Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L101/00—Compositions of unspecified macromolecular compounds
  • C08L101/12—Compositions of unspecified macromolecular compounds characterised by physical features, e.g. anisotropy, viscosity or electrical conductivity
  • C08L101/14—Compositions of unspecified macromolecular compounds characterised by physical features, e.g. anisotropy, viscosity or electrical conductivity the macromolecular compounds being water soluble or water swellable, e.g. aqueous gels
• • A—HUMAN NECESSITIES
  • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
  • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
  • A61L15/00—Chemical aspects of, or use of materials for, bandages, dressings or absorbent pads
  • A61L15/16—Bandages, dressings or absorbent pads for physiological fluids such as urine or blood, e.g. sanitary towels, tampons
  • A61L15/42—Use of materials characterised by their function or physical properties
  • A61L15/60—Liquid-swellable gel-forming materials, e.g. super-absorbents
• • A—HUMAN NECESSITIES
  • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
  • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
  • A61L15/00—Chemical aspects of, or use of materials for, bandages, dressings or absorbent pads
  • A61L15/16—Bandages, dressings or absorbent pads for physiological fluids such as urine or blood, e.g. sanitary towels, tampons
  • A61L15/22—Bandages, dressings or absorbent pads for physiological fluids such as urine or blood, e.g. sanitary towels, tampons containing macromolecular materials
  • A61L15/225—Mixtures of macromolecular compounds
• • A—HUMAN NECESSITIES
  • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
  • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
  • A61L15/00—Chemical aspects of, or use of materials for, bandages, dressings or absorbent pads
  • A61L15/16—Bandages, dressings or absorbent pads for physiological fluids such as urine or blood, e.g. sanitary towels, tampons
  • A61L15/42—Use of materials characterised by their function or physical properties
  • A61L15/58—Adhesives

Definitions

• the present invention relates to absorbent materials that, upon contacting liquids such as water or body fluids, swell and imbibe such liquids. More specifically, the present invention relates to improved structural stability in the dry and wet states of absorbent materials.
• the absorbent material of the present invention has particular applicability to absorbent articles such as diapers, adult incontinence pads, sanitary napkins, and the like.
• Water-insoluble, water-swellable, hydrogel-forming absorbent polymers are capable of absorbing large quantities of liquids such as water, body fluids (e.g., urine, blood, menstrual fluid), industrial fluids and household fluids and are further capable of retaining such absorbed liquids under moderate pressures. These absorption characteristics of such polymer materials make them especially useful for incorporation into absorbent articles such as disposable diapers, adult incontinence pads and briefs, and catamenial products such as sanitary napkins, and the like.
• a highly desired characteristic for such absorbent articles is thinness. For example, thinner diapers are less bulky to wear, fit better under clothing, and are less noticeable. They are also more compact in the package, making the diapers easier for the consumer to carry and store. Compactness in packaging also results- in reduced distribution costs for the manufacturer and distributor, including less shelf space required in the store per diaper unit.
• prior absorbent articles have generally comprised relatively low amounts (e.g., less than about 50% by weight) of absorbent gelling particles of the WAHPs.
• relatively low amounts e.g., less than about 50% by weight
• absorbent gelling particles of the WAHPs See, for example, U.S. Patent 4,834,735 (Alemany et. al), issued May 30, 1989. It discloses that an absorbent structure or core contains preferably from about 9 to about 50% of WAHP in the fibrous matrix.
• Unfortunately several problems are encountered when one attempts to provide a thin absorbent core having more than 50% concentration of absorbent gelling particles by weight.
• absorbent articles have the limitation that the absorbent gelling particles are not immobilized and are free to migrate(shift) during the manufacturing process and/or use(wearing). Migrations(shifting) of the absorbent gelling particles during manufacture can lead to absorbent material handling losses during manufacturing operations as well as nonhomogerous incorporation of the particles being used. A more significant problem, though, occurs when these absorbent gelling particles of WAHPs migrate during or after swelling. This inability to fix the particles at optimum locations leads to an insufficient urine storage capacity in one area and over-capacity in other areas due to the lack of stability.
• One important factor is to minimize and/or eliminate the shifting of particles of WAHPs from the first applying location to another position and handling losses during manufacture.
• One problem encountered is the shifting and/or leakage of swollen (e.g., with urine) particles of WAHP due to wear-related movement and pressure on the absorbent article.
• the inability to fix the particles at optimum location is another issue that results in insufficient urine storage capacity in one area and over-capacity in other areas. Subsequently the absorbent article will leak during use.
• the shifting of wet particles of WAHPs can cause core shifting and more incidence of gel leakage when in use, especially from an absorbent material containing high concentration of WAHPs.
• WAHPs used in thinner absorbent article are jelly and mushy feel when touching and handling the absorbent article after usage.
• WAHP is dispersed in region or regions at a high concentration
• the swollen gel formed by absorbing body fluids is a gel layer, in which the particulate is mobile and the gel layer collapses when subjected to forces such as pushing, squeezing, etc. when handling the absorbent article after usage.
• absorbent articles having high concentration of WAHP give users or consumers "wet/mushy" feel when touching or handling them from outside.
• the present invention seeks to resolve the above problems by providing an absorbent material having improved structural stability in dry and wet status.
• the present invention relates to absorbent materials having improved structural stability in dry and wet states.
• These absorbent materials comprise (a) absorbent gelling particles comprising a water-insoluble absorbent hydrogel-forming polymer; (b) a polycationic polymer; (c) glue microfibers; and (d) a carrier layer; wherein the polycationic polymer is bonded to the absorbent gelling particles; and the glue microfibers act as an adhesive between the absorbent gelling particles and the carrier layer. Because the glue microfibers are tacky, the absorbent gelling particles comprising a WAHP fix to the desired location on the carrier layer and do not shift to the another area in dry state.
• the absorbent gelling particles contained in the absorbent material fix to the location first applied due to bonding of the polycationic polymer to the absorbent gelling particles comprising a WAHP, and the absorbent material does not shift.
• the polycationic polymer bonded to the absorbent gelling particles prevents the particles from shifting after they swell with liquid. Consequently, the absorbent material of the invention has improved liquid acquisition speed and low rewetness when in use. It has been found that when the absorbent material is contacted with liquids, the absorbent material swells, imbibes such liquids into the absorbent gelling particles, and absorbs even under moderate confining pressures.
• the carrier layer is selected from the group consisting of a woven material and a nonwoven material.
• absorbent materials may further comprise the cellulose fibers dispersed in the absorbent gelling particles, wherein the cellulose fibers are adhered to the absorbent gelling particles by the glue microfibers.
• the absorbent material of present invention comprises from about 50% to about 90% of the absorbent gelling particle, from about 0.1 % to about 10% of the polycationic polymer, from about 1% to about 10% of the thermoplastic polymeric microfiber and from about 5% to about 50% of the carrier layer by weight.
• the invention further relates to a method of make the absorbent materials, and the absorbent articles comprising the absorbent materials.
• Figure 1 is a schematic view of an apparatus for making the absorbent materials of the present invention.
• “Dry state” means the state of the absorbent material during manufacture.
• “Wet state” means the swollen absorbent materials due to absorption of large quantities of liquids such as water, body fluids, industrial fluids and household fluids, when the absorbent materials of the present invention are used in, e.q., a diaper and worn.
• “Structural stability” means immobilizing(fixing) the absorbent materials onto the right position in a diaper where first located.
• WAHP means a water-insoluble absorbent hydrogel-forming polymer.
• the absorbent material of the present invention is capable of absorbing large quantities of liquids such as water, body fluids, industrial fluids and household fluids at a rapid rate and is capable of retaining such fluids under moderate pressures.
• the absorbent material of the present invention has an improved structural stability in the dry and wet states, while the absorbent material has a high concentration of WAHPs.
• the absorbent material comprises greater than about 50% by weight of a WAHP.
• the absorbent materials are no shifting in the dry and wet states.
• the absorbent gelling particles tend to shift during manufacturing process, resulting in, e.g., clumping of absorbent gelling particles and a lack of uniform distribution of the particles.
• the particles may shift, resulting in insufficient urine storage capacity in one area and over-capacity in other areas. Subsequently the absorbent article will leak during use(wearing).
• the shifting of wet absorbent gelling particles of WAHP can cause core shifting and more incidence of gel leakage when in use or wearing, especially from an absorbent article using absorbent materials comprising a high concentration of WAHP.
• the present invention in its aspects contemplates the absorbent materials comprising the absorbent gelling particles, the polycationic polymer bonded to the absorbent gelling particles, the glue microfibers dispersed in the absorbent gelling particles and the carrier layer.
• its object is to fix the absorbent gelling particles to the desired location of the carrier layer by an adhesive glue microfiber in the dry state and to fix the absorbent gelling particles bonding to the polycationic polymer on the surface, when the absorbent materials contact liquids such as body fluids in the wet state.
• the glue microfiber used herein can be meltblown to form fibers that are tacky in at least one step of the manufacture of the absorbent materials. It is possible that the glue microfiber are initially fixed the absorbent gelling particles to the desired location of the absorbent materials during the manufacturing process.
• the melt blown adhesive polymers which can be utilized for forming the absorbent materials include the elastomeric and non-elastomeric polymers. These polymers must be tacky enough to be blown into fiber forms.
• the tackiness can be modified with the usage of tackifying resins, which include rosin esters, mixed polyalkenes, polyterpenes, waxes, or incorporating carboxylic acid contained polymers or oligomers within the adhesive resin.
• tackifying resins which include rosin esters, mixed polyalkenes, polyterpenes, waxes, or incorporating carboxylic acid contained polymers or oligomers within the adhesive resin.
• blends of adhesive polymers, or blends of adhesive polymers and other polymers are also contemplated by the invention.
• Useful elastomeric polymers include polyolefins and blends (e.g., polypropylene, polybutylene, or ethyleneacrylic acid copolymers), ethylenevinyl acetate copolymers, polyamides, polyesters, and reactive polyamide and polyesters.
• polyolefins and blends e.g., polypropylene, polybutylene, or ethyleneacrylic acid copolymers
• ethylenevinyl acetate copolymers e.g., polyamides, polyesters, and reactive polyamide and polyesters.
• Pressure sensitive adhesives are also useful for forming the absorbent structure of this invention. They are permanently tacky and do not change their physical state from an initial liquid to a solid after final bond formation.
• Exemplified elastomeric polymers are ethylenevinyl acetate copolymer, styrene/diene triblock copolymer, poly(vinylether)s, polyacrylates, and silicones.
• Thermoplastic elastomeric triblock copolymers of the ABA type have great adhesive capability and processing convenience in this invention.
• the end block (A) in these polymers are plastic in nature with a high glass transition (or melt) temperature, which the block (B) is rubbery.
• the non-elastomeric polymer may be a non-elastomeric fiber forming resin or blend containing the same.
• such polymers include polyolefins, non-elastomeric polyamides, cellulosic derived polymers, vinyl chlorides, and polyvinyl alcohols.
• the types of elastomeric Styrene-lsoprene-Styrene block copolymers are HL-1358 or Finely H-6752A supplied by Fuller Co.
• the types of non-elastomeric glue microfiber include polyethyloxazoline, for example XR-2676 (Fuller Co.,), polyvinylpyrolidone, for example H-1716 (Fuller Co.,) and ethylenevinyacetate copolymer, for example HT-480 (Fuller Co.,).
• the glue microfibers comprising polyethyloxazoline would provide the absorbent article comprising the absorbent material of the present invention sufficient structural integrity in the dry state, while in the wet state the polycationic polymers comprising polyethyleneimine are activated to maintain the structural integrity of the absorbent article.
• the polycationic polymer used herein is a polymer which has multiple functional groups that are capable of bonding to the surface of the absorbent gelling particles.
• an amino-group or iminegroup containing polymer is used as the polycationic polymer.
• Such polycationic polymers include polyamines, polyimines and mixtures thereof. More preferably, the polyamine is selected from the group consisting of polymers having first amine groups (e.g., polyvinylamine, polyallylamine), polymers having second amine groups (e.g., polyethyleneamines) and polymers having third amine groups (e.g., poly-N, N- dimethylalkyl amine, poly-N-alkylamine).
• the polyimines preferably used include polyethyleneimines, modified polyethyleneimines crosslinked with epihalohydrine, polyamidoamines grafted with ethyleneimine and mixtures thereof.
• Other suitable polycationic polymers include modified polyamidoamine grafted with ethyleneimine, polyetheramine, polyvinylamine, polyallylamine, polyamidopolyamine and mixtures thereof.
• the polycationic polymer is a cationic polymer having an average molecular weight of at least about 200, more preferably of at least more than 5,000, and most preferably of more than about 10,000.
• the polycationic polymers useful in the invention include those polymers having a single maximum value (a peak) in molecular weight distribution, as well as those polycationic polymers having one or more maximum values.
• the molecular weight distribution can be analyzed by, for example, gel permeation chromatography.
• the amount of polycationic polymer used in the absorbent material is from about 0.1% to 10% by weight of the absorbent materials.
• the polycationic polymer used for the present invention has a concentration of from about 80% to 99% by weight so that it can be tacky by itself.
• the polycationic polymers having the characteristic of tackiness can be meltblown without glue microfibers, consequently acting as an adhesive between the absorbent gelling particles and the carrier layer.
• the polycationic polymer fiber has a molecular weight of at least about 70,000.
• the WAHPs useful in the present invention are commonly referred to as "hydrogel-forming", “hydrocolloid”, or “superabsorbent” polymers and can include polysaccharides such as carboxymethyl starch, carboxymethyl cellulose, and hydroxypropyl cellulose; nonionic types such as polyvinyl alcohol, and polyvinyl ethers; cationic types such as polyvinyl pyridine, polyvinyl morpholinione, and N,N-dimethylaminoethyl or N,N- diethylaminopropyl acrylates and methacrylates, and the respective quaternary salts thereof.
• polysaccharides such as carboxymethyl starch, carboxymethyl cellulose, and hydroxypropyl cellulose
• nonionic types such as polyvinyl alcohol, and polyvinyl ethers
• cationic types such as polyvinyl pyridine, polyvinyl morpholinione, and N,N-dimethylaminoethy
• WAHPs useful in the present invention have a plurality of anionic, functional groups, such as sulfonic acid, and more typically carboxy, groups.
• polymers suitable for use herein include those which are prepared from polymerizable, unsaturated, acid- containing monomers.
• such monomers include the olefinically unsaturated acids and anhydrides that contain at least one carbon to carbon olefinic double bond. More specifically, these monomers can be selected from olefinically unsaturated carboxylic acids and acid anhydrides, olefinically unsaturated sulfonic acids, and mixtures thereof.
• non-acid monomers can also be included, preferably in minor amounts, in preparing the WAHPs herein.
• Such non-acid monomers can include, for example, the water-soluble or water-dispersible esters of the acid- containing monomers, as well as monomers that contain no carboxylic or sulfonic acid groups at all.
• Optional non-acid monomers can thus include monomers containing the following types of functional groups: carboxylic acid or sulfonic acid esters, hydroxyl groups, amide-groups, amino groups, nitrile groups, quaternary ammonium salt groups, aryl groups (e.g., phenyl groups, such as those derived from styrene monomer).
• non-acid monomers are well-known materials and are described in greater detail, for example, in U.S. Patent 4,076,663 (Masuda et. al), issued February 28, 1978, and in U.S. Patent 4,062,817 (Westerman), issued December 13, 1977.
• Olefinically unsaturated carboxylic acid and carboxylic acid anhydride monomers include the acrylic acids typified by acrylic acid itself, methacrylic acid, ethacrylic acid, -chloroacrylic acid, -cyanoacrylic acid, -methylacrylic acid (crotonic acid), -phenylacrylic acid, -acryloxypropionic acid, sorbic acid, -chlorosorbic acid, angelic acid, oinnamic acid, p-chlorocinnamic acid, -sterylacrylic acid, itaconic acid, citroconic acid, mesaconic acid, glutaconic acid, aconitic acid, maleic acid, fumaric acid, tricarboxyethylene and maleic acid anhydride.
• acrylic acids typified by acrylic acid itself, methacrylic acid, ethacrylic acid, -chloroacrylic acid, -cyanoacrylic acid, -methylacrylic acid (crotonic acid), -phenyl
• Olefinically unsaturated sulfonic acid monomers include aliphatic or aromatic vinyl sulfonic acids such as vinylsulfonic acid, allyl sulfonic acid, vinyl toluene sulfonic acid and styrene sulfonic acid; acrylic and methacrylic sulfonic acid such as sulfoethyl acrylate, sulfoethyl methacrylate, sulfopropyl acrylate, sulfopropyl methacrylate, 2-hydroxy-3-methacryloxypropyl sulfonic acid and 2-acrylamide-2-methyipropane sulfonic acid.
• vinylsulfonic acid allyl sulfonic acid, vinyl toluene sulfonic acid and styrene sulfonic acid
• acrylic and methacrylic sulfonic acid such as sulfoethyl acrylate, sulf
• Preferred WAHPs for use in the present invention contain carboxy groups.
• These polymers include hydrolyzed starch-acrylonitrile graft copolymers, partially neutralized hydrolyzed starch-acrylonitrile graft copolymers, starch- acrylic acid graft copolymers, partially neutralized starch-acrylic acid graft copolymers, saponified vinyl acetate-acrylic ester copolymers, hydrolyzed acrylonitrile or acrylamide copolymers, slightly network crosslinked polymers of any of the foregoing copolymers, partially neutralized polyacrylic acid, and slightly network crosslinked polymers of partially neutralized polyacrylic acid.
• polymers can be used either solely or in the form of a mixture of two or more different polymers.
• examples of these polymer materials are disclosed in U.S. Patent 4,076,663 (Masuda et. al), issued February 28, 1978, U.S. Patent 4,093,776 (Aoki et. al), issued June 6, 1978, U.S. Patent 4,666,983 (Tsubakimoto et. al), issued May 19, 1987, and U.S. Patent 4,734,478 (Tsubakimoto et. al), issued March 29, 1988.
• polymer materials used in making the WAHPs are slightly network crosslinked polymers of partially neutralized polyacrylic acids and starch derivatives thereof. More preferably still, the WAHPs comprise from about 50 to about 95%, more preferably about 75%, neutralized, slightly network crosslinked, polyacrylic acid (i.e., poly (sodium acrylate/acrylic acid) ). Network crosslinking renders the polymer substantially water- insoluble and, in part, determines the absorptive capacity and extractable polymer content characteristics of the WAHPs. Processes for network crosslinking these polymers and typical network crosslinking agents are described in greater detail in U.S. Patent 4,076,663 (Masuda et. al), issued February 28.
• Surface crosslinked WAHPs are used in a preferred embodiment of the present invention. They have a higher level of crosslinking in the vicinity of the surface than in the interior.
• surface describes the outer-facing boundaries of, e.g., the particle, fiber.
• exposed internal boundaries can also be included.
• a higher level of crosslinking at the surface it is meant that the level of functional crosslinks for the WAHP in the vicinity of the surface is generally higher than the level of functional crosslinks for the WAHP in the interior.
• the gradation in crosslinking from surface to interior can vary, both in depth and profile.
• the depth of surface crosslinking can be shallow, with a relatively sha ⁇ transition to a lower level of crosslinking.
• the depth of surface crosslinking can be a significant fraction of the dimensions of the WAHP, with a broader transition.
• the degree and gradient of surface crosslinking can vary within a given WAHP.
• surface crosslinking can vary with particle size, porosity, etc.
• the overall level of crosslinking e.g., be greater for smaller particles.
• Surface crosslinking is generally accomplished after the final boundaries of the WAHP is essentially established (e.g., by grinding, extruding, foaming, etc.) However, it is also possible to effect surface crosslinking concurrent with the creation of final boundaries. Furthermore, some additional changes in boundaries can occur even after surface crosslinks are introduced.
• the surface crosslinking can be accomplished before or, simultaneously, with the covalent bonding of the polycationic polymer to the surface of the absorbent gelling particles.
• WAHP is preferably of one type (i.e., homogeneous)
• mixtures of polymers can also be used in the present invention.
• mixtures of starch-acrylic acid graft copolymers and slightly network crosslinked polymers of partially neutralized polyacrylic acid can be used in the present invention.
• the absorbent gelling particles used in the present invention can have a size, shape and/or morphology varying over a wide range.
• the absorbent gelling particles may have a large ratio of greatest dimension to smallest dimension (e.g., granules, flakes, pulverulents, interparticle aggregates, interparticle crosslinked aggregates, and the like) and can be in the form of fibers, foams, and the like.
• the particle size is in the range of from about 10 to about 1000 microns.
• the WAHPs can also comprise mixtures with low levels of one or more additives, such as, for example, powdered silica, surfactants, celloluse microfiber and the like.
• the components in this mixture can be physically and/or chemically associated in a form such that the WAHP component and the non-hydrogel-forming polymer additive are not readily physically separable.
• the WAHPs can be essentially non-porous or have substantial internal porosity.
• particle size is defined as the dimension determined by sieve size analysis.
• a particle that is retained on a U.S.A. Standard Testing Sieve with 710 micron openings (e.g., No. 25 U.S. Series Alternate Sieve Designation) is considered to have a size greater than 710 microns;
• a particle that passes through a sieve with 710 micron openings and is retained on a sieve with 500 micron openings e.g., No. 35 U.S, Series Alternate Sieve Designation
• a particle that passes through a sieve with 500 micron openings is considered to have a size less than 500 microns.
• the absorbent materials according to the present invention can be used for many purposes in many fields of use.
• the absorbent material can be used for packing containers; drug delivery devices; wound cleaning devices; burn treatment devices; ion exchange column materials; construction materials; agricultural or horticultural materials such as seed sheets or water-retentive materials; and industrial uses such as sludge or oil dewatering agents, materials for the prevention of dew formation, desiccants, and humidity control materials.
• the absorbent material of the invention can have a number of shapes and sizes.
• the absorbent material can be in the form of sheets, films, cylinders, blocks or other shaped elements.
• the absorbent material can comprise a cellulosic material for enhancing absorbency and/or be in a form amenable to these and other applications as described hereinafter. Because of the unique absorbent properties of the absorbent material of the present invention, it is especially suitable for use as an absorbent core in absorbent articles, especially disposable absorbent articles.
• absorbent article refers to articles which absorb and contain body fluids and more specifically refers to articles which are placed against or in proximity to the body of the wearer to absorb and contain the various fluids discharged from the body.
• absorbent articles are those which are intended to be discarded after a single use (i.e., the original absorbent article in its whole is not intended to be laundered or otherwise restored or reused as an absorbent article, although certain materials or all of the absorbent article may be recycled, reused, or composted).
• an absorbent article comprise (a) a liquid pervious topsheet; (b) a liquid impervious backsheet; and (c) an absorbent core positioned between the topsheet and the backsheet wherein the absorbent core comprises at least one absorbent material.
• the term "absorbent core” refers to the component of the absorbent article that is primarily responsible for fluid handling properties of the article, including acquiring, transporting, distributing and storing body fluids. As such, the absorbent core preferably does not include the topsheet or backsheet of the absorbent article.
• the absorbent core or absorbent member can further comprise fibers or fluff pulp (fibrous or fiber material); more specifically, non-absorbent-gelling fibers.
• Such fiber material can be used as a reinforcing or absorbent member in the absorbent core, improving fluid handling of the core, as well as serving as a co-absorbent with the absorbent polymers.
• the term "absorbent member” refers to the components of the absorbent core that typically provide one or more fluid handling properties, e.g., fluid acquisition, fluid distribution, fluid transportation, fluid storage, etc.
• the absorbent member can comprise the entire absorbent core or only a portion of the absorbent core, i.e., the absorbent core can comprise one or more absorbent members.
• any type of fiber material which is suitable for use in conventional absorbent products can be used in the absorbent core or absorbent member herein.
• fiber material include cellulose fibers, improved cellulose fibers, rayon, polypropylene, and polyester fibers such as polyethylene terephthalate (DACRON), hydrophilic nylon (HYDROFIL), and the like.
• DACRON polyethylene terephthalate
• HODROFIL hydrophilic nylon
• other fiber materials for use in the present invention in addition to some already discussed are hydrophilized hydrophobic fibers, such as surfactant-treated or silica-treated thermoplastic fibers derived, for example, from polyolefins such as polyethylene or polypropylene, polyacrylics, polyamides, polystyrenes, polyurethanes and the like.
• hydrophilized hydrophobic fibers which are in and of themselves not very absorbent and which, therefore, do not provide webs of sufficient absorbent capacity to be useful in conventional absorbent structures, are suitable for use in the absorbent core by virtue of their good wicking properties.
• the wicking propensity of the fibers is as important, if not more important, than the absorbent capacity of the fiber material itself due to the high rate of fluid uptake and lack of gel blocking properties of the absorbent core.
• Synthetic fibers are generally preferred for use herein as the fiber component of the absorbent core. More preferred are polyolefin fibers, preferably polyethylene fibers.
• cellulosic fiber materials which can be useful in certain absorbent cores or absorbent members herein are chemically stiffened cellulosic fibers.
• Preferred chemically stiffened cellulosic fibers are the stiffened, twisted, curled cellulosic fibers which can be produced by internally crosslinking cellulose fibers with a crosslinking agent.
• Suitable stiffened, twisted, curled cellulose fibers useful as the hydrophilic fiber materials herein are described in greater detail in U.S. Patent 4,888,093 (Dean et. al), issued December 19, 1989; U.S. Patent 4,889,596 (Herron et. al), issued December 26, 1989; U.S. Patent 4,889,596 (Schoggen et.
• a preferred embodiment of the disposable absorbent article is a diaper.
• the term "diaper” refers to a garment, generally worn by infants and incontinent persons, that is worn about the lower torso of the wearer.
• a preferred diaper configuration for a diaper comprising an absorbent core is described generally in U.S. Patent 3,860,003 (Buell), issued January 14, 1975.
• Alternatively preferred configurations for disposable diapers herein are also disclosed in U.S. Patent 4,808,178 (Aziz et. al), issued February 28, 1989; U.S. Patent 4,695,278 (Lawson), issued September 22, 1987; U.S. Patent 4,816,025 (Foreman), issued March 28, 1989; and U.S. Patent 5,151 ,092 (Buell et. al.), issued September 29, 1992.
• Preferred catamenial products comprise a formed-film, apertured topsheet as disclosed in U.S. Patent 4,285,343 (McNair), issued
• Preferred catamenial products can comprise wings, side flaps, and other structures and elements, as described in co-pending, commonly assigned U.S. application serial No. 984,071 , to Yasuko Morita, entitled “Absorbent Article Having Elasticized Side Flaps", filed November 30, 1992.
• FIG. 1 illustrates a preferred apparatus useful in the process of the present invention.
• the forming apparatus generally indicated as 1 , is composed of a particle applying unit 10, and a carrier layer apparatus 11.
• the particle applying unit 10 includes an absorbent gelling particles applying unit 12, a glue microfibers applying unit 16 and a polycationic polymer spray unit 17.
• the absorbent gelling particles are first loaded in, for example, a K- tron screw feeder 12 for continuously feeding absorbent gelling particles to Vibratory feeder 13 and then hopper 14. After absorbent gelling particles are carried away from the outlet of hopper 14 into an eductor 15, absorbent gelling particles leave the nozzle 16 as the first air stream 21 by about 50-psi air stream.
• the eductor 15 and the nozzle 16 concentrates the absorbent gelling particles into a constant flow in order to inject the absorbent gelling particles through the glue microfibers.
• the average diameter of the absorbent gelling particle is usually from about 10 microns to about 1 ,000 microns. While the absorbent gelling particles are predominately discontinuous, they generally have a length exceeding that normally associated with particles.
• the glue microfibers are extruded via glue gun 17 (J&M Co.) with rate between about 0.2 to about 2.0 Kgcm- 1 hr 1 as the second air stream 22.
• the glue microfibers extrusion thins out when guided through a second air stream.
• the temperature range is set up enough to solute and spray the glue microfibers.
• the air gap is preferably kept about 0.18 mm.
• the second air stream of glue microfibers is controlled to preferably deliver about 10 g/m2 basis weight of the resulting absorbent material and the operation range is preferably from about 3.0 gm/m ⁇ to about 50.0 gm/rr»2.
• the first air stream 21 is merged with the second air stream 22 to form an integrated air stream 23.
• the integrated air stream 23 is injected onto a carrier layer in mechanical direction, preferably about 70 meter/min.
• the injection rate of integrated air stream 23 preferably is about 1.0 m/sec which is adjusted to match the carrier unit's speed.
• a vacuum conveyor 19 is placed beneath the nozzle 16 and the glue gun 17. As the carrier layer 25 is run through the vacuum conveyor 19, the incoming integrated air stream 23 is attracted and firmly attached to the carrier layer 25.
• the absorbent gelling particles cover the center line of the carrier layer, preferably at least one half of the width.
• a third air stream containing pre-agitated polycationic polymer is located after laydown of the absorbent gelling particles applying unit 18.
• the third air stream is sprayed onto the absorbent gelling particles attached to the carrier layer and the polycationic polymer bonds to the absorbent gelling particles on the surface.
• the line speed is controlled preferably at about 8 gm/m2.
• a folding board 20 is placed adjacent to the polycationic polymer unit 18.
• the absorbent material comprising the absorbent gelling particles, the glue microfibers, the polycationic polymer and the carrier layer are folded to form an edge closed laminate structure of final width.
• the laminated product of absorbent material is wound at the end of the line.
• the present invention also provides a method for making the absorbent material.
• the method comprises (a) applying absorbent gelling particles comprising a WAHP onto a carrier layer; (b) applying glue microfibers onto the carrier layer; and (c) applying a polycationic polymer onto the absorbent gelling particles to form a bond between the absorbent gelling particles and the polycationic polymer; wherein the absorbent gelling particles adhere to the glue microfibers prior to the glue microfibers adhering to the carrier layer.
• the method further comprises the step of dispersing cellulose fibers into the absorbent gelling particles, wherein the glue microfibers act as an adhesive between the cellulose fibers and the absorbent gelling particles.
• the absorbent gelling particles are applied via a first air stream on a carrier layer.
• the glue microfibers are applied via the second air stream.
• the second air stream comprising glue microfibers preferably has a temperature of from about 100°C to about 400°C.
• the polycationic polymer is applied via the third air stream.
• the third air stream comprising the polycationic polymer is used as a solution having a concentration preferably from about 0.1% to about 10% by weight.
• the solution containing the polycationic polymer is then applied to a plurality of the absorbent gelling particles.
• at least two, preferably all, of the absorbent gelling particles have at least some portion covered with the solution.
• at least 70% of the surface area of the gelling particles are covered with the solution applied thereon.
• the solution can be applied using any of the various techniques and apparatus well known in the art which are suitable for applying a solution to a material including coating, dumping, pouring, dropping, spraying, atomizing, condensing, or immersing the solution onto the absorbent gelling particles.
• the polycationic polymer is applied, preferably greater than about 90% of the surface area of the gelling particles is covered with the solution.
• the method further comprises the step of heating the resulting material of step (c) at a temperature of from about 50°C to about 300°C so as to covalently bond the polycationic polymer to the WAHP of the absorbent gelling particles.
• the polycationic polymer are reacted with the absorbent gelling particles such that the polycationic polymer becomes covalently bonded to the absorbent gelling particles at the surface area of the absorbent gelling particles. More preferably, the covalent bonds are made between the surface-located carboxy groups of the absorbent gelling particles and the amino groups of the polycationic polymer.
• the absorbent articles comprising the absorbent material have more fluid permeable.
• the improved fluid permeability the spreading of, e.g., urine throughout the absorbent articles comprising the absorbent material is increased, and therefore the absorbent gelling particles fluid abso ⁇ tion efficiency can be raised.
• the present invention also relates to a method of making an absorbent material.
• the method comprises (a) forming a first air stream comprising absorbent gelling particles comprising a WAHP; (b) forming a second air stream comprising glue microfibers; (c) merging the second air stream with the first air stream to form an integrated air stream comprising a through mixture of the glue microfibers and the absorbent gelling particles; (d) directing the integrated air stream onto a carrier layer; (e) forming a third air stream comprising a polycationic polymer; and (f) directing the third air stream onto the carrier layer so the polycationic polymer bonds to the absorbent gelling particles.
• the method of forming an absorbent material comprises (a) forming a first air stream comprising absorbent gelling particles comprising a WAHP; (b) forming a second air stream comprising a polycationic polymer; (c) merging the second air stream with the first air stream to form an integrated air stream, wherein the polycationic polymer bonds to the absorbent gelling particles; (d) forming a third air stream comprising glue microfibers; (e) merging the integrated air stream with the third air stream to form a mixture air stream; and (f) directing the mixture air stream onto a carrier layer so the absorbent gelling particles bonded to the polycationic polymer adhere to the glue microfibers, and the glue microfibers adhere to the carrier layer.
• the second air stream is formed a temperature of at least about 400°C and about 50 psi air pressure at sonic velocity.
• the method comprises (a) applying polycationic polymer fibers comprising a polycationic polymer having a concentration of from about 80% to about 99% by weight onto absorbent gelling particles comprising a WAHP; and (b) applying the absorbent gelling particles onto a carrier layer; wherein the polycationic polymer fibers act as an adhesive between the absorbent gelling particles and the carrier layer.
• the polycationic polymer fiber has the molecular weight of at least about 70,000.
• the polycationic polymer fibers form a first air stream containing the polycationic polymer fibers and the absorbent gelling particles from the second air stream to form an integrated air stream containing a thorough mixture of the polycationic polymer fibers and the absorbent gelling particles.
• the method comprises (a) forming a first air stream containing polycationic polymer fibers; (b) forming a second air stream containing absorbent gelling particles comprising a WAHP; (c) merging the second air stream with the first air stream to form an integrated air stream, wherein the polycationic polymer fibers bond to the absorbent gelling particles; and (d) directing the integrated air stream onto a carrier layer so that the absorbent gelling particles bond to the polycationic polymer fibers on the carrier layer.
• the specific synthetic urine used in the test methods set forth herein is referred to as "Synthetic Urine".
• the Synthetic Urine is commonly known as Jayco SynUrine or Jayco Synthetic Urine and is available from Jayco Pharmaceuticals Company of Camp Hill, Pennsylvania.
• the formula for the Synthetic Urine is: 2.0 g/l of KCl; 2.0 g/l of Na 2 SO4; 0.85 g/l of (NH4)H2PO4; 0.15 g/l (NH4)H2PO4; 0.19 g/l of CaCl2 and 0.23 g/l of MgCl2. All of the chemicals are of reagent grade.
• the PH of the Synthetic Urine is in the range of 6.0 to 6.4.
• the standard burst test program measures load, deflection and energy at peak load, and fail load at test end.
• the purpose of this test is to evaluate the gram force of a absorbent-geiling-particle-contained laminate structure after subjecting to a constant loading of synthetic urine.
• Laminate samples with a dimension of 10 cm x 10 cm and of 310 gm/m2 absorbent gelling particle basis weights, typically weigh at 3.6 ⁇ 0.3 gm and are allowed to soak in 70mL of synthetic urine. Synthetic urine is fully absorbed by the absorbent-gelling-particle-contained laminate, with 20 times synthetic urine loading of its original weight.
• the sample holder is a plexi glass disk of 4.5-inch diameter and 0.125 inch of thickness, and with a hole of 0.75 inch diameter in the center of plexiglass.
• a stainless ball head of 0.25- inch diameter is used to puncture the samples.
• Gel volume of a WAHP is defined as its retention absorbent capacity after swollen in an excess of Jaycee Synthetic Urine. It provides a measure of the maximum absorbent capacity of the polymer under conditions of use where the pressures on the polymer are relatively low. Gel volume is determined by centrifuge capacity method described below by using the Jaycee Synthetic Urine. The gel volume is calculated on a dry-weight basis. The dry weight used in the gel volume calculation is determined by oven drying the WAHP at 105°C for three hours. All of the chemicals are of reagent grade. The pH of the Jaycee Synthetic Urine is in the range of 6.0 to 6.4.
• Heat-sealable tea-bag paper is cut into 6cm x 12cm, folded in half lengthwise and sealed close to the edge along two sides with a T-bar sealer to produce 6cm x 6cm tea bag squares.
• 0.200(+ 0.005) gm of a WAHP is transferred into a tea-bag, and the top of the bag is sealed at its edge. The top of an empty tea-bag is sealed and is used as a blank.
• Approximately 300ml of Jayco Synthetic Urine is poured into a 1,000ml beaker, and the tea- bag containing WAHP and the blank are submerged into the beaker. After being soaked for 30 minutes, the blank and the WAHP-filled tea bag are removed from the solution by using tongs.
• a centrifuge (H-122 type, Kokusan Enshinki Co. Ltd., Tokyo, Japan) with a direct read tachometer, electric timer is used for this measurement.
• the sample tea bags and the blank tea bags are positioned in the centrifuge basket and centrifuged at 110Orpm for three minutes.
• Gel volume is calculated as follows:
• Ws is the sample tea bag weight after centrifuge
• Wb is the blank tea bag weight after centrifuge
• Wo is the WAHP weight (0.200g). The average of at least two determinations should be reported.
• the Acquisition Speed and Rewetness which are the laminate production properties comprising this absorbent material made according to present invention, are evaluated in diapers.
• the typical diaper design includes airfilt as the acquisition layer and the laminate production as fluid storage core of at least 310 gm/m2 absorbent gelling particle basis weight.
• the acquisition speed and rewet measurements are performed with 0.30 psi external pressure in a flat configuration. After continuous loading of 200 mL synthetic urine, several pieces of filter papers are placed on the wet pad and allowed to soak for 30 min under 0.40 psi.
• the rewet values as measured from the weight increase of filter paper, are summed up from front, middle, to back part of diaper.
• a composite in accordance with the present invention is prepared on a process line for laminate production illustrated in FIG 1.
• Styrene-lsoprene-Styrene block copolymer (HL-1358-XZP) produced by H.B. Fuller Co. is used as a glue microfiber, and is heated and kept at least 350°C during laminate production process.
• L76lf produced by Nippon Shokubai Co. Ltd. is used as absorbent gelling particles, and has particle size distribution ranging from 300 ⁇ m to 600 ⁇ m.
• the Polyethyleneimine produced by Wako Chem Co. is used as a polycationic polymer, and is a 30% solid and has molecular weight of 70,000 Daltons.
• a tissue produced by Havix Company LTD is used as a wet laid tissue of 18 gms and has the tensile strength of 1.1 Kg/in in mechanical direction.
• L76lf is prepared in K-tron screw feeder.
• L76lf is loaded in a K-tron screw feeder for continuously feeding L76lf into a vibrator feeder and then a hopper.
• a compressed air stream is kept at 50 psi air pressure.
• L76lf is carried away from the outlet of the hopper into an educator and is combined with the compressed air stream, so as to provide a first air stream.
• Injection rate of the first air stream of L76lf is kept about 1.0 msec 1 which is adjusted to match the web line speed.
• Styrene-lsoprene-Styrene block copolymer (HL-1358-XZP), is prepared in the apparatus of glue gun (J&M Co.). HL-1358-XZP is extruded through glue gun at a rate between about 0.2 to about 2.0 Kgcr ⁇ r 1 hr 1 . The air gap of the glue gun is kept at about 0.18 mm, as the glue block-copolymer becomes thin fibers.
• the extruded HL-1358-XZP is combined with an air stream, so as to provide a second air stream.
• the second air stream is kept at a temperature of about 400°C and about 50 psi air pressure at about sonic velocity.
• the second air stream of HL-1358-XZP is controlled to deliver 10 g/m 2 basis weight of the laminate production.
• the operation range of the second air stream can be between about 3.0 gm/m2 and about 50.0 gm/m2.
• the first air stream of L76lf is subsequently injected through the second air stream of HL-1358-XZP, to form an integrated air stream, onto a vacuum conveyer.
• the vacuum conveyor is placed beneath the glue gun and the educator.
• a tissue is introduced to the vacuum conveyor at a typical speed of about 70 meter/min.. As the tissue is run over the vacuum conveyor, the incoming integrated air stream is attracted and firmly attached to the tissue.
• the tissue width is at least about 23 cm and a coverage width of the integrated air stream is at least about 9.50 cm.
• a polyethyleneimine is dissolved in distilled water at a concentration of from about 10 to about 20% by weight.
• a third air stream spray is forwarded an air pressure spray system (B1/8 BAU-SS+SUV 67-SS from Spraying System Co. of 0.5-1.2 Kg/cm 2 ) containing a pre-agitated solution of polyethyleneimine and water is located after the integrated air stream containing HL-1358-XZP and L76lf laydown.
• the speed-of spraying and the level of polyethyleneimine solution is controlled at 8 gm/m2, which is equal to about 2.0% by weight of the laminate production.
• a folding board is placed next to the third air stream spray of polyethyleneimine solution.
• Tissue, L76lf, HL-1358-XZP and polyethyleneimine are folded to form an edge closed laminate structure of about 10 cm final width.
• the laminate production is wound at the end of the line.
• the thickness of a formed laminate of about 310 gm/m2 absorbent gelling particle is about 1.3 mm.
• the laminate production properties comprising this absorbent material made according to this example are evaluated.
• the Tea Bag gel Volume is 61 gm and 33 g/g.
• the basic composition of sample is similar to Example 1, except no third air stream spray of polyethyleneimine additive is used.
• the laminate production properties comprising this absorbent material made according to this example are evaluated.
• the Wet Burst Strength and The Tea Bag gel Volume is 25 gm and 35 g/g.
• EXAMPLE 3 the basic composition of sample is similar to Example 1 , except as set forth below.
• URIC absorbent gelling particle is prepared in K-tron screw feeder for use in the first air stream.
• URIC absorbent gelling particle is an absorbent gelling particle having improved absorbent property by the absorbent property modification polymer, such as the polycationic polymer, bonded to the absorbent gelling particles.
• the laminate production properties comprising this absorbent material made according to this example are evaluated.
• the Wet Burst Strength and The Tea Bag gel Volume is 45 gm and 31 g/g.
• EXAMPLE 4 The basic composition of the sample is similar to Example 1 , except no second air stream of the thermoplastic polymeric microfiber and the third air stream spray of polyethyleneimine additive are used.
• the laminate production properties comprising this absorbent material made according to this example are evaluated.
• the Wet Burst Strength and The Tea Bag gel Volume is Ogm and 38g/g. Table-1. Tea bag gel volume and effects on wet strength by adding polyethyleneimine
• the acquisition speeds and rewet values are evaluated in a diaper.
• the diaper is made of by laminate production comprising the absorbent material according to above examples.
• the properties of the diaper are evaluated and presented in Table 2.
• Diapers of this invention show faster acquisition speeds at high urine loading, e.g., urine volume levels of at least 150mL than the Sample #2.
• the improved acquisition speeds are caused by faster fluid transportation among the well-bonded absorbent gelling particle particulate in the wet state.
• Sample #3 where absorbent gelling particle is treated with polyethyleneimine alternatively during absorbent gelling particle production process, the laminate shows even faster acquisition speeds.
• the degree of bonding forces in Sample #3 is higher than that of Sample #1.
• the rewet values of the invention maintain control diaper that is used to the absorbent material of no polycationic polymer.

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• 1996
  • 1996-04-24 JP JP10273696A patent/JP3720118B2/ja not_active Expired - Lifetime
• 1997
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