Classifications

• • D—TEXTILES; PAPER
  • D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
  • D04H—MAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
  • D04H1/00—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
  • D04H1/40—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
  • D04H1/42—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties characterised by the use of certain kinds of fibres insofar as this use has no preponderant influence on the consolidation of the fleece
• • 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
  • D01F6/66—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyethers
• • 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
  • D01F6/78—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolycondensation products
  • D01F6/84—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolycondensation products from copolyesters
• • 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
  • D01F6/78—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolycondensation products
  • D01F6/86—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolycondensation products from polyetheresters
• • 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
  • D01F8/00—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof
  • D01F8/04—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers
  • D01F8/14—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers with at least one polyester as constituent
• • 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
  • D01F8/00—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof
  • D01F8/04—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers
  • D01F8/16—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers with at least one other macromolecular compound obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds as constituent
• • D—TEXTILES; PAPER
  • D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
  • D04H—MAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
  • D04H1/00—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
  • D04H1/40—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
  • D04H1/54—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties by welding together the fibres, e.g. by partially melting or dissolving

Definitions

• the present invention relates to thermoplastic fibers and fabrics.
• the present invention is a fiber comprising at least one thermoplastic hydroxy-functionalized polyether or polyester and, optionally, a thermoplastic polymer which is not a hydroxy-functionalized polyether or polyester.
• the present invention is a bicomponent fiber having (1) a first component comprising a thermoplastic hydroxy-functionalized polyether or polyester or a blend of hydroxy-functionalized polyether or polyester and (2) a second component comprising a thermoplastic polymer which is not a hydroxy-functionalized polyether or polyester.
• the present invention is a method of forming a non- woven fabric by forming a web of at least one fibrous component and heating the web to cause bonding of fibrous components of the web, characterized in that at least one fibrous component comprises a thermoplastic hydroxy-functionalized polyether or polyester.
• the fiber of the present invention can be a single component or a bicomponent fiber.
• the single component fiber comprises at least one thermoplastic hydroxy- functionalized polyether or polyester and, optionally, a thermoplastic polymer which is not a hydroxy-functionalized polyether or polyester.
• the bicomponent fiber of the present invention has (1) a first component comprising a thermoplastic hydroxy-functionalized polyether or polyester or a blend of hydroxy-functionalized polyether or polyester and (2) a second component comprising a thermoplastic polymer which is not a hydroxy-functionalized polyether or polyester.
• the thermoplastic hydroxy-functionalized polyethers or polyesters are prepared by the reaction of a dinucleophilic monomer with a diglycidyl ether, a diglycidyl ester or epihalohydrin.
• thermoplastic hydroxy-functionalized polyether or polyester is selected from :
• R is a divalent organic moiety which is primarily hydrocarbon
• R 2 is independently a divalent organic moiety which is primarily hydrocarbon
• R 3 is
• R 5 is hydrogen or alkyl
• R 6 is a divalent organic moiety which is primarily hydrocarbon
• R 7 and R 9 are independently alkyl, substituted alkyl, aryl, substituted aryl
• R 8 is a divalent organic moiety which is primarily hydrocarbon
• A is an amine moiety or a combination of different amine moieties
• B is a divalent organic moiety which is primarily hydrocarbon
• m is an integer from 5 to 1000
• n is an integer from 0 to 100.
• A is 2- hydroxyethylimino-, 2-hydroxypropyl-imino-, piperazenyl, N,N'-bis(2-hydroxyethyl)-1 ,2- ethylenediimino; and B and R 1 are independently 1 ,3-phenylene, 1 ,4-phenylene; sulfonyldiphenylene, oxydiphenylene, thiodiphenylene or isopropylidene-diphenylene; R 6 is hydrogen; R 7 and R 9 are independently methyl, ethyl, propyl, butyl, 2-hydroxyethyl or phenyl; and B and R 8 are independently 1 ,3-phenylene, 1 ,4-phenylene, sulfonyldiphenylene, oxydiphenylene, thiodiphenylene or isopropylidenediphenylene.
• the poly(hydroxy ester ethers) represented by Formula I are prepared by reacting diglycidyl esters of aliphatic or aromatic diacids, such as diglycidyl terephthalate, or diglycidyl ethers of dihydric phenols with aliphatic or aromatic diacids such as adipic acid or isophthalic acid. These polyesters are described in U.S. Patent 5,171 ,820.
• the poly(hydroxyester ethers) are prepared by reacting a diglycidyl ester with a bisphenol or by reacting a diglycidyl ester, diglycidyl ether, or an epihalohydrin with a dicarboxylic acid.
• the polyetheramines represented by Formula II also referred to as poly(hydroxy amino ethers) are prepared by contacting one or more of the diglycidyl ethers of a dihydric phenol with an amine having two amine hydrogens under conditions sufficient to cause the amine moieties to react with epoxy moieties to form a polymer backbone having amine linkages, ether linkages and pendant hydroxyl moieties.
• polyetheramines are described in U.S. Patent 5,275,853.
• the polyetheramines can also be prepared by contacting a diglycidyl ether or an epihalohydrin with a difunctional amine.
• the hydroxy-functionalized polyethers represented by Formula III are prepared, for example, by contacting a diglycidyl ether or a combination of diglycidyl ethers with a dihydric phenol or combination of dihydric phenols using the process described in U.S. Patent 5,164,472.
• the poly(hydroxy ethers) are obtained by allowing a dihydric phenol or a combination of dihydric phenols to react with an epihalohydrin by the process described by Reinking, Bamabeo, and Hale in the Journal of Applied Polymer Science, Volume 7, page 2135 (1963).
• Formulae IVa and IVb are prepared, for example, by polymerizing an N,N'-dialkyl or N,N'-diaryldisulfonamide with a diglycidyl ether as described in U.S. Patent 5,149,768.
• hydroxy-functionalized polyethers commercially available from Phenoxy Associates, Inc. are also suitable for use in the present invention. These hydroxy-functionalized polyethers are the condensation reaction products of a dihydric polynuclear phenol, such as bisphenol A, and an epihalohydrin and have the repeating units represented by Formula III wherein B is an isopropylidene diphenylene moiety. These hydroxy-phenoxyether polymers and the process for preparing them are described in U.S. Patents 3,305,528.
• Other hydroxy functional polyethers that are suitable for use in the present invention are poly(alkylene oxides), which are typically produced through the polymerization of ethylene oxide, propylene oxide or butylene oxide.
• the polymers which are not hydroxy-functionalized polyesters or polyethers which can be employed in the practice of the present invention for preparing the fibers include polyolefins, polyesters, polyamides, polysaccharides, modified polysaccharides or naturally-occurring fibers or particulate fillers; thermoplastic polyurethanes, thermoplastic elastomers and glycol-modified copolyester (PETG).
• Other polymers of the polyester or polyamide type can also be employed in the practice of the present invention for preparing the fiber.
• Such polymers include poly(hexamethylene adipamide), polycaprolactone, poly(hexamethylene sebacamide), poly(ethylene 2,6- naphthalate) and poly(ethylene 1 ,5-naphthalate), poly(tetramethylene 1 ,2-dioxybenzoate) and copolymers of ethylene terephthalate and ethylene isophthalate.
• polyesters and methods for their preparation are well known in the art and reference is made thereto for the purposes of this invention.
• reference is particularly made to pages 1-62 of Volume 12 of the Encyclopedia of Polymer Science and Engineering, 1988 revision, John Wiley & Sons.
• the polymers which are not hydroxy-functionalized polyesters or polyethers can be blended with the hydroxy-functionalized polyether or polyester at levels of less than 50 weight percent and, preferably less than 30 weight percent, based on the weight of the fiber. These other polymers can be blended into the hydroxy-functionalized polyether or polyester in order to reduce composition cost, to modify physical properties, barrier or permeability properties, or adhesion characteristics.
• the separate non-hydroxy-functional-containing component may be used at levels of up to 99 percent, preferably less than 95 percent, based on the weight of the fiber.
• polyamides which can be employed in the practice of the present invention for preparing the fibers include the various grades of nylon, such as nylon 6, nylon 6,6 and nylon 12.
• polyolefin is meant a polymer or copolymer derived from simple olefin monomers such as ethylene, propylene, butylene, or isoprene, and one or more monomers copolymerizable therewith.
• Such polymers including raw materials, their proportions, polymerization temperatures, catalysts and other conditions) are well- known in the art and reference is made thereto for the purpose of this invention.
• Additional comonomers which can be polymerized with ethylene include olefin monomers having from 3 to 12 carbon atoms, ethylenically unsaturated carboxylic acids (both mono- and difunctional) and derivatives of such acids such as esters (for example, alkyl acrylates) and anhydrides; monovinylidene aromatics and monovinylidene aromatics substituted with a moiety other than halogen such as styrene and methylstyrene; and carbon monoxide.
• Exemplary monomers which can be polymerized with ethylene include
• 1-octene acrylic acid, methacrylic acid, vinyl acetate and maleic anhydride.
• the polyolefins which can be employed in the practice of the present invention for preparing the fibers include polypropylene, polyethylene, and copolymers and blends thereof, as well as ethylene-propylene-diene terpolymers.
• Preferred polyolefins are polypropylene, such as Pro-fax TM PF635 (Trademark of Montell North American Inc.) and INSPIRE TM (Trademark of The Dow Chemical Company), linear high density polyethylene (HDPE), heterogeneously-branched linear low density polyethylene (LLDPE) such as DOWLEXTM polyethylene resin (Trademark of The Dow Chemical Company), heterogeneously-branched ultra low linear density polyethylene (ULDPE) such as ATTANETM ULDPE (Trademark of The Dow Chemical Company); homogeneously-branched, linear ethylene/ ⁇ -olefin copolymers such as TafmerTM (Trademark of Mitsui Petrochemicals Company Limited) and ExactTM (Trademark of Exxon
• polyolefin elastomers which can be prepared as disclosed in U.S. Patents 5,272,236 and 5,278,272; and high pressure, free radical polymerized ethylene polymers and copolymers such as low density polyethylene (LDPE), ethylene-acrylic acid (EAA) copolymers such as PRIMACORTM (Trademark of The Dow Chemical Company), and ethylene-vinyl acetate (EVA) copolymers such as EscoreneTM polymers (Trademark of Exxon Chemical Company), and ElvaxTM (Trademark of E.I. du Pont de Nemours & Co.).
• LDPE low density polyethylene
• EAA ethylene-acrylic acid copolymers
• EVA ethylene-vinyl acetate copolymers
• EscoreneTM polymers Trademark of Exxon Chemical Company
• ElvaxTM Trademark of E.I. du Pont de Nemours & Co.
• the more preferred polyolefins are the homogeneously-branched linear and substantially linear ethylene copolymers with a density (measured in accordance with ASTM D-792) of 0.85 to 0.99 g/cm 3 , a weight average molecular weight to number average molecular weight ratio (Mw/Mn) from 1.5 to 3.0, a measured melt index (measured in accordance with ASTM D-1238 (190/2J6)) of 0.01 to 100 g/10 minutes, and an 110/12 of 6 to 20 (measured in accordance with ASTM D-1238 (190/10)).
• high density polyethylene has a density of at least about 0.94 grams per cubic centimeter (g/cc) (ASTM Test Method D-1505).
• HDPE is commonly produced using techniques similar to the preparation of linear low density polyethylenes. Such techniques are described in U.S. Patents 2,825,721 ; 2,993,876; 3,250,825 and 4,204,050.
• the preferred HDPE employed in the practice of the present invention has a density of from 0.94 to 0.99 g/cc and a melt index of from 0.01 to 35 grams per 10 minutes as determined by ASTM Test Method D-1238.
• the polysaccharides which can be employed in the practice of the present invention are the different starches, celluloses, hemicelluloses, xylanes, gums, pectins and pullulans. Polysaccharides are known and are described, for example, in Encyclopedia of Polymer Science and Technology, 2nd edition, 1987.
• the preferred polysaccharides are starch and cellulose.
• the modified polysaccharides which can be employed in the practice of the present invention are the esters and ethers of polysaccharides, such as, for example, cellulose ethers and cellulose esters, or starch esters and starch ethers. Modified polysaccharides are known and are described, for example, in Encyclopedia of Polymer Science and Technology, 2nd edition, 1987.
• starch refers to carbohydrates of natural vegetable origin, composed mainly of amylose and/or amylopectin, and includes unmodified starches, starches which have been dewatered but not dried, physically modified starches, such as thermoplastic, gelatinized or cooked starches, starches with a modified acid value (pH) where acid has been added to lower the acid value of a starch to a range of from 3 to 6, gelatinized starches, ungelatinized starches, cross-linked starches and disrupted starches (starches which are not in particulate form).
• the starches can be in granular, particulate or powder form. They can be extracted from various plants, such as, for example, potatoes, rice, tapioca, corn, pea, and cereals such as rye, oats, and wheat.
• Celluloses are known and are described, for example, in Encyclopedia of Polymer Science and Technology, 2nd edition, 1987.
• Celluloses are natural carbohydrate high polymers (polysaccharides) consisting of anhydroglucose units joined by an oxygen linkage to form long molecular chains that are essentially linear.
• Cellulose can be hydrolyzed to form glucose.
• the degree of polymerization ranges from 1000 for wood pulp to 3500 for cotton fiber, giving a molecular weight of from 160,000 to 560,000.
• Cellulose can be extracted from vegetable tissues (wood, grass, and cotton). Celluloses can be used in the form of fibers.
• the naturally-occurring fibers or particulate fillers which can be employed in the practice of the present invention are, for example, wood flour, wood pulp, wood fibers, cotton, flax, hemp, or ramie fibers, rice or wheat straw, chitin, chitosan, cellulose materials derived from agricultural products, nut shell flour, corn cob flour, and mixtures thereof.
• the fibers of the present invention can be formed by well known processes such as melt spinning, wet spinning, or conjugate spinning.
• the fibers of the present invention may be extruded into any size, or length desired. They may also be extruded into any shape desired, such as, for example, cylindrical, cross-shaped, trilobal or ribbon-like cross-section.
• the bicomponent fibers of the present invention can have the following fiber cross-section structures:
• a method for producing side-by-side bicomponent fibers is described in U.S. Patent 5,093,061.
• the method comprises (1 ) feeding two polymer streams through orifices separately and converging at substantially the same speed to merge side-by-side as a combined stream below the face of the spinneret; or (2) feeding two polymer streams separately through orifices, which converge at the surface of the spinneret, at substantially the same speed to merge side-by-side as a combined stream at the surface of the spinneret.
• the velocity of each polymer stream at the point of merge is determined by its metering pump speed and the size of the orifice.
• the fiber cross- section has a straight interface between two components.
• Side-by-side fibers are generally used to produce self-crimping fibers. All commercially available self-crimping fibers are produced by using a system based on the different shrinkage characteristics of each component.
• Sheath-core bicomponent fibers are those fibers where one of the components (core) is fully surrounded by a second component (sheath). Adhesion is not always essential for fiber integrity.
• sheath-core fibers The most common way to produce sheath-core fibers is a technique in which two polymer liquids (melts) are separately led to a position very close to the spinneret orifices and then extruded in sheath-core form.
• the orifice supplying the "core" polymer is in the center of the spinning orifice outlet and flow conditions of core polymer fluid are strictly controlled to maintain the concentricity of both components when spinning. Modifications in spinneret orifices enable one to obtain different shapes of core or/and sheath within the fiber cross-section.
• the sheath-core structure is employed when it is desirable for the surface to have the property of one of the polymers such as luster, dyeability or stability, while the core may contribute to strength, and reduced cost.
• the sheath-core fibers are used as crimping fibers and as bonding fibers in the non-woven industry.
• the sheath-core bicomponent fiber can have a core comprising the hydroxy-functionalized polyether or polyester and a sheath comprising a polymer which is not a hydroxy-functionalized polyether or polyester.
• the hydroxy- functionalized polyether or polyester can be the sheath and the polymer that is not the hydroxy-functionalized polyether or polyester the core of the bicomponent fiber.
• the sheath-core may be circular in cross-section or may have some other geometry, such as trilobal.
• a variant such as "tipped trilobal" can also be constructed wherein the sheath component is no longer continuous about the core but exists only at the tips of the lobes formed by the core.
• Other configurations which may be utilized are illustrated in International Fiber Journal, Volume 13, No, 3, June 1998 ⁇ n the articles beginning on pages 20, 26, and 49.
• Islands-in-the sea fibers are also called matrix-filament fibers which include heterogeneous bicomponent fibers.
• a method for producing islands-in-the sea fibers is described in U.S. Patent 4,445,833. The method comprises injecting streams of core polymer into sheath polymer streams through small tubes with one tube for each core stream. The combined sheath-core streams converge inside the spinneret hole and form one island-in-the sea conjugate stream.
• the hydroxy-functionalized polyether or polyester can be the sea polymer and the polymer which is not a hydroxy-functionalized polyether or polyester can be the island polymer.
• the hydroxy-functionalized polyether or polyester can also be the island polymer and the polymer which is not a hydroxy-functionalized polyether or polyester, the sea polymer.
• the islands-in-the-sea structure is employed when it is desirable to increase the modulus of the fiber, reduce moisture regain, reduce dyeability, improve the texturing capability or give the fiber a unique lustrous appearance.
• the citrus type bicomponent or segmented pie bicomponent fibers can be made by polymer distribution and/or spinneret modifications of the pack assemblies employed in the methods described above for producing the side-by-side, sheath-core or islands-in-the-sea fibers. For example, by introducing a first polymer stream and a second polymer stream alternately through eight radial channels toward the spinneret hole instead of two channels, the resultant fiber is an eight-segment citrus type fiber. If the spinneret orifice has the configuration of three or four slots on a circle (a common orifice configuration to produce hollow fibers), the fiber is a hollow citrus type fiber with eight segments.
• the hollow citrus type fiber can also be made by the use of special spinneret orifice configurations with a sheath-core spin pack as described in U.S. Patents 4,246,219 and 4,357,290.
• the fibers of the present invention can be blended with other synthetic or natural fibers, such as carbon fibers, cotton, wool, polyester, polyolefin, nylon, rayon, glass fibers, fibers of silica, silica alumina, potassium titanate, silicone carbide, silicone nitride, boron nitride, boron, acrylic fibers, tetrafluoroethylene fibers, polyamide fibers, vinyl fibers, protein fibers, ceramic fibers, such as aluminum silicate, and oxide fibers, such as boron oxide.
• other synthetic or natural fibers such as carbon fibers, cotton, wool, polyester, polyolefin, nylon, rayon, glass fibers, fibers of silica, silica alumina, potassium titanate, silicone carbide, silicone nitride, boron nitride, boron, acrylic fibers, tetrafluoroethylene fibers, polyamide fibers, vinyl fibers, protein fibers, ceramic fibers, such as aluminum silicate, and oxide fibers
• Additives such as pigments, stabilizers, impact modifiers, plasticizers, carbon black, conductive metal particles, abrasives and lubricating polymers may be incorporated into the fibers.
• the method of incorporating the additives is not critical.
• the additives can conveniently be added to the hydroxy-functionalized polyether or polyester prior to preparing the fibers. If the hydroxy-functionalized polyether or polyester is prepared in solid form, the additives can be added to the melt prior to preparing the fibers.
• the fibers of the present invention can be crosslinked by chemical treatment, heating or irradiation with ultraviolet light.
• the fibers can be chemically treated with crosslinking agents such as diisocyanates, glycidylmethacrylate, bisepoxides and anhydrides.
• the fibers of the present invention are suitable for use in filtration media, binder fibers for glass or carbon fibers, binder fibers in non-woven fabrics made of thermoplastic polymers which are not hydroxy-functionalized polyethers or polyesters or binder fibers in non-woven fabrics made of cellulosic-based materials. These fibers are also useful in the manufacture of medical apparels. They are also useful in making woven and non-woven fabrics which can be used in making apparels, water-absorbent cloths, antistatic wipes, or water-absorbent mats.
• Woven fabrics are formed from the fibers of the present invention by techniques commonly used in the woven textiles industry, such as weaving or knitting.
• Non-woven fabrics are based on a fibrous web.
• the fibers of the present invention can be formed into webs using the following known technologies: (1 ) Dry-formed, carded or air-laid and bonded -
• the webs are formed from staple fibers by carding or air-laying, bonded overall or in a pattern with latex or other water-borne adhesives.
• carding clumps of staple fibers are separated mechanically into individual fibers and formed into a coherent web.
• fibers are introduced into an airstream and are captured on a screen from the air stream.
• Spun-bonded - Webs composed of long filaments with normal textile diameter are formed directly from bulk polymer and are usually bonded thermally.
• melt-blown - Webs of long, extremely fine diameter fibers are formed directly from bulk polymer and are usually bonded by hot embossing processes.
• Spun-laced - Dry-formed webs are mechanically entangled by multiple fine, high pressure water jets, in most cases, without adhesive binder.
• Needle-punched - Fibers are mechanically entangled by multiple reciprocating banks of barbed needles.
• Laminated - Different layers are combined in composite or reinforced fabric by an adhesive, thermal fusion or entanglement.
• Stitch-bonded - Staple fiber webs are reinforced or mechanically entrapped by yarns stitched or knitted through the webs.
• Non-woven fabrics and processes for preparing them are described in the Encyclopedia of Polymer Science And Engineering, Second Edition, Volume 10, pages 204-251.
• Example 1 A 3/8-inch (0.95 cm) single-screw extruder fitted with an 8-hole spinneret was used to spin monofilaments based on 100 percent thermoplastic hydroxy-functional polyether. The melt temperature was 200°C. The fibers were rolled onto bobbins without further stretching.
• Example 2 Bicomponent fibers containing polypropylene as the core and a thermoplastic hydroxy-functionalized polyether as the sheath were spun. Two single- screw extruders, one feeding the polypropylene and another feeding the thermoplastic hydroxy-functionalized polyether were used. The extruders fed the molten polymers (melt temperature was 200°C) to a 288-holed spinneret from which the bicomponent fibers were spun. Fibers with polypropylene:thermoplastic hydroxy-functionalized polyether ratios of 90:10, 80:20, 70:30, 40:60 and 50:50 were spun. The fibers were also stretched after exiting the spinneret by using extender rolls and then taken up on bobbins.
• a polyetheramine poly(hydroxy amino ether) (derived from the reaction of the diglycidyl ether of bisphenol A and ethanolamine) and a polypropylene were spun into bicomponent fibers.
• the poly(hydroxy amino ether) had an MFI (Melt Flow Index) of 8 at 230°C using a 2J6 kg weight.
• the polypropylene source was a 35 MFI Pro-fax TM PF635 polypropylene from Montell. This sheath/core bicomponent fiber was produced under the conditions listed in Table I. Table I
• a 30/70 weight/weight (w/w) poly(hydroxy amino ether) (derived from the reaction of the diglycidyl ether of bisphenol A and ethanolamine) sheath/polypropylene core bicomponent fiber was treated on a Tech Tex texturizing unit to impart a crimp .
• This equipment uses the stuffer box method of texturizing.
• the texturized yarn was cut into staple fiber of 2-inch (5 cm) length on an Ace Strip Cutter, Model C-75. After the crimping and staple cutting operations the fiber was opened a 12-inch (30.5 cm) wide microdenier metallic card in lots of 30 grams.
• the open fiber was then used to produce a batt on a sample card line. This carded batt was needled on a James Hunter Fiberlocker Needle machine to give a resultant needle-punched fabric.
• Cotton fibers (4 kg, 1.5 to 5 cm in length) and 7-denier bicomponent fibers (30/70 (w/w) poly(hydroxyaminoether)/polypropylene), (0.45 kg, 2.5 cm in length) were manually mixed and then opened up. The blend was carded and converted into a non- woven web, which was thermally bonded with calender rolls at 170°C.
• Cotton linters (150 g) and 7-denier bicomponent fibers (30/70 (w/w) polyetheramine/polypropylene) were added to 300 L of water in a cylindrical tank and the contents were agitated for 5 minutes.
• the polyetheramine was derived from the reaction of the diglycidyl ether of bisphenol A and ethanolamine.
• the ratio of bicomponent fibers to cotton linters was 5 percent on a weight basis.
• the slurry was then pumped to a moving belt made of polyester mesh and the webs formed were collected.
• the wet webs were dried by passing them through a 165°C oven with approximately one minute of dwell time.
• the dried webs were then bonded with heated calender rolls at temperatures from 100°C to 180°C.
• the basis weight of the webs after bonding was about 90 gsm.
• a bicomponent, sheath/core spunbond fabric was produced under the conditions shown in Table II.
• the polyetheramine derived from the reaction of the diglycidyl ether of bisphenol A and ethanolamine
• sheath had a MFI of 15.
• the polypropylene core was composed of a 35 MFI Pro-fax TM PF635.
• the sheath/core ratio was 20/80 (w/w).
• the system was run at slot air pressures of 20, 25 and 30 psi and the spunbond material was collected on perforated belt/vacuum collection system. Collection speeds ranged from 50 to 75 meters per minute. Calender rolls were set to 60°C and appeared to provide adequate bonding for dry web stock.
• the poly(hydroxy amino ether) (“PHAE”) used in the following Examples 8 through 15 was produced by The Dow Chemical Company from the polymerization of a diglycidyl ether of Bisphenol A and ethanol amine.
• Mn number average molecular weight
• Mw weight average molecular weight
• melt index 15 (measured at 190°C with a 2J 6 kg weight)
• glass transition temperature (Tg) 78°C.
• PEG refers to poly(ethylene glycol)
• PEO refers to poly(ethylene oxide).
• PEG and PEO have the same polyoxyethylene repeating unit shown below:
• EPE refers to a block copolymer with the general structure shown below:
• the EPE block copolymers contain a hydrophobic block of polypropylene oxide), having a molecular weight ranging from a minimum of 900 to a maximum of 4000, with two hydrophilic polyoxyethylene blocks such that the combined weight of the polyoxyethylene blocks constitutes from 10 to 90 weight percent of the total molecule.
• the EPE block copolymers are nonionic surfactants [see L. G. Lundsted and I.R. Schmolka, "The Synthesis and Properties of Block Copolymer Polyol Surfactants” in Block and Graft Copolymerization, volume 2 (edited by R. J. Ceresa), John Wiley and Sons, New York, chapter 1 , pp. 1 -103].
• the EPE block copolymers are marketed under the Trademark PLURONIC® polyols (BASF Wyandotte Corporation) and are also sold by The Dow Chemical Co. (for example, Polyglycol EP-1730 and EP-1660).
• EPE block copolymers give the weight percent ethylene glycol and the average calculated molecular weight (Mn), as given in the Aldrich catalog.
• Mn average calculated molecular weight
• EPE-30 Mn 5800 refers to an EPE block copolymer containing 30 weight percent ethylene glycol and having a calculated number average molecular weight of 5800.
• Glass transition temperature was determined using a TA Instruments DSC 2010 Differential Scanning Calorimeter. Samples (5 to 10 mg) were prepared in hermetically sealed pans. Two scans were made for each sample. The first scan was made from ambient to 200°C at 10°C per minute. The sample was then cooled to ambient temperature or below using dry ice, whereupon the second scan was made at 10 minute to 200°C. The Tg was determined from the second scan inflection point.
• pH7 Buffer Contact Angle was determined for compression molded films using a Kr ⁇ ss G40 Contact Angle Measuring System (Goniometer) equipped with a Eurometrix fiber optic light source, a Kernco model G-1 microscope, stage, light source, and camera mount, and a Kruss Panasonic CCTV camera and WV-5410 monitor. A small drop of the pH7 buffer was applied to the film and the angle formed at the film/drop/air interface was measured using the system software (G40 V1.32-US). In the examples that follow the terms "water contact angle” and "pH7 buffer contact angle" are synonymous.
• the apparatus for spinning fiber consisted of a Rheometrix capillary melt rheometer equipped with a 1000 ⁇ m die, a Rheotens attachment, and a 12 inch (30.5 cm) circumference variable speed roll onto which the fiber was spun.
• Example 8 - PHAE Blend With 10 Weight Percent PEG 10.000
• PHAE 243.0 g
• PEG 10,000 (27.1 g, Aldrich Chemical Co., Tm 63°C) were melt blended for 20 minutes in a large capacity Haake Torque rheometer (with roller mixing blades) at 170°C isothermal metal temperature and 100 rpm mixing rate.
• the resulting blend had a Tg of 53°C with no crystalline melting point.
• a compression molded film of the blend was transparent and had a water contact angle of 67. Fiber was melt spun at 190°C with a rheometer plunger speed of 0.3 inch/minute and a take-up roll speed of 1780 rpm (543 m/minute). Additional blends with 5 and 25 weight percent PEG
• PHAE PHAE
• PEO 100,000 3.1 g, Aldrich Chemical Co., Tm 65°C
• the resulting blend had a Tg of 66°C with no crystalline melting point.
• a compression molded film of the blend was transparent and had a water contact angle of 68.
• Fiber was melt spun at 190°C with a plunger speed of 0.3 inch/minute (8mm/minute) and a take-up speed of 1780 rpm (543 m/minute).
• the denier of the fiber was 9 g (equals the weight of 9000 m of continuous fiber). Additional blends with 10 percent and 25 percent PEO 100,000 were prepared and the results are included in Table III.
• Example 10 - PHAE blend with 5 Weight Percent PEO 4.000.000
• PHAE PHAE
• PEO 4,000,000 3.0 g, Aldrich Chemical Co., Tm 65°C
• the resulting blend had a Tg of 67°C with no crystalline melting point.
• a compression molded film of the blend was transparent and had a water contact angle of 65.
• Fiber was melt spun at 190°C with a plunger speed of 0.3 inch/minute (8 mm/minute) and a take-up speed of 1780 rpm (543 m/minute).
• the denier of the fiber was 10 g.
• Example 11 - PHAE Blend With 10 Weight Percent PEO 4.000,000
• PHAE 243.0 g
• PEO 4,000,000 27.0 g, Aldrich Chemical Co., Tm 65°C
• the resulting blend had a Tg of 55°C with no crystalline melting point.
• a compression molded film of the blend was transparent and had a water contact angle of 72. Fiber was melt spun at 190°C with a plunger speed of 0.3 inch/minute (8 mm/minute) and a take-up speed of 1780 rpm (543 m/minute).
• Example 13 - PHAE Blend With 3.7 Weight Percent EPE-30 (Mn 5800)
• PHAE (73.4 g) and EPE-30 (2.8 g, Aldrich Chemical Company, Tm 39°C) were melt blended in a Haake torque rheometer for 20 minutes at 180°C isothermal metal temperature and 100 rpm mixing rate.
• the resulting blend had a Tg of 69°C with no crystalline melting point.
• a compression molded film of the blend had a pearlescent, semi-transparent appearance and had a water contact angle of 24.
• Fiber was melt spun at 200°C with a plunger speed of 0.3 inch/minute and a take-up speed of 1780 rpm (543 m/minute). The denier of the fiber produced was 8g.
• a small hand sample of fabric was made from the fiber as follows: A portion of the fiber (1.4 g) was cut into 2 inch staple and carded to make a web. The web was folded in half and then run through a Beloit Wheeler Model 700 Lab Calendar Roll. The calender rolls were set at 210°F and 1000 psi which gave a well bonded fabric. A sample of pure PHAE fiber (1.4 g) was made into fabric using a similar procedure. The ability of the fabrics to wick water was then tested by immersing one end of a small strip (19 by 81 mm) of each fabric into deionized water and measuring the time required for the water to advance up the fabric strip to a line drawn 25 mm from the surface of the water.
• the PHAE blend with EPE-30 (Mn 5800) wicked water to the line in 2.5 minutes whereas the pure PHAE fabric showed no wicking of water at all.
• the fabrics were redried and the wicking test was repeated 3 times. The same results were observed each time - the fabric made with the EPE-30 blend wicked water and the pure PHAE fabric did not.
• Example 14 - PHAE blend with 5 Weight Percent EPE-80 (Mn 8400) PHAE (57.0 g) and EPE-80 (3.0 g, Aldrich Chemical Co., Tm 58°C) were melt blended in a Haake torque rheometer for 20 minutes at 180°C isothermal metal temperature and 100 rpm mixing rate.
• the resulting blend had a Tg of 64°C with no crystalline melting point.
• a compression molded film of the blend was transparent and had a water contact angle of 56.
• Fiber was melt spun at 200°C with a plunger speed of 0.3 inch/minute and a take-up speed of 850 rpm (259 m/minute). The denier of the fiber produced was 274g.
• Blends of PHAE with other EPE block copolymers including EPE-30 (Mn 4400); EPE-40 (Mn 2,900); and EPE-50 (Mn 1 ,900), were also prepared using procedures analogous to those described above. The results for these blends are listed in Table IV.
• Example 15 - PHAE blend with 5 Weight Percent Polypropylene glycol) (Aldrich. Mn 3500)

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