EP0223922A1 - Process for producing paper webs impregnated with synthetic resins in a soluble or dispersed form - Google Patents

Process for producing paper webs impregnated with synthetic resins in a soluble or dispersed form Download PDF

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Publication number
EP0223922A1
EP0223922A1 EP86110511A EP86110511A EP0223922A1 EP 0223922 A1 EP0223922 A1 EP 0223922A1 EP 86110511 A EP86110511 A EP 86110511A EP 86110511 A EP86110511 A EP 86110511A EP 0223922 A1 EP0223922 A1 EP 0223922A1
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EP
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Prior art keywords
paper
paper web
dispersion
mixture
impregnation
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EP86110511A
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German (de)
French (fr)
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EP0223922B1 (en
EP0223922B2 (en
Inventor
Bernd Dr. Ing. Reinhardt
Helmut Ing. Grad. Dottermusch
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Kammerer GmbH
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Kammerer GmbH
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Priority to AT86110511T priority Critical patent/ATE59416T1/en
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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
    • D21H17/20Macromolecular organic compounds
    • D21H17/33Synthetic macromolecular compounds
    • D21H17/34Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • 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
    • D21H17/20Macromolecular organic compounds
    • D21H17/33Synthetic macromolecular compounds
    • D21H17/34Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/41Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups
    • D21H17/42Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups anionic

Definitions

  • the invention relates to a method for producing paper webs impregnated with synthetic resins in the form of solutions and dispersions.
  • PVC films are e.g. B. glued on chipboard and then are made of this composite material in accordance with furniture engineering principles furniture parts or housings in one operation, d. H. that one cuts into the chipboard V-shaped grooves and then folds or bends the plates in these grooves and so produces housing, furniture part or the like in one operation.
  • a disadvantage of this process is that the PVC film must be subjected to a corresponding surface treatment, for example a corona treatment, before it can be used directly and in order to achieve good printability.
  • the chipboard must have a very clean and smooth surface so that economically justifiable results can be achieved (application of thin foils).
  • the PVC film has a very unfavorable dimensional stability (expansion / shrinkage behavior) when there are temperature changes, has low tear resistance, has low light stability and has high electrostatic chargeability and softening at 75 to 85 ° C .
  • HCl separation When heated to more than 120 ° C, HCl separation also takes place.
  • the object of the present invention is therefore to produce a sheet-like, synthetic resin-containing, sheet-like material which does not have the disadvantages of the commonly used pure plastic film, moreover has good flexibility, has water resistance and resistance to solvents as well as internal strength and good dimensional stability when exposed to moisture and temperature changes.
  • Impregnating resin solutions are resins based on urea, melamine and phenolic resins and contain formaldehyde and lead to brittle products.
  • DE-OS 30 24 394 describes a process for producing a plastic tournament in a paper machine, in which the paper web in the dryer section is provided with an impregnation which is carried out in the size press.
  • the impregnation of the paper web with the impregnation liquid which is not described in any more detail, in the press is only complete when the paper web is already pre-impregnated, so that additional devices are also required here.
  • the problem is now solved in that the paper web is formed from a cellulose fiber mixture of high absorbency and strength, which is ground to a grinding degree of at most 35 ° SR and the impregnation liquid consists of a mixture of aqueous, anionic copolymer dispersions and aqueous, anionic polymeric solutions with a pH between 7.5 and 10 and the application is carried out with a size press in the dryer section of the paper machine.
  • the pH is preferably between 8 and 9.
  • the pulp of the paper web preferably consists of eucalyptus pulp and pine wood sulfate pulp in a ratio of 50:50 to 10:90, preferably 30:70 to 15:85.
  • the degree of grinding is preferably between 15 and 25 ° SR .
  • the fillers are to be understood as white pigments e.g. B. TiO2, chalk, kaolin.
  • Formaldehyde-free wet strength agent in an amount of 1 to 5% by weight, based on the atro fibrous material, in the form of, for example, polyamideamine-epichlorohydrin resin and addition of a synthetic resin dispersion, for example based on acrylic acid ester, has proven particularly advantageous in the sense of the invention or styrene-butadiene in an amount of 1 to 20%, based on dry fiber and a small addition of surfactants for better wettability of the paper, in an amount of ⁇ 0.5% based on dry fiber.
  • the dispersed particles are preferably less than 0.2 ⁇ m and of low to medium film hardness and a low minimum Film formation temperature, preferably below 30 ° C.
  • the ratio between the two copolymers of the dispersion and the solution is preferably 500: 1 to 1: 1, preferably 100: 1 to 10: 1, based on the active substance, ie. H. 500 parts of dispersion in 1 part of solution to 10 parts of dispersion in 1 part of solution.
  • plastics for.
  • the brittle character of the impregnated paper can be reduced by using the mixture according to the invention with a portion of impregnating resin solution.
  • auxiliaries such as wetting agents, viscosity regulators, non-stick and penetration aids, pigments, dyes and defoamers can also be added to these impregnation substance mixtures.
  • Substances are used as wetting and penetration agents that change the interfacial tension between the liquid phase and solid phase, e.g. B. surfactants and emulsifiers.
  • the penetration of the impregnation liquid can be advantageously influenced by a combination of maleic acid copolymers and these substances which change the interfacial tension.
  • this impregnation substance is used in the form of a mixture of solution and dispersion with a solids content of 5 to 60%, the viscosity being between 10 and 60 s (according to DIN cup, 4 mm).
  • This impregnation and coating mixture is applied to the nonwoven within the paper machine in a roller application device (size press).
  • a roller application device size press
  • the nonwoven fabric with a dry matter content of 98 to 92% is fed through a size press and the impregnation is carried out on both sides.
  • a further one-sided or double-sided surface covering ie. H. Coating
  • the nonwoven fabric can be carried out within the paper machine with the same or a similarly structured copolymer mixture, intermediate drying should take place between the two individual process stages.
  • a subsequently applied coating on one side of the dried web results in a denser surface which is easier to print or coat or laminate. If only a further one-sided surface coating is carried out, this can be carried out by means of a doctor application device. One-sided rolling of the coated paper web can be avoided by an additional application on the back.
  • Such an application can be, for example, a strongly aqueous solution of starch or CMC.
  • An additional smoothing of the impregnated and coated on one side z. B. with known smoothing machines or in a separate operation in a calender increases the desired printability and paintability of the coated side.
  • This fibrous film of different thicknesses and different bulk densities produced in this way is particularly suitable in a firm bond with a relatively rigid and rigid base, e.g. B. chipboard, as a decorative and protective covering of furniture parts such. B. television and radio housings or hi-fi towers (housing casing).
  • a relatively rigid and rigid base e.g. B. chipboard
  • the fiber-containing film produced according to the invention of high flexibility, dimensional stability with temperature changes and with good barrier properties against water and solvent is also excellently suitable for other purposes such as, for. B. as the base material of high quality sanding paper for wet sanding, printing and advertising media, decorative wall material (e.g. flame retardant pigmented or unpigmented dimensionally stable wallpaper), adhesive tapes, backing paper z. B. for floor coverings.
  • decorative wall material e.g. flame retardant pigmented or unpigmented dimensionally stable wallpaper
  • adhesive tapes e.g. flame retardant pigmented or unpigmented dimensionally stable wallpaper
  • a base paper of the following composition and quality was produced as two-ply paper on a duplex paper machine: 80% pine wood sulfate pulp 20% eucalyptus pulp Freeness 30 ° SR (Schopper-Riegler) Additives, commercially available (calculated on dry cellulose): 1% talc 3% formaldehyde-free wet strength agent 0.3% wetting and dispersing agent
  • This base paper with a mass per unit area of 90 g / m 2 was impregnated on both sides with the synthetic resin mixture of dispersion and solution in a ratio of 20: 1 in a size press.
  • the surprisingly strong impregnation effect with this synthetic resin mixture according to the invention is probably due to a synergistic effect of the dispersion and solution used, which, when used alone, are far from the same desired good Allow paper properties to be achieved.
  • a pure synthetic resin dispersion reduces the due to its good film-forming properties Most water absorption, but the penetration into the base paper is insufficient. This is demonstrated by the only slightly improved values with regard to layer strength and rigidity.
  • wet strength agent does not cause any significant change in the properties of the impregnated paper.
  • the medium-hard synthetic resin dispersion (5) was replaced by a hard dispersion with a particle size of approximately 0.15 ⁇ m, minimum film-forming temperature approximately 25 ° C.
  • This dispersion was an aqueous copolymer dispersion based on acrylic acid ester and styrene.
  • Combinations of synthetic resin dispersions and impregnating resins such as. B. urea-formaldehyde resin, as are common for the impregnation of decorative base paper in separate impregnation plants, lead to the improvement of the properties of the base paper.
  • the type of synthetic resin dispersions used essentially determines the liquor absorption, porosity, water absorption and layer strength of the paper (see recipes 8 and 10).

Abstract

A description is given of the soaking or impregnation of a paper web consisting mostly of cellulose fibres by a combination of dispersions and solutions of synthetic resins in a roll-type application unit installed in the papermaking machine, where the nature, degree of beating and dispersion particle size and the mixing ratio of dispersion and solution are matched to one another, for the manufacture of a fibre-containing sheet, in particular for covering parts of furniture.

Description

Die Erfindung betrifft ein Verfahren zur Herstellung von mit Kunstharzen in Form von Lösungen und Dispersionen imprägnierten Papierbahnen.The invention relates to a method for producing paper webs impregnated with synthetic resins in the form of solutions and dispersions.

Es ist üblich und bekannt, Gehäuse für Fernseh- und Radiogeräte, Hi-Fi-Türme und andere Möbelteile mit Kunst­stoffolie vollständig zu beschichten bzw. zu umhüllen. Man verwendet dazu vorzugsweise PVC-Folie unterschiedlicher Dicke.It is customary and known to completely coat or encase housings for televisions and radios, hi-fi towers and other furniture parts with plastic film. PVC film of various thicknesses is preferably used for this.

Diese PVC-Folien werden z. B. auf Holzspanplatten ge­klebt und anschließend werden aus diesem Verbundmaterial nach möbeltechnischen Grundsätzen Möbelteile oder Gehäuse in einem Arbeitsgang hergestellt, d. h. daß man in die Holz­spanplatten V-förmige Nuten einschneidet und dann die Platten in diesen Nuten faltet oder umbiegt und so in einem Arbeits­gang Gehäuse, Möbelteil oder dergleichen herstellt.These PVC films are e.g. B. glued on chipboard and then are made of this composite material in accordance with furniture engineering principles furniture parts or housings in one operation, d. H. that one cuts into the chipboard V-shaped grooves and then folds or bends the plates in these grooves and so produces housing, furniture part or the like in one operation.

Wichtig ist bei diesem Verfahren, daß an der Faltlinie kein Einreißen der Folie eintritt. Nachteilig an diesem Verfahren ist es wiederum, daß die PVC-Folie vor ihrer Ver­wendung direkt und zur Erzielung einer guten Bedruckbarkeit einer entsprechenden Oberflächenbehandlung, beispielsweise einer Koronabehandlung unterzogen werden muß.It is important in this process that the film does not tear at the fold line. A disadvantage of this process is that the PVC film must be subjected to a corresponding surface treatment, for example a corona treatment, before it can be used directly and in order to achieve good printability.

Außerdem müssen die Spanplatten eine sehr saubere und glatte Oberfläche aufweisen, damit noch wirtschaftlich ver­tretbare Ergebnisse erzielt werden können (Auftragung dünner Folien).In addition, the chipboard must have a very clean and smooth surface so that economically justifiable results can be achieved (application of thin foils).

Besonders nachteilig ist es aber, daß die PVC-Folie eine sehr ungünstige Dimensionsstabilität (Dehnungs-/Schrump­fungsverhalten) aufweist, wenn Temperaturänderungen erfolgen, niedrige Weiterreißfestigkeit aufweist, eine geringe Licht­stabilität besitzt sowie hohe elektrostatische Aufladbarkeit und eine Erweichung bei 75 bis 85° C bereits stattfindet. Bei Erwärmung auf mehr als 120° C findet außerdem eine HCl-­Abscheidung statt.However, it is particularly disadvantageous that the PVC film has a very unfavorable dimensional stability (expansion / shrinkage behavior) when there are temperature changes, has low tear resistance, has low light stability and has high electrostatic chargeability and softening at 75 to 85 ° C . When heated to more than 120 ° C, HCl separation also takes place.

Aufgabe der vorliegenden Erfindung ist es daher, ein folienförmiges, kunstharzhaltiges, bahnförmiges Material her­zustellen, das die Nachteile der üblicherweise verwendeten reinen Kunststoffolie nicht aufweist, darüber hinaus eine gute Flexibilität aufweist, Wasserfestigkeit besitzt und Beständigkeit gegen Lösungsmittel sowie auch eine innere Festigkeit und eine gute Dimensionsstabilität bei Feuchte­einwirkung und Temperaturänderungen.The object of the present invention is therefore to produce a sheet-like, synthetic resin-containing, sheet-like material which does not have the disadvantages of the commonly used pure plastic film, moreover has good flexibility, has water resistance and resistance to solvents as well as internal strength and good dimensional stability when exposed to moisture and temperature changes.

Außerdem soll das bahnförmige Material aus günstigen Rohstoffen in wirtschaftlicher Weise und mit möglichst keinen zusätzlichen Verfahrensstufen herstellbar sein, mit Ausnahme der Herstellung der geglätteten Papierbahn selbst.In addition, it should be possible to produce the web-shaped material from inexpensive raw materials in an economical manner and with as few additional process steps as possible, with the exception of the production of the smoothed paper web itself.

Aus der Literatur, beispielsweise aus der DE-PS 25 50 980 ist es bekannt, Rohpapierbahnen mit wäßrigen Tränkharzlösungen und/oder Dispersionen durch Einsaugen der Tränkflüssigkeit an einer Saugzone zu imprägnieren, wobei man eine wenigstens zur vollständigen Sättigung ausreichende Menge auf die Oberfläche der Papierbahn aufträgt und die Papierbahn anschließend über eine Saugzone führt, in der die Imprägnierflüssigkeit zur anderen Oberfläche durchgesaugt wird. Tränkharzlösungen sind aber Harze auf der Basis von Harnstoff-, Melamin- und Phenolharzen und formaldehydhaltig und führen zu spröden Produkten.From the literature, for example from DE-PS 25 50 980, it is known to impregnate raw paper webs with aqueous impregnating resin solutions and / or dispersions by sucking in the impregnating liquid at a suction zone, an amount sufficient at least for complete saturation being applied to the surface of the paper web and then the paper web over leads to a suction zone in which the impregnation liquid is sucked through to the other surface. Impregnating resin solutions, however, are resins based on urea, melamine and phenolic resins and contain formaldehyde and lead to brittle products.

Bei diesem Verfahren ist es erforderlich, die Roh­papierbahn nach ihrer Herstellung einer zweiten Vorrichtung zuzuführen und sie erneut abzurollen, zu imprägnieren unter Verwendung zusätzlicher Einrichtungen wie einer Saugzone und Trockenvorrichtung und sie wieder aufzurollen.With this method, it is necessary to feed the raw paper web to a second device after it has been produced and to unroll it again, to impregnate it using additional devices such as a suction zone and drying device, and to re-roll it.

Außerdem ist bei diesem Verfahren die Verteilung der Imprägnierflüssigkeit über den Papierquerschnitt ungleich­mäßig, so daß Zonen stärkerer Imprägnierung entstehen neben Zonen geringerer Imprägnierung, was zur Aufspaltung des Papierkerns führen kann.In addition, with this method the distribution of the impregnation liquid over the paper cross-section is uneven, so that zones of stronger impregnation are formed alongside zones of less impregnation, which can lead to the splitting of the paper core.

In der DE-OS 30 24 394 wird ein Verfahren zur Herstellung eines Kunststoffurniers in einer Papiermaschine beschrieben, bei dem die Papierbahn in der Trockenpartie mit einer Im­prägnierung versehen wird, die in der Leimpresse erfolgt. Die Durchtränkung der Papierbahn mit der nicht näher bezeichneten Imprägnierflüssigkeit in der Presse ist jedoch nur dann voll­ständig, wenn die Papierbahn bereits vorimprägniert ist, so daß also auch hier zusätzliche Einrichtungen erforderlich sind.DE-OS 30 24 394 describes a process for producing a plastic tournament in a paper machine, in which the paper web in the dryer section is provided with an impregnation which is carried out in the size press. However, the impregnation of the paper web with the impregnation liquid, which is not described in any more detail, in the press is only complete when the paper web is already pre-impregnated, so that additional devices are also required here.

Eine möglichst vollständige Durchtränkung und Imprägnierung des Rohpapieres ist erfindungsgemäß deshalb nur dann gegeben, wenn neben der Auswahl einer geeigneten Auftrags- bzw. Im­ prägniervorrichtung die Eigenschaften des Papieres wie z. B. Mahlungszustand und Mahlgrad, Absorptionsfähigkeit der Faser­stoffe, Porosität und Oberflächenrauheit auf die Eigenschaften der Imprägnierungs- bzw. der Beschichtungsmischung, d. h. deren Oberflächenspannung, Viskosität, Ladungszustand und Feststoffgehalt, abgestimmt sind.The most complete impregnation and impregnation of the raw paper is therefore only possible according to the invention if, in addition to the selection of a suitable application or embossing device the properties of the paper such. B. state of grinding and degree of grinding, absorbency of the fibrous materials, porosity and surface roughness are matched to the properties of the impregnation or coating mixture, ie the surface tension, viscosity, state of charge and solids content.

Erfindungsgemäß wird das Problem nun dadurch gelöst, daß die Papierbahn aus einem Zellstoffasergemisch von hoher Saug­fähigkeit und Festigkeit gebildet ist, das auf einen Mahlgrad von maximal 35° SR gemahlen ist und die Imprägnierflüssigkeit aus einem Gemisch wäßriger, anionischer Copolymerdispersionen und wäßriger, anionischer polymeren Lösungen besteht mit einem pH-Wert zwischen 7,5 und 10 und der Auftrag mit einer Leim­presse in der Trockenpartie der Papiermaschine durchgeführt wird. Vorzugsweise liegt der pH-Wert zwischen 8 und 9.According to the invention, the problem is now solved in that the paper web is formed from a cellulose fiber mixture of high absorbency and strength, which is ground to a grinding degree of at most 35 ° SR and the impregnation liquid consists of a mixture of aqueous, anionic copolymer dispersions and aqueous, anionic polymeric solutions with a pH between 7.5 and 10 and the application is carried out with a size press in the dryer section of the paper machine. The pH is preferably between 8 and 9.

Der Zellstoff der Papierbahn besteht in Verfolg der Er­findung vorzugsweise aus Eukalyptus-Zellstoff und Kiefernholz­sulfat-Zellstoff in einem Verhältnis von 50 : 50 bis 10 : 90, vorzugsweise von 30 : 70 bis 15 : 85. Der Mahlgrad liegt vor­zugsweise zwischen 15 und 25° SR.In accordance with the invention, the pulp of the paper web preferably consists of eucalyptus pulp and pine wood sulfate pulp in a ratio of 50:50 to 10:90, preferably 30:70 to 15:85. The degree of grinding is preferably between 15 and 25 ° SR .

Dem Faserstoff der Papierbahn können weitere chemische Hilfsmittel wie Naß- und Trockenfestmittel, Fällungsmittel (Fixiermittel), Kunstharzdispersionen, Tenside, Farbstoffe und Füllstoffe zugesetzt werden, die die Eigenschaften des Rohpapieres variieren.Further chemical auxiliaries such as wet and dry strength agents, precipitants (fixing agents), synthetic resin dispersions, surfactants, dyes and fillers, which vary the properties of the base paper, can be added to the fibrous material of the paper web.

Unter den Füllstoffen sollen verstanden werden Weiß­pigmente z. B. TiO₂, Kreide, Kaolin.The fillers are to be understood as white pigments e.g. B. TiO₂, chalk, kaolin.

Besonders günstig im erfindungsgemäßen Sinne hat sich formaldehydfreies Naßfestmittel in einer Menge von 1 bis 5 Gew.-%, bezogen auf den atro Faserstoff erwiesen, in Form von beispielsweise Polyamidamin-Epichlorhydrin-Harz sowie ein Zusatz einer Kunstharzdispersion z B. auf der Basis von Acrylsäureester oder Styren-Butadien in einer Menge von 1 bis 20 %, bezogen auf atro Faserstoff und ein geringer Zusatz von Tensiden zur besseren Benetzbarkeit des Papieres, in einer Menge von < 0,5 % bezogen auf atro Faserstoff.Formaldehyde-free wet strength agent in an amount of 1 to 5% by weight, based on the atro fibrous material, in the form of, for example, polyamideamine-epichlorohydrin resin and addition of a synthetic resin dispersion, for example based on acrylic acid ester, has proven particularly advantageous in the sense of the invention or styrene-butadiene in an amount of 1 to 20%, based on dry fiber and a small addition of surfactants for better wettability of the paper, in an amount of <0.5% based on dry fiber.

Bei der erfindungsgemäßen Verwendung der wäßrigen an­ionischen Copolymerdispersion, die beispielsweise auf der Basis von Acrylsäure, Acrylsäureestern, Vinylacetat und/oder Styrol aufgebaut sein kann, sind die dispergierten Teilchen vorzugsweise kleiner als 0,2 my und von geringer bis mittlerer Filmhärte und einer niedrigen Mindest-Filmbildungstemperatur, vorzugsweise unter 30° C.When the aqueous anionic copolymer dispersion, which can be based, for example, on acrylic acid, acrylic acid esters, vinyl acetate and / or styrene, is used according to the invention, the dispersed particles are preferably less than 0.2 μm and of low to medium film hardness and a low minimum Film formation temperature, preferably below 30 ° C.

Das Verhältnis zwischen den beiden Copolymerisaten der Dispersion und der Lösung beträgt vorzugsweise 500 : 1 bis 1 : 1, vorzugsweise 100 : 1 bis 10 : 1 auf die Wirksubstanz bezogen, d. h. 500 Teile Dispersion auf 1 Teil Lösung bis 10 Teile Dispersion auf 1 Teil Lösung.The ratio between the two copolymers of the dispersion and the solution is preferably 500: 1 to 1: 1, preferably 100: 1 to 10: 1, based on the active substance, ie. H. 500 parts of dispersion in 1 part of solution to 10 parts of dispersion in 1 part of solution.

Im Rahmen der vorliegenden Erfindung ist es auch möglich, andere Kunststoffe, z. B. Styren-Butadien-Mischpolymerisate, Polyurethan- oder Polyolefindispersionen sowie Tränkharz­ lösungen auf der Basis von Harnstoff- oder Melamin-Formalde­hyd-Harzen in Anteilen der Imprägniersubstanz zuzusetzen.In the context of the present invention, it is also possible to use other plastics, for. B. styrene-butadiene copolymers, polyurethane or polyolefin dispersions and impregnating resin Add solutions based on urea or melamine-formaldehyde resins in proportions of the impregnating substance.

Durch die Verwendung der erfindungsgemäßen Mischung mit einem Anteil Tränkharzlösung kann der spröde Charakter des imprägnierten Papieres vermindert werden.The brittle character of the impregnated paper can be reduced by using the mixture according to the invention with a portion of impregnating resin solution.

Diesen Imprägniersubstanzmischungen können auch weitere Hilfsmittel wie Benetzungsmittel, Viskositätsregler, Antihaft- ­und Penetrationshilfsmittel, Pigmente, Farbstoffe und Ent­schäumer zugesetzt werden.Other auxiliaries such as wetting agents, viscosity regulators, non-stick and penetration aids, pigments, dyes and defoamers can also be added to these impregnation substance mixtures.

Als Benetzungs- und Penetrationsmittel werden Stoffe eingesetzt,die die Grenzflächenspannung zwischen flüssiger Phase und fester Phase verändern, z. B. Tenside und Emulgatoren.Substances are used as wetting and penetration agents that change the interfacial tension between the liquid phase and solid phase, e.g. B. surfactants and emulsifiers.

Erfindungsgemäß kann durch eine Kombination von Malein­säure-Copolymerisaten und diesen die Grenzflächenspannung ver­ändernden Substanzen die Penetration der Imprägnierflüssigkeit vorteilhaft beeinflußt werden.According to the invention, the penetration of the impregnation liquid can be advantageously influenced by a combination of maleic acid copolymers and these substances which change the interfacial tension.

Erfindungsgemäß wird diese Imprägniersubstanz in Form eines Gemisches aus Lösung und Dispersion mit einem Feststoff­gehalt von 5 bis 60 % eingesetzt, wobei die Viskosität zwischen 10 und 60 s (nach DIN-Becher, 4 mm) liegt.According to the invention, this impregnation substance is used in the form of a mixture of solution and dispersion with a solids content of 5 to 60%, the viscosity being between 10 and 60 s (according to DIN cup, 4 mm).

Der Auftrag dieser Imprägnierungs- und Beschichtungs­mischung auf das Faservlies erfolgt innerhalb der Papierma­schine in einer Walzenauftragsvorrichtung (Leimpresse). Dabei wird erfindungsgemäß das Faservlies mit einem Trockengehalt von 98 bis 92 % durch eine Leimpresse zugeführt und so die beiderseitige Tränkung vorgenommen.This impregnation and coating mixture is applied to the nonwoven within the paper machine in a roller application device (size press). According to the invention, the nonwoven fabric with a dry matter content of 98 to 92% is fed through a size press and the impregnation is carried out on both sides.

Erfindungsgemäß kann nach dieser ersten Prozeßstufe der Imprägnierung eine weitere einseitige oder beidseitige Oberflächenabdeckung, d. h. Beschichtung, des Faservlieses innerhalb der Papiermaschine mit der gleichen oder einer ähnlich aufgebauten Copolymermischung vorgenommen werden, wobei zwischen den beiden einzelnen Prozeßstufen eine Zwischentrocknung stattfinden sollte.According to the invention, a further one-sided or double-sided surface covering, ie. H. Coating, the nonwoven fabric can be carried out within the paper machine with the same or a similarly structured copolymer mixture, intermediate drying should take place between the two individual process stages.

Durch eine nachträglich aufgebrachte Beschichtung auf einer Seite der getrockneten Bahn wird eine dichtere Ober­fläche erreicht, die eine bessere Bedruck- oder Lackierbarkeit oder Kaschierbarkeit erreicht. Wenn nur eine weitere einsei­tige Oberflächenbeschichtung erfolgt, kann diese vermittels einer Rakelauftragsvorrichtung vorgenommen werden. Ein ein­seitiges Rollen der beschichteten Papierbahn kann durch einen zusätzlichen Auftrag auf der Rückseite vermieden werden.A subsequently applied coating on one side of the dried web results in a denser surface which is easier to print or coat or laminate. If only a further one-sided surface coating is carried out, this can be carried out by means of a doctor application device. One-sided rolling of the coated paper web can be avoided by an additional application on the back.

Ein solcher Auftrag kann beispielsweise eine stark wäßrige Lösung von Stärke oder CMC sein. Eine zusätzliche Glättung der imprägnierten und einseitig beschichteten Bahn z. B. mit bekannten Maschinenglättwerkseinrichtungen oder in einem separaten Arbeitsgang in einem Kalander erhöht noch die gewünschte Bedruck- und Lackierbarkeit der beschichteten Seite.Such an application can be, for example, a strongly aqueous solution of starch or CMC. An additional smoothing of the impregnated and coated on one side z. B. with known smoothing machines or in a separate operation in a calender increases the desired printability and paintability of the coated side.

Diese auf solche Art und Weise hergestellte faserhaltige Folie unterschiedlicher Dicke und unterschiedlicher Rohdichte, je nach angewandtem Druck bei der Vliesherstellung und Glättung der getränkten und beschichteten Bahn, eignet sich vorzüglich im festen Verbund mit einer relativ starren und steifen Un­terlage, z. B. Holzspanplatte, als dekorative und schützen­de Umhüllung von Möbelteilen wie z. B. Fernseh- und Radio­gehäuse oder Hi-Fi-Türme (Gehäuseummantelung). Durch Anwen­dung dieser wirtschaftlich günstig herstellbaren faserhal­tigen Folie werden die eingangs erwähnten Nachteile bei Verwendung von PVC- oder anderer Kunststofffolie vermieden.This fibrous film of different thicknesses and different bulk densities produced in this way, depending on the pressure used in the manufacture of nonwovens and the smoothing of the impregnated and coated web, is particularly suitable in a firm bond with a relatively rigid and rigid base, e.g. B. chipboard, as a decorative and protective covering of furniture parts such. B. television and radio housings or hi-fi towers (housing casing). By using this economically inexpensive to produce fiber-containing film, the disadvantages mentioned above are avoided when using PVC or other plastic film.

Die erfindungsgemäß hergestellte faserhaltige Folie von hoher Flexibilität, Dimensionsstabilität bei Temperatur­veränderung und mit guten Sperreigenschaften gegen Wasser und Lösungsmittel ist ebenfalls für andere Zwecke vorzüg­lich geeignet wie z. B. als Basismaterial von hochwertigen Schleifpapieren für den Naßschliff, Druck- und Werbeträger, dekoratives Wandmaterial (z. B. schwer entflammbare pigmen­tierte oder unpigmentierte dimensionsstabile Tapete), Klebe­bänder, Trägerpapier z. B. für Fußbodenbeläge.The fiber-containing film produced according to the invention of high flexibility, dimensional stability with temperature changes and with good barrier properties against water and solvent is also excellently suitable for other purposes such as, for. B. as the base material of high quality sanding paper for wet sanding, printing and advertising media, decorative wall material (e.g. flame retardant pigmented or unpigmented dimensionally stable wallpaper), adhesive tapes, backing paper z. B. for floor coverings.

Die Erfindung wird nun anhand von Beispielen näher erläutert.The invention will now be explained in more detail by means of examples.

Beispiel 1example 1

Erfindungsgemäß wurde ein Rohpapier folgender Zusammen­setzung und Beschaffenheit als zweilagiges Papier auf einer Duplex-Papiermaschine hergestellt:
80 % Kiefernholzsulfat-Zellstoff
20 % Eukalyptus-Zellstoff
Mahlgrad 30° SR (Schopper-Riegler)
Zusätze, handelsüblich (auf atro Zellstoff berechnet):
1 % Talkum
3 % formaldehydfreies Naßfestmittel
0,3 % Netz- und Dispergiermittel
According to the invention, a base paper of the following composition and quality was produced as two-ply paper on a duplex paper machine:
80% pine wood sulfate pulp
20% eucalyptus pulp
Freeness 30 ° SR (Schopper-Riegler)
Additives, commercially available (calculated on dry cellulose):
1% talc
3% formaldehyde-free wet strength agent
0.3% wetting and dispersing agent

Dieses Rohpapier mit einer Flächenmasse von 90 g/m² wurde mit der erfindungsgemäßen Kunstharz-Mischung von Dis­persion und Lösung im Verhältnis 20 : 1 in einer Leimpresse beidseitig imprägniert. Der mit dieser erfindungsgemäßen Kunstharz-Mischung überraschend starke Imprägniereffekt, sonders charakterisiert anhand der Schichtfestigkeit und Steifigkeit unter Berücksichtigung der sich dabei einstellen­den Wasserabsorption, beruht wohl auf einem synergistischen Effekt der verwendeten Dispersion und Lösung, die, allein eingesetzt, bei weitem nicht die gleichen angestrebten guten Papiereigenschaften erreichen lassen.This base paper with a mass per unit area of 90 g / m 2 was impregnated on both sides with the synthetic resin mixture of dispersion and solution in a ratio of 20: 1 in a size press. The surprisingly strong impregnation effect with this synthetic resin mixture according to the invention, particularly characterized on the basis of the layer strength and rigidity, taking into account the water absorption which results, is probably due to a synergistic effect of the dispersion and solution used, which, when used alone, are far from the same desired good Allow paper properties to be achieved.

Nachfolgende Beispiele belegen das. Die Leimflotten mußten z. T. mit Wasser auf die optimale Viskosität ( < 60 s nach DIN-Becher, 4 mm) eingestellt werden.The following examples prove this. T. with water to the optimal viscosity (<60 s according to DIN cup, 4 mm).

Leimpressen-Rezepturen:Size press recipes:

  • 1 - Kunstharz-Dispersion allein (wäßrige anionische Copoly­merdispersion auf Basis von Acrylsäureester, Acrylnitril und Styrol), Feststoffgehalt 50 %, mittlere Teilchengröße ca. 0,1 µm, mittlere Filmhärte, Mindest-Filmbildungs­temperatur < 1° C.1 - synthetic resin dispersion alone (aqueous anionic copolymer dispersion based on acrylic acid ester, acrylonitrile and styrene), solids content 50%, average particle size approx. 0.1 µm, average film hardness, minimum film formation temperature <1 ° C.
  • 2 - Kunststoff-Dispersion, mit Wasser verdünnt, Feststoff­gehalt 25 %2 - plastic dispersion, diluted with water, solids content 25%
  • 3 - Kunststoff-Lösung allein, mit Wasser verdünnt (an­ionische wäßrige Lösung eines carboxylgruppenhaltigen Copolymers auf Basis von Maleinsäureanhydrid), Fest­stoffgehalt ca. 12 %3 - plastic solution alone, diluted with water (anionic aqueous solution of a carboxyl group-containing copolymer based on maleic anhydride), solids content approx. 12%
  • 4 - Kunststoff-Lösung mit formaldehydfreiem Naßfestmittel, mit Wasser verdünnt, Feststoffgehalt ca. 10 %4 - plastic solution with formaldehyde-free wet strength agent, diluted with water, solids content approx. 10%
  • 5 - erfindungsgemäße Kunststoffmischung, bestehend aus Dispersion (gemäß Beispiel 1) und Lösung (gemäß Bei­spiel 3) im Verhältnis 20 : 1, mit Zusätzen von
    - formaldehydfreiem Naßfestmittel und
    - Entschäumer,
    verdünnt mit Wasser auf einen Feststoffgehalt von ca. 25%.
    5 - plastic mixture according to the invention, consisting of dispersion (according to Example 1) and solution (according to Example 3) in a ratio of 20: 1, with additions of
    - formaldehyde-free wet strength agent and
    - defoamer,
    diluted with water to a solids content of approx. 25%.
Figure imgb0001
Figure imgb0001

Eine reine Kunstharz-Dispersion (Rezeptur 1) reduziert zwar aufgrund ihrer guten filmbildenden Eigenschaften die Wasserabsorption am stärksten, die Penetration in das Roh­papier ist jedoch unzureichend. Das belegen die nur gering­fügig verbesserten Werte bezüglich Schichtfestigkeit und Steifigkeit.A pure synthetic resin dispersion (recipe 1) reduces the due to its good film-forming properties Most water absorption, but the penetration into the base paper is insufficient. This is demonstrated by the only slightly improved values with regard to layer strength and rigidity.

Durch eine Verdünnung dieser Dispersion mit Wasser (Rezeptur 2) erfolgt eine stärkere Penetration in das Roh­papier bei gleichzeitig erhöhter Wasserabsorption und noch ungenügender Elastizität des imprägnierten Papiers.By diluting this dispersion with water (recipe 2), there is a greater penetration into the base paper with increased water absorption and still insufficient elasticity of the impregnated paper.

Die ungenügende Imprägnierung machte sich außerdem in einer unzureichenden Ribbelfestigkeit der Papierober­fläche bemerkbar. Die Imprägnierung des Rohpapiers mit der wasserverdünnten Kunstharz-Lösung (Rezeptur 3) führt zwar zu einer verbesserten Elastizität, jedoch auf Kosten einer stark verschlechterten Schichtfestigkeit.The insufficient impregnation was also noticeable in the inadequate rub resistance of the paper surface. The impregnation of the base paper with the water-diluted synthetic resin solution (recipe 3) leads to an improved elasticity, but at the expense of a greatly deteriorated layer strength.

Auch der Zusatz von Naßfestmittel (Rezeptur 4) be­wirkt keine wesentliche Eingenschaftsveränderung des im­prägnierten Papiers.The addition of wet strength agent (recipe 4) does not cause any significant change in the properties of the impregnated paper.

Erst durch die erfindungsgemäße Kunstharz-Mischung von Dispersion und Lösung (Rezeptur 5) wird der gewünschte hohe Imprägniereffekt der Leimflotte und damit alle ange­strebten guten Papiereigenschaften erreicht, charakterisiert durch eine um ca. 10 % höhere Schichtfestigkeit als bei Rezeptur 2, relativ niedrige Wasserabsorption und höchste Elastizität (ca. 10 % niedrigere Steifigkeit als bei Re­zeptur 3).It is only through the synthetic resin mixture of dispersion and solution (formulation 5) that the desired high impregnation effect of the glue liquor and thus all the desired paper properties are achieved, characterized by an approximately 10% higher layer strength than with formulation 2, relatively low water absorption and the highest Elasticity (approx. 10% lower stiffness than with recipe 3).

Dieser anhand der Wirkung der Einzelkomponenten (Dis­persion, Lösung, Naßfestmittel) nicht zu erwartende über­proportional hohe Imprägniereffekt ist auf den Synergismus von Dispersion und Lösung zurückzuführen.This disproportionately high impregnation effect, which cannot be expected on the basis of the action of the individual components (dispersion, solution, wet strength agent), can be attributed to the synergism of dispersion and solution.

Beispiel 2Example 2

In einer weiteren Versuchsreihe wurde die mittelharte Kunstharzdispersion (5) durch eine harte Dispersion mit einer Teilchengröße von ca. 0,15 µm, Mindest-Filmbildungstemperatur ca. 25° C, ausgetauscht. Bei dieser Dispersion handelte es sich um eine wäßrige Copolymerdispersion auf Basis von Acrylsäureester und Styrol.In a further series of experiments, the medium-hard synthetic resin dispersion (5) was replaced by a hard dispersion with a particle size of approximately 0.15 μm, minimum film-forming temperature approximately 25 ° C. This dispersion was an aqueous copolymer dispersion based on acrylic acid ester and styrene.

Folgende Eigenschaften des damit imprägnierten Roh­papiers wurden erhalten (die mit der Rezeptur 5 aus der vorhergehenden 1. Versuchsreihe erreichten Ergebnisse wurden zum besseren Verständnis nochmals aufgeführt):

Figure imgb0002

  • 6 - Kunstharz-Dispersion, mit Wasser verdünnt, mit Zusatz von formaldehydfreiem Naßfestmittel, Feststoffgehalt ca. 25 %
  • 7 - erfindungsgemäße Kunstharzmischung, bestehend aus Dispersion und der Lösung gemäß Beispiel 3 im Verhält­nis 20 : 1, mit Zusätzen von
    - formaldehydfreiem Naßfestmittel und
    - Entschäumer,
    verdünnt mit Wasser auf einen Feststoffgehalt von ca. 25%.
The following properties of the base paper impregnated with it were obtained (the results achieved with recipe 5 from the previous first series of tests were listed again for better understanding):
Figure imgb0002
  • 6 - synthetic resin dispersion, diluted with water, with the addition of formaldehyde-free wet strength agent, solids content approx. 25%
  • 7 - synthetic resin mixture according to the invention, consisting of dispersion and the solution according to Example 3 in a ratio of 20: 1, with additions of
    - formaldehyde-free wet strength agent and
    - defoamer,
    diluted with water to a solids content of approx. 25%.

Mit einer reinen Kunstharz-Dispersion gemäß Rezeptur 6 ist, wie auch bereits bei den Rezepturen 1 und 2 belegt, nicht der angestrebte hohe Imprägniereffekt zu erreichen. Erst die erfindungsgemäße Kombination von Dispersion und Lösung führt wiederum zu den gewünschten Papiereigenschaften, wobei aufgrund der hohen Filmhärte der gewählten Dispersion die Elastizität des imprägnierten Papieres schlechter als bei Verwendung der Rezeptur 5 ausfällt.A pure synthetic resin dispersion according to recipe 6, as already demonstrated for recipes 1 and 2, cannot achieve the desired high impregnation effect. Only the combination of dispersion and solution according to the invention in turn leads to the desired paper properties, the elasticity of the impregnated paper being poorer than when using formulation 5 due to the high film hardness of the selected dispersion.

Durch eine nachfolgende Satinage dieser erfindungsge­mäß imprägnierten Papiere wird die Steifigkeit um ca. 10 bis 20 %, die Wasserabsorption um ca. 15 bis 20 % erniedrigt, während die Schichtfestigkeit nahezu konstant bleibt.Subsequent calendering of these papers impregnated according to the invention lowers the stiffness by approximately 10 to 20% and water absorption by approximately 15 to 20%, while the layer strength remains almost constant.

Beispiel 3Example 3

In der nächsten Versuchsreihe wurde die erfindungsge­mäße Kunstharz-Mischung von Dispersion und Lösung in Kombi­ nation mit einem Harnstoff-Formaldehyd-Harz im Verhältnis 2 : 1 zur Imprägnierung des Rohpapiers nach Beispiel 1 ver­wendet.

  • 8 - Kunstharz-Dispersion allein gemäß Rezeptur 6 in Kombi­nation mit Harnstoff-Fomaldehyd-Harz im Verhältnis 2 : 1
  • 9 - erfindungsgemäße Kunstharzmischung, bestehend aus Dis­persion und Lösung gemäß Rezeptur 7 (im Verhältnis 20 : 1) in Kombination mit Harnstoffharz im Verhältnis 2 : 1
  • 10 - Kunstharz-Dispersion allein (wäßrige anionische Copolymer­dispersion auf Basis von Acrylaten) Feststoffgehalt 50 %, mittlere Teilchengröße ca. 0,15 µm, mittlere Filmhärte, Mindest-Filmbildungstemperatur 12° C in Kombination mit Harnstoff-Formaldehyd-Harz im Verhältnis 2 : 1
  • 11 - erfindungsgemäße Kunstharzmischung, bestehend aus Dis­persion (gemäß Rezeptur 10) und Lösung (gemäß Rezeptur 3) im Verhältnis 20 : 1 in Kombination mit Harnstoffharz im Verhältnis 2 : 1
In the next series of experiments, the synthetic resin mixture of dispersion and solution according to the invention was combined nation with a urea-formaldehyde resin in a ratio of 2: 1 used to impregnate the base paper according to Example 1.
  • 8 - synthetic resin dispersion alone according to recipe 6 in combination with urea-fomaldehyde resin in a ratio of 2: 1
  • 9 - synthetic resin mixture according to the invention, consisting of dispersion and solution according to recipe 7 (in a ratio of 20: 1) in combination with urea resin in a ratio of 2: 1
  • 10 - synthetic resin dispersion alone (aqueous anionic copolymer dispersion based on acrylates) solids content 50%, average particle size approx. 0.15 µm, average film hardness, minimum film formation temperature 12 ° C in combination with urea-formaldehyde resin in a ratio of 2: 1
  • 11 - synthetic resin mixture according to the invention, consisting of dispersion (according to recipe 10) and solution (according to recipe 3) in a ratio of 20: 1 in combination with urea resin in a ratio of 2: 1

Die erhaltenen Eigenschaften des imprägnierten Papiers sind in der folgenden Tabelle zusammengefaßt:

Figure imgb0003
The properties of the impregnated paper obtained are summarized in the following table:
Figure imgb0003

Auch Kombinationen von Kunstharz-Dispersionen und Tränk­harzen, wie z. B. Harnstoff-Formaldehyd-Harz, wie sie zur Imprägnierung von Dekorrohpapieren in separaten Imprägnier­anlagen üblich sind, führen zur Verbesserung der Eigenschaften des Rohpapiers. Der Typ der verwendeten Kunstharz-Dispersionen bestimmt dabei wesentlich Flottenaufnahme, Porosität, Wasser­absorption und Schichtfestigkeit des Papiers (s. Rezepturen 8 und 10).Combinations of synthetic resin dispersions and impregnating resins, such as. B. urea-formaldehyde resin, as are common for the impregnation of decorative base paper in separate impregnation plants, lead to the improvement of the properties of the base paper. The type of synthetic resin dispersions used essentially determines the liquor absorption, porosity, water absorption and layer strength of the paper (see recipes 8 and 10).

Aber erst durch die erfindungsgemäße Kunstharz-Mischung von Dispersion und Lösung werden auch bei diesen speziellen Tränkharz-Kunstharz-Kombinationen der gewünschte hohe Im­prägniereffekt und damit die angestrebten Eigenschaften des imprägnierten Papiers erreicht (s. Rezepturen 9 und 11). Dazu zählt die z. B. beträchtliche Reduzierung von Poro­sität und Wasserabsorption sowie die Erhöhung der Schicht­festigkeit. Aufgrund des relativ hohen Tränkharz-Anteils liegt jedoch das Niveau der Schichtfestigkeit etwas niedriger als bei den Rezepturen 1 und 2.But it is only through the synthetic resin mixture of dispersion and solution according to the invention that the desired high impregnation effect and thus the desired properties of the impregnated paper are achieved even with these special impregnating resin / synthetic resin combinations (see recipes 9 and 11). This includes the z. B. considerable reduction in porosity and water absorption and the increase in layer strength. However, due to the relatively high proportion of impregnating resin, the level of layer strength is somewhat lower than that of recipes 1 and 2.

Claims (10)

1. Verfahren zur Herstellung von mit Kunstharzen in Form von Lösungen und Dispersionen imprägnierten Papierbahnen, dadurch gekennzeichnet, daß die Papierbahn aus einem Zellstoffaserge­misch von hoher Saugfähigkeit und Festigkeit gebildet wird, das auf einen Mahlgrad von maximal 35° SR gemahlen ist und die Imprägnierflüssigkeit aus einem Gemisch wäßriger anionischer Copolymerdispersionen und wäßriger anionischer Lösungen besteht, mit einem pH-Wert zwischen 7,5 und 10, und der Auftrag mit einer Leimpresse in der Trockenpartie der Papiermaschine durchgeführt wird.1. A process for the production of paper webs impregnated with synthetic resins in the form of solutions and dispersions, characterized in that the paper web is formed from a cellulose fiber mixture of high absorbency and strength, which is ground to a grinding degree of at most 35 ° SR and the impregnating liquid from one There is a mixture of aqueous anionic copolymer dispersions and aqueous anionic solutions, with a pH between 7.5 and 10, and the application is carried out with a size press in the dryer section of the paper machine. 2. Verfahren nach Anspruch 1, dadurch gekennzeichnet, daß der pH-Wert vorzugsweise auf einen Bereich zwischen 8 und 9 eingestellt wird.2. The method according to claim 1, characterized in that the pH is preferably adjusted to a range between 8 and 9. 3. Verfahren nach Anspruch 1 und 2, dadurch gekennzeichnet, daß der Zellstoff der Papierbahn aus Eukalyptus-Zellstoff und Kiefernholzsulfat-Zellstoff in einem Verhältnis von 50 : 50 bis 10 : 90, vorzugsweise 30 : 70 bis 15 : 85, gebildet wird, gegebenenfalls in Kombination mit synthetischen Faserstoffen und einer vorzugsweise schneidenden Mahlung bis zu einem Mahlgrad von 15 bis 25° SR unterworfen wird.3. The method according to claim 1 and 2, characterized in that the pulp of the paper web from eucalyptus pulp and pine wood sulfate pulp is formed in a ratio of 50:50 to 10:90, preferably 30:70 to 15:85, if appropriate in combination with synthetic fibers and a preferably cutting grinding up to a grinding degree of 15 to 25 ° SR is subjected. 4. Verfahren nach Anspruch 1 bis 3, dadurch gekennzeichnet, daß dem Faserstoff der Papierbahn weitere chemische Hilfs­mittel wie pH-Regulierer, Naß- und Trockenfestmittel, Kunst­harzdispersionen, Fällungsmittel (Fixiermittel), Tenside, Farbstoffe, Füllstoffe und dergleichen zugesetzt werden.4. The method according to claim 1 to 3, characterized in that the fibrous material of the paper web further chemical auxiliaries such as pH regulators, wet and dry strength agents, synthetic resin dispersions, precipitants (fixatives), surfactants, dyes, fillers and the like are added. 5. Verfahren nach Anspruch 1 bis 4, dadurch gekennzeichnet, daß als Tränk- bzw. Beschichtungssubstanz für die Behandlung des Faservlieses übliche wäßrige, anionische Copolymerdis­persionen auf Basis von Acrylsäure, Acrylsäureester, Acryl­nitril, Vinylacetat und/oder Styrol mit einer mittleren Teilchengröße unter 0,2 my, geringer bis mittlerer Film­härte und Mindest-Filmbildungstemperatur unter 30° in Kom­bination mit üblichen wäßrigen, anionischen Lösungen von Copolymerisaten auf Basis von Maleinsäureanhydrid bzw. Maleinsäure mit z. B. Styrol, Acrylsäure, Acrylsäureestern und dergleichen im Verhältnis 100 : 1 bis 10 : 1 (auf Wirk­substanz berechnet), vorzugsweise 25 : 1 bis 15 : 1, sowie mit weiteren Zusätzen, wie Härtungs-, Viskositätsregulie­rungs-, Antihaft- und Penetrationshilfsmittel sowie Pig­menten und Farbstoffen verwendet werden.5. The method according to claim 1 to 4, characterized in that as an impregnating or coating substance for the treatment of the nonwoven fabric conventional aqueous, anionic copolymer dispersions based on acrylic acid, acrylic acid ester, acrylonitrile, vinyl acetate and / or styrene with an average particle size below 0, 2 my, low to medium film hardness and minimum film formation temperature below 30 ° in combination with conventional aqueous, anionic solutions of copolymers based on maleic anhydride or maleic acid with, for. B. styrene, acrylic acid, acrylic acid esters and the like in a ratio of 100: 1 to 10: 1 (calculated on active substance), preferably 25: 1 to 15: 1, and with other additives such as hardening, viscosity control, non-stick and penetration aids and Pigments and dyes are used. 6. Verfahren nach Anspruch 1 bis 4, dadurch gekennzeichnet, daß zusätzlich die Mischung aus Dispersion und Lösung einen Anteil eines Tensides enthält.6. The method according to claim 1 to 4, characterized in that the mixture of dispersion and solution additionally contains a proportion of a surfactant. 7. Verfahren nach Anspruch 1 bis 6, dadurch gekennzeichnet, daß der Anteil eines Tensides, bezogen auf die Mischung aus Dispersion und Lösung, 0,05 bis 1,5 % beträgt.7. The method according to claim 1 to 6, characterized in that the proportion of a surfactant, based on the mixture of dispersion and solution, is 0.05 to 1.5%. 8. Verfahren nach Anspruch 1 bis 7, dadurch gekennzeichnet, daß die Durchtränkung des Faservlieses der Papierbahn inner­halb der Papiermaschine in einer ersten Prozeßstufe beid­seitig mittels Walzenauftrag und eine Beschichtung in einer zweiten Prozeßstufe einseitig mittels Rakelauftrag erfolgt, der sich eine Oberflächenglättung der Papierbahn anschließt.8. The method according to claim 1 to 7, characterized in that the impregnation of the nonwoven fabric of the paper web within the paper machine in a first process stage on both sides by means of roller application and a coating in a second process stage on one side by means of doctor blade application, which is followed by surface smoothing of the paper web. 9. Verfahren nach Anspruch 1 bis 8, dadurch gekennzeichnet, daß die Papierbahn nach erfolgter Trocknung und Oberflächen­glättung einer weiteren Oberflächenvergütung einer Seite, wie Beschichtung, Bedruckung und/oder Lackierung unterworfen wird.9. The method according to claim 1 to 8, characterized in that the paper web is subjected to a further surface treatment of one side, such as coating, printing and / or painting after drying and surface smoothing. 10. Verwendung einer getrockneten Papierbahn, hergestellt nach Anspruch 1 bis 9 zur Umhüllung von Möbelteilen (Gehäuseum­mantelung) durch Aufkleben derselben auf eine steife Unterlage und Weiterverarbeitung eines solchermaßen erhaltenen Verbund­stoffes durch Anbringung von Gehrungsschnitten und Faltung im Bereich der Gehrungsschnitte zu dreidimensionalen Möbel­teilen (Faltkorpus).10. Use of a dried paper web, produced according to claim 1 to 9 for wrapping furniture parts (housing casing) by gluing them onto a rigid base and further processing of a composite material obtained in this way by applying miter cuts and folding in the area of the miter cuts to three-dimensional furniture parts (folding body).
EP86110511A 1985-11-21 1986-07-30 Process for producing paper webs impregnated with synthetic resins in a soluble or dispersed form Expired - Lifetime EP0223922B2 (en)

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PT (1) PT83153B (en)

Cited By (9)

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EP0261316A1 (en) * 1986-09-19 1988-03-30 Kämmerer Gmbh Process for producing yellowing-resistant papers, in particular against the action of heat
EP0889168A2 (en) * 1997-07-02 1999-01-07 Koehler decor GmbH &amp; Co. KG Process for making a prepreg, and use of the same for making decorative laminates
DE19728250A1 (en) * 1997-07-02 1999-01-07 Koehler Decor Gmbh & Co Kg Production of preimpregnate for making decorative laminate
DE19946151A1 (en) * 1999-09-27 2001-04-05 Koehler Decor Gmbh & Co Kg Preparation of pre-impregnate, useful for production of edging materials for doors, window frames and flooring, comprise impregnating paper with specific aqueous impregnating liquor
WO2001077438A1 (en) * 2000-04-05 2001-10-18 Basf Aktiengesellschaft Polymer dispersion for impregnating paper
WO2002079571A1 (en) * 2001-03-30 2002-10-10 Kronospan Technical Company Ltd. Paper for producing panels and paper-making method
DE102008041296A1 (en) 2007-08-22 2009-03-19 Basf Se Aqueous impregnating agent, useful for impregnating raw or glued papers, comprises an urea derivative and an emulsion polymer, where the emulsion polymer contains ethylenically unsaturated monomer containing e.g. epoxide group
DE102013114420A1 (en) 2012-12-23 2014-06-26 Michael Jokiel Impregnated paper comprises base paper which is impregnated on one side with water-based impregnating solution comprising e.g. aqueous dispersion of styrene-ethyl-butyl acrylate copolymer and aqueous dispersion of styrene-acrylate copolymer
CN109489104A (en) * 2017-09-11 2019-03-19 南京新莱尔材料科技有限公司 A kind of fever wallpaper and its manufacturing method for indoor heating

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DE4413619C2 (en) * 1993-12-02 1996-09-26 Wkp Wuerttembergische Kunststo Process for making paper and laminates
DE10104820C1 (en) * 2001-02-01 2002-08-08 Erfurt & Sohn Kg wall covering
NL1036705C2 (en) 2009-03-13 2010-09-14 Trespa Int Bv METHOD FOR MANUFACTURING A DECOR PAPER IMPREGNATED WITH A RESIN AND A DECOR PANEL
DE102009043958A1 (en) * 2009-09-07 2011-03-17 Michael Wiederschein Impregnated material and process for producing an impregnated material
DE102010016864B4 (en) 2010-05-10 2018-09-27 Papierfabrik Julius Schulte Söhne GmbH & Co. KG Fibrous core paper, process for its preparation and its use
NL2007494C2 (en) 2011-09-28 2013-04-02 Trespa Int Bv METHOD FOR MANUFACTURING A DECORATIVE FILM AND A DECOR PANEL
DE102011122012B4 (en) * 2011-12-22 2017-04-06 Neenah Gessner Gmbh Impregnated abrasive base paper, process for producing impregnated abrasive base paper and its use
NL2011719C2 (en) 2013-11-01 2015-05-04 Trespa Int Bv A decorative panel.
NL2014060B1 (en) 2014-12-24 2016-09-30 Trespa Int Bv A method for producing a printed decorative paper.

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DE2949306A1 (en) * 1979-12-07 1981-06-11 Letron GmbH, 8750 Aschaffenburg Synthetic veneer of paper fibre compsn. impregnated with resin - contg. equal wt. of long and short fibres, can be made on paper machine
DE3024394A1 (en) * 1980-06-28 1982-01-21 Letron GmbH, 8750 Aschaffenburg Paper coating process - has glue press in paper drying section to apply agent by impregnation

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US3026217A (en) * 1958-04-11 1962-03-20 Kimberly Clark Co Fiber products and methods of manufacturing comprising base sheet of cellulose fibers saturated with a mixture comprising elastomeric polymer and polar adjunct polymer having carboxylic acid functional group
DE2034263B2 (en) * 1970-07-10 1977-04-07 Bayer Ag, 5090 Leverkusen MODIFIED ANIONIC PAPER SIZES
DE2551479A1 (en) * 1974-11-20 1976-05-26 Billingsfors Bruks Ab PROCESS FOR THE PRODUCTION OF AN IMPRAEGNATED FILM WITH SURFACE AFTER-TREATMENT
DE2949306A1 (en) * 1979-12-07 1981-06-11 Letron GmbH, 8750 Aschaffenburg Synthetic veneer of paper fibre compsn. impregnated with resin - contg. equal wt. of long and short fibres, can be made on paper machine
DE3024394A1 (en) * 1980-06-28 1982-01-21 Letron GmbH, 8750 Aschaffenburg Paper coating process - has glue press in paper drying section to apply agent by impregnation

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ABSTRACT BULLETIN OF THE INSTITUTE OF PAPER CHEMISTRY, Band 53, Nr. 9, M{rz 1983, Seite 1070, Zusammenfassung Nr. 9942, Appleton, Wisconsin, US; & JP-A-82 597/82 (KOHJIN CO. LTD) 24-05-1982 *
ABSTRACT BULLETIN OF THE INSTITUTE OF PAPER CHEMISTRY, Band 55, Nr. 9, M{rz 1985, Seite 1046, Zusammenfassung Nr. 9868, Appleton, Wisconsin, US; R. VALLS ENRICH: "Use of polyacrylamides in paper ÄasÜ additives for increasing dry strength", & PROD. QUIM. AUXIL. IND. PAPELERA (CURSO) 1982, 139-152 (publ. 1984) *
CHEMICAL ABSTRACTS, Band 98, Nr. 18, 2. Mai 1983, Seite 108, Zusammenfassung Nr. 145318t, Columbus, Ohio, US; & JP-A-57 173 163 (KOHJIN CO., LTD) 25-10-1982 *

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0261316A1 (en) * 1986-09-19 1988-03-30 Kämmerer Gmbh Process for producing yellowing-resistant papers, in particular against the action of heat
DE19728250C2 (en) * 1997-07-02 2002-01-17 Koehler Decor Gmbh & Co Kg Process for producing a pre-impregnate, the pre-impregnate obtained therewith and its use for the production of decorative composite structures
EP0889168A3 (en) * 1997-07-02 2000-03-01 Koehler decor GmbH &amp; Co. KG Process for making a prepreg, and use of the same for making decorative laminates
EP0889168A2 (en) * 1997-07-02 1999-01-07 Koehler decor GmbH &amp; Co. KG Process for making a prepreg, and use of the same for making decorative laminates
DE19758479C2 (en) * 1997-07-02 2002-07-11 Koehler Decor Gmbh & Co Kg impregnating
DE19728250A1 (en) * 1997-07-02 1999-01-07 Koehler Decor Gmbh & Co Kg Production of preimpregnate for making decorative laminate
DE19946151C5 (en) * 1999-09-27 2010-02-04 Koehler Decor Gmbh & Co Kg Process for the preparation of a prepreg, the prepreg prepared therefrom and its use
DE19946151A1 (en) * 1999-09-27 2001-04-05 Koehler Decor Gmbh & Co Kg Preparation of pre-impregnate, useful for production of edging materials for doors, window frames and flooring, comprise impregnating paper with specific aqueous impregnating liquor
DE19946151B4 (en) * 1999-09-27 2005-09-08 Koehler Decor Gmbh & Co Kg Process for the preparation of a prepreg, the prepreg prepared therefrom and its use
WO2001077438A1 (en) * 2000-04-05 2001-10-18 Basf Aktiengesellschaft Polymer dispersion for impregnating paper
US6767646B2 (en) 2000-04-05 2004-07-27 Basf Aktiengesellschaft Polymer dispersion for impregnating paper
WO2002079571A1 (en) * 2001-03-30 2002-10-10 Kronospan Technical Company Ltd. Paper for producing panels and paper-making method
DE102008041296A1 (en) 2007-08-22 2009-03-19 Basf Se Aqueous impregnating agent, useful for impregnating raw or glued papers, comprises an urea derivative and an emulsion polymer, where the emulsion polymer contains ethylenically unsaturated monomer containing e.g. epoxide group
DE102013114420A1 (en) 2012-12-23 2014-06-26 Michael Jokiel Impregnated paper comprises base paper which is impregnated on one side with water-based impregnating solution comprising e.g. aqueous dispersion of styrene-ethyl-butyl acrylate copolymer and aqueous dispersion of styrene-acrylate copolymer
CN109489104A (en) * 2017-09-11 2019-03-19 南京新莱尔材料科技有限公司 A kind of fever wallpaper and its manufacturing method for indoor heating

Also Published As

Publication number Publication date
NO174725B (en) 1994-03-14
EP0223922B1 (en) 1990-12-27
ATE59416T1 (en) 1991-01-15
NO863075D0 (en) 1986-07-30
NO863075L (en) 1987-05-22
JPH0726355B2 (en) 1995-03-22
DE3676648D1 (en) 1991-02-07
DE3541187C2 (en) 1994-10-06
FI86902C (en) 1992-10-26
ES2000141A6 (en) 1987-12-16
PT83153B (en) 1988-07-29
FI86902B (en) 1992-07-15
JPS62125097A (en) 1987-06-06
DE3541187C1 (en) 1987-06-11
NO174725C (en) 1994-06-22
PT83153A (en) 1986-09-01
CA1329072C (en) 1994-05-03
FI863177A (en) 1987-05-22
EP0223922B2 (en) 1997-10-29
FI863177A0 (en) 1986-08-04
DD259885A5 (en) 1988-09-07

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