WO2002044470A1 - Procede pour la production d'un substrat plat fibreux cellulosique couche et presse, compositions de revetement appropriees, leur production, substrats ainsi couches et presses et leur utilisation comme substrats pour traitements graphiques - Google Patents

Procede pour la production d'un substrat plat fibreux cellulosique couche et presse, compositions de revetement appropriees, leur production, substrats ainsi couches et presses et leur utilisation comme substrats pour traitements graphiques Download PDF

Info

Publication number
WO2002044470A1
WO2002044470A1 PCT/IB2001/002256 IB0102256W WO0244470A1 WO 2002044470 A1 WO2002044470 A1 WO 2002044470A1 IB 0102256 W IB0102256 W IB 0102256W WO 0244470 A1 WO0244470 A1 WO 0244470A1
Authority
WO
WIPO (PCT)
Prior art keywords
coated
coating
substrate
paper
production
Prior art date
Application number
PCT/IB2001/002256
Other languages
English (en)
Inventor
Scott Myatt
Original Assignee
Clariant Finance (Bvi) Limited
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
Application filed by Clariant Finance (Bvi) Limited filed Critical Clariant Finance (Bvi) Limited
Priority to EP01998162A priority Critical patent/EP1341965A1/fr
Priority to CA002424360A priority patent/CA2424360A1/fr
Priority to US10/432,520 priority patent/US20040094279A1/en
Publication of WO2002044470A1 publication Critical patent/WO2002044470A1/fr

Links

Classifications

    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP 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
    • D21H19/00—Coated paper; Coating material
    • D21H19/36—Coatings with pigments
    • D21H19/38—Coatings with pigments characterised by the pigments
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K21/00—Fireproofing materials
    • C09K21/02—Inorganic materials
    • C09K21/04—Inorganic materials containing phosphorus
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K21/00—Fireproofing materials
    • C09K21/14—Macromolecular materials
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP 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
    • D21H21/00—Non-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
    • D21H21/14—Non-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
    • D21H21/34—Ignifugeants
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP 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
    • D21H21/00—Non-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
    • D21H21/50—Non-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 form
    • D21H21/52—Additives of definite length or shape

Definitions

  • a coating composition is usually applied to the web of paper or other fibrous material and is pressed e g. with a plate or through press rolls or by other means, in order to obtain a surface with certain physical and aesthetic properties such as gloss, strength, pliability and p ⁇ ntability
  • a flame retarding paint may be applied to the substrate after it has been finished (either uncoated or coated, as mentioned above) so that, when applied on a coated substrate, this paint may impair the aesthetic aspect and also some of the physical properties which were provided by the previously applied coating (such as gloss or p ⁇ ntability) or, when applied on an uncoated substrate, it may not replace a coating (or "enamel") because of its different way of application and mostly also because of its different composition
  • the application of such paints is sometimes also designated as "coating”, but this term signifies in this case only that the paint is applied as a continuous film, and this is usually directly dried after its application without subjecting it to a particular pressure treatment
  • fire retardant aqueous coating solutions for use in forming a fire retardant protective overcoat on a surface requiring such protection, which are comprised of l) a water soluble film-forming cross-linkable copolymer of methyl vinyl ether and maleic anhydride, 2) a water-soluble polyhyd ⁇ c alcohol which serves to cross-link the copolymer when a coating of the composition is applied over the surface and dried, and 3) a water-soluble ammonium polyphosphate, these compositions are useful for forming a transparent overcoat in particular for photographic elements, AMGARD PI of Albright & Wilson Americas Inc being mentioned among others as an example of an ammonium polyphosphate component 3)
  • EP-460516-A and GB-2243846-A relate to flame retardant aqueous compositions comprising an ammonium polyphosphate, a defined heat-curable resin and some defined further components (the same AMGARD PI as above being mentioned as an example of the ammonium polyphosphate) These compositions on standing form a gel which on shearing forms a pourable emulsion which on application to a fabric under shearing then regels rapidly They are applied to the back of the fabric by back-coating
  • US-5498471-A describes an aqueous non-flowing coating or impregnating composition for a non- woven or paper substrate for flexible circuit boards, which composition includes a) a cross-linked product of an aqueous dispersion of a cross-linkable copolyme ⁇ sate of acrylic esters and styrene and b) an aqueous solution of a precondensate containing hydroxymethyl groups (aminoplastics and phenoplastics) and which further contains as a particulate dispersed flame retardant red phosphorus of a grain size of 45 to 100 ⁇ m (Exolit 405 being named as an example) and an ammo- mum polyphosphate of a grain size of 25 to 75 ⁇ m (Exolit 422 being named as an example)
  • the coating composition is applied to the substrate and dried, then the coated substrate is laminated under pressure with the conductive metal (copper) foil, by which the surface appearance of the coating is no longer visible If it were desired to print the paper or
  • CS-B-239173 there is described a coating of paper, cardboard or carton with a coating mix containing 10-40 % of aluminium hydroxide and 60 to 90 % of kaolin as pigments, 0 2 to 2 % based on the pigment, of a flame retardant, e g of secondary ammonium phosphate, and further 0 1 to 1 5 %, based on the pigment, of molecular colloids and 5 to 15 %, based on the pigment, of polyvinyl acetate
  • ammonium polyphosphates are employed in a form, a way of application and concentration that provides just a form of flame retarding effect but that is of no particular bearing in the appearance and graphic utilization of the treated substrate
  • particularly hard and insoluble flame retarding polyphosphates of a particular particle size, as defined below and which are not combined with red phosphorus are surprisingly well suitable in particular also as fillers or white pigments in coating compositions for the production of coated and pressed substrates, as defined below, of outstanding surface properties, particularly suitable for graphic processing, and of outstanding non-flammability properties
  • the invention relates to a process for the production of coated and pressed cellulosic fibrous substrates of loose, optionally bonded fibers, to suitable coating compositions of defined particle size of the dispersed particles, to their production, to the coated and pressed substrates and to their use as substrates for graphic processes, especially printing
  • the invention thus firstly provides a process for the production of a coated and pressed cellulosic fibrous flat substrate of loose, optionally bonded fibers, by application of
  • a flat substrate of loose, optionally bonded fibers there is meant any such substrate in which the fibers are processed in loose form to a web, which may be bonded with suitable binders
  • These substrates are in particular those in which the loose fibers in the form of webs serve for the production of paper, paperboard, board or non-wovens, or are in the form of non-coated sheets of paper, paperboard or board or of pre-formed non-coated non-woven webs or tissues
  • any such substrate in which loose fibres have been directly processed to a flat substrate from an aqueous suspension or by forming a fiber mat from dry loose fibers mechanically or also with the aid of air, I e by processes in which the fibres are not in the form of yarns or strands or any woven or knitted fabric
  • any fibrous cellulosic flat substrate made of loose optionally bonded fibers as is suitable for the application of a particulate- pigment-containing coating and subjecting to pressure (e g with plates, air knives or press rolls), in particular webs of cellulosic fibers, mainly webs or sheets of paper, papcrboard or board or non-woven tissue webs or mats
  • the process of the invention is employed for the production of coated paperboard or, most preferably, coated paper
  • the said mat, web or sheet may be formed of any conventional cellulosic fibrous material
  • the webs, mats or sheets to be employed as a substrate may have been produced by any conventional methods.
  • a web of paper or paperboard the loose fibers may be bonded only mechanically and with the own fibre substance (e.g starch, pectme etc ) or preferably also by means of suitable additives, e.g. a size
  • the coating may be applied in one same sequence during papermaking, or analogously in making the board or paperboard Alternatively the production of paper, paperboard or board may be carried out only until a non-coated sheet of paper, paperboard or board is formed and coating and pressing may be carried out separately Also for non-wovens it is possible to apply the coating to the optionally bonded web in one same sequence in the production of the non-woven tissue or in a separate treatment.
  • the aqueous coating composition (M) to be employed in the process of the invention contains as an essential component a white pigment (W) which is in particulate solid form, suitably dispersed in the coating formulation.
  • the particulate white pigment (W) may consist substantially only of (A) or may be a mixture of (A) with a one or more components, in particular with one or more white mineral pigments (P) and/or with one or more melamine (poly)phosphates (L)
  • (W) may thus consist of one particulate component or of a mixture of particulate components, at least a part of which is the particulate ammonium polyphosphate (A) of crystalline form II which is of the stated very small particle size and very low solubility
  • the water solubility is ⁇ 6 g/1 at 25°C
  • the ammonium polyphosphates (A) are preferably of high molecular weight and are preferably substantially linear They may be represented by the average formula (NH 4 P0 3 ) n , wherein n represents the degree of polymerisation and is preferably > 800, more preferably > 1000, e g even
  • the acid number of (A) is preferably ⁇ 1 , more preferably ⁇ 0 8, and the viscosity of an aqueous 20 % suspension of (A) is preferably below 200 mPa-s, more preferably below 120 mPa s, most preferably in the range of 50 to 100 mPa-s.
  • the particulate ammonium polyphosphate (A) is of crystalline form II, which may have been produced by any known or conventional methods as are suitable for the production of such an ammonium polyphosphate of low water solubility, e.g. by reaction of phosphoric acid anhydride with ammonia and/or diammoniumphosphate, optionally in the presence of urea or melamine, at elevated temperature, at least a part of the reaction being carried out preferably at a temperature in the range of 170 to 375°C, or/and by tempering of a corresponding ammonium polyphosphate of crystalline form I, IV or V at a suitable temperature between 200 and 375°C.
  • the ammonium polyphosphates II known in the art usually have a varying average particle size, e g. in the range of 500 to 5 ⁇ m
  • average particle size below 40 ⁇ m
  • the average particle size is low, preferably in the range of 0.1 to 35 ⁇ m, more preferably 1 to 25 ⁇ m, most preferably 2 to 15 ⁇ m, the lower average particle sizes, in particular below 25 ⁇ m, especially below 15 ⁇ m or even ⁇ 10 ⁇ m (e.g. in the range of 2 to 15 ⁇ m) being particularly preferred.
  • the particles of (A) be all of a size below 40 ⁇ m.
  • the particles of (A) may even be all below 30 ⁇ m or even below 25 ⁇ m.
  • the small particle size of (A) may e.g. be produced by comminuting a conventional ammonium polyphosphate II, suitably by grinding or milling to the desired particle size, and if necessary screening, or e.g. by selecting the inferior size particles in production lots of a broad range of particle sizes e.g by suitable screening and/or sieving.
  • ammonium polyphosphate II For the purpose of the invention it is in particular preferred to comminute crystalline ammonium polyphosphate II produced by tempering at the high temperatures mentioned above, although it is very hard and milling will require suitable ball mills or bead mills and a corresponding milling time, or to separate correspondingly small particle size proportion from a so produced ammonium polyphosphate II.
  • the harder qualities of ammonium polyphosphate II are preferred for the process of the invention.
  • these small particle size ammonium polyphosphates II are suitable as white pigments or white fillers in coatings, especially paper coatings, and more particularly that they are of similar or even superior properties as compared to conventional mineral white pigments or fillers
  • As (P), l e as a white mineral pigment or filler there is intended any such inorganic white pigment or filler as conventionally employed in coating compositions and which may comprise true minerals and also inorganic compounds analogous to mineral products, i.e. modified minerals or also synthetically produced inorganic compounds of analogous or related properties to mineral white pigments or fillers.
  • mineral products there may be mentioned e.g kaolin, calcium carbonate, barytes, bentomte, mica, montmo ⁇ llonite, slate, talc and titanium dioxide
  • products obtained by processing minerals there may be mentioned e.g. calcium carbonate or sulphate, barium sulphate, satin white and argillaceous minerals.
  • products obtained by a synthetic reaction to produce a compound of properties similar to those of mineral forms there may be mentioned e.g.
  • Their particle size may range in a scope as per se conventionally employed in coating compositions; in particular their average particle size may be well below 40 ⁇ m and also well below 25 ⁇ m
  • White mineral pigments used in coating compositions for paper are mostly of a particle size in the range of 0.1 to 10 ⁇ m, best pigment properties and light scattering being achieved mostly at a particle size in the range or 0.2 to 2 ⁇ m, particle sizes in the higher ranges of e.g. 2 to 10 ⁇ m being usually more suitable for fillers
  • white pigment as used herein is intended to include as well particulate white components with typical white pigment properties (such as crystalhnity, size and light refraction) as also particulate white components which may be used as fillers (e.g. where the light scattering proper- ties may be somewhat inferior to those of the typical pigments, but which still contribute to the whiteness and opacity of the coating).
  • (W) contains also a particulate melamine (poly)phosphate (L).
  • Melamine (poly)phosphates are known substances and may be represented by the general formula (C H 6 N 6 ) m (NH 3 ) p *(HP0 3 ) n , in which n is as defined above, m is a number corresponding to the proportion of melamine employed and is ⁇ n (e.g n/2 to n), and p is a number in the range from 0 to n-m.
  • the average particle size is below 40 ⁇ m, preferably below 25 ⁇ m, with preferably no particles exceeding 40 ⁇ m, those with an average particle size below 15 ⁇ m or even ⁇ 10 ⁇ m (e g in the range of 0 5 to 15 or 1 to 10 ⁇ m) being particularly preferred.
  • Their solubility in water is also very low, in particular lower than the one of (A) and they are preferably practically insoluble; their solubility in water at 20°C is e.g. below 6 g/1, especially below 1 g/1.
  • Commercially available grades are e.g. of a water solubility ⁇ 0.1 g/1.
  • (P) or (L) or both is present together with (A) in (W)
  • this may be e.g. (P) alone or (L) alone or a mixture of (P) and (L).
  • (W) is a mixture of (A) with other components, in particular with mineral pigments (P) and/or with (L)
  • (A) is expediently present in an efficient proportion.
  • (A) constitutes at least 4 % by weight of (W), advantageously 5 to 100 % of (W), more preferably 20 to 100 %, the remaining up to 96, 95 or respectively 80 % being (P) or (L) or (P)+(L).
  • the weight ratio of (P) to (A) in (W) is e.g. in the range of from 0.1/10 to 10/0.5 advantageously 0.1/10 to 10/1 , preferably 0.1/10 to 5/1 , more preferably 0.1/10 to 4/1.
  • the weight ratio of [(L)+(P)]:(A) is e.g. in the range of from 0.1/10 to 10/0.5, advantageously 0.1/10 to 10/1, preferably 0.1/10 to 5/1, more preferably 0.1/10 to 4/10.
  • the weight ratio of (P) to (L) may be in any desired range as suitable for the envisaged purpose, e.g. in the range of from 0.1/10 to 10/0 1 advantageously 0.1/10 to 4/10, preferably 0.1/10 to 2/10, more preferably 0.1/10 to 1/10.
  • a further essential component of the aqueous coating compositions (M) is the binder (B).
  • a binder (B) there may be employed any conventional binder or mixture of binders as is usually employed in coating compositions, especially in paper coatings.
  • Representative binders are conventional polymers, e.g.
  • the binder (B) may be present in (M) in concentrations conventional per se, as suitable for binding the pigment particles to the substrate
  • the ratio of (B) to (W) on a dry basis is e.g in the range of 1/0.2 to 1/20, preferably 1/1 to 1/12, more preferably 1/3 to 1/8
  • the dispersants (D) may be any dispersants or mixtures of dispersants as conventionally employed in paper coating compositions and are preferably anionic or non-ionic dispersants They may be simple non-polymeric compounds or polymers, e.g. also of protective colloid character
  • non-polymeric non-ionic dispersants there may be mentioned adducts of ethylene oxide and optionally propylene oxide to an aliphatic alcohol such as Cn_ 24 -fatty alkohols (natural or synthetic alkohols) to a mono- or dialkylphenol with 6 to 18 carbon atoms in the total of alkyl radicals present, with an HLB e.g. in the range of 8 to 16.
  • non- polymeric anionic dispersants there may mentioned aliphatic sulphonic acids in salt form such as sodium C ⁇ . 24 -alkane sulphonates, or arahphatic sulphonic acids in salt form such as sodium mono- or dialkylbenzenesulphonates with 6 to 18 carbon atoms in the total of alkyl radicals present, and aliphatic carboxylic acid salts (soaps) such as C
  • the dispersants (D) are polymers, more preferably water soluble polymers, in particular polyacryh
  • alkali metal or ammonium salt usually of an average molecular weight in the range of 2000 to 10000
  • polyphosphates e.g. a water soluble ammonium polyphosphates, e.g. of a degree of polymerisation of 3 to 30, e g terra or hexametaphosphate
  • concentration of (D) is in the range of 0 01 to 1 %, more preferably 0.1 to 0.5 % referred to the weight of the dry content of the coating composition (M).
  • the coating compositions (M) may optionally contain further components, as may be desired or suitable depending on the desired effect, on the employed method and employed apparatus for application and on the nature and composition of the substrate, e.g. dyestuffs and/or optical b ⁇ ghteners and any optional assistants such as surface active agent, thickeners, resins and/or formulation additives
  • (M) may further contain one or more further additives selected from
  • ) may be any optical bnghtener suitable for the optical brightening of cellulosic substrates, especially paper, and/or for use in coating compositions, and is preferably anionic Among the anionic optical bnghteners are preferred those of the 4,4'-b ⁇ st ⁇ az ⁇ nylam ⁇ nost ⁇ lbene-2,2'-d ⁇ - sulphonic acid series, especially those in which each t ⁇ azinyl ring is substituted with two amino groups, one of which is an optionally sulphonated aniline radical and the other is aliphatic. There may be employed known optical bnghteners as are commercially available and as are conventionally employed also in coatings.
  • (C 2 ) may be any dye suitable for the dyeing of cellulosic substrates, especially paper, for which it is preferably a water soluble preferably anionic dye, and/or for use in coating compositions, for which it may be a water soluble preferably anionic dye, or may also be a dye insoluble in water
  • anionic dyes are preferred (C 2 ') direct dyes.
  • the insoluble dyes are in particular (C 2 ”) colour pigments.
  • (E) there may be employed known thickening agents, in particular as are conventionally employed in coating compositions for paper coatings; preferably (E) an acrylic polymer or a poly- urethane.
  • (F) there may be employed any resins as conventionally employed in coating pastes, in particular a resin containing hydroxymethyl groups or oxirane rings and which is curable, in particular with a suitable binder (B)
  • (F) is a curable resin selected from (F,) melamine/formaldehyde resins,
  • Components (E) and (F) serve for adjusting the consistency of (M) and the mechanical properties of the final coating, such as strength, pliability, elasticity and touch of the coated and pressed dry product, and their amount and kind will also depend on the chosen application method and apparatus
  • a binder such as (B) depending on its particular constitution may also contribute to a minor degree to the thickness of the composition and/or to the mechanical properties of the final coated product, and vice versa (E) or (F) may also contribute to a minor degree to the binding of the components in (M)
  • the choice and concentration of any components (E) and/or (F) will mainly depend on the desired properties of (M) and the mechanical properties of the coated product in the presence of a certain chosen binder (B), and it is in the skill of the coating specialist to choose the components and to adjust their concentrations depending on the desired mechanical properties of the coating mass (M) and of the coated product and also on the employed apparatus and method
  • Component (G) is at least one formulation additive, 1 e a product for providing and maintaining a certain constitution of the composition (M), in particular - for example - in order to protect it against the damaging action of micro-organisms or to avoid a disturbing foam formation or further, if desired, in order to provide or modify the flowabihty properties of the composition and/or also in order to select a preferred pH which may be suitable for the particular composition and favour its storage and application properties
  • (G 3 ) a flow agent and/or (G 4 ) an acid, base and/or buffer for pH-adjustment
  • any antimicrobial agent as commercially available and conventionally employed for protecting an aqueous coating composition from the damaging action of micro-organisms, it may e g be microbial growth inhibitor or a microbicide (e g a fungicide), as commercially available, e g of the l,2-benz ⁇ soth ⁇ azohn-3-one series, and may be employed in an efficient concentration, e g ⁇ 3 % by weight referred to (M), suitably in the commercially indicated concentrations, e g in a concentration of 0 01 to 3 %, preferably 0 05 to 1 %, more preferably 0 1 to 0 2 % by weight referred to (M)
  • any flow agents as commercially available and conventionally employed for modifying the flow properties of coating compositions (G 3 ) may e g be a prefer- ably saturated fatty acid salt (e g of 16-24 carbon atoms in the fatty acid) preferably a stea ⁇ c acid salt, e g an alkali metal salt, alkaline earth metal salt or ammonium salt, and is present in a suitable efficient concentration, e g in the range of 0 01 to 5 %, preferably 0 05 to 2 %, more preferably 0 1 to 1 5 % by weight referred to (M)
  • a flow agent (G 3 ) is preferably employed, in particular to adjust the viscosity of the coating dispersion to such values as suitable for the employed coating apparatus and speed and depending also on the kind of substrate, the particular composition of (M) and the desired effect, preferably so that the viscosity is kept at values below 3000 mPa s, preferably below 1500 mPa s
  • the pH of (M) may vary broadly, in particular from distinctly acidic to strongly basic, especially from 5 5 to 13, preferably 7 to 10, more preferably 8 to 9, if required or desired, it may be adjusted by the addition of one or more additives (G 4 ), which may e g be a base such as ammonium hydroxide, alkali metal hydroxide or carbonate or magnesium oxide, a strong mineral acid such as phosphoric acid or sulphuric acid, or a strong aliphatic carboxyhc acid e g with 1 to 6 carbon atoms (such as formic, acetic, oxalic, lactic or citric acid) and/or optionally a buffer salt such as ammonium or sodium hydrogen phosphates
  • G 4 additives
  • the consistency of the flame-proofing coating composition (M), in particular its dry substance content, density and viscosity may vary broadly, depending e g on the method of application and the employed apparatus, on the substrate and on the desired effect
  • the dry substance content of (M) may in particular be in the range of 1 to 90 %, advantageously 5 to 85 %, preferably 20 to 80 %, more preferably 25 to 75 %
  • the proportion of (W) and of (A) in (M) may thus also vary accordingly
  • (W) represents the main component - l e > 50 %, more preferably 60 to 95 % by weight - of the dry substance content of (M) and more preferably (A) or even a mixture of (A) with (L) as described above represents a substantial proportion, e g > 8 %, or even the main component - l e > 50 %, more preferably 60 to 95 % by weight - of the dry substance content of (M), and thus (A) may outweigh each or even all other components
  • the coating compositions of the invention is a dispersion of the above described very fine particle size of the dispersed particulate solid components, I e white pigment (W) [(A) and, if present, also (P) and/or (L), being in particular of an average particle size below 25 ⁇ m] and any other optionally present pigment (C 2 ") which is also of a particle size in the stated range (in particular in the microcrystalhne to kryptocrystalhne grain size range), which are present together with the binder (B), the dispersant (D) and any further component of (M)
  • the binders (B) present which may be more or less hydrophihc and more or less dissolved or swollen in the aqueous phase, are not considered within the above definition of dispersed particulate solid components of very fine particle size More particularly the particulate dispersed pigment components present in (M) essentially consist only of (W) and optionally (C 2 ") More preferably no pigments (C 2 ") are present and
  • the aqueous compositions (M) can be produced by mixing the components in a suitable way, analogous to conventional methods
  • the coating compositions (M) may be produced by first mixing (W), more particularly the pigment components (A) and optionally any (L) and/or (P), with water and optionally (G 3 ), adding (D) and then (B) followed by the addition of any further of the components (C), (E), (F) and/or (G) as required or desired
  • the mixing is advan- ageously carried out at a temperature not exceeding 35°C, preferably at a temperature in the range of 12 to 25°C, and any further water may be added as required for achieving a certain desired concentration and viscosity
  • the mixing is expediently carried out with stirring and at a concentration of the components in water at which the composition is readily stirrable
  • the produced composition (M) - which in particular is a flowable aqueous dispersion - is ready for use and can be handled and applied analogously to any other coating composition for paper
  • any suitable support web or sheet especially paper, paperboard or board made from any desired conventional primary and/or secondary substances which are suitable for the production of paper, paperboard or board, in particular made from conventional fibre material, principally cellulosic fibre material, for example from hardwood (for example maple, birch, beech, poplar), from softwood (for example pine, spruce, larch, fir), from annual plants (for example straw, jute, ramie, bagasse, flax, hemp, reed, sisal, coconut, cotton) or from textile fibres (for example rags, cotton, linen, flax, ramie, jute) or also from recycled paper production waste or from used paper, where the non- digested fibres, namely textile fibres, wood fibres and fibres from annual plants, can be processed in a manner which is conventional per se to give pulp, for example by mechanical and/or chemical and/or thermal methods (in particular wood pulp
  • the material can be bleached with conventional bleaching agents, for example reductively and/or oxidatively (for example with sodium hydrosulphite, thiourea dioxide or hydrogen peroxide)
  • the substrates may be lignm-free or Iignin-contaming, e.g. containing > 5 %, preferably > 10 %, of hgnin, based on dry fibres, such as paper containing wood pulp or semichemical pulp or board containing wood pulp or semichemical pulp.
  • the pulp or the corresponding fibres can, if desired after blending various types of fibre and/or types of pulp with one another, for example from mechanically digested pulp and/or chemically (sulphite or sulphate method) and/or thermally digested pulp and/or combination-digested pulp (semichemical pulp), be processed further, optionally with at least 10 % of recycled paper or used paper
  • any desired conventional additives which are suitable for papermaking, such as, for example drainage and/or retention agents, and if desired optical bnghteners, dyes, sizing agents and/or fillers (for example kaolin, talc or other silicates or calcium carbonate), as can usually be admixed with the aqueous pulp composition before sheet formation, and fixatives.
  • the aqueous pulp suspension intended and formulated for the production of the web can be applied in any conventional manner to the wire end, where the dewate ⁇ ng to the desired water content takes place.
  • the web is then transported to the press section, where the water content is reduced further, for example usually in the range from 70 to 30 %, so that the moist sheet reaches the dry end with a water content of ⁇ 30 %.
  • the support sheet produced is usually fed through the calender (intermediate or dry calender) or otherwise through drying rolls and can if desired by given a surface sizing.
  • the coating with (M) can be carried out subsequently during papermaking, or the not yet coated paper or board may be dried and rolled up and the coating with (M) is then carried out afterwards, more particularly at the final user's factory, more particularly immediately before printing.
  • (M) may be applied to the face of the substrate or also to both sides.
  • the coating of the invention may be carried out by any suitable method conventional per se in which pressure is applied either during coating or after application of the coating composition (M) to the substrate or both
  • the substrate coated with (M) may thus be dried at elevated temperature, preferably at a temperature in the range of 60 to 150°C, preferably through drier rolls, and may then optionally be calendered or embossed, or the coated and not yet dried web may be subjected to pressure by conventional means, e g. by means of an air knife, a rod or bar, a blade or brushes (for improving penetration and distribution of the coating) or to roll pressure, and is then dried, or/and the coated substrate may be subjected to plate or cylinder pressure optionally after drying e g through drier rolls.
  • Conventional application coating techniques which may be mentioned and are suitable for the application of (M) according to the invention are e.g.: air knife coating, rod or bar coating, blade coating, transfer roll coating, size press coating, kiss roll coating, spray coating, brush coating, dip coating, reverse roll coating and cast coating
  • air knife coating, rod or bar coating, blade coating, transfer roll coating, size press coating, kiss roll coating, spray coating, brush coating, dip coating, reverse roll coating and cast coating In some of these pressure is already applied during application of the coating composition, such as in air knife coating, rod or bar coating, blade coating, transfer roll coating, size press coating, reverse roll coating and cast coating, in the other pressure is applied after application of the coating composition, such as in kiss roll coating, spray coating, brush coating and dip coating.
  • the applied pressure may vary broadly and is e g > 0.5 bar, preferably is > 1 bar superatmosphe ⁇ c pressure, and may range e.g. up to the maximum pressure allowed by the employed machine and system.
  • the coated paper or board after having been coated is subjected to pressure, e g through drier rolls, or according to a still further preferred feature, it is subjected to pressure after having been intermediately dried, preferably this latter variant comprises subjecting the coated and intermediately dried substrate to pressure by means of cylinders or plates, in particular by calendering or embossing, or/and when applying a water mark to the paper or/and when printing
  • the quantity of (A) applied to the substrate may be in any desired range, suitably it is present in such a proportion as to provide - in the (M)-coated substrate - a perceivable effect in the coating, in particular in the physical properties of the coated material (mainly brilliance, whiteness, opacity and pnntabihty) and especially in flame retarding properties
  • the invention thus further provides a process for coating and flame-proofing the stated substrates by coating with (M) as described above, wherein (A) is present in a concentration efficient for providing a flame- proofing action (M) may be applied to the substrate in a coating weight (dry substance) e g in the range of 0 1 to 100 g/m (for paper preferably 0 1 to 60 g/m more preferably - depending on
  • the suitable and preferred concentrations and viscosities may vary not only depending on the particular substrate, composition and desired effect but also on the chosen particular application method and apparatus Thus for some representative application methods of those mentioned above the preferred way of working is as follows
  • An excess of coating mix (M) is applied to the base paper and the mobile portion is metered off by means of air
  • the air is delivered through a carefully controlled slot having an air pressure between 5 and 45 kilo Pascals, that cuts into the fluids portion of the coating layer like a knife
  • the solids content of (M) is preferably in the range 35-50 % and and the viscosity is preferably in the range of 100-400 mPa s, with which defect free and print mottle free coatings may be achieved
  • Typical coat weights using air knife configurations preferably range from 4-30 g/m
  • the preferred metering will in particular be selected depending on the particular employed apparatus, nature of the substrate and composition of (M), mainly by 1
  • An excess of coating mix (M) is applied to the base paper with the surplus being metered off using a rod or bar (normally termed metering bar or rod)
  • the metering bar may be stationary or rotating with or against the direction of the web Smooth bars normally meter the coating by an applied pressure, whilst wire wound bars (sometimes called Meyer bars), have a secondary metering effect
  • the coating mix is contained in the valleys between the windings, thus depending on the size of the wire used, the valleys will contain a corresponding amount of coating mix
  • a particular bar may be chosen
  • the solids content of (M) is preferably in the range 30-63 % and and the viscosity is preferably in the range of 100-1500 mPa s, with which defect free and print mottle free coatings may be achieved
  • Typical coat weights using bar or rod configurations preferably range from 2-15 g/m
  • the preferred metering will in particular be selected depending on the particular employed apparatus, nature of the substrate and composition of (M), mainly by
  • An excess of coating mix (M) is applied to the base paper with the surplus being metered off (scraped off) using a blade
  • the viscosity of the coating mix (M) will change depending on the shear rate applied to it during the coating process This will depend upon the coater speed, pressure applied to the blade, blade geometry (l e angle, thickness, etc ) and the degree of compressibility of the web
  • the solids content of (M) is preferably in the range 45-75 % and the viscosity is preferably in the range of 700-3500 mPa s, with which defect free and print mottle free coatings may be achieved
  • Typical coat weights using blade configu- rations preferably range from 2-25 g/m
  • the preferred metering will in particular be selected depending on the particular employed apparatus, nature of the substrate and composition of (M), mainly by
  • the coating mix (M) is progressively transferred from one roll to other, being evened out as it travels before being transferred to the web
  • Any conventional number of transfer rolls can be employed, but preferably 2 to 15 are used
  • the rolls can be made of various materials and can operate in different directions and speeds
  • the solids content of (M) is preferably in the range of 30-60 % and the viscosity is preferably in the range of 100-800 mPa s, with which defect free and print mottle free coatings may be achieved
  • Typical coat weights using transfer roll configurations preferably range from 0 5-15g/m
  • the preferred metering will in particular be selected depending on the particular employed apparatus, nature of the substrate and composition of (M), mainly by
  • the application of (M) can be carried out on one or both sides, depending on the type and purpose of the paper or board
  • One-sided application is suitable, for example, for a cardboard top layer, for label, poster or packing paper
  • Two-sided application is suitable, for example, for graphic papers, book printing, magazine, newspaper, letter, drawing or office paper, or also for special single-layer types of cardboard, such as, for example Bristol board
  • the invention provides the possibility of producing a most broad choice of coatings in various kinds and of optimum properties and in particular of high flame retarding properties In particular, by the possibility of using various ways of application and of processing (also in the drier section and/or in calendering), by employing various kinds, consistencies and quantities of coating composition on various kinds of substrates, a correspondingly very broad choice of coated product of high flame retarding efficiency and fine appearance, in particular optimum whiteness and graphic properties, becomes available
  • the coating process of the invention it is possible to obtain, even with coating compositions (M) that do not contain any (P), coatings of excellent, surprisingly high whiteness, bnllancy, opacity and surface properties and simultaneously with high flame retarding efficiency
  • coating compositions (M) that do not contain any (P)
  • the whiteness may even be increased
  • They are suitable for producing coated substrates, especially paper, paperboard and board, of outstanding graphic properties, especially pnntabihty properties, for which any kind of printing method is suitable, e g offset printing, ink jet, laser or screen printing or any other kind of printing methods, including typing and photocopying
  • the further physical properties of the coated material are not impaired, such as strength, pliability and compressibility, and the flame retarding properties are optimal
  • the coating process of the invention is suitable for producing any kind of coated paper, paperboard, board or non-woven tissue, especially coated paper for printing purposes, preferably of 50 to 400 g/m , such as letter, magazine, newspaper, drawing or office paper, book
  • a further subject-matter of the invention is the process for the production of a substrate which has been graphically processed, in particular written on, printed and/or graphically processed in any other manner by application of at least one graphic ink pattern to said substrate, and drying, which is characterized in that the substrate used for this purpose is a flat substrate as described above, especially paper, paperboard, board or non-woven tissue, which has been coated with (M) and subjected to pressure as described above
  • the coating process of the invention in particular as described above, there may be produced coated paper or paperboard with a smooth, level, regular surface, which is particularly suitable as a substrate for printing.
  • Especially printing processes as mentioned above can be used, principally intaglio printing, newspaper printing, letterpress printing and offset printing in general
  • a same level paper or paperboard can be used as substrate both for intaglio printing and for offset printing.
  • Printing can be carried out using any desired conventional printing inks which contain constituents which are conventional per se, essentially at least one dye and a suitable carrier or a suitable binder and optionally additives.
  • dyes principally pigments (for example those as defined and also listed under "Pigments" in the Colour Index), optionally combined with mineral fillers, come into consideration, as usually employed in printing inks; as binders, principally resins, which are advantageously mixed with oils, come into consideration.
  • the resins are mostly alkyd resins and/or or phenyl-modified colophony resins and can, if desired, be blended with further carrier substances, such as suitable types of asphalt; as oils, oxidatively drying oils (principally vegetable oils, in particular linseed oil or wood oil) and physically drying mineral oils can be employed
  • drying agents are advantageously employed, such as, for example, tin, cobalt or manganese salts, for example manganese octanoate, or/and optionally further additives, such as waxes
  • Such components and additives or corresponding printing inks are known in general terms and are described in large number in the specialised literature, for example in EP-A-42515, 228372 and 666293. If desired, however, water-borne printing inks can also be used, for example those as described in EP-A-633143 The composition of such printing inks is, for example,
  • additives for example drying agents and, if desired, waxes.
  • the employed ammonium polyphosphate II is of average particle size 10 ⁇ m with no particles exceeding 40 ⁇ m obtained by comminuting the commercially available ammonium polyphosphate II Exolit® AP 422 in a ball mill, the other components employed in the compositions and examples are commercially available products
  • the papers employed in the following examples are those produced in the paper mill and how they are employed in the respective paper production step which corresponds to the following examples. DIN stands for Manual Industrie-Norm, NF stans for Norme Francaise and BS stands for British Standard.
  • the following coating compositions (M) are employed, which are produced by mixing at 22°C the ammonium polyphosphate and any further pigment with water and with calcium stearate with stirring, and then adding the binder and then the other components.
  • sodium polyacrylate dispersant in Coating Compositions Ml to M5 there may be employed e.g. DISPEX N40 (Ciba)
  • ammonium polyacrylate dispersant in Coating Compositions M6 and M7 there may be employed e.g. Mowiplus XW330 (Clanant)
  • acrylic copolymer binder in Coating Compositions M2 and M5 there may be employed e g
  • melamine/formaldehyde resin in Coating Compositions M l and M3 to M7 there may be employed e.g. Beetle Resin PT-3745 (BIP).
  • BIP Beetle Resin PT-3745
  • the melamine polyphosphate of coating composition M7 is of water solubility ⁇ 0.1 g/1 at 20°C, particle size distribution: 98 % ⁇ 25 ⁇ m and 50 % ⁇ 10 ⁇ m, nitrogen content 42-44 % and phosphor content 12-14 %, e.g. MELAPUR® 200 (DSM).
  • MELAPUR® 200 DSM
  • calcium stearate there may be employed e.g. NOPCOTE C104 (Henkel).
  • the l,2-benz- ⁇ soth ⁇ azol ⁇ n-3-one fungicide may be employed e.g. in the form of the commercial product PROXEL BD20 (Avecia).
  • optical bnghtener in Coating Composition M6 is of formula
  • a wood free, surface sized and uncoated paper (100g/m 2 )[made of 50% hardwood, 50 % softwood] is coated with Coating Composition Ml by means of a trailing blade (set 30° to backing roll), at a pressure of 6 bar/mm, at a speed of 600 m/min to a coating weight of 20 g/m (dry substance), and is then pre-dned using short wave infrared and completed using conventional high velocity hot air driers.
  • a wood free, unsized and uncoated paper (150g/m 2 )[made of 20% hardwood, 80% softwood] is coated with M2 by means of a screen coater (1mm mesh), at a pressure of 1 bar, at a speed of 100 m/min to a coating weight of 50 g/m (dry substance), and is then dried using conventional high velocity hot air driers, before being embossed at 5 bar
  • Coating Composition M2 Coating Compositions M3 and M5 are employable in Example 2
  • a wood free, unsized and uncoated paper (85 g/m 2 )[made of 45 % hardwood, 55 % softwood] is coated with M3 by means of a smooth metering rod, at a pressure of 3 bar, at a speed of 600 m/min to a coating weight of 15 g/m (dry substance), and is then pre-dned using short wave infrared drier and completed using conventional high velocity hot air driers, before being super- calendered at 350 kN/m
  • Coating Composition M3 Coating Compositions Ml, M2, M4, M5 and M6 are employable in Example 3
  • a wood free, unsized and uncoated paper (85 g/m 2 )[made of 45 % hardwood, 55 % softwood] is coated with M4 by means of a airknife, at a air pressure of 30 Kpa (0 4 mm gap), at a speed of 300 m/min to a coating weight of 15 g/m (dry substance), and is then pre-dned using short wave lnfrared drier and completed using conventional high velocity hot air driers, before being super- calendered at 350 kN/m.
  • Coating Composition M4 Analogously as the Coating Composition M4, Coating Compositions M2, M3 and M5 are employable in Example 4.
  • a wood free, unsized and uncoated paper (90 g/m 2 )[made of 45 % hardwood, 55 % softwood] is coated with M5 by means of a air knife, at a air pressure of 30 Kpa (0.4 mm gap), at a speed of 400 m/min to a coating weight of 15 g/m (dry substance), and is then pre-dned using short wave infrared drier and completed using conventional high velocity hot air driers, before being calendered at 100 kN/m.
  • Coating Composition M5 Coating Compositions M2, M3 and M4 are employable in Example 5
  • a wood free, surface sized and uncoated paper (100 g/m 2 )[made of 50 % hardwood, 50 % softwood] is coated with Coating Composition Ml by means of a trailing blade (set 30° to backing roll), at a pressure of 6 bar/mm, at a speed of 600 m/min to a coating weight of 20 g/m (dry substance), and is then pre-dned using short wave infrared and passed through a soft nip calender located after the last drying section, using a combination of hard-chilled iron rolls and elastomer- covered rolls.
  • Coating Composition Ml Coating Compositions M2, M3, M6 and M7 are employable in Example 6.
  • a wood free, coated paper produced according to Example 1 (120 g/m 2 ) cut to the dimensions 360 mm x 520 mm (B3) is printed with inks conforming to BS 4666 by means of a sheet fed four colour off-set litho printing press, at a speed of 4000 impressions an hour. There is obtained a high quality print.
  • Example 1 In the same way as the coated paper produced according to Example 1 there may be printed the papers coated according to each of Examples 2, 3, 4, 5 and 6.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Paper (AREA)

Abstract

Cette invention se rapporte à un procédé servant à produire un substrat plat fibreux cellulosique couché et pressé, en fibres non filées, éventuellement non-tissées, ce procédé consistant à appliquer sur la face du substrat: (M) une composition de revêtement aqueuse, contenant un liant (B), un pigment blanc (W) et un dispersant (D), au moins une partie dudit pigment blanc (W) étant constituée par (A) un polyphosphate d'ammonium particulaire de forme cristalline II ayant une granulométrie moyenne inférieure à 40 νm et une solubilité dans l'eau inférieure à 10 g/l à 25 °C; puis à soumettre une tel substrat à une pression. Cette invention concerne en particulier un tel procédé pour la production de substrats couchés et pressés aux propriétés de surface exceptionnelles, particulièrement appropriés pour des traitements graphiques, et aux propriétés de non inflammabilité exceptionnelles, à des compositions de revêtement appropriées, à leur production, aux substrats ainsi couchés et pressés et à leur utilisation comme substrats pour des traitements graphiques, tels que notamment l'impression.
PCT/IB2001/002256 2000-11-29 2001-11-28 Procede pour la production d'un substrat plat fibreux cellulosique couche et presse, compositions de revetement appropriees, leur production, substrats ainsi couches et presses et leur utilisation comme substrats pour traitements graphiques WO2002044470A1 (fr)

Priority Applications (3)

Application Number Priority Date Filing Date Title
EP01998162A EP1341965A1 (fr) 2000-11-29 2001-11-28 Procede pour la production d'un substrat plat fibreux cellulosique couche et presse, compositions de revetement appropriees, leur production, substrats ainsi couches et presses et leur utilisation comme substrats pour traitements graphiques
CA002424360A CA2424360A1 (fr) 2000-11-29 2001-11-28 Procede pour la production d'un substrat plat fibreux cellulosique couche et presse, compositions de revetement appropriees, leur production, substrats ainsi couches et presses etleur utilisation comme substrats pour traitements graphiques
US10/432,520 US20040094279A1 (en) 2000-11-29 2001-11-28 Process for the production of a coated and pressed cellulosic fibrous flat substrate, suitable coating compositions, their production, the coated and pressed substrates and their use as substrates for graphic processes

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GBGB0029071.8A GB0029071D0 (en) 2000-11-29 2000-11-29 Coating
GB0029071.8 2000-11-29

Publications (1)

Publication Number Publication Date
WO2002044470A1 true WO2002044470A1 (fr) 2002-06-06

Family

ID=9904081

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/IB2001/002256 WO2002044470A1 (fr) 2000-11-29 2001-11-28 Procede pour la production d'un substrat plat fibreux cellulosique couche et presse, compositions de revetement appropriees, leur production, substrats ainsi couches et presses et leur utilisation comme substrats pour traitements graphiques

Country Status (5)

Country Link
US (1) US20040094279A1 (fr)
EP (1) EP1341965A1 (fr)
CA (1) CA2424360A1 (fr)
GB (1) GB0029071D0 (fr)
WO (1) WO2002044470A1 (fr)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004044322A1 (fr) * 2002-11-06 2004-05-27 Kimberly-Clark Worldwide, Inc. Melanges de copolymeres d'acrylate cationiques/polysiloxanes modifies d'un point de vue hydrophobique et utilisation dans les tissus ouates
EP1960485A2 (fr) * 2005-12-12 2008-08-27 Osmose, Inc. Composition et processus de coloration de bois
WO2008131985A3 (fr) * 2007-04-30 2009-11-05 Pfleiderer Holzwerkstoffe Gmbh & Co. Kg Composition biocide et compositions de résine, matériaux composites et laminés qui la contiennent
WO2009144379A2 (fr) * 2008-05-27 2009-12-03 Ahlstrom Corporation Procédé de fabrication de papiers résineux, papiers résineux et leur utilisation comme ébauches de préforme résineuse
US7794565B2 (en) 2002-11-06 2010-09-14 Kimberly-Clark Worldwide, Inc. Method of making low slough tissue products
WO2013003944A1 (fr) 2011-07-06 2013-01-10 National Research Counsil Of Canada Matière cellulosique résistante au feu
EP2784216A1 (fr) * 2013-03-27 2014-10-01 Dow Global Technologies LLC Formulation de revêtement de papier

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20100239467A1 (en) * 2008-06-17 2010-09-23 Brent Constantz Methods and systems for utilizing waste sources of metal oxides
JP5373079B2 (ja) 2008-07-16 2013-12-18 カレラ コーポレイション 電気化学システム中でのｃｏ２の利用
US8869477B2 (en) 2008-09-30 2014-10-28 Calera Corporation Formed building materials
TW201026597A (en) 2008-09-30 2010-07-16 Calera Corp CO2-sequestering formed building materials
US7815880B2 (en) * 2008-09-30 2010-10-19 Calera Corporation Reduced-carbon footprint concrete compositions
EP2245215A4 (fr) 2009-02-10 2011-04-27 Calera Corp Production à basse tension d'agents alcalins au moyen d'hydrogène et d'électrodes électrocatalytiques
US8883104B2 (en) 2009-03-02 2014-11-11 Calera Corporation Gas stream multi-pollutants control systems and methods
WO2011008631A2 (fr) * 2009-07-16 2011-01-20 Omnova Solutions Inc. Compositions de revêtement protecteur
DE102013222223A1 (de) * 2013-10-31 2015-04-30 Bk Giulini Gmbh Blutstillendes Mittel enthaltend kristallines Polyphosphat
FI127949B (fi) * 2014-04-09 2019-05-31 Metsae Board Oyj Päällystetty kartonki ja menetelmä sen valmistamiseksi
ES2588261B1 (es) * 2016-04-15 2017-05-10 Universidad Politécnica De Cartagena Envase de cartón para envasado activo de frutas y hortalizas frescas, y procedimiento de fabricación del mismo
WO2022152574A1 (fr) * 2021-01-18 2022-07-21 Foresa Technologies, S.L.U. Formulation ignifuge et antifumée et matériaux cellulosiques comprenant une telle formulation

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0357421A2 (fr) * 1988-08-31 1990-03-07 ALBRIGHT & WILSON UK LIMITED Agents ignifuges et méthode d'utilisation
US5049187A (en) * 1990-03-26 1991-09-17 Eastman Kodak Company Aqueous solution for forming a fire-retardant protective coating
EP0460516A2 (fr) * 1990-05-29 1991-12-11 Albright & Wilson Limited Composition à couchage et procédé
JPH06287892A (ja) * 1993-03-31 1994-10-11 Nippon Paper Ind Co Ltd 難燃紙及びその製造方法
DE19528721A1 (de) * 1994-08-05 1996-02-08 Jujo Paper Co Ltd Tapetengrundlage
US5498471A (en) * 1990-08-21 1996-03-12 Firma Carl Freudenberg Flame-resistant substrate for flexible circuit boards

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2867549A (en) * 1956-03-06 1959-01-06 Albemarle Paper Mfg Company Process for flameproofing paper
US3658579A (en) * 1970-04-15 1972-04-25 Monsanto Co Flame-retardant, bonded nonwoven fibrous product employing a binder comprising an ethylene/vinyl chloride interpolymer and an ammonium polyphosphate
US4247435A (en) * 1978-10-02 1981-01-27 Monsanto Company Intumescent fire retardant coating compositions
DE4343668A1 (de) * 1993-12-21 1995-06-22 Hoechst Ag Aufblähbare, flammhemmende Überzugsmassen
DE19909387C2 (de) * 1999-03-04 2001-01-25 Clariant Gmbh Brandschutzbeschichtung

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0357421A2 (fr) * 1988-08-31 1990-03-07 ALBRIGHT & WILSON UK LIMITED Agents ignifuges et méthode d'utilisation
US5049187A (en) * 1990-03-26 1991-09-17 Eastman Kodak Company Aqueous solution for forming a fire-retardant protective coating
EP0460516A2 (fr) * 1990-05-29 1991-12-11 Albright & Wilson Limited Composition à couchage et procédé
US5498471A (en) * 1990-08-21 1996-03-12 Firma Carl Freudenberg Flame-resistant substrate for flexible circuit boards
JPH06287892A (ja) * 1993-03-31 1994-10-11 Nippon Paper Ind Co Ltd 難燃紙及びその製造方法
DE19528721A1 (de) * 1994-08-05 1996-02-08 Jujo Paper Co Ltd Tapetengrundlage

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
DATABASE WPI Section Ch Week 199445, Derwent World Patents Index; Class F09, AN 1994-364164, XP002192482 *

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004044322A1 (fr) * 2002-11-06 2004-05-27 Kimberly-Clark Worldwide, Inc. Melanges de copolymeres d'acrylate cationiques/polysiloxanes modifies d'un point de vue hydrophobique et utilisation dans les tissus ouates
US7794565B2 (en) 2002-11-06 2010-09-14 Kimberly-Clark Worldwide, Inc. Method of making low slough tissue products
EP1960485A2 (fr) * 2005-12-12 2008-08-27 Osmose, Inc. Composition et processus de coloration de bois
EP1960485A4 (fr) * 2005-12-12 2009-07-08 Osmose Inc Composition et processus de coloration de bois
WO2008131985A3 (fr) * 2007-04-30 2009-11-05 Pfleiderer Holzwerkstoffe Gmbh & Co. Kg Composition biocide et compositions de résine, matériaux composites et laminés qui la contiennent
WO2009144379A2 (fr) * 2008-05-27 2009-12-03 Ahlstrom Corporation Procédé de fabrication de papiers résineux, papiers résineux et leur utilisation comme ébauches de préforme résineuse
WO2009144379A3 (fr) * 2008-05-27 2010-01-21 Ahlstrom Corporation Procédé de fabrication de papiers résineux, papiers résineux et leur utilisation comme ébauches de préforme résineuse
WO2013003944A1 (fr) 2011-07-06 2013-01-10 National Research Counsil Of Canada Matière cellulosique résistante au feu
US9175147B2 (en) 2011-07-06 2015-11-03 National Research Council Of Canada Fire-resistant cellulosic material
EP2784216A1 (fr) * 2013-03-27 2014-10-01 Dow Global Technologies LLC Formulation de revêtement de papier

Also Published As

Publication number Publication date
GB0029071D0 (en) 2001-01-10
EP1341965A1 (fr) 2003-09-10
CA2424360A1 (fr) 2002-06-06
US20040094279A1 (en) 2004-05-20

Similar Documents

Publication Publication Date Title
US20040094279A1 (en) Process for the production of a coated and pressed cellulosic fibrous flat substrate, suitable coating compositions, their production, the coated and pressed substrates and their use as substrates for graphic processes
US20190309478A1 (en) Paper substrate having enhanced print density
EP1214470B1 (fr) Finition de surface de papier ou de carton et agent a cet effet
CA2627050C (fr) Substrat en papier presentant une densite d'impression accrue
EP1303668B1 (fr) Procede et composition de revetement pour le revetement d'une bande de papier
US4867844A (en) Method for treating paper to improve the holdout characteristics of printing inks
US8057637B2 (en) Paper substrate containing a wetting agent and having improved print mottle
CN100519936C (zh) 涂覆的纤维网及其制备方法
CN101952508A (zh) 制纸用添加剂和含有其的纸
CA2929377A1 (fr) Procede pour ameliorer l'efficacite de collage d'une emulsion asa emulsifiee par un emulsifiant polymere
KR20110106472A (ko) 종이 코팅 용도에서의 알루미늄 포스페이트, 폴리포스페이트 및 메타포스페이트 입자의 용도
EP1794366B1 (fr) Procede de production d'une substance a base de cellulose, et substance ainsi produite
Auhorn Chemical additives
US8778504B2 (en) Paper coating composition, paper coated therewith and method for producing coated paper
WO2000022232A1 (fr) Application de colorants dans la partie humide d'une machine a papier
CA1148706A (fr) Preparation de fibres hydrophiles de polyolefine pour l'emploi en fabrication du papier
JP2015110848A (ja) 印刷用塗工紙の製造方法
EP3877588A1 (fr) Papier d'impression de livre
JP2019014984A (ja) 中芯原紙

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): CA US

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE TR

DFPE Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101)
121 Ep: the epo has been informed by wipo that ep was designated in this application
WWE Wipo information: entry into national phase

Ref document number: 2424360

Country of ref document: CA

WWE Wipo information: entry into national phase

Ref document number: 2001998162

Country of ref document: EP

WWE Wipo information: entry into national phase

Ref document number: 10432520

Country of ref document: US

WWP Wipo information: published in national office

Ref document number: 2001998162

Country of ref document: EP

WWW Wipo information: withdrawn in national office

Ref document number: 2001998162

Country of ref document: EP