more preferably from about 2 to about 25 percent by weight, and most preferably from about 5 to about 15 percent by weight.
- the weight of the colorant in the coating material may be significantly less than the weight of the colored coating.
- the amount of colorant in the colored coating may range from about 0.5 to about 20 weight percent, more preferably from about 2 to about 15 weight percent, and most preferably from about 4 to about 10 weight percent.
- any suitable twisting device may be employed for this purpose, such as a ring twister, a direct cabler, and the like.
- the yarns are imparted with a minimum twist of about 2 turns per inch (79 turns per meter). More preferably, the yarn or yarns are twisted to a relatively high degree, such as from about 3 to about 15 turns per inch (1 18 to 590 turns per meter), more preferably from about 4 to about 11 turns per inch (157 to 433 turns per meter), and most preferably from about 5 to about 7 turns per inch (197 to 276 turns per meter).
- Two or more multifilament yarn ends may be twisted together and then further processed, or each multifilament yarn end may be twisted and then two or more of the twisted yarn ends can be cabled together for further processing.
- the yarns may be twisted first in a "z" direction a suitable number of times and then in the opposite "s" direction a desired number of times to obtain a balanced cable yarn, or vice versa.
- the colored coated and twisted multifilament yarn or yarns are then subjected to a drawing step at an elevated temperature.
- the drawing step may be a single drawing step or multiple drawing steps.
- the yarns are drawn in a hot air oven.
- Such ovens are known in the art, and an example of such an oven is described in U.S. Patent 7,370,395, the disclosure of which is hereby incorporated by reference to the extent that it is not inconsistent herewith.
- Drawing of the multifilament yarn or yarns is preferably conducted within the melting point range of the polyolefin.
- Drawing is desirably achieved by one or more stretch rollers that desirably may be outside of the ovens, or alternatively inside or between one or more ovens.
- One oven or the first part of one oven may be employed to soften the filaments and another oven or another party of an oven may be employed to fuse the filaments together into a line.
- the multifilament yarn or yarns are heated to a relatively high temperature, such as from about 135 to about 160°C, more preferably from about 152 to about 157°C, and most preferably from about 153 to about 155°C.
- a relatively high temperature such as from about 135 to about 160°C, more preferably from about 152 to about 157°C, and most preferably from about 153 to about 155°C.
- the multifilament yarns are drawn (or stretched) to a desired degree. Any desired stretch ratio may be employed, typically at least about 2, such as from about 2 to about 10, more preferably from about 3 to about 8, and most preferably from about 4 to about 6.
- line tension is applied throughout the drawing step.
- the yarn or yarns are heated and drawn for a desired period of time.
- the actual dwell time in a heating apparatus depends on several factors, such as the temperature of the oven, the length of the oven, the type of oven (e.g., hot air circulating oven, heated bath, etc.), etc.
- the conditions of heat and drawing are chosen such that the adjacent filaments of a multifilament yarn are at least partially fused together. It is believed that the outer surface temperature of the filaments are at or within the melting range of the polymer constituting the filaments such that the surfaces of the filaments begin to soften and fuse at contact points along the length of the outer surfaces of the filaments.
- the colored coating penetrates the polyolefin fiber and thus becomes an integral part thereof.
- the heating and drawing step transforms the multifilament yarn or yarns into monofilament line, with the multifilament yarn being fused together at least to some degree.
- the resultant line is a monofilament or is substantially a monofilament (monofilament-like) has the feel of a monofilament fishing line. However, in contrast to braided yarns it does not unravel when cut.
- the term "monofilament” means monofilament or monofilament-like.
- the feeder yarn is a relatively heavy denier, low tenacity yarn whereas the monofilament after drawing has a relatively low denier and high tenacity.
- the resulting fishing line may be of any suitable diameter.
- the monofilament fishing line may have a diameter of from about 0.001 mm to about 3 mm, more preferably from about 0.1 mm to about 1 mm, and most preferably from about 0.15 mm to about 0.5 mm.
- fishing line formed from such yarns exhibits increased color-fastness.
- the fishing line is resistant to fading due to exposure to sunlight (UV light) as well as due to rubbing or other abrasion action.
- the resulting fishing line exhibits improved abrasion resistance.
- a fishing line is formed from multifilament extended chain polyethylene yarns.
- Each yarn is formed from SPECTRA® 900 fibers, available from Honeywell International Inc.
- the yarns have a denier of 1200, with 120 filaments in each yarn.
- the yarn tenacity is 30 g/d.
- One multifilament yarn having essentially zero twist is fed into a coating bath containing an aqueous solution of green dye pigment, based on copper phthalocyanine, dispersed in a polyethylene thermoplastic resin.
- the solids content of the coating solution is about 40 weight percent.
- the pick up weight of the coating onto the yarns is about 15 percent, based on the total weight of the multifilament yarns.
- the yarns are dried in a hot air oven (temperature of about 80 to about 110 0 C).
- the yarns are then given a twist of 11 turns per inch (433 turns per meter). Tension is maintained in the process to prevent untwisting of the yarns.
- the twisted yarns are fed into a heating apparatus as disclosed in the aforementioned U.S. Patent 7,370,395, using a total of 6 horizontally aligned and abutting hot air circulating ovens.
- a first set of rolls is adjacent the inlet side of the ovens and a second set of rolls are adjacent the outlet side of the ovens.
- the yarns are unsupported in the ovens and are transported through the ovens in an approximate straight line.
- the speeds of the first and second set of rolls are selected to provide a draw ratio in the ovens of about 4.0.
- the oven temperature is about 155°C.
- the multifilament yarns are fused in the ovens, with adjacent yarns being at least partially fused together.
- the resulting structure is wound up on a take off roll and is in the form of a monofilament-like fishing line.
- the color-fastness of the fishing line is tested by abrading it against a metal bar with hexagonal cross-section (the Hex Bar abrasion resistance test).
- the monofilament fishing line is tensioned with a 50 gram weight, and abraded back and forth over the hexagonal metal bar with "shoe-shining" like action for 2,500 cycles.
- the fishing line is then examined for retained color and residual breaking strength.
- the monofilament fishing line retains its vibrant color and the coating also provides added abrasion resistance, such that the fishing line retains about 50 to 80 percent of its original breaking strength.
- Fishing line is prepared in a manner similar to Example 1 , with the colored coating being applied after the yarn has been twisted, and fused and drawn.
- the color fishing line is tested for color-fastness and abrasion resistance via the same Hex Bar test. After 2,500 cycles, the color coating is found to have been mostly abraded from the line.
- the fishing line retains only about 20 to 40 percent of its original breaking strength.
Abstract
Description
Claims
Priority Applications (9)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA2728670A CA2728670A1 (en) | 2008-06-25 | 2009-06-22 | Method of making monofilament fishing lines of high tenacity polyolefin fibers |
CN2009801240743A CN102076894B (en) | 2008-06-25 | 2009-06-22 | Method of making monofilament fishing lines of high tenacity polyolefin fibers |
EP09770827.5A EP2291557B1 (en) | 2008-06-25 | 2009-06-22 | Method of making monofilament fishing lines of high tenacity polyolefin fibers |
JP2011516484A JP5238075B2 (en) | 2008-06-25 | 2009-06-22 | Production method of monofilament fishing line of high tenacity polyolefin fiber |
RU2011101655/05A RU2506355C2 (en) | 2008-06-25 | 2009-06-22 | Method of production of coloured single-core line of ultra-high molecular polyolefin and line made by this method |
BRPI0915005A BRPI0915005A2 (en) | 2008-06-25 | 2009-06-22 | method of producing high molecular weight polyolefin monofilament fishing line and very high molecular weight polyolefin monofilament fishing line |
ES09770827.5T ES2583255T3 (en) | 2008-06-25 | 2009-06-22 | Method for obtaining monofilament fishing lines of high tenacity polyolefin fibers |
MX2010013795A MX2010013795A (en) | 2008-06-25 | 2009-06-22 | Method of making monofilament fishing lines of high tenacity polyolefin fibers. |
IL209812A IL209812A0 (en) | 2008-06-25 | 2010-12-07 | Method of making monofilament fishing lines of high tenacity polyolefin fibers |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US12/215,135 | 2008-06-25 | ||
US12/215,135 US7966797B2 (en) | 2008-06-25 | 2008-06-25 | Method of making monofilament fishing lines of high tenacity polyolefin fibers |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2009158293A2 true WO2009158293A2 (en) | 2009-12-30 |
WO2009158293A3 WO2009158293A3 (en) | 2010-03-25 |
Family
ID=41445245
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US2009/048078 WO2009158293A2 (en) | 2008-06-25 | 2009-06-22 | Method of making monofilament fishing lines of high tenacity polyolefin fibers |
Country Status (12)
Country | Link |
---|---|
US (1) | US7966797B2 (en) |
EP (1) | EP2291557B1 (en) |
JP (1) | JP5238075B2 (en) |
KR (1) | KR20110033213A (en) |
CN (1) | CN102076894B (en) |
BR (1) | BRPI0915005A2 (en) |
CA (1) | CA2728670A1 (en) |
ES (1) | ES2583255T3 (en) |
IL (1) | IL209812A0 (en) |
MX (1) | MX2010013795A (en) |
RU (1) | RU2506355C2 (en) |
WO (1) | WO2009158293A2 (en) |
Cited By (1)
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EP3051010A1 (en) * | 2013-01-25 | 2016-08-03 | DSM IP Assets B.V. | Method of manufacturing a drawn multifilament yarn |
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US8658244B2 (en) * | 2008-06-25 | 2014-02-25 | Honeywell International Inc. | Method of making colored multifilament high tenacity polyolefin yarns |
US8474237B2 (en) * | 2008-06-25 | 2013-07-02 | Honeywell International | Colored lines and methods of making colored lines |
US7964518B1 (en) | 2010-04-19 | 2011-06-21 | Honeywell International Inc. | Enhanced ballistic performance of polymer fibers |
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JP2015507704A (en) * | 2011-12-14 | 2015-03-12 | ディーエスエム アイピー アセッツ ビー.ブイ. | Ultra high molecular weight polyethylene multifilament yarn |
JP6408988B2 (en) | 2012-08-06 | 2018-10-17 | ハネウェル・インターナショナル・インコーポレーテッドHoneywell International Inc. | Multi-directional fiber reinforced tape / film article and manufacturing method thereof |
US9834872B2 (en) | 2014-10-29 | 2017-12-05 | Honeywell International Inc. | High strength small diameter fishing line |
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- 2009-06-22 WO PCT/US2009/048078 patent/WO2009158293A2/en active Application Filing
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- 2009-06-22 ES ES09770827.5T patent/ES2583255T3/en active Active
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- 2009-06-22 MX MX2010013795A patent/MX2010013795A/en not_active Application Discontinuation
- 2009-06-22 BR BRPI0915005A patent/BRPI0915005A2/en not_active IP Right Cessation
- 2009-06-22 JP JP2011516484A patent/JP5238075B2/en not_active Expired - Fee Related
- 2009-06-22 KR KR1020117001221A patent/KR20110033213A/en not_active Application Discontinuation
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2010
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Also Published As
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MX2010013795A (en) | 2011-01-21 |
US7966797B2 (en) | 2011-06-28 |
CA2728670A1 (en) | 2009-12-30 |
CN102076894A (en) | 2011-05-25 |
JP5238075B2 (en) | 2013-07-17 |
CN102076894B (en) | 2013-02-06 |
JP2011525947A (en) | 2011-09-29 |
EP2291557B1 (en) | 2016-04-20 |
EP2291557A2 (en) | 2011-03-09 |
RU2506355C2 (en) | 2014-02-10 |
IL209812A0 (en) | 2011-02-28 |
US20090321976A1 (en) | 2009-12-31 |
BRPI0915005A2 (en) | 2015-10-27 |
ES2583255T3 (en) | 2016-09-20 |
KR20110033213A (en) | 2011-03-30 |
WO2009158293A3 (en) | 2010-03-25 |
EP2291557A4 (en) | 2013-02-06 |
RU2011101655A (en) | 2012-07-27 |
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