WO2012018746A1 - Ajout de produits ignifugeants endothermiques pour fournir des bandes de fibre de pâte de ph presque neutre - Google Patents

Ajout de produits ignifugeants endothermiques pour fournir des bandes de fibre de pâte de ph presque neutre Download PDF

Info

Publication number
WO2012018746A1
WO2012018746A1 PCT/US2011/046169 US2011046169W WO2012018746A1 WO 2012018746 A1 WO2012018746 A1 WO 2012018746A1 US 2011046169 W US2011046169 W US 2011046169W WO 2012018746 A1 WO2012018746 A1 WO 2012018746A1
Authority
WO
WIPO (PCT)
Prior art keywords
pulp fiber
fiber web
fire
fire retardants
endothermic
Prior art date
Application number
PCT/US2011/046169
Other languages
English (en)
Inventor
James E. Sealey
Brent Alan Fields
Original Assignee
International Paper Company
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from US13/081,759 external-priority patent/US8663427B2/en
Application filed by International Paper Company filed Critical International Paper Company
Publication of WO2012018746A1 publication Critical patent/WO2012018746A1/fr

Links

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/03Non-macromolecular organic compounds
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D5/00Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes
    • C09D5/18Fireproof paints including high temperature resistant paints
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/03Non-macromolecular organic compounds
    • D21H17/05Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
    • D21H17/07Nitrogen-containing compounds
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/63Inorganic compounds
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H21/00Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
    • D21H21/14Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
    • D21H21/22Agents rendering paper porous, absorbent or bulky
    • D21H21/24Surfactants
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H21/00Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
    • D21H21/14Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
    • D21H21/34Ignifugeants

Definitions

  • the present invention broadly relates to a process for treating a partially delignified pulp fiber web with an aqueous endothermic fire retardant solution having a pH of about 10 or less, wherein at least about 5% of the total amount of endothermic fire retardants are added at a point prior to when the pulp fiber web is formed to provide a treated pulp fiber web having a near neutral pH (i.e., from about 5 to about 9).
  • the present invention also broadly relates to a fire resistant pulp fiber web having a near neutral pH and comprising a partially delignified pulp fiber web; and a fire retardant component present in and/or on the pulp fiber web, wherein the fire retardant component comprises at least about 10% by weight of the fire retardant component of one or more endothermic fire retardants.
  • Fire resistant fibrous materials may be used in upholstery, cushions, mattress ticking, panel fabric, padding, bedding, insulation, materials for parts in devices or appliances, etc. Such materials may be formed from natural and/or synthetic fibers, and then treated with fire retardant chemicals which may include halogen-based and/or phosphorous- based chemicals, along with certain metal oxides such as ferric oxide, stannic oxide, antimony trioxide, titanium dioxide, etc. These fire resistant materials may be produced by depositing these metal oxides, within or on the fibers, for example, by the successive precipitation of ferric oxides and a mixture of tungstic acid and stannic oxide, by the successive deposition of antimony trioxide and stannic oxide, by the successive deposition of antimony trioxide and titanium dioxide.
  • a single processing bath may be used wherein a dispersion of a chlorinated hydrocarbon and finely divided antimony oxide is padded on the fabric material. Near the fibrous material's combustion temperature, the antimony oxide reacts with hydrogen chloride (generated by degradation of the chlorinated hydrocarbon) to form antimony oxychloride which acts to suppress the flame.
  • the fire retardant chemicals may be reacted with the cellulose or protein functionalities of the natural fibers in the material.
  • the cellulose in the fabric fibers may be esterified with diammonium hydrogen orthophosphate.
  • amidophosphates may be reacted with trimethylol melamine to form a thermosetting resin within the fibrous materials (see U.S. Pat. No. 2,832,745 (Hechenblefkner), issued April 29, 1958) or a phosphorous containing N-hydroxy-methyl amide and tetrakis(hydroxymethyl)phosphonium chloride may be incorporated in the fibrous materials by thermal induced pad curing (see U.S. Pat. No. 4,026,808 (Duffy), issued May 31, 1977).
  • Fire retardant chemicals may also be coated onto the fibrous materials.
  • U.S. Pat. No. 3,955,032 (Mischutin), issued May 4, 1976, which discloses a process using chlorinated-cyclopentadieno compounds and chlorobrominated-cyclpentadieno compounds, either alone or in combination with metal oxides, which are suspended in a latex medium and then cured to render natural and synthetic fibrous materials and blends of thereof fire retardant.
  • U.S. Pat. No. 3,955,032 Mischutin
  • an article comprising a fire resistant pulp fiber web having a pH of from about 5 to about 9, and comprising: an at least partially delignified pulp fiber web having a Kappa number of less than about 130; and a fire retardant component present in and/or on the pulp fiber web in an amount of at least about 20 lbs fire retardant component per ton of the pulp fiber web, the fire retardant component comprising: at least about 10% by weight of the fire retardant component of one or more endothermic fire retardants; and up to about 90% by weight of the fire retardant component of one or more other fire retardants; and one or more fire retardant distributing surfactants in an amount sufficient to distribute the fire retardant component in and/or on the pulp fiber web; wherein the fire retardant component is in an amount and is distributed in and/or on the pulp fiber web in a manner so that the fire resistant pulp fiber web passes one or more of the following tests: the UL 94 HBF test, the Horizontal Burn Through test,
  • FIG. 1 is a schematic diagram which shows an illustrative process for providing a fire resistant pulp fiber web having a near neutral pH according to an embodiment of the present invention.
  • FIG. 2 is side sectional view of an air-laid fibrous structure which comprises a fire resistant pulp fiber web according to an embodiment of the present invention as the respective outer layers of the air-laid fibrous core of the structure.
  • directional terms such as “top,” “bottom,” “upper,” “lower,” “side,” “front,” “frontal,” “forward,” “rear,” “rearward,” “back,” “trailing,” “above”, “below,” “left,” “right,” “horizontal,” “vertical,” “upward,” “downward,” etc. are merely used for convenience in describing the various embodiments of the present invention.
  • the embodiments shown in FIGS. 1 through 2 may be flipped over, rotated by 90° in any direction, etc.
  • pulp fibers refers to a wood pulp fibers which may be softwood pulp fibers, hardwood pulp fibers or a mixture of softwood and hardwood pulp fibers.
  • the pulp fiber web may be in the form of, for example, sheets, strips, pieces, batts/battings, blankets, etc., which may be in the form of a continuous roll, a discrete sheet, etc.
  • flufluff pulp refers to pulp fibers which may be comminuted to provide an air-laid fibrous structure. Fluff pulps may also be referred to as "fluffy pulp,” or “comminution pulp.” Some illustrative examples of commercially available fluff pulp may include one or more of: RW SupersoftTM, Supersoft LTM, RW Supersoft PlusTM, GT Supersoft PlusTM, RW Fluff LITETM, RW Fluff 110TM, RW Fluff 150TM, RW Fluff 160TM, GP 4881TM, GT PulpTM, RW SSPTM, GP 4825TM, etc.
  • Pulp fiber web refers to a fibrous cellulosic matrix comprising wood pulp fibers. Pulp fiber webs may be in the form of, for example, sheets, strips, pieces, batts/battings, blankets, etc., which may be in the form of a continuous roll, a discrete sheet, etc.
  • softwood pulp fibers refers to fibrous pulps derived from the woody substance of coniferous trees (gymnosperms) such as varieties of fir, spruce, pine, etc., for example, loblolly pine, slash pine, Colorado spruce, balsam fir, Douglas fir, jack pine, radiata pine, white spruce, lodgepole pine, redwood, etc. North American southern softwoods and northern softwoods may be used to provide softwood fibers, as well as softwoods from other regions of the world.
  • hardwood pulp fibers refers to fibrous pulps derived from the woody substance of deciduous trees (angiosperms) such as birch, oak, beech, maple, eucalyptus, poplars, etc.
  • the term "at least partially delignified pulp fibers” refers to pulp fibers which have been subjected to chemical and/or mechanical processing (e.g., kraft pulping processes) to at least partially remove lignin from the pulp fibers so that the pulp fibers have a Kappa number (also referred to as "K number") of about 130 or less, such as about 50 or less (e.g., about 35 or less). Kappa numbers may be determined by the ISO 302:2004 method. See G. A.
  • basis weight refers to the grammage of the pulp fibers, pulp web, etc., as determined by TAPPI test T410. See G. A. Smook, Handbook for Pulp and Paper Technologists (2 nd Edition, 1992), page 342, Table 22- 11 , the entire contents and disclosure of which is herein incorporated by reference, which describes the physical test for measuring basis weight.
  • Basis weight variability refers to the statistical variation from the target basis weight value. For example, if the target basis weight is 750 gsm and the area of the sample being evaluated is 755 gsm, the basis weight variability would be 0.06%. Basis weight variability may be measured in the machine direction (MD) or the cross machine direction (CD).
  • the term "caliper,” refers to the thickness of a web (e.g., pulp fiber web) in mils, as determined by measuring the distance between smooth, flat plates at a defined pressure.
  • moisture content refers to the amount of water present in the pulp fiber web as measured by TAPPI test T210 cm-03.
  • the term "fiberization energy,” refers to the amount of energy (in kJ/kg) required to comminute (e.g., defiberize, disintegrate, shred, fragment, etc.) a pulp fiber web to individualized pulp fibers by using a hammermill (such as a Kamas Type H 01 Laboratory Defribrator manufactured by Kamas Industri AB).
  • the energy required to comminute the pulp web is normally measured and displayed by the hammermill in, for example, watt hours (wH).
  • the term "pulp filler” refers commonly to mineral products (e.g., calcium carbonate, kaolin clay, calcium sulfate hemihydrate, calcium sulfate dehydrate, chalk, etc.) which may be used in pulp fiber web making to reduce materials cost per unit mass of the web, increase opacity, etc. These mineral products may be finely divided, for example, in the size range of from about 0.5 to about 5 microns.
  • pulp pigment refers to a material (e.g., a finely divided particulate matter) which may be used or may be intended to be used to affect optical properties of the pulp fiber web.
  • Pulp pigments may include one or more of: calcium carbonate, kaolin clay, calcined clay, modified calcined clay, aluminum trihydrate, titanium dioxide, talc, plastic pigment, amorphous silica, aluminum silicate, zeolite, aluminum oxide, colloidal silica, colloidal alumina slurry, etc.
  • calcium carbonate refers various calcium carbonates which may be used as pulp pigments, such as precipitated calcium carbonate (PCC), ground calcium carbonate (GCC), modified PCC and/or GCC, etc.
  • the term "precipitated calcium carbonate (PCC)” refers to a calcium carbonate which may be manufactured by a precipitation reaction and which may used as a pulp pigment.
  • PCC may comprise almost entirely of the calcite crystal form of CaC0 3 .
  • the calcite crystal may have several different macroscopic shapes depending on the conditions of production.
  • Precipitated calcium carbonates may be prepared by the carbonation, with carbon dioxide (CO 2 ) gas, of an aqueous slurry of calcium hydroxide ("milk of lime”).
  • the starting material for obtaining PCC may comprise limestone, but may also be calcined (i.e., heated to drive off CO 2 ), thus producing burnt lime, CaO.
  • PCC may be not continuously agitated or stored for many days, it may be necessary to add more than a trace of such anionic dispersants as polyphosphates.
  • Wet PCC may have a weak cationic colloidal charge.
  • dried PCC may be similar to most ground CaCC ⁇ products in having a negative charge, depending on whether dispersants have been used.
  • the calcium carbonate may be precipitated from an aqueous solution in three different crystal forms: the vaterite form which is thermodynamically unstable, the calcite form which is the most stable and the most abundant in nature, and the aragonite form which is metastable under normal ambient conditions of temperature and pressure, but which may convert to calcite at elevated temperatures.
  • the aragonite form has an orthorhombic shape that crystallizes as long, thin needles that may be either aggregated or unaggregated.
  • the calcite form may exist in several different shapes of which the most commonly found are the rhombohedral shape having crystals that may be either aggregated or unaggregated and the scalenohedral shape having crystals that are generally unaggregated.
  • pulp binders refers to a binder agent for pulp fibers which may be used to improve the binding strength of the pulp fibers in the web.
  • Suitable pulp binders may include one or more synthetic or naturally occurring polymers (or a combination of different polymers), for example, a polyvinyl alcohol (PVOH), polyacrylamide, modified polyacrylamide, starch binders, proteinaceous adhesives such as, for example, casein or soy proteins, etc; polymer latexes such as styrene butadiene rubber latexes, acrylic polymer latexes, polyvinyl acetate latexes, styrene acrylic copolymer latexes, wet strength resins such as Amres (a Kymene type), Bayer Parez, etc, polychloride emulsions, polyols, polyol carbonyl adducts, ethanedial/polyol condensates, poly
  • PVOH polyvinyl alcohol
  • air-laid fibrous structure refers to a nonwoven, bulky, porous, soft, fibrous structure obtained by air-laying comminuted pulp fiber webs and/or pulp fibers, and which may optionally comprise synthetic fibers such as bicomponent fibers.
  • Air-laid fibrous structures may include air-laid fibrous cores, air-laid fibrous layers, etc
  • the term “comminuting” refers to defibrizing, disintegrating, shredding, fragmenting, etc, a pulp fiber web and/or pulp fibers to provide an air-laid fibrous structure.
  • synthetic fibers refers to fibers other than wood pulp fibers (e.g., other than pulp fibers) and which be made from, for example, cellulose acetate, acrylic, polyamides (such as, for example, Nylon 6, Nylon 6/6, Nylon 12, polyaspartic acid, polyglutamic acid, etc.), polyamines, polyimides, polyamides, polyacrylics (such as, for example, polyacrylamide, polyacrylonitrile, esters of methacrylic acid and acrylic acid, etc.), polycarbonates (such as, for example, polybisphenol A carbonate, polypropylene carbonate, etc.), polydienes (such as, for example, polybutadiene, polyisoprene, polynorbomene, etc.), polyepoxides, polyesters (such as, for example, polyethylene terephthalate, polybutylene terephthalate, polytrimethylene terephthalate, polycaprol
  • bicomponent fibers refers to fibers comprising a core and sheath configuration.
  • the core and sheath portions of bicomponent fibers may be made from various polymers.
  • bicomponent fibers may comprise a PE (polyethylene) or modified PE sheath which may have a PET (polyethylene terephthalate) or PP (polypropylene) core.
  • the bicomponent fiber may have a core made of polyester and sheath made of polyethylene.
  • Various geometric configurations may be used for the bicomponent fiber, including concentric, eccentric, islands-in-the-sea, side-by-side, etc.
  • the relative weight percentages and/or proportions of the core and sheath portions of the bicomponent fiber may also be varied.
  • trivalent metal refers to a metal which may have a positive charge of three (e.g., boron, zinc, an iron (ferric), cobalt, nickel, aluminum, manganese, chromium, etc), and may include combinations of one or more of these trivalent metals.
  • Sources of trivalent metals may include one or more of organic or inorganic salts, for example, from one or more of the following anions: acetate, lactate, EDTA, halide, chloride, bromide, nitrate, chlorate, perchlorate, sulfate, acetate, carboxylate, hydroxide, nitrite, etc.
  • the salt may be a simple salt, wherein the trivalent metal forms a salt with one or more of the same anion, or a complex salt, wherein the trivalent metal forms a salt with two or more different anions.
  • the salt may be aluminum chloride, aluminum carbonate, aluminum sulfate, alum (e.g., aluminum ammonium sulfate, aluminum potassium sulfate, aluminum sulfate, etc.), etc.
  • debonder surfactant refers to surfactants which are useful in the treatment of pulp fibers to reduce inter-fiber bonding.
  • Suitable debonder surfactants may include one or more of: cationic surfactants or nonionic surfactants, such as linear or branched monoalkyl amines, linear or branched dialkyl amines, linear or branched tertiary alkyl amines, linear or branched quaternary alkyl amines, linear or branched, saturated or unsaturated hydrocarbon surfactants, fatty acid amides, fatty acid amide quaternary ammonium salts, dialkyl dimethyl quaternary ammonium salts, dialkylimidazolinium quaternary ammonium salts, dialkyl ester quaternary ammonium salts, triethanolamine-ditallow fatty acids, fatty acid ester of ethoxylated primary amines, ethoxyl
  • fire resistant article refers to an article (e.g., pulp fiber web, air-laid fibrous structure, etc.) which has been treated with a fire retardant in an amount sufficient to make the treated material resistant to fire, flame, burning, etc., as determined by certain fire resistance test(s), such as the UL 94 test, the Horizontal Burn Through method test, the ASTM D 5132-04 test, etc.
  • fire resistance test refers to a test which measures the fire resistant characteristics, properties, etc., of an article, a material, etc. These tests may include the UL 94 test, the Horizontal Burn Through method test, the ASTM D 5132-04 test, etc.
  • the term "UL 94 HBF test” (also known as the "Horizontal Burning Foamed Material Test”) refers to a fire resistance test (authored by Underwriters Laboratories) which is used to measure the flammability of articles, such as foamed plastic materials, used in parts in devices or appliances, etc.
  • the UL HBF 94 test measures the ability of such articles to prevent flame propagation.
  • the UL HBF 94 test may be conducted on specimens which are 150 ( ⁇ 5) mm long x 50 ( ⁇ 1) mm wide and having a minimum/maximum covering the thickness range of materials to be tested. See pages 27-33 and FIG.
  • the term "Horizontal Burn Through test” refers to fire resistance test which measures the ability of the article being tested to resist burning by forming, for example, a stable char that insulates the remaining uncharred material of the article from heat. Articles, materials, etc., are considered to have passed the Horizontal Burn Through test is there is no burn through after the specimen being tested is exposed to a flame for at least 15 minutes.
  • the Horizontal Burn Through test may be conducted on specimens which are 10 cm x 10 cm square and which are then centrally positioned on a 6.35 mm (0.25 inch) thick square steel plate approximately 15 cm.times.15 cm (6.times.6 inches).
  • the plate has a circular hole of a diameter of 50.8 mm (or 2 inches) machined concentrically through the center portion.
  • the specimen is mounted level over a Bunsen burner which is fed with a natural gas flow rate of 415 ml/min. so that when moved under the specimen, the tip of the flame just touches the underside of the barrier in the center of the hole, the flame being held in contact with the specimen for a total of 15 minutes after which the condition of the specimen is assessed for burn through.
  • Specimen preparation for specimens used in carrying out the Horizontal Burn Through test method according to the present invention are described in the section below entitled "Fire Resistant Test Specimen Preparation.”
  • ASTM D 5132-04 test also known as the "Horizontal Burning Rate of Polymeric Materials Used in Occupant Compartments of Motor Vehicles” test
  • This test method employs a test specimen having test dimensions of 100 ( ⁇ 5) mm wide by 300 mm in length with a thickness of up to 13 mm which is mounted on a U-shaped metal frame.
  • the test specimen is ignited by using a 38-mm flame from an appropriate burner, with burning rate of the material then being determined.
  • the rate of burning is calculated by measuring the distance, D, (in mm.) the flame travels on the test specimen, divided by the time, T, (in seconds) required to travel the distance, D, multiplied by 60.
  • fire retardant refers to one or more substances (e.g., composition, compound, etc.) which are able to reduce, impart resistance to, etc., the flammability, the ability to burn, etc., of a material, article, etc.
  • Fire retardants may include one or more endothermic fire retardants, and optionally one or more other (nonendothermic) fire retardants.
  • Endothermic fire retardant refers to fire retardants which absorb heat when exposed to a source of flame.
  • Endothermic fire retardants may include one or more of: boron-containing fire retardants such as borate fire retardants (e.g., boric acid, borax, sodium tetraborate decahydrate, zinc borate, etc.), borosilicate (i.e., condensates of boron oxides and silica with other metal oxides, for example sodium oxide and aluminum oxide) fire retardants (e.g., may include borosilicates used in making glass, etc.), other substances which retain water or water vapor at room temperature such as alum (aluminum ammonium sulfate), talc (magnesium silicate), aluminum hydroxide (as known as alumina trihydrate), magnesium hydroxide (also known as magnesium dihydroxide), mixtures (e.g., equal mixtures) of huntite (calcium magnesium carbonate
  • borate fire retardants e.g.,
  • other fire retardant refers to fire retardants which are not endothermic fire retardants.
  • Other fire retardants may include one or more of phosphorous fire retardants, halogenated hydrocarbon fire retardants, metal oxide fire retardants, etc.
  • these other fire retardants may comprise a mixture, blend, etc., of one or more phosphorous fire retardants, one or more halogenated hydrocarbon fire retardants, and one or more metal oxide fire retardants.
  • phosphorous fire retardant refers to a fire retardant substance, compound, molecule, etc., which comprises one or more phosphorous atoms.
  • Phosphorous fire retardants may include one or more of: phosphates, such as sodium phosphates, ammonium phosphates, sodium polyphosphates, ammonium polyphosphates, melamine phosphates, ethylenediamine phosphates etc.; red phosphorus; metal hypophosphites, such as aluminum hypophosphite and calcium hypophosphite; phosphate esters; etc.
  • the phosphorus fire retardant disperses on and/or in the cellulosic fibers and may, in some embodiments (e.g., ammonium phosphates) form a bond (i.e., crosslink) to cellulose which forms a stable char during exposure to the flame.
  • Some proprietary phosphorous fire retardants may include, for example: SpartanTM AR 295 Flame Retardant from Spartan Flame Retardants Inc. of Crystal Lake, III, include both organic and inorganic constituents, GLO-TARD FFR2, which is an ammonium polyphosphate fire retardant from GLO-TEX International, Inc.
  • Fire Retard 3496 which is a phosphate ester supplied by Manufacturers Chemicals, L.P. of Cleveland, Tenn, Flovan CGN, a multi-purpose phosphate-based flame retardant supplied by Huntsman (Salt Lake City, Utah); SPARTANTM AR 295, a diammonium phosphate based flame retardant from Spartan Flame Retardants, Inc. (Crystal Lake, 111.), FRP 12TM, FR 165TM, and FR 8500TM supplied by Cellulose Solutions, LLC (Daphne, Alabama), etc.
  • halogenated organic fire retardant refers to a halogenated organic compound which alone, or in combination with other substances, compounds, molecules, etc., are capable of functioning as a fire retardant.
  • Halogenated organic fire retardants may include one or more of: halogenated (e.g., chlorinated, brominated, etc.) hydrocarbons, such as halogenated aliphatics (e.g., haloalkanes), halogenated aromatics, etc.
  • Halogenated organic fire retardants may include chloroparaffins, Dechorane Plus (a chlorine-containing halogenated fire retardant), decabromodiphenyl oxide, tetradecabromodiphenoxybenzene, ethylenebispentabromobenzene (EBPB); tetrabromobisphenol A (TBBA), tetrabromobisphenol A bis-hexabromocyclododecane, ethylenebis-(tetrabromophthalimide). These halogenated organic fire retardants may work by eliminating oxygen from the burn zone which quenches, extinguishes, smothers, puts out, etc., the flame.
  • EBPB ethylenebispentabromobenzene
  • TBBA tetrabromobisphenol A
  • tetrabromobisphenol A bis-hexabromocyclododecane ethylenebis-(tetrabromophthalimide).
  • metal oxide fire retardant refers to metal oxides which alone, or in combination with other substances, are capable of functioning as a fire retardant.
  • Metal oxide fire retardants may include one or more of: aluminum oxide (alumina), antimony trioxide, ferric oxide, titanium dioxide, stannic oxide, etc.
  • fire retardant distributing surfactant refers to surfactants which function to distribute, disperse, etc., the fire retardant over, through, etc., the fibrous matrix of the pulp fiber web.
  • Suitable fire retardant distributing surfactants may be ionic or nonionic, have a rheology which permits the surfactant to be dispersed on and/or through the pulp fiber web being treated with the fire retardant component, carries the fire retardant component on and/or through the pulp fiber web (i.e., the fire retardant component is not fully dissolved in the surfactant), enables or at least does not inhibit crosslinking between fire retardants (e.g., crosslinkable phosphorous fire retardants such as the ammonium phosphates) in the fire retardant component and the cellulosic fibers in the pulp fiber web, etc.
  • fire retardants e.g., crosslinkable phosphorous fire retardants such as the ammonium phosphates
  • Suitable fire retardant distributing surfactants may include one or more of: alkoxylated alcohols/alcohol alkoxylates (e.g., BASF's Plurafac® alcohol alkoxylates) which may include ethoxylated alcohols (e.g., Eka Chemical's F60 surfactant, etc.
  • alkoxylated alcohols/alcohol alkoxylates e.g., BASF's Plurafac® alcohol alkoxylates
  • ethoxylated alcohols e.g., Eka Chemical's F60 surfactant, etc.
  • Suitable ethoxylated alcohols for use as fire retardant distributing surfactants may comprise from about 1 to about 30 ethylene oxide (EO) units, for example, from about 4 to about 25 EO units, with an alcohol carbon chain length of from about 6 to about 30 carbon atoms, for example, from about 6 to about 22 carbon atoms, such as from about 12 to about 18 carbon atoms (e.g., from about 16 to 18 carbon atoms).
  • EO ethylene oxide
  • near neutral pH refers to a pH in the range of from about 5 to about 9, for example, from about 6 to about 8, such as about 7.
  • pH adjusting agent refers a composition, compound, etc., which may be included to raise or lower the pH of the endothermic fire retardant solution, the pulp slurry to which the endothermic fire retardant solution, as well as other fire retardants, fire retardant distributing surfactants, etc., are added, etc., to provide a treated pulp fiber web having a near neutral pH.
  • Suitable pH adjusting agents may include acids or bases, buffering agents which may be may be weak acids or weak bases (i.e., proton acceptors) and may include one or more of: trivalent metal ammonium sulfates, such as aluminum ammonium sulfate (e.g., alum), ferric ammonium sulfate, chromium ammonium sulfate, cobalt ammonium sulfate, manganese ammonium sulfate, nickel ammonium sulfate, etc., other ammonium salts which function as weak bases such as ammonium sulfate, etc.
  • endothermic fire retardants by themselves may also function as the pH adjusting (e.g., buffering) agent.
  • the term "at a point prior to when the pulp fiber web is formed” refers any point any point prior to when the pulp fiber web is formed (e.g., prior to forming the pulp fiber web on a forming wire) and may include the forming the pulp slurry in the blend chest, after the pulp slurry is formed by the blend chest and prior to transfer to the head box, after transfer of the pulp slurry to the head box but prior to depositing a furnish from the headbox, e.g., prior to depositing on the a forming wire, etc.
  • the term "at a point after the pulp fiber web is formed and prior to drying of the fibrous web” refers any point any point after the pulp fiber web is formed and prior to the point when the pulp fiber web is dried, and may include forming pulp fiber web on a forming wire, passing the pulp fiber web through a size press, passing the pulp fiber web past or through a sprayer or other applicating device (e.g., coater), etc.
  • the term "at a point after drying of the fibrous web” refers any point any point after the pulp fiber web is dried and up to and including when an air-laid fibrous structure is constructed from the dried pulp fiber web.
  • solids basis refers to the weight percentage of each of the respective solid materials (e.g., fire retardants, surfactants, dispersants, etc.) present in the pulp fibers, web, composition, etc., in the absence of any liquids (e.g., water). Unless otherwise specified, all percentages given herein for the solid materials, compounds, substances, etc., are on a solids basis.
  • solids content refers to the percentage of non-volatile, non-liquid components (by weight) that are present in the pulp fibers, web, composition,, etc.
  • grams is used in the conventional sense of referring to grams per square meter.
  • the term "mil(s)" is used in the conventional sense of referring to thousandths of an inch.
  • liquid refers to a non-gaseous fluid composition, compound, material, etc., which may be readily flowable at the temperature of use (e.g., room temperature) with little or no tendency to disperse and with a relatively high compressibility.
  • room temperature refers to the commonly accepted meaning of room temperature, i.e., an ambient temperature of 20° to 25°C.
  • optical brightness refers to the diffuse reflectivity of the pulp fiber web/pulp fibers, for example, at a mean wavelength of light of 457 nm.
  • optical brightness of pulp fiber webs may be measured in terms of ISO Brightness which measures brightness using, for example, an ELREPHO Datacolor 450 spectrophotometer, according to test method ISO 2470-1, using a C illuminant with UV included.
  • optical brightener agent refers to certain fluorescent materials which may increase the brightness (e.g., white appearance) of pulp fiber web surfaces by absorbing the invisible portion of the light spectrum (e.g., from about 340 to about 370 nm) and converting this energy into the longer- wavelength visible portion of the light spectrum (e.g., from about 420 to about 470 nm).
  • the OBA converts invisible ultraviolet light and re-emits that converted light into blue to blue-violet light region through fluorescence.
  • OBAs may also be referred to interchangeably as fluorescent whitening agents (FWAs) or fluorescent brightening agents (FBAs).
  • OBAs are often for the purpose of compensating for a yellow tint or cast of paper pulps which have, for example, been bleached to moderate levels.
  • This yellow tint or cast is produced by the absorption of short-wavelength light (violet-to-blue) by the pulp fiber webs.
  • this short-wavelength light that causes the yellow tint or cast is partially replaced, thus improving the brightness and whiteness of the pulp fiber web.
  • OBAs are desirably optically colorless when present on the pulp fiber web surface, and do not absorb light in the visible part of the spectrum.
  • OBAs may be anionic, cationic, anionic (neutral), etc., and may include one or more of: stilbenes, such as 4,4 '-bis- (triazinylamino)-stilbene-2,2'-disulfonic acids, 4,4'-bis-(triazol-2-yl)stilbene-2,2'-disulfonic acids, 4,4'-dibenzofuranyl-biphenyls, 4,4'-(diphenyl)-stilbenes, 4,4'-distyryl-biphenyls, 4- phenyl-4'-benzoxazolyl-stilbenes, stilbenzyl-naphthotriazoles, 4-styryl-stilbenes, bis- (benzoxazol-2-yl) derivatives, bis-(benzimidazol-2-yl) derivatives, coumarins, pyrazolines, naphthalimides, triazinyl-pyrenes, 2-styryl
  • these OBAs may comprise, for example, one or more stilbene-based sulfonates (e.g., disulfonates, tetrasulfonates, or hexasulfonates) which may comprise one or two stilbene residues.
  • stilbene-based sulfonates e.g., disulfonates, tetrasulfonates, or hexasulfonates
  • Illustrative examples of such anionic stilbene-based sulfonates may include 1,3,5-triazinyl derivatives of 4,4'-diaminostilbene-2,2'-disulphonic acid (including salts thereof), and in particular the bistriazinyl derivatives (e.g., 4,4-bis(triazine-2- ylamino)stilbene-2,2'-disulphonic acid), the disodium salt of distyrlbiphenyl disulfonic acid, the disodium salt of 4,4'-di-triazinylamino-2,2'-di-sulfostilbene, etc.
  • the bistriazinyl derivatives e.g., 4,4-bis(triazine-2- ylamino)stilbene-2,2'-disulphonic acid
  • disodium salt of distyrlbiphenyl disulfonic acid e.g., 4,4-bis(triazine-2- ylamino
  • disulfonate, tetrasulfonate and hexasulfonate stilbene-based OBAs may also be obtained, for example, from Ciba Geigy under the trademark TINOPAL®, from Clariant under the trademark LEUCOPHOR®, from Lanxess under the trademark BLANKOPHOR®, and from 3V under the trademark OPTIBLANC®.
  • the term "treating" with reference to the fire retardant compositions may include adding, depositing, applying, spraying, coating, daubing, spreading, wiping, dabbing, dipping, etc., to the pulp fibers, pulp fiber web, air-laid fibrous structure, etc.
  • the term "applicator” refers to a device, equipment, machine, etc., which may be used to treat, apply, coat, etc., one or more sides or surfaces of a pulp fiber web, air-laid fibrous structure, etc., with the fire retardant composition.
  • Applicators may include air-knife coaters, rod coaters, blade coaters, size presses, etc. See G. A. Smook, Handbook for Pulp and Paper Technologists (2 nd Edition, 1992), pages 289-92, the entire contents and disclosure of which is herein incorporated by reference, for a general description of coaters that may be useful herein.
  • Size presses may include a puddle size press, a metering size press, etc. See G. A. Smook, Handbook for Pulp and Paper Technologists (2 nd Edition, 1992), pages 283-85, the entire contents and disclosure of which is herein incorporated by reference, for a general description of size presses that may be useful herein.
  • flooded nip size press refers to a size press having a flooded nip (pond), also referred to as a "puddle size press.”
  • Flooded nip size presses may include vertical size presses, horizontal size presses, etc.
  • metering size press refers to a size press that includes a component for spreading, metering, etc., deposited, applied, etc., the fire retardant composition on a pulp fiber web, air-laid fibrous structure, etc.
  • Metering size presses may include a rod metering size press, a gated roll metering size press, a doctor blade metering size press, etc.
  • the term “rod metering size press” refers to metering size press that uses a rod to spread, meter, etc., the fire retardant composition on a pulp fiber web, air-laid fibrous structure, etc.
  • the rod may be stationary or movable relative to the web.
  • the term “gated roll metering size press” refers to a metering size press that may use a gated roll, transfer roll, soft applicator roll, etc.
  • the gated roll, transfer roll, soft applicator roll, etc. may be stationery relative to the web, may rotate relative to the web, etc.
  • doctor blade metering size press refers to a metering press which may use a doctor blade to spread, meter, etc., the fire retardant composition on a pulp fiber web, air-laid fibrous structure, etc.
  • Embodiments of the process of the present invention comprise providing an at least partially delignified pulp fiber web having a Kappa number of less than about 130 (e.g., less than about 50).
  • the pulp fiber web may comprise at least about 50% (for example, from about 50 to about 70%, such as from about 70 to about 80%) softwood pulp fibers and up to about 50% (for example, from about 30 to about 50%, such as from about 20 to about 30%) hardwood pulp fibers.
  • Embodiments of the process of the present invention also comprise treating the pulp fiber web with an aqueous endothermic fire retardant solution having a pH of about 10 or less (e.g., a pH of from about 5 to about 9, such as from about 6 to about 8) and comprising at least about 10% (e.g., from about 10 to about 70% based on the total solids in the solution) of one or more endothermic fire retardants.
  • an aqueous endothermic fire retardant solution having a pH of about 10 or less (e.g., a pH of from about 5 to about 9, such as from about 6 to about 8) and comprising at least about 10% (e.g., from about 10 to about 70% based on the total solids in the solution) of one or more endothermic fire retardants.
  • the pulp fiber web is treated with a total amount of endothermic fire retardants of at least about 20 lbs (e.g., from about 20 to about 250 lbs) of endothermic fire retardants per ton of the pulp fiber web, wherein at least about 5% (e.g., an initial portion of from about 5 to about 33%) of the total amount of endothermic fire retardants are added at a point prior to when the pulp fiber web is formed. In some embodiments, the remaining portion of from about 67 to about 95% of the total amount of endothermic fire retardants are added at a point after the pulp fiber web is formed, for example, at a point after the pulp fiber web is dried.
  • the pulp fiber web may also be treated with one or more other fire retardants in an amount up to about 90% (e.g., from about 10 to about 90%) of the total fire retardants used to treat the pulp fiber web); and optionally one or more fire retardant distributing surfactants in an amount sufficient to distribute the other fire retardants in and/or on the pulp fiber web.
  • Treatment with the endothermic fire retardant solution provides a treated pulp fiber web having a near neutral pH (e.g., a pH of from about 5 to about 9, such as from about 6 to about 8).
  • Providing a fire retardant treated pulp fiber web having a near neutral pH enables the resultant web, for example, to be to provide an air-laid fibrous structure, avoids/minimizes corrosion of metal components the retardant treated pulp fiber web comes into contact with, avoids/minimizes skin irritation, etc.
  • the other optional fire retardants and optional fire retardant distributing surfactants are added to the pulp fiber web at a point after the pulp fiber web is formed and prior to drying of the fibrous web.
  • any remaining endothermic fire retardant is added (e.g., sprayed, dosed, etc.) on the pulp fiber web at a point after drying of the fibrous web.
  • one type of endothermic fire retardant e.g., aluminum ammonium sulfate or alum
  • a different type of endothermic fire retardant e.g., ammonium phosphate or borosilicate
  • ammonium phosphate or borosilicate is added (e.g., sprayed, dosed, etc.) on the pulp fiber web at a point after drying of the fibrous web.
  • Embodiments of the fire resistant pulp fiber webs of the present invention having a near neutral pH comprise: an at least partially delignified pulp fiber web having a Kappa number as previously described; a fire retardant component present in and/or on the pulp fiber web in an amount of at least about 20 lbs (e.g., from about 20 to about 250 lbs) of fire retardant component per ton of the pulp fiber web; and one or more fire retardant distributing surfactants in an amount sufficient (e.g., from about 1 to about 10 lbs per ton of the pulp fiber web) to distribute the fire retardant component in and/or on the pulp fiber web.
  • the fire retardant component comprises at least about 10% (e.g., from about 10 to about 90%, such as from about 40 to about 60%) by weight of the fire retardant component of one or more endothermic fire retardants; and up to about 90% (e.g., from about 10 to about 90%, such as from about 40 to about 60%) by weight of the fire retardant component of one or more other fire retardants.
  • the fire retardant component is also present in an amount and is distributed in and/or on the pulp fiber web in a manner so that the fire resistant pulp fiber web passes one or more of the following tests: the UL 94 HBF test, the Horizontal Burn Through test, or the ASTM D 5132-04 test.
  • Embodiments of the fire resistant pulp fiber webs of the present invention may also be used in air-laid fibrous structures which may comprise: an air-laid fibrous core having an upper surface and a lower surface; a first fire resistant outer layer positioned over the upper surface; and a second fire resistant outer layer positioned under the lower surface.
  • the air- laid fibrous core may comprise: from about 50 to about 97% (e.g., from about 80 to about 95%) by weight of the core of comminuted pulp fibers; and from about 3 to about 50% (e.g., from about 5 to about 20%) by weight of the core of bicomponent fibers.
  • Each of the upper and lower outer layers may comprise: from about 50 to about 95% (e.g., from about 80 to about 95%) by weight of the core of comminuted fire resistant pulp fiber fibers according to embodiments of the present invention; and from about 5 to about 50% (e.g., from about 5 to about 20%) by weight of the core of bicomponent fibers, and may comprise the same proportions by weight of fire resistant pulp fiber fibers and bicomponent fibers, or may comprise different proportions by weight of fire resistant pulp fiber fibers and bicomponent fibers.
  • These outer layers may also optionally comprise up to about 20% (for example, up to about 10%, such as up to about 3%) by weight of the outer layer of melamine fibers or melamine resin powder to increase the fire resistant properties of these outer layers.
  • outer layers may also be treated with additional fire retardant in amounts of up to about 5% (for example, up to about 3%, such as up to about 2%) by weight of the outer layer to further increase the fire resistance of the outer layer.
  • This additional fire retardant may be the same or a may be different from the fire retardant used to treat the pulp fiber web to provide the fire resistant pulp fiber web.
  • Embodiments of these fire retardant air-laid fibrous structures may be used, for example, in upholstery cushions, mattress ticking, panel fabric, padding, bedding, insulation, materials for parts in devices and appliances, etc.
  • the pulp fiber web may be prepared from the pulp fiber by any suitable process for providing pulp fiber webs.
  • the pulp fiber web may be formed from a pulp fiber mixture into a single or multi-ply web on a papermaking machine such as a Fourdrinier machine or any other suitable papermaking machine known in the art for making pulp fiber webs. See, for example, U.S. Pat. No. 4,065,347 (Aberg et al.), issued December 27, 1997; U.S. Pat. No. 4,081,316 (Aberg et al), issued March 28, 1978; U.S. Pat. No. 5,262,005 (Ericksson et al.), issued November 16, 1993, the entire contents and disclosure of which are herein incorporated by reference.
  • the pulp fiber mixture may also be treated with one or more debonder surfactants (as described above) to make the process of comminuting such pulp fiber webs (e.g., for providing air-laid fibrous structures) easier to carry out.
  • the resulting pulp fiber web which is formed may be dried to remove a portion, most or all of the water from the web, with the dried web being optionally treated with one or more additional debonder surfactants to again enhance the process of comminuting such pulp fiber webs.
  • the pulp fiber web may be dried in a drying section prior to and/or after treatment with an aqueous solution of the endothermic fire retardant and/or other fire retardants.
  • Any suitable method for drying pulp fiber webs known in the making art may be used.
  • the drying section may include a drying can, flotation dryer, cylinder drying, Condebelt drying, infrared (IR) drying, etc.
  • the treated and/or untreated pulp fiber web may be dried to a moisture content of about 10% or less, such as about 7% or less.
  • the pulp fiber web may be dried to a moisture content of between 0 and about 10% (which includes any value and subrange, for example, values or subranges including 3, 4, 5, 6, 7, 8, 9, 10, etc.).
  • the pulp fiber web may have a basis weight in the range of from about 500 to about 850 gsm (which includes any value and subrange, for example, values or subranges including about 500, 550 600, 650, 700, 750, 800, 850 gsm, etc.).
  • the pulp fiber web may have a density of about 0.3 g/cc or less, and in the range of from about 0.1 to about 0.3 g/cc (which includes any value and subrange, for example, values or subranges including about 0.1, 0.15, 0.2, 0.25, and 0.3 g/cc, etc.).
  • the pulp fiber web may have a caliper of at least about 30 mils, for example in the range of from about 30 to about 85 mils, such as from about 45 to about 65 mils (which includes any value and subrange, for example, values or subranges including about 30, 35, 40, 45, 50, 55, 65, 70, 75, 80, 85 mils, etc.).
  • the pulp fiber may have a fiberization (shred) energy of less than about 170 kJ/kg (which includes any value and subrange, for example, values or subranges including about 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 95, 100, 105, 1 10, 115, 120, 125, 130, 135, 140, 145, 150, 155, 160, 165 kJ/kg, etc.).
  • the pulp fiber web may have a fiberization energy in the range of from about 120 to less than about 145 kJ/kg, in the range of from about 100 to less than about 120 kJ/kg.
  • the pulp fiber web may have a fiberization energy of less than about 135 kJ/kg for example, a fiberization energy of less than about 120 kJ/kg, such as less than about 100 kJ/kg, or less than about 90 kJ/kg. In other embodiments, the pulp fiber web may have a fiberization energy in the range of from about 120 to less than about 145 kJ kg, in the range of from about 100 to less than about 120 kJ kg.
  • the pulp fiber web may comprise debonder surfactant in an amount of about 1 lb solids or greater per ton of the pulp fibers (which includes any value and subrange, for example, values or subranges including about 1, 1.1, 1.2, 1.3, 1.4, 1.5, 1.6, 1.7, 1.8, 1.9, 2, 2.0, 2.1, 2.2, 2.3, 2.4, 2.5, 2.6, 2.7, 2.8, 2.9, 3, 3.0, 3.1, 3.2, 3.3, 3.4, 3.5, 3.6, 3.7, 3.8, 3.9, 4, 4.0, 5, 5.0, 6, 7, 8, 9, 10, 15, 20 lbs solids debonder surfactant per ton of the pulp fibers, etc., or higher).
  • the pulp fiber web may comprise a trivalent metal (or salt thereof) in an amount of about 1 lb solids or greater per ton of the pulp fiber fibers (which includes any value and subrange, for example, values or subranges including about 1, 1.1, 1.2, 1.3, 1.4, 1.5, 1.6, 1.7, 1.8, 1.9, 2, 2.0, 2.1, 2.2, 2.3, 2.4, 2.5, 2.6, 2.7, 2.8, 2.9, 3, 3.0, 3.1, 3.2, 3.3, 3.4, 3.5, 3.6, 3.7, 3.8, 3.9, 4, 4.0, 5, 5.0, 6, 7, 8, 9, 10, 15, 20, 25, 30, 35 lbs cationic trivalent metal/salt thereof, etc., or higher).
  • the pulp fiber web may comprise the trivalent metal in an amount of about 150 ppm or greater per ton of the pulp fibers (which includes any value and subrange, for example, values or subranges including about 150, 155, 160, 165, 170, 175, 180, 185, 190, 195, 200, 205, 210, 215, 220, 225, 230, 235, 240, 245, 250, 300, 330, 400, 450, 500, 550, 750, 1000 ppm, etc., or higher).
  • Embodiments of the fire resistant pulp fiber web of the present invention may be used, for example, to provide air-laid fibrous structures, including air-laid fibrous cores, air- laid fibrous layers (including outer layers for air-laid fibrous cores), etc. See, for example, U.S. Pat. Appln. No. 20080050565 (Gross et al), published February 28, 2008; U.S. Pat. No. 6,059,924 (Hoskins), issued May 9, 2000); U.S. Pat. No. 7,549,853 (Fegelman et al), issued June 23, 2009, the entire disclosure and contents of which are herein incorporated by reference.
  • the fire resistant pulp fiber webs may be comminuted (e.g., defiberized, disintegrated, shredded, fragmented, etc.) to provide such air-laid fibrous structures using known methods for making such structures. See, for example, U.S. Pat. No. 3,591,450 (Murphy et al.), issued July 6, 1971, the entire contents and disclosure of which is herein incorporated by reference.
  • the fire resistant pulp fiber webs may be defiberized, disintegrated, shredded, fragmented, etc., by using a hammermill.
  • hammer milling is carried out in a manner which does not induce significant dust creation in the comminuted fire resistant pulp fibers.
  • the resultant air-laid fibrous structure may be used in a variety of products, for example, upholstery cushions, mattress ticking, panel fabric, padding, bedding, insulation, materials for parts in devices and appliances, etc.
  • the air-laid fibrous structures may comprise a mixture, blend, etc., of comminuted fire resistant pulp fibers and synthetic fibers (e.g., bicomponent fibers).
  • the air-laid fibrous structure may be in the form of an air-laid fibrous core which comprises a mixture, blend, etc., of comminuted fire resistant pulp fibers and synthetic fibers (e.g., bicomponent fibers).
  • these structures may comprise about 50% or greater (for example, about 75% or greater) by weight fire resistant pulp fiber, about 50% or less (for example, about 15% or less) synthetic fiber (e.g., bicomponent fiber), and optionally up to about 20% (e.g., from about 3 to about 10%) melamine fiber/powder.
  • fire resistant pulp fiber about 50% or less (for example, about 15% or less)
  • synthetic fiber e.g., bicomponent fiber
  • optionally up to about 20% e.g., from about 3 to about 10%
  • melamine fiber/powder Air- laid fibrous structures without melamine fiber may pass the UL 94 TMVB test when those structures comprise, for example, about 90% fire resistant pulp fiber and about 10% bicomponent fiber, and are sprayed with about 3% fire retardant on the surface of the outer layers of such structures.
  • Embodiments of the air-laid fibrous structures may be prepared by comminuting (e.g., disintegrating, defibrizing, etc.) a pulp fiber web (e.g., a pulp fiber sheet), for example, by using a hammermill (such as a Kamas Hammermill), to provide individualized comminuted pulp fibers.
  • the comminuted pulp fibers may then be air conveyed to forming heads on an air-laid web-forming machine.
  • a number of manufacturers provide air-laid web forming machines suitable for use in embodiments of the air-laid fibrous structures of the present invention, including Dan- Web Forming of Aarhus, Denmark, M&J Fibretech A/S of Horsens, Denmark, Rando Machine Corporation of Cincinnati, N.Y. (for example, as described in U.S. Pat. No. 3,972,092 to Wood, issued August 3, 1976, the entire contents and disclosure of which is herein incorporated by reference), Margasa Textile Machinery of Cerdanyola del Valles, Spain, and DOA International of Wels, Austria. While these various forming machines may differ in how the comminuted pulp fiber is opened and air-conveyed to the forming wire, all of these machines are capable of producing webs useful for forming embodiments of air-laid fibrous structures.
  • the Dan- Web forming heads may include rotating or agitated perforated drums, which serve to maintain fiber separation until the fibers are pulled by vacuum onto a foraminous forming conveyor, forming wire, etc.
  • the forming head may basically be a rotary agitator above a screen.
  • the rotary agitator may comprise a series or cluster of rotating propellers or fan blades.
  • Synthetic fibers e.g., bicomponent fibers
  • a fiber dosing system such as a textile feeder supplied by Laroche S.A. of Cours-La Ville, France.
  • the synthetic fibers may be air conveyed to the forming heads of the air-laid machine where those synthetic fibers are further mixed with the comminuted pulp fibers from the hammermill(s) and may be deposited on a continuously moving forming wire.
  • the forming heads may be used for each type of fiber.
  • the air-laid fibrous web may be transferred from the forming wire to a calender or other densification stage to densify the air-laid fibrous web, if necessary, to increase its strength and to control web thickness.
  • the fibers of the air-laid fibrous web may then be bonded by passage through an oven set to a temperature high enough to fuse any included thermoplastic synthetic fibers or other binder materials. Secondary binding from the drying or curing of a latex spray or foam application may also occur in the same oven.
  • the oven may be a conventional through-air oven or may be operated as a convection oven, but may also achieve the necessary heating by infrared or even microwave irradiation.
  • FIG. 1 is a schematic diagram which shows an illustrative process for providing a fire resistant pulp fiber web according to an embodiment of the present invention, which is indicated generally as 100.
  • the at least partially delignified pulp fibers (indicated as Delignified Pulp Fibers 102) are used, as indicated by arrow 104, in formulating Pulp Slurry 106.
  • an aqueous endothermic fire retardant solution comprising an initial portion of endothermic fire retardant such as aluminum ammonium sulphate or alum (indicated as Initial Endothermic FR 1 12, which may also provide a source trivalent metal ions), is added to Pulp Slurry 106, as indicated by arrow 114.
  • Pulp Slurry 106 is then deposited (e.g., using a headbox), as indicated by arrow 108, onto Forming Wire 1 10 to form the fire retardant-treated pulp fiber web.
  • the pulp fiber web is eventually transferred from Forming Wire 110 to Dryer 1 18.
  • other fire retardants such as a phosphorous fire retardant (indicated as Other FRs 120), along with a fire retardant distributing surfactant (indicated as Surfactant 122), are added, as indicated, respectively, by arrows 124 and 126.
  • Other FRs 120 and Surfactant 122 may be mixed together before being added to the pulp fiber web, or may added separately to the pulp fiber web.
  • Air-Laid Structure 134 may be treated (e.g., sprayed with, dosed with, etc.) any of the remaining endothermic fire retardant, such as a borate fire retardant (indicated as Remaining Endothermic FR 138) along with any additional and optional fire retardant distributing surfactant (indicated as Surfactant 140), as indicated by arrow 142.
  • a borate fire retardant indicated as Remaining Endothermic FR 138
  • Surfactant 140 any additional and optional fire retardant distributing surfactant
  • Dried Web 130 may be directly treated with (e.g., sprayed with, dosed with, etc.) Remaining Endothermic FR 138 (when, for example, not being formed into Air-Laid Structure 134 or prior to being formed into Air-Laid Structure 134).
  • some or all of the other fire retardants, plus fire retardant distributing surfactant may also be added (e.g., sprayed with, dosed with, etc.) to Dried Web 130.
  • FIG. 2 is side sectional view of an air-laid fibrous structure which comprises a fire resistant pulp fiber web according to an embodiment of the present invention as the respective outer layers of the air-laid fibrous core of the structure, which is indicated generally as 200.
  • Structure 200 comprises an air-laid fibrous core, indicated generally as 204, and two outer fire retardant outer air-laid fibrous layers, indicated respectively as upper layer 208 and lower layer 212.
  • Upper outer layer 208 is positioned on or adjacent upper surface 216 of core 204, while lower outer layer 212 is positioned on or adjacent lower surface 220 of core 204.
  • Outer layers 208 and/or 212 of structure 200 may be treated with additional fire retardant (for example, the additional fire retardant may be diluted with water and/or other solvent(s), with the water/solvent(s) being removed, for example, by heating after treatment).
  • additional fire retardant for example, the additional fire retardant may be diluted with water and/or other solvent(s), with the water/solvent(s) being removed, for example, by heating after treatment.
  • the specimens for the fire resistance tests are prepared as follows: Fire retardant- treated pulp fiber web sheets are defiberized in a lab hammermill (Kamas Type H 01 Laboratory Defribrator) by shredding 2 inch width strips at 3300 rpm using a 10 mm screen opening and 7 cm/sec. feed speed. The defiberized pulp fibers are mixed in the plastic bag by hand and by vigorously shaking the sealed bag which contains air space, to achieve as uniform a distribution of fiber fractions as possible, i.e., to achieve a representative test specimen. Approximately 3.4 g of the mixed pulp fibers are weighed out to provide a target weight of 3.16 g ⁇ 0.1 g (300 g/m 2 ).
  • a piece of the nonwoven barrier material is inserted into a collection basket/cup of an 11 cm diameter forming funnel which is attached in the hammermill.
  • the weighed pulp fibers are refiberized in the hammermill using the front chute with a rotor setting at -750 rpm and with a 14 mm screen in place.
  • the refiberized pulp in the funnel is evenly spaced using long handle tweezers, and then pressed firmly into the funnel with a tamping tool.
  • the resultant specimen is then removed and weighed.
  • the weighed specimen is then placed without the nonwoven barrier material between two blotters and feed through a press.
  • the thickness of the resultant specimen is then measured with the target density of the specimen being 0.1 g/cm 3 which equals a thickness of 1.32 mm or 0.052" (i.e., 52 mils).
  • the fiberization energy of the specimen may be calculated as described above based on energy measured and displayed by the Kamas Type H 01 Laboratory Defribrator (converted, if necessary from watt hours or wH), divided by the fiberized fiber weight, to provide a value in kJ/kg.
  • Pulp fiber webs treated with endothermic fire retardants are prepared as described below:
  • a fluff pulp (which contains 20 lbs per ton of aluminum ammonium sulfate (alum) as an endothermic fire retardant) is treated with 60 lbs/air dried metric ton of FR165 (phosphorus fire retardant, distributed by Cellulose Solutions) and 2 lbs/ton F60 surfactant (an ethoxylated alcohol surfactant, distributed by Eka Chemical).
  • FR165 phosphorus fire retardant, distributed by Cellulose Solutions
  • 2 lbs/ton F60 surfactant an ethoxylated alcohol surfactant, distributed by Eka Chemical
  • This air- laid fibrous core is sprayed with a solution of a neutral pH endothermic fire retardant (Pre- Tec 3000 SF, a borosilicate endothermic fire retardant, distributed by Pre-Tec) at a 6% dose by weight of the core.
  • a neutral pH endothermic fire retardant Pre- Tec 3000 SF, a borosilicate endothermic fire retardant, distributed by Pre-Tec
  • the surface-treated air-laid fibrous core is tested according to the UL 94 HBF test method and passes this test without any after burn.
  • the air-laid core has a pH of 6.9.
  • a fluff pulp (which contains 20 lbs per ton of aluminum ammonium sulfate (alum) as an endothermic fire retardant) is treated with 60 lbs/air dried metric ton of FR165 phosphorus fire retardant and 2 lb/ton F60 surfactant.
  • This treated fluff pulp is used in preparing an air-laid fibrous core which comprises 90% of the treated fluff pulp and 10% bicomponent PE/PE 6 mm fibers.
  • this air-laid fibrous core is sprayed with a solution of a neutral pH blend of endothermic fire retardant and other (phosphorous) fire retardant (CS-FR 30-S, a silica and ammonium phosphate fire retardant distributed by Cellulose Solutions) at a 10% dose by weight of the core.
  • CS-FR 30-S endothermic fire retardant and other (phosphorous) fire retardant
  • silica and ammonium phosphate fire retardant distributed by Cellulose Solutions

Abstract

La présente invention concerne un procédé dans lequel une bande de fibre de pâte au moins en partie délignifiée présentant un indice Kappa inférieur à environ 130 est traitée avec une solution aqueuse de produit ignifugeant endothermique présentant un pH d'environ 10 ou moins. La bande de fibre de pâte traitée présente un pH presque neutre d'environ 5 à environ 9, et est traitée avec au moins environ 20 livres de produits ignifugeants endothermiques par tonne de la bande de fibre de pâte, au moins environ 5 % de la quantité totale de produits ignifugeants endothermiques étant ajoutés à un moment précédant celui où la bande de fibre de pâte est formée. L'invention concerne également une bande de fibre de pâte ignifugée présentant un pH presque neutre.
PCT/US2011/046169 2010-08-03 2011-08-02 Ajout de produits ignifugeants endothermiques pour fournir des bandes de fibre de pâte de ph presque neutre WO2012018746A1 (fr)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US37023610P 2010-08-03 2010-08-03
US61/370,236 2010-08-03
US13/081,759 2011-04-07
US13/081,759 US8663427B2 (en) 2011-04-07 2011-04-07 Addition of endothermic fire retardants to provide near neutral pH pulp fiber webs

Publications (1)

Publication Number Publication Date
WO2012018746A1 true WO2012018746A1 (fr) 2012-02-09

Family

ID=45559780

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2011/046169 WO2012018746A1 (fr) 2010-08-03 2011-08-02 Ajout de produits ignifugeants endothermiques pour fournir des bandes de fibre de pâte de ph presque neutre

Country Status (1)

Country Link
WO (1) WO2012018746A1 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019099380A1 (fr) * 2017-11-17 2019-05-23 ADAMOLI, James, R. Agent ignifuge pour un produit d'isolation

Citations (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2832745A (en) 1956-08-31 1958-04-29 Shea Chemical Corp Aqueous flameproofing compositions and cellulosic materials treated therewith
US3591450A (en) 1967-08-30 1971-07-06 Int Paper Co Method and apparatus for conditioning and defibrating a web of paper pulp prior to air laying
US3955032A (en) 1972-10-25 1976-05-04 White Chemical Corporation Flame retardants for natural and synthetic materials
US3972092A (en) 1973-03-01 1976-08-03 Rando Machine Corporation Machine for forming fiber webs
US4026808A (en) 1972-03-30 1977-05-31 Hooker Chemicals & Plastics Corporation Flame retardant textile finishes
US4065347A (en) 1975-02-26 1977-12-27 Molnlycke Ab Method of producing fluffed pulp
US4081316A (en) 1974-12-05 1978-03-28 Molnlycke Ab Method for producing fluffed pulp
US4184969A (en) * 1978-08-04 1980-01-22 Bhat Industries, Inc. Fire- and flame-retardant composition
US4212675A (en) * 1978-04-03 1980-07-15 Retroflame International Limited Fireproofing
US4425186A (en) 1981-03-24 1984-01-10 Buckman Laboratories, Inc. Dimethylamide and cationic surfactant debonding compositions and the use thereof in the production of fluff pulp
US4600606A (en) 1979-04-18 1986-07-15 White Chemical Corporation Process for rendering non-thermoplastic fibrous materials flame resistant to molten materials by application thereto of a flame resistant composition, and related articles and compositions
US4702861A (en) 1986-05-14 1987-10-27 Certified Technologies Corporation Flame retardant materials
US5056508A (en) 1990-10-09 1991-10-15 Brunell Gladys B Neck support for cervical or whiplash problems
US5262005A (en) 1988-11-17 1993-11-16 Sca Pulp Ab Easily defibered web-shaped paper product
US6059924A (en) 1998-01-02 2000-05-09 Georgia-Pacific Corporation Fluffed pulp and method of production
US6719862B2 (en) 1998-10-09 2004-04-13 Weyerhaeuser Company Compressible wood pulp product
US20050274472A1 (en) * 2004-05-27 2005-12-15 Robert Steif Flame resistant paper product and method for manufacturing
US7381300B2 (en) 2006-10-31 2008-06-03 International Paper Company Process for manufacturing paper and paperboard products
US7549853B2 (en) 2006-11-15 2009-06-23 The Procter & Gamble Company Apparatus for making air-laid structures
US7604715B2 (en) 2005-11-17 2009-10-20 Akzo Nobel N.V. Papermaking process

Patent Citations (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2832745A (en) 1956-08-31 1958-04-29 Shea Chemical Corp Aqueous flameproofing compositions and cellulosic materials treated therewith
US3591450A (en) 1967-08-30 1971-07-06 Int Paper Co Method and apparatus for conditioning and defibrating a web of paper pulp prior to air laying
US4026808A (en) 1972-03-30 1977-05-31 Hooker Chemicals & Plastics Corporation Flame retardant textile finishes
US3955032A (en) 1972-10-25 1976-05-04 White Chemical Corporation Flame retardants for natural and synthetic materials
US3972092A (en) 1973-03-01 1976-08-03 Rando Machine Corporation Machine for forming fiber webs
US4081316A (en) 1974-12-05 1978-03-28 Molnlycke Ab Method for producing fluffed pulp
US4065347A (en) 1975-02-26 1977-12-27 Molnlycke Ab Method of producing fluffed pulp
US4212675A (en) * 1978-04-03 1980-07-15 Retroflame International Limited Fireproofing
US4184969A (en) * 1978-08-04 1980-01-22 Bhat Industries, Inc. Fire- and flame-retardant composition
US4600606A (en) 1979-04-18 1986-07-15 White Chemical Corporation Process for rendering non-thermoplastic fibrous materials flame resistant to molten materials by application thereto of a flame resistant composition, and related articles and compositions
US4425186A (en) 1981-03-24 1984-01-10 Buckman Laboratories, Inc. Dimethylamide and cationic surfactant debonding compositions and the use thereof in the production of fluff pulp
US4702861A (en) 1986-05-14 1987-10-27 Certified Technologies Corporation Flame retardant materials
US5262005A (en) 1988-11-17 1993-11-16 Sca Pulp Ab Easily defibered web-shaped paper product
US5056508A (en) 1990-10-09 1991-10-15 Brunell Gladys B Neck support for cervical or whiplash problems
US6059924A (en) 1998-01-02 2000-05-09 Georgia-Pacific Corporation Fluffed pulp and method of production
US6719862B2 (en) 1998-10-09 2004-04-13 Weyerhaeuser Company Compressible wood pulp product
US20050274472A1 (en) * 2004-05-27 2005-12-15 Robert Steif Flame resistant paper product and method for manufacturing
US7604715B2 (en) 2005-11-17 2009-10-20 Akzo Nobel N.V. Papermaking process
US7381300B2 (en) 2006-10-31 2008-06-03 International Paper Company Process for manufacturing paper and paperboard products
US7549853B2 (en) 2006-11-15 2009-06-23 The Procter & Gamble Company Apparatus for making air-laid structures

Non-Patent Citations (5)

* Cited by examiner, † Cited by third party
Title
"Tests for Flammability of Plastic Materials for Parts in Devices and Appliances", 2009, UNDERWRITERS LABORATORIES INC., pages: 32
G. A. SMOOK: "Handbook for Pulp and Paper Technologists", 1992, pages: 283 - 85
G. A. SMOOK: "Handbook for Pulp and Paper Technologists", 1992, pages: 289 - 92
G. A. SMOOK: "Handbook for Pulp and Paper Technologists", 1992, pages: 342
WEIL ET AL.: "Flame Retardants for Plastics and Textiles", 2009, HANSER PUBLISHERS, pages: 4 - 8

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019099380A1 (fr) * 2017-11-17 2019-05-23 ADAMOLI, James, R. Agent ignifuge pour un produit d'isolation
US10815427B2 (en) 2017-11-17 2020-10-27 Branislav R. Simonovic Fire-retardant for an insulation product

Similar Documents

Publication Publication Date Title
US8871058B2 (en) Addition of endothermic fire retardants to provide near neutral pH pulp fiber webs
US8871053B2 (en) Fire retardant treated fluff pulp web
EP1963573B1 (fr) Articles ameliores en cellulose contenant une composition d additif
JP5816357B2 (ja) 多価カチオン性金属とアミン含有帯電防止剤とを含有する組成物、およびそれらの製造方法と使用方法
US8871054B2 (en) Process for preparing fluff pulp sheet with cationic dye and debonder surfactant
US8388807B2 (en) Partially fire resistant insulation material comprising unrefined virgin pulp fibers and wood ash fire retardant component
US20160237624A1 (en) Dry fluff pulp sheet additive
EP3535452B1 (fr) Procede de production de fibres de pulpe a volume eleve, fibres de pulpe obtenues et produits incorporant celles-ci
PL201227B1 (pl) Dekoracyjny papier podłożowy i jego zastosowanie
WO2012018746A1 (fr) Ajout de produits ignifugeants endothermiques pour fournir des bandes de fibre de pâte de ph presque neutre
CN109476129A (zh) 带有胶粘剂的装饰片材
JP7166263B2 (ja) 多層シート及びその製造方法
Dutt et al. Cost reduction studies of decorative laminates
JP2021161555A (ja) 板紙
MX2008007679A (en) Improved cellulose articles containing an additive composition

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 11745866

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 11745866

Country of ref document: EP

Kind code of ref document: A1