EP2139655B1 - Production of non-woven elements made of natural fibres - Google Patents

Production of non-woven elements made of natural fibres Download PDF

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Publication number
EP2139655B1
EP2139655B1 EP20080714781 EP08714781A EP2139655B1 EP 2139655 B1 EP2139655 B1 EP 2139655B1 EP 20080714781 EP20080714781 EP 20080714781 EP 08714781 A EP08714781 A EP 08714781A EP 2139655 B1 EP2139655 B1 EP 2139655B1
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Prior art keywords
fibers
raw material
intermediate product
grass
suspension
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German (de)
French (fr)
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EP2139655A1 (en
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Stefan Grass
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Clean Insulating Technologies SA
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Clean Insulating Technologies SA
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B27WORKING OR PRESERVING WOOD OR SIMILAR MATERIAL; NAILING OR STAPLING MACHINES IN GENERAL
    • B27NMANUFACTURE BY DRY PROCESSES OF ARTICLES, WITH OR WITHOUT ORGANIC BINDING AGENTS, MADE FROM PARTICLES OR FIBRES CONSISTING OF WOOD OR OTHER LIGNOCELLULOSIC OR LIKE ORGANIC MATERIAL
    • B27N3/00Manufacture of substantially flat articles, e.g. boards, from particles or fibres
    • B27N3/04Manufacture of substantially flat articles, e.g. boards, from particles or fibres from fibres
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21BFIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
    • D21B1/00Fibrous raw materials or their mechanical treatment

Definitions

  • the invention relates to a method according to claim 1 for the production of insulating mats from a raw material of grass plants, wherein the grass plants are first processed with a conditioner, which strikes the Strängel Modellen the grass plants.
  • US 2007/0044891 describes the production of a nonwoven fabric for the production of paper tissues, wipes, etc. from a mixture of pulp with binder fibers and possibly other additives, a nonwoven fabric is formed in a dry process.
  • the fleece can be further dried, steamed, treated with other materials and crosslinked by heating and fusing the binder fibers.
  • the pulp Before being laid, the pulp can be processed in a wet process to separate the fibers ("debonding"). Subsequently, the pulp is dried again before, for example, the binding fibers are added.
  • FR-A-2294648 teaches the mechanical dehydration of alfalfa and grass for subsequent drying of the press cake to feed cubes.
  • WO 2005/017251 shows the defibration of grass for the production of fiber material. None of these publications relates to non-woven fabrics made from grass fibers and three-dimensionally bonded using supporting fibers.
  • the first intermediate product therefore consists of pre-processed grass fibers, also referred to below as natural fibers or as plant fibers.
  • the second intermediate product is a mixture of these natural fibers with binder fibers and additives, which mixture can be used for a subsequent nonwoven production.
  • grass covers all sorts of grasses (Gramineae family), including cereals such as wheat, barley, oats, rye and millet, as well as sugar cane and corn. These raw materials are harvested in the green state and stored in the form of silage for year-round, weather-independent processing. Also covered by the term “grass” are residues from the processing of sugar millet and sugar cane, which are known in professional circles as bagasse.
  • binder fiber includes fibers that are thermally activated and in mixture with the natural fibers give them a three-dimensionally fixed structure. These may be melt fibers made of polypropylene or polyethylene, plastic recyclate or bico (bi-component) fibers with a shedding component and a temperature-resistant core component. Binder fibers also include fibers made, for example, from starch or lactic acid which are biodegradable. These fibers are also referred to in the art as support fibers. In a preferred embodiment of the invention, the weight fraction of the binder fibers is 4% to 20%, preferably 5% to 15% or 10%. The inventive method, the proportion of binder fibers and thus the costs can be reduced.
  • the admixing of the binding fibers preferably takes place before the introduction of the additives (such as flame retardants and biocides), so that the binding fibers are also provided by the additives.
  • the additives such as flame retardants and biocides
  • the blending of the binder fibers can be done at different degrees of moisture of the natural fibers of the first intermediate product.
  • the admixing occurs at a dry matter content of natural fibers of about about 85%. This requires that the pre-drying of natural fibers already happens before mixing.
  • admixing occurs at a dry matter content of the natural fibers of about 40% to about 85%.
  • a dry matter content of the natural fibers of about 40% to about 85%.
  • An apparatus for carrying out a core function of this invention i. Pre-drying, blending of binder fibers and spraying of additives, preferably consists of a standing container which is fed from above with moist natural fibers and binder fibers and in which rising from below hot air is blown.
  • the two types of fiber are confused and mixed in the container and withdrawn from the container with the flow of hot air through a dispensing nozzle and tubing.
  • the natural fibers are pre-dried.
  • a spray device is installed, which allows a uniform application of the additives and at the same time does not hinder the material passage.
  • the container may have a propeller which rotates about a vertical axis.
  • admixing takes place in an aqueous suspension, ie at a dry matter content of the natural fibers of less than about 10%.
  • aqueous suspension ie at a dry matter content of the natural fibers of less than about 10%.
  • the temperature of the drying air is kept below the temperature required to activate the binding fibers.
  • the Temperature of the hot air in the range between about 80 ° C and about 200 ° C.
  • this pre-drying is done in a transport section in which the fibers are conveyed by hot air.
  • the second intermediate is thus a mixture of natural fibers and binder fibers, with a binder fiber content of 4% to 20%, preferably 5% to 15% or 10%, equipped with additives, and having a dry matter content of preferably about 40% to 75%.
  • the amount of dry matter depends very much on how much liquid is added by the spraying of the additives, and whether pre-drying takes place even after spraying.
  • the preparation of the first intermediate product ie the preprocessed plant fibers, is preferably done by the raw material is fiberized and digestible components of the raw material are separated.
  • Digestible components are in particular e.g. Lactic acid, acetic acid, amino acids, proteins and minerals.
  • the raw material according to the invention grass silage (silated grass), preferably with a dry matter content of 20% to 40%, in particular 25% to 35%.
  • the raw material is gold oat (Trisetum flavescens).
  • the defibering takes place in an aqueous suspension with a macerator and / or a deflaker, which is also preceded by a hammer mill for tearing the raw material.
  • a macerator in conjunction with a Entstipper the macerator is preferably upstream of the Entstipper.
  • the separation of the digestible components is preferably done by separating the fibers from the aqueous suspension after defibering, leaving the digestible components in the suspension.
  • the digestible ingredients are preferably processed into feed or food additives in a separate branch of processing. This is done by concentrating these ingredients in the suspension into nutrients, with the water portion preferably being recycled.
  • the digestible components preferably comprise organic acids, proteins and minerals, and preferably also enzymes, vitamins and / or hormone-like substances, in particular vitamin D3 hormone.
  • the presence of these substances depends on the choice of the raw material, ie on the plants used and on optional silage additives.
  • a nonwoven fabric is preferably formed and the binding fibers are activated by heating, so that they bond with the natural fibers and form a matrix.
  • the web formation can be done by the second intermediate product has a dry matter content of about 60% to 85% or higher and is thus used directly for the formation of the web, wherein optionally a residual drying takes place during heating of the web to activate the binder fibers.
  • the web formation can be done by the second intermediate product has a dry matter content of 40% to about 60%, placed on a conveyor belt, after-dried by hot air, for example, and optionally loosened again, and then heated to activate the binding fibers.
  • the fleece laying, eventual drying and activation is preferably carried out in a continuous process for producing a nonwoven tape.
  • the nonwoven elements can be cut off.
  • the nonwoven laying, etc., but also done in batch mode, with individual nonwoven elements are formed in predetermined shapes ..
  • FIG. 1 schematically shows a procedure
  • FIG. 2 a structure of a plant for fleece production from grass plants.
  • the raw grass is mowed on the field.
  • it is preferably processed with a conditioner which strikes the stem structures in such a way that they soften and lose moisture more quickly.
  • the mown grass is wilted on the field, that is, dried to a dry matter content of 25-40%. It is then picked up and pressed in a silo with the exclusion of air or ensiled.
  • the raw material can be stored without loss over a very long period of time and is available for processing at any time and weather-independent.
  • Silage is preferably carried out in large, horizontal silos, but can also be done in silo bales or silos standing. Furthermore, also Silierangesstoff can be added.
  • the raw material is tapped from the silo, loosened 1 and fed to a metering device 2. This leads the raw material into one or more hammer mills, where it is torn 3 or torn open and crushed to about 10-30 mm in length and about 1-3 mm in thickness. This will prepare the plant parts for subsequent defibering.
  • the raw material suspension is fed to a mechanical defibration 5.
  • This is accomplished by fiberizing aggregates which have been successfully used in the pulp industry for decades, e.g. Deflaker, macerators or refiner. To optimize the fiberization with regard to the fiber length and the fiber thickness, these aggregates can also be connected in series. It has been shown that the sequence of macerator and deflaker is particularly well suited for the present task. In this sequence, the macerator, which can suck in the raw material suspension itself, takes over the further homogenization of the raw material suspension as well as the feed of the directly downstream degasser.
  • the fibers are mechanically dewatered. 7. This is preferably done by removing the fibers from the suspension and then pressing the fibers in a screw press. The removal from the suspension is preferably carried out with a screening device, e.g. with a bow sieve or a drum sieve. With a screw press, for example, the fiber mixture can be dewatered to a dry matter content of approx. 36-46%.
  • the soluble and digestible raw material components of the suspension consist mainly of organic acids (lactic acid, acetic acid, amino acids), non-fermented sugars, proteins and minerals.
  • suitable silage aids eg bacterial cultures, the conversion of the raw material into the raw material can controlled fermentable sugars are controlled. For example, such a ratio of lactic acid to acetic acid can be achieved.
  • the soluble and digestible raw material components can be concentrated after separation from the fibers and used as a special feed.
  • this special feed is an acidifier, as a flavor carrier and as an actual feed.
  • valuable enzymes, vitamins or hormone-like substances may also be present in this material stream.
  • An example of this is the grass species Goldgrass (Trisetum flavescens), which contains a vitamin D3 derivative, which is partially water-soluble and supports the bone formation of mammals and humans.
  • All listed ingredients and properties can be used not only in animal nutrition, but also as an additive for human nutrition.
  • the required concentration of the ingredients can be done by filtration and / or evaporation. It should be noted that the minerals may partially precipitate out of the solution during the concentration.
  • binder fibers For the admixture 9 of binder fibers, the textile industry offers both continuous and batch processes which are well suited.
  • the binder fibers When processing grass fibers, the binder fibers are added at a weight fraction of 4-25%, preferably 5-15% of the product weight.
  • the equipment 10 of the fibers with additives is made by spraying the loose fibers.
  • the spraying is preferably carried out in an air stream in which the fibers move freely.
  • the spraying can be carried out with flame retardants customary in the insulating industry, e.g. with borates or ammonium compounds and with a water repellent and / or a fungicide. These additives can be mixed in a solution or sprayed individually onto the fibers.
  • the fibers are adjusted to a dry matter content which is advantageous for the subsequent nonwoven laying and thermal bonding.
  • This dry matter content is preferably 60-85% of the total weight of the fibers.
  • the fibers are still elastic and can withstand mechanical processing well.
  • the fibers are less prone to sticking in cards or similar, possibly used for web forming equipment.
  • the fibers have limited self-weight at this moisture content and can therefore be laid to a non-woven with the largest possible volume or the lowest possible density.
  • the drying or pre-drying 8 can be achieved with various drying techniques, e.g. Air-layer dryer, drum dryer or belt dryer.
  • pre-drying 8 it is also possible to use the fibers provided with bonding fibers and additives without actual pre-drying 8, i. with a dry matter content of 36-50% of the web formation.
  • pre-drying 8 it is also possible to completely remove the fibers prior to web formation, i. to dry to a dry matter content of over 85%.
  • thermobonding 12 of the nonwoven fabric the heating of the nonwoven fabric takes place at the melting temperature of the sheath component of the support fibers and the setting of the desired plate thickness or density.
  • the plate density or thickness is adjusted with an overflowing band, which compresses the nonwoven fabric to a thickness of about 3 mm to 250 mm, thereby giving it a uniform surface.
  • the heating of the web takes place with a supply air temperature of 120-180 ° C, preferably 140-170 ° C.
  • Thermobondierofen is also suitable for removing the residual moisture in the nonwoven fabric.
  • the nonwoven fabric After heating, the nonwoven fabric is cooled, cut to the desired mass of fiber mats 13, palletized and packaged.
  • FIG. 2 shows an overview of the structure of a plant for nonwoven production: a pre-processing unit 21 has the devices for tearing, fraying and dewatering, so to provide the plant fibers 101.
  • a core unit 22 has the means for mixing 9, spraying 9 of additives and drying 8 and thus to Forming the fiber mixture 102 on.
  • a web-forming device 23 comprises the devices for fleece laying, Thermobondtechnik and for cutting to form nonwoven elements 103.
  • An optional concentrator 24 has means for concentrating the digestible constituents 104 separated from the suspension into feeds 105.
  • Nonwovens having a density of 25-90 kg / m 3 were produced from grass using the method according to the invention.
  • the low density panels are slightly flexible, somewhat compressible and comfortable to handle.
  • a thermal conductivity of 0.034-0.040 W / (m, K) was measured.
  • the binder fibers can be selected so that the product has increased mechanical compressive strength and is thus also suitable for impact sound insulation as well as directly plastered exterior facades.
  • Odorlessness and water repellency can be achieved by targeted influencing of the fibers, for example by being treated with an oxidizing agent or with a hydrophobing agent.
  • the process allows the use of a hitherto barely used raw material for the production of a high quality product. Associated with this are significant ecological advantages in the provision of raw materials (renewable raw material), the processing (low energy consumption), product use (optimal combination of cold protection, thermal insulation and sound insulation) and product disposal (recyclability).

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  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Wood Science & Technology (AREA)
  • Forests & Forestry (AREA)
  • Mechanical Engineering (AREA)
  • Nonwoven Fabrics (AREA)

Description

Die Erfindung betrifft ein Verfahren gemäß Anspruch 1 zur Herstellung von Dämmmatten aus einen Rohstoff aus Graspflanzen, wobei die Graspflanzen zuerst mit einem Konditionierer bearbeitet werden, welcher die Strängelstrukturen der Graspflanzen aufschlägt.The invention relates to a method according to claim 1 for the production of insulating mats from a raw material of grass plants, wherein the grass plants are first processed with a conditioner, which strikes the Strängelstrukturen the grass plants.

Sie betrifft auch eine Dämmmatte gemäß Anspruch 13 hergestellt nach diesem Verfahren und eine Vorrichtung gemäß Anspruch 15 dafür.It also relates to an insulating mat according to claim 13 produced by this method and an apparatus according to claim 15 therefor.

STAND DER TECHNIKSTATE OF THE ART

Die Herstellung von Faservliesen aus Kunstfasern unter Beimischung von Stützfasern wird seit Jahrzehnten industriell ungesetzt. Ebenfalls bekannt ist die Herstellung von Dämmplatten aus Holz-, Flachs- oder Hanffasem unter Einsatz von Stützfasern. Eine solche Art der Herstellung von Dämmelementen aus Naturfasern ist beispielsweise aus DE 200 23 167 U1 bekannt: Holzfasern oder Flachsfasern werden mit Stützfasern aus Kunststoff vermengt und durch Erhitzen vernetzt.The production of fibrous webs of synthetic fibers with admixture of supporting fibers has been industrially unset for decades. Also known is the production of insulation boards from wood, flax or hemp fibers using support fibers. Such a way of producing insulating elements made of natural fibers, for example DE 200 23 167 U1 Known: wood fibers or flax fibers are mixed with plastic supporting fibers and crosslinked by heating.

US 2007/0044891 beschreibt die Herstellung eines Faservlieses zur Herstellung von Papiertaschentüchern, Wischtüchern etc. aus einem Gemisch aus Zellstoff mit Bindefasern und eventuell weiteren Additiven wird in einem trockenen Verfahren ein Vlies gebildet. Das Vlies kann weiter getrocknet, bedampft, mit weiteren Stoffen behandelt und durch Erhitzen und Verschmelzen der Bindefasern vernetzt werden. US 2007/0044891 describes the production of a nonwoven fabric for the production of paper tissues, wipes, etc. from a mixture of pulp with binder fibers and possibly other additives, a nonwoven fabric is formed in a dry process. The fleece can be further dried, steamed, treated with other materials and crosslinked by heating and fusing the binder fibers.

Vor der Vlieslegung kann der Zellstoff in einem nassen Verfahren aufbereitet werden, um die Fasern voneinander zu trennen (" debonding "). Anschliessend wird der Zellstoffbrei wieder getrocknet, bevor beispielsweise die Bindefasern zugesetzt werden.Before being laid, the pulp can be processed in a wet process to separate the fibers ("debonding"). Subsequently, the pulp is dried again before, for example, the binding fibers are added.

Die Verarbeitung von Gras ist Inhalt von mehreren Patentanmeldungen : FR-A-2294648 lehrt die mechanische Entwässerung von Luzerne und Gras zur anschliessenden Trocknung des Presskuchens zu Futterwürfeln. WO 2005/017251 zeigt die Zerfaserung von Gras zur Herstellung von Fasermaterial. Keine dieser Veröffentlichungen bezieht sich auf Faservliese, die aus Grasfasern hergestellt werden und unter Einsatz von Stützfasern dreidimensional gebunden sind.The processing of grass is content of several patent applications: FR-A-2294648 teaches the mechanical dehydration of alfalfa and grass for subsequent drying of the press cake to feed cubes. WO 2005/017251 shows the defibration of grass for the production of fiber material. None of these publications relates to non-woven fabrics made from grass fibers and three-dimensionally bonded using supporting fibers.

DASTELLUNG DER ERFINDUNGDASTELLUNG OF THE INVENTION

Es ist Aufgabe der Erfindung ein Verfahren und eine Vorrichtung der eingangs genannten Art zu schaffen zur Herstellung von Dämmmatten welche verbesserte Eigenschaften gegenüber bisher bekannten Dämmmatten aufweisen.It is an object of the invention to provide a method and an apparatus of the type mentioned for the production of insulating mats which have improved properties over previously known insulating mats.

Diese Aufgabe wird erfindungsgemäss gelöst durch das obige Verfahren, dadurch gekennzeichnet dass die Graspflanzen auf dem Feld bis zu einem Trockensubstanzgehalt von 25-40% angetrocknet werden, anschliessend aufgenommen und in einem Silo unter Luft verpresst werden, weiter durch Hammermühlen zerrissen und aufgerissen und auf 10-30 mm Länge und 1-3 mm Dicke zerkleinert und zuletzt für Zerfaserung vorbereitet werden, dass ein erstes Zwischenprodukt aus feuchten Graspflanzenfasern mit einem Trockensubstanzanteil von 30 bis 50%, vorzugsweise annähernd 40% bestehend, hergestellt wird und ein zweites Zwischenprodukt aus dem ersten Zwischenprodukt hergestellet wird, wobei die folgenden Verfahrensschritte durchgeführt werden :

  • Vertrocknen der Graspflanzenfasern,
  • Zumischen von thermoaktivierbaren Bindefasern,
  • Aufsprühen von Additiven.
This object is achieved according to the invention by the above method, characterized in that the grass plants are dried in the field to a dry matter content of 25-40%, then taken up and pressed in a silo under air, further torn by hammer mills and torn open and 10 -30 mm in length and 1-3 mm in thickness, and finally prepared for defibration to produce a first intermediate product of moist grass weed fibers having a dry matter content of 30 to 50%, preferably approximately 40%, and a second intermediate of the first intermediate is produced, wherein the following process steps are carried out:
  • Drying up the grass plant fibers,
  • Admixing of thermally activated binding fibers,
  • Spraying additives.

Das erste Zwischenprodukt besteht also aus vorverarbeiten Grasfasern, im Folgenden auch als Naturfasern oder als Pflanzenfasern bezeichnet. Das zweite Zwischenprodukt ist ein Gemisch dieser Naturfasern mit Bindefasern und Additiven, welches Gemisch für eine anschliessende Vliesherstellung verwendbar ist.The first intermediate product therefore consists of pre-processed grass fibers, also referred to below as natural fibers or as plant fibers. The second intermediate product is a mixture of these natural fibers with binder fibers and additives, which mixture can be used for a subsequent nonwoven production.

Die Bezeichnung "Gras" umfasst alle Arten von Gräsern (Familie der Gramineen), einschliesslich Getreide wie Weizen, Gerste, Hafer, Roggen und Hirse sowie Zuckerrohr und Mais. Diese Rohstoffe werden in grünem Zustand geerntet und in Form von Silage für die ganzjährige, witterungsunabhängige Verarbeitung zwischengelagert. Ebenfalls unter den Begriff "Gras" fallen Rückstände aus der Verarbeitung von Zuckerhirse sowie Zuckerrohr, welche in Fachkreisen als Bagasse bezeichnet werden.The term "grass" covers all sorts of grasses (Gramineae family), including cereals such as wheat, barley, oats, rye and millet, as well as sugar cane and corn. These raw materials are harvested in the green state and stored in the form of silage for year-round, weather-independent processing. Also covered by the term "grass" are residues from the processing of sugar millet and sugar cane, which are known in professional circles as bagasse.

Die Bezeichnung "Bindefasem" umfasst Fasern, die thermisch aktiviert werden und in Mischung mit den Naturfasern diesen eine dreidimensional fixierte Struktur geben. Es kann sich dabei um Schmelzfasern aus Polypropylen oder Polyäthylen, um Kunststoff-Rezyklat oder auch um Bico (Bi-Component)-Fasern mit einer schmeizenden Mantelkomponente und einer temperaturbeständigeren Kernkomponente handeln. Bindefasern umfassen auch Fasern, die z.B. aus Stärke oder Milchsäure hergestellt wurden und biologisch abbaubar sind. Diese Fasern werden in der Fachwelt auch als Stützfasern bezeichnet. In einer bevorzugten Ausführungsform der Erfindung beträgt der Gewichtsanteil der Bindefasern 4% bis 20%, vorzugsweise 5% bis 15% oder bis 10%. Durch das erfindungsgemässe Verfahren können der Anteil von Bindefasern und damit die Kosten reduziert werden.The term "binder fiber" includes fibers that are thermally activated and in mixture with the natural fibers give them a three-dimensionally fixed structure. These may be melt fibers made of polypropylene or polyethylene, plastic recyclate or bico (bi-component) fibers with a shedding component and a temperature-resistant core component. Binder fibers also include fibers made, for example, from starch or lactic acid which are biodegradable. These fibers are also referred to in the art as support fibers. In a preferred embodiment of the invention, the weight fraction of the binder fibers is 4% to 20%, preferably 5% to 15% or 10%. The inventive method, the proportion of binder fibers and thus the costs can be reduced.

Mit dem Begriff "Vlieselemente" werden dreidimensionale, flexible oder starre Matten aus einem Vliesstoff, also aus einer Struktur von vernetzten Fasern bezeichnet. Die Vlieselemente können flexibel oder starr sein, verschiedene Dicken und Dichten aufweisen und für zahlreiche Anwendungen genutzt werden. Dazu gehören unter anderem Anwendungen

  • Als Dämmstoff zum Schutz vor Kälte, Hitze und Schall.
  • In der Automobilindustrie zur Herstellung von Innenverkleidungen.
  • Als Matratzen.
  • Als Bodenabdeckung und/oder Nährsubstrat in der Landwirtschaft.
  • Ähnliches.(Schuheinlagen, ...)
The term "nonwoven elements" refers to three-dimensional, flexible or rigid mats of a nonwoven fabric, that is to say of a structure of cross-linked fibers. The nonwoven elements can be flexible or rigid, have different thicknesses and densities and can be used for numerous applications. These include applications
  • As an insulating material to protect against cold, heat and sound.
  • In the automotive industry for the production of interior trim.
  • As mattresses.
  • As a soil cover and / or nutrient substrate in agriculture.
  • Similar things (shoe inserts, ...)

Die Dämmelemente weisen vorzugsweise die folgenden Dimensionen und Flächengewichte auf:

  • Dämmmatten mit einer Dichte von 30-50 kg/m3 und einer Dicke von 50-250 mm: Flächengewicht 1,5-12,5 kg/m2, vorzugsweise 3-10 kg/m2
  • Trittschallelemente und Fassadenplatten mit einer Dichte von 90-120 kg/m3 und einer Dicke von 10-100 mm: Flächengewicht 0,9-12 kg/m2, vorzugsweise 2-10 kg/m2.
The insulating elements preferably have the following dimensions and basis weights:
  • Insulating mats with a density of 30-50 kg / m 3 and a thickness of 50-250 mm: basis weight 1.5-12.5 kg / m 2 , preferably 3-10 kg / m 2
  • Impact sound elements and façade panels with a density of 90-120 kg / m 3 and a thickness of 10-100 mm: basis weight 0.9-12 kg / m 2 , preferably 2-10 kg / m 2 .

Das Zumischen der Bindefasern geschieht vorzugsweise vor dem Einbringen der Additive (wie Flammschutzmittel und Biozide), so dass auch die Bindefasern durch die Additive ausgerüstet werden.The admixing of the binding fibers preferably takes place before the introduction of the additives (such as flame retardants and biocides), so that the binding fibers are also provided by the additives.

Das Zumischen der Bindefasern kann bei verschiedenen Feuchtigkeitsgraden der Naturfasern des ersten Zwischenproduktes geschehen. In einer bevorzugten Ausführungsform der Erfindung geschieht das Zumischen bei einem Trockensubstanzanteil der Naturfasern von über ca. 85%. Dies bedingt, dass das Vortrocknen der Naturfasern bereits vor dem Zumischen geschieht.The blending of the binder fibers can be done at different degrees of moisture of the natural fibers of the first intermediate product. In a preferred embodiment of the invention, the admixing occurs at a dry matter content of natural fibers of about about 85%. This requires that the pre-drying of natural fibers already happens before mixing.

In einer anderen bevorzugten Ausführungsform der Erfindung geschieht das Zumischen bei einem Trockensubstanzanteil der Naturfasern von rund 40% bis rund 85%. Je nachdem, wie gross der Trockensubstanzanteil des ersten Zwischenproduktes ist, findet keine Vortrocknung vor dem Zumischen statt, sondern lediglich nach oder während des Zumischens.In another preferred embodiment of the invention, admixing occurs at a dry matter content of the natural fibers of about 40% to about 85%. Depending on how large the dry matter content of the first intermediate product, there is no pre-drying before mixing, but only after or during mixing.

Eine Vorrichtung zur Ausführung einer Kernfunktion dieser Erfindung, d.h. des Vortrocknens, Zumischen von Bindefasern und Aufsprühen von Additiven, besteht vorzugsweise aus einem stehenden Behälter, der von oben mit feuchten Naturfasern sowie mit Bindefasern beschickt und in welchen von unten her aufsteigende Heissluft eingeblasen wird. Die zwei Fasertypen werden in dem Behälter durcheinander verwirbelt und durchmischt und mit dem Heissluftstrom durch einen Entnahmestutzen und eine Rohrleitung aus dem Behälter abgezogen. Dabei werden die Naturfasern vorgetrocknet. In die Rohrleitung ist eine Sprühvorrichtung eingebaut, die eine gleichmässige Beaufschlagung mittels der Additive erlaubt und gleichzeitig den Materialdurchzug nicht behindert. Zur Unterstützung der Verwirbelung und/oder der Heissluftförderung kann der Behälter einen Propeller aufweisen, der um eine senkrechte Achse rotiert.An apparatus for carrying out a core function of this invention, i. Pre-drying, blending of binder fibers and spraying of additives, preferably consists of a standing container which is fed from above with moist natural fibers and binder fibers and in which rising from below hot air is blown. The two types of fiber are confused and mixed in the container and withdrawn from the container with the flow of hot air through a dispensing nozzle and tubing. The natural fibers are pre-dried. In the pipeline, a spray device is installed, which allows a uniform application of the additives and at the same time does not hinder the material passage. To support the turbulence and / or the hot air promotion, the container may have a propeller which rotates about a vertical axis.

In einer weiteren bevorzugten Ausführungsform der Erfindung geschieht das Zumischen in einer wässrigen Suspension, also bei einem Trockensubstanzanteil der Naturfasern von unter ca. 10%. Damit sind die Anforderungen an die Entwässerung durch eine Vorverarbeitung zur Herstellung des ersten Zwischenproduktes relativ gering. Die Vortrocknung der Suspension nach dem Zumischen geschieht vorzugsweise mechanisch, optional gekoppelt mit einer Lufttrocknung.In a further preferred embodiment of the invention, admixing takes place in an aqueous suspension, ie at a dry matter content of the natural fibers of less than about 10%. Thus, the requirements for dewatering by preprocessing for the production of the first intermediate product are relatively low. The pre-drying of the suspension after admixing is preferably done mechanically, optionally coupled with air drying.

Bei einer Vortrocknung durch Heissluft während oder nach dem Zumischen der Bindefasern wird die Temperatur der Trocknungsluft unterhalb der Temperatur gehalten, die zum Aktivieren der Bindefasern erforderlich ist. Vorzugsweise liegt die Temperatur der Heissluft im Bereich zwischen rund 80° C und rund 200° C. Vorzugsweise geschieht diese Vortrocknung in einem Transportabschnitt, in welchem die Fasern durch Heissluft gefördert werden.When pre-drying by hot air during or after admixing the binding fibers, the temperature of the drying air is kept below the temperature required to activate the binding fibers. Preferably, the Temperature of the hot air in the range between about 80 ° C and about 200 ° C. Preferably, this pre-drying is done in a transport section in which the fibers are conveyed by hot air.

Das zweite Zwischenprodukt ist also eine Mischung von Naturfasern und Bindefasern, mit einem Bindefaseranteil von 4% bis 20%, vorzugsweise 5% bis 15% oder bis 10%, mit Additiven ausgerüstet, und mit einem Trockensubstanzanteil von vorzugsweise rund 40% bis 75%. Der Trockensubstanzanteil hängt natürlich stark davon ab, wie viel Flüssigkeit durch das Aufsprühen der Additive zugefügt wird, und ob auch nach dem Aufsprühen eine Vortrocknung stattfindet.The second intermediate is thus a mixture of natural fibers and binder fibers, with a binder fiber content of 4% to 20%, preferably 5% to 15% or 10%, equipped with additives, and having a dry matter content of preferably about 40% to 75%. Of course, the amount of dry matter depends very much on how much liquid is added by the spraying of the additives, and whether pre-drying takes place even after spraying.

Die Herstellung des ersten Zwischenproduktes, also der vorverarbeiteten Pflanzenfasern, geschieht vorzugsweise, indem der Rohstoff zerfasert wird und verdauliche Bestandteile des Rohstoffes abgetrennt werden. Verdauliche Bestandteile sind insbesondere z.B. Milchsäure, Essigsäure, Aminosäuren, Proteine und Mineralstoffe.The preparation of the first intermediate product, ie the preprocessed plant fibers, is preferably done by the raw material is fiberized and digestible components of the raw material are separated. Digestible components are in particular e.g. Lactic acid, acetic acid, amino acids, proteins and minerals.

Der Rohstoff ist gemäß der Erfindung Grassilage (siliertes Gras), vorzugsweise mit einem Trockensubstanzanteil von 20% bis 40%, insbesondere 25% bis 35%. In einer anderen bevorzugten Variante der Erfindung ist der Rohstoff Goldhafer (Trisetum flavescens).The raw material according to the invention grass silage (silated grass), preferably with a dry matter content of 20% to 40%, in particular 25% to 35%. In another preferred variant of the invention, the raw material is gold oat (Trisetum flavescens).

Das Zerfasern wiederum geschieht in einer wässrigen Suspension mit einem Mazerator und/oder einem Entstipper, denen auch eine Hammermühle zum Zerreissen des Rohstoffes vorgeschaltet ist. Bei Verwendung eines Mazerators in Verbindung mit einem Entstipper ist vorzugsweise der Mazerator dem Entstipper vorgeschaltet.The defibering, in turn, takes place in an aqueous suspension with a macerator and / or a deflaker, which is also preceded by a hammer mill for tearing the raw material. When using a macerator in conjunction with a Entstipper the macerator is preferably upstream of the Entstipper.

Das Abtrennen der verdaulichen Bestandteile geschieht vorzugsweise durch Abtrennen der Fasern aus der wässrigen Suspension nach dem Zerfasern, wobei die verdaulichen Bestandteile in der Suspension verbleiben.The separation of the digestible components is preferably done by separating the fibers from the aqueous suspension after defibering, leaving the digestible components in the suspension.

Die verdaulichen Bestandteile werden vorzugsweise in einem separaten Zweig der Verarbeitung zu Futter- oder Nahrungsmittelzusätzen verarbeitet. Dies geschieht durch Aufkonzentrieren dieser Bestandteile in der Suspension zu Nahrungsstoffen, wobei das Wasseranteil vorzugsweise rezykliert wird.The digestible ingredients are preferably processed into feed or food additives in a separate branch of processing. This is done by concentrating these ingredients in the suspension into nutrients, with the water portion preferably being recycled.

Die verdaulichen Bestandteile umfassen vorzugsweise organische Säuren, Proteine und Mineralstoffe, ferner vorzugsweise auch Enzyme, Vitamine und/oder hormonähnliche Stoffe, insbesondere Vitamin D3-Hormon. Das Vorhandensein dieser Stoffe hängt von der Wahl des Rohstoffes ab, also von den verwendeten Pflanzen und von optional eingesetzten Silierhilfsmitteln.The digestible components preferably comprise organic acids, proteins and minerals, and preferably also enzymes, vitamins and / or hormone-like substances, in particular vitamin D3 hormone. The presence of these substances depends on the choice of the raw material, ie on the plants used and on optional silage additives.

Zur Herstellung des Vlieselementes aus dem zweiten Zwischenprodukt, also aus dem fertigen und konditionierten Fasergemisch wird vorzugsweise ein Vlies gebildet und werden durch Erhitzen die Bindefasern aktiviert, so dass sie mit den Naturfasern verkleben und eine Matrix bilden. Die Vliesbildung kann geschehen, indem das zweite Zwischenprodukt einen Trockensubstanzanteil von ca. 60% bis 85% oder höher aufweist und so direkt zur Bildung des Vlieses verwendet wird, wobei gegebenenfalls eine Resttrocknung beim Erhitzen des Vlieses zur Aktivierung der Bindefasern stattfindet. Alternativ kann die Vliesbildung geschehen, indem das zweite Zwischenprodukt einen Trockensubstanzanteil von 40% bis ca. 60%, aufweist, auf ein Transportband aufgelegt, durch beispielsweise Heissluft nachgetrocknet und optional wieder aufgelockert wird, und anschliessend zur Aktivierung der Bindefasern erhitzt wird.To produce the nonwoven element from the second intermediate product, ie from the finished and conditioned fiber mixture, a nonwoven fabric is preferably formed and the binding fibers are activated by heating, so that they bond with the natural fibers and form a matrix. The web formation can be done by the second intermediate product has a dry matter content of about 60% to 85% or higher and is thus used directly for the formation of the web, wherein optionally a residual drying takes place during heating of the web to activate the binder fibers. Alternatively, the web formation can be done by the second intermediate product has a dry matter content of 40% to about 60%, placed on a conveyor belt, after-dried by hot air, for example, and optionally loosened again, and then heated to activate the binding fibers.

Die Vlieslegung, eventuelle Nachtrocknung und Aktivierung geschieht vorzugsweise in einem kontinuerlichen Prozess zur Erzeugung eines Vliesbandes. Vom fertigen Vliesband können die Vlieselemente abgeschnitten werden. Alternativ kann die Vlieslegung etc. aber auch im Batch-Betrieb geschehen, wobei einzelne Vlieselemente in vorgegebenen Formen gebildet werden..The fleece laying, eventual drying and activation is preferably carried out in a continuous process for producing a nonwoven tape. From the finished Fleece band, the nonwoven elements can be cut off. Alternatively, the nonwoven laying, etc., but also done in batch mode, with individual nonwoven elements are formed in predetermined shapes ..

Zusammengefasst weist das erfindungsgemässe Verfahren in einer bevorzugten Ausführungsform der Erfindung die folgenden Schritte auf:

  1. (a) Der Rohstoff Gras wird in feuchtem Zustand verdichtet und luftdicht verpackt. Dieses Verfahren ist in der Landwirtschaft seit langem unter dem Begriff "silieren" bekannt.
  2. (b) Das silierte Gras wird für die weitere Verarbeitung konditioniert, das heisst, so vorbereitet, dass die Herstellung einer rühr- und pumpfähigen Suspension möglich ist.
  3. (c) Der konditionierte Rohstoff wird zerfasert und von verdaulichen Begleitstoffen weitgehend befreit.
  4. (d) Die Grasfasern werden entwässert, mit Bindefasern gemischt, mit Additiven ausgerüstet und für die Vlieslegung vorbereitet.
  5. (e) Aus dem vorbereiteten Fasergemisch wird ein dreidimensionales Vlies hergestellt und thermisch fixiert.
In summary, in a preferred embodiment of the invention, the method according to the invention comprises the following steps:
  1. (a) The raw material grass is compacted in a moist state and packed airtight. This process has long been known in agriculture as "ensiling".
  2. (b) The ensiled grass is conditioned for further processing, that is prepared so as to allow the production of a stirrable and pumpable suspension.
  3. (c) The conditioned raw material is defibered and largely freed of digestible accompanying substances.
  4. (d) The grass fibers are dewatered, mixed with binder fibers, provided with additives and prepared for lay-up.
  5. (e) From the prepared fiber mixture, a three-dimensional nonwoven fabric is produced and thermally fixed.

Die Erfindung ermöglicht also

  • Die Bereitstellung des Rohstoffs für die ganzjährige Nutzung in gleich bleibender Qualität.
  • Die Herstellung von Grasfasern aus diesem Rohstoff.
  • Die Verarbeitung der Grasfasern zu einem dreidimensionalen, stabilen Vlies- bzw. Dämmstoff.
The invention thus enables
  • The provision of raw material for year-round use in consistent quality.
  • The production of grass fibers from this raw material.
  • The processing of grass fibers into a three-dimensional, stable fleece or insulating material.

Weitere bevorzugte Ausführungsformen gehen aus den abhängigen Patentansprüchen hervor. Dabei sind Merkmale der Verfahrensansprüche sinngemäss mit den Vorrichtungsansprüchen kombinierbar und umgekehrt.Further preferred embodiments emerge from the dependent claims. Characteristics of the method claims are analogously combined with the device claims and vice versa.

KURZE BESCHREIBUNG DER ZEICHNUNGENBRIEF DESCRIPTION OF THE DRAWINGS

Im folgenden wird der Erfindungsgegenstand anhand von bevorzugten Ausführungsbeispielen, welche in den beiliegenden Zeichnungen dargestellt sind, näher erläutert. Figur 1 zeigt schematisch einen Verfahrensablauf und Figur 2 eine Struktur einer Anlage zur Vliesherstellung aus Graspflanzen.In the following, the subject invention will be explained in more detail with reference to preferred embodiments, which are illustrated in the accompanying drawings. FIG. 1 schematically shows a procedure and FIG. 2 a structure of a plant for fleece production from grass plants.

WEGE ZUR AUSFÜHRUNG DER ERFINDUNGWAYS FOR CARRYING OUT THE INVENTION

Im Folgenden wird eine Vliesherstellung, beginnend mit der Rohstoffproduktion, anhand von Figur 1 beschrieben: Zunächst wird der Rohstoff Gras auf dem Feld gemäht. Dabei wird er vorzugsweise mit einem Konditionierer bearbeitet, welcher die Stängelstrukturen so aufschlägt, dass diese weicher werden und schneller Feuchtigkeit verlieren. Das gemähte Gras wird auf dem Feld angewelkt, das heisst, bis zu einem Trockensubstanzgehalt von 25-40% angetrocknet. Anschliessend wird es aufgenommen und in einem Silo unter Ausschluss von Luft verpresst bzw. siliert. In dieser Form ist der Rohstoff über sehr lange Zeit verlustfrei lagerfähig und steht jederzeit und witterungsunabhängig für die Verarbeitung zur Verfugung. Die Silierung erfolgt vorzugsweise in grossen, horizontalen Fahrsilos, kann aber auch in Siloballen oder stehenden Silos erfolgen. Ferner können auch Silierhilfsmittel beigegeben werden.The following is a nonwoven production, starting with the production of raw materials, based on FIG. 1 described: First, the raw grass is mowed on the field. In this case, it is preferably processed with a conditioner which strikes the stem structures in such a way that they soften and lose moisture more quickly. The mown grass is wilted on the field, that is, dried to a dry matter content of 25-40%. It is then picked up and pressed in a silo with the exclusion of air or ensiled. In this form, the raw material can be stored without loss over a very long period of time and is available for processing at any time and weather-independent. Silage is preferably carried out in large, horizontal silos, but can also be done in silo bales or silos standing. Furthermore, also Silierhilfsmittel can be added.

Zur Verarbeitung wird der Rohstoff vom Silo abgestochen, aufgelockert 1 und einer Dosiereinrichtung 2 zugeführt. Diese führt den Rohstoff in eine oder mehrere Hammermühlen, wo er zerrissen 3 oder aufgerissen und auf ca. 10-30 mm Länge und ca. 1-3 mm Dicke zerkleinert wird. Dadurch werden die Pflanzenteile für die nachfolgende Zerfaserung vorbereitet.For processing, the raw material is tapped from the silo, loosened 1 and fed to a metering device 2. This leads the raw material into one or more hammer mills, where it is torn 3 or torn open and crushed to about 10-30 mm in length and about 1-3 mm in thickness. This will prepare the plant parts for subsequent defibering.

Mit dem zerkleinerten Pflanzenmaterial ist unter Zugabe von Wasser die Herstellung 4 einer rühr- und pumpfähigen Rohstoffsuspension möglich. Die Rohstoffsuspension wird einer mechanischen Zerfaserung 5 zugeführt. Diese wird durch Zerfaserungsaggregate bewerkstelligt, die in der Zellstoffindustrie seit Jahrzehnten erfolgreich eingesetzt werden, z.B. Entstipper (defibrator), Mazeratoren oder Refiner. Zur Optimierung der Zerfaserung im Hinblick auf die Faserlänge und die Faserdicke können diese Aggrregate auch hintereinander geschaltet werden. Es hat sich gezeigt, dass die Abfolge von Mazerator und Entstipper für die vorliegende Aufgabenstellung besonders gut geeignet ist. In dieser Abfolge übernimmt der Mazerator, der die Rohstoffsuspension selber ansaugen kann, die weitere Homogenisierung der Rohstoffsuspension sowie die Beschickung des direkt nachgeschalteten Entstippers. Dadurch entstehen Fasern mit vorwiegend ca. 3-30 mm Länge und ca. 0,05-0,5 mm Dicke. Im Zuge der Zerfaserung erfolgt auch ein Massentrasfer der löslichen und verdaulichen Rohstoffbestandteile in die Flüssigphase. Die Zerfaserung kann Temperatur-unabhängig durchgeführt werden. Es hat sich jedoch gezeigt, dass eine Temperatur von über 40°C in der Suspension Vorteile bezüglich der Verarbeitbarkeit, der erzielten Faserqualität sowie der Faserreinigung bringt.With the crushed plant material with the addition of water, the production of a 4 stirrable and pumpable raw material suspension is possible. The raw material suspension is fed to a mechanical defibration 5. This is accomplished by fiberizing aggregates which have been successfully used in the pulp industry for decades, e.g. Deflaker, macerators or refiner. To optimize the fiberization with regard to the fiber length and the fiber thickness, these aggregates can also be connected in series. It has been shown that the sequence of macerator and deflaker is particularly well suited for the present task. In this sequence, the macerator, which can suck in the raw material suspension itself, takes over the further homogenization of the raw material suspension as well as the feed of the directly downstream degasser. This results in fibers with predominantly about 3-30 mm in length and about 0.05-0.5 mm thickness. In the course of defibration, a mass transfer of the soluble and digestible raw material components into the liquid phase takes place. The defibration can be carried out temperature-independently. However, it has been shown that a temperature of over 40 ° C in the suspension brings advantages in terms of processability, the quality of the fibers obtained and the fiber cleaning.

Nach der Zerfaserung werden die Fasern mechanisch entwässert 7. Dies erfolgt vorzugsweise durch Entnahme 6 der Fasern aus der Suspension und anschliessende Verpressung der Fasern in einer Schneckenpresse. Die Entnahme aus der Suspension erfolgt vorzugsweise mit einer Siebeinrichtung, z.B. mit einem Bogensieb oder einem Trommelsieb. Mit einer Schneckenpresse lässt sich das Fasergemisch beispielsweise auf einen Trockensubstanzgehalt von ca. 36-46% entwässern.After defibration, the fibers are mechanically dewatered. 7. This is preferably done by removing the fibers from the suspension and then pressing the fibers in a screw press. The removal from the suspension is preferably carried out with a screening device, e.g. with a bow sieve or a drum sieve. With a screw press, for example, the fiber mixture can be dewatered to a dry matter content of approx. 36-46%.

Die löslichen und verdaulichen Rohstoffbestandteile aus der Suspension bestehen vor allem aus organischen Säuren (Milchsäure, Essigsäure, Aminosäuren), nicht fermentierten Zuckern, Proteinen und Mineralstoffen. Durch Zugabe von geeigneten Silier-Hilfsmitteln, z.B. Bakterienkulturen, kann die Umwandlung der im Rohstoff enthaltenen fermentierbaren Zucker gezielt gesteuert werden. Zum Beispiel kann so ein bestimmtes Verhältnis von Milchsäure zu Essigsäure erreicht werden.The soluble and digestible raw material components of the suspension consist mainly of organic acids (lactic acid, acetic acid, amino acids), non-fermented sugars, proteins and minerals. By adding suitable silage aids, eg bacterial cultures, the conversion of the raw material into the raw material can controlled fermentable sugars are controlled. For example, such a ratio of lactic acid to acetic acid can be achieved.

Die löslichen und verdaulichen Rohstoffbestandteile können nach der Abtrennung von den Fasern aufkonzentriert und als Spezialfuttermittel verwendet werden. Hervorzuheben ist dabei der Wert dieses Spezialfuttermittels als Säuerungsmittel, als Geschmacksträger und als eigentliches Futtermittel. Zusätzlich können je nach der verwendeten Grasart auch wertvolle Enzyme, Vitamine oder hormonähnliche Substanzen in diesem Stoffstrom enthalten sein. Ein Beispiel hierzu ist die Grasart Goldhafer (Trisetum flavescens), welche ein Vitamin D3-Derivat enthält, welches teilweise wasserlöslich ist und den Knochenaufbau von Säugetieren und Menschen unterstützt.The soluble and digestible raw material components can be concentrated after separation from the fibers and used as a special feed. Of particular note is the value of this special feed as an acidifier, as a flavor carrier and as an actual feed. In addition, depending on the type of grass used, valuable enzymes, vitamins or hormone-like substances may also be present in this material stream. An example of this is the grass species Goldgrass (Trisetum flavescens), which contains a vitamin D3 derivative, which is partially water-soluble and supports the bone formation of mammals and humans.

Alle aufgeführten Inhaltstoffe und Eigenschaften können nicht nur in der tierischen Ernährung, sondern auch als Zusatzstoff für die menschliche Ernährung genutzt werden. Die erforderliche Aufkonzentration der Inhaltstoffe kann durch Filtration und/oder Eindampfung erfolgen. Dabei ist zu beachten, dass die Mineralstoffe bei der Aufkonzentration teilweise aus der Lösung ausfallen können.All listed ingredients and properties can be used not only in animal nutrition, but also as an additive for human nutrition. The required concentration of the ingredients can be done by filtration and / or evaporation. It should be noted that the minerals may partially precipitate out of the solution during the concentration.

Im Folgenden wird die weitere Verarbeitung der entwässerten Fasern beschrieben: In den nachfolgenden Schritten erfolgen die Trocknung bzw. Vortrocknung 8 der Fasern, die Beimischung 9 der Bindefasern sowie die Ausrüstung 10 der Fasern mit Additiven.The further processing of the dewatered fibers is described below: In the subsequent steps, the drying or pre-drying 8 of the fibers, the admixture 9 of the binding fibers and the equipment 10 of the fibers with additives take place.

Für die Beimischung 9 der Bindefasern bietet die Textilindustrie sowohl kontinuierliche als auch chargenweise Verfahren an, die gut geeignet sind. Bei der Verarbeitung von Grasfasern erfolgt die Zudosierung der Bindefasern mit einem Gewichtsanteil von 4-25%, vorzugsweise von 5-15% des Produktgewichtes.For the admixture 9 of binder fibers, the textile industry offers both continuous and batch processes which are well suited. When processing grass fibers, the binder fibers are added at a weight fraction of 4-25%, preferably 5-15% of the product weight.

Die Ausrüstung 10 der Fasern mit Additiven erfolgt durch Besprühen der losen Fasern. Um einen möglichst gleichmässigen Auftrag der Additive auf die Fasern sicher zu stellen, erfolgt die Besprühung vorzugsweise in einem Luftstrom, in welchem sich die Fasern frei bewegen. Die Besprühung kann mit den in der Dämmstoffindustrie üblichen Flammhemmern, z.B. mit Boraten oder Ammoniumverbindungen sowie mit einem Hydrophobierungsmittel und/oder einem Fungizid erfolgen. Diese Additive können in einer Lösung gemischt oder einzeln auf die Fasern aufgesprüht werden.The equipment 10 of the fibers with additives is made by spraying the loose fibers. In order to ensure the most uniform application of the additives to the fibers, the spraying is preferably carried out in an air stream in which the fibers move freely. The spraying can be carried out with flame retardants customary in the insulating industry, e.g. with borates or ammonium compounds and with a water repellent and / or a fungicide. These additives can be mixed in a solution or sprayed individually onto the fibers.

Mit der Trocknung bzw. Vortrocknung 8 werden die Fasern auf einen Trockensubstanzgehalt eingestellt, der für die nachfolgende Vlieslegung und Thermobondierung vorteilhaft ist. Dieser Trockensubstanzgehalt liegt vorzugsweise bei 60-85% des Gesamtgewichtes der Fasern. In diesem Zustand sind die Fasern noch elastisch und können einer mechanischen Bearbeitung gut standhalten. Zudem neigen die Fasern weniger zum Anhaften in Karden oder ähnlichen, eventuell zur Vliesbildung eingesetzten Geräten. Im Weiteren haben die Fasern bei diesem Feuchtigkeitsgehalt in beschränktes Eigengewicht und können deshalb zu einem Vlies mit möglichst grossem Volumen bzw. möglichst geringer Dichte gelegt werden.With the drying or predrying 8, the fibers are adjusted to a dry matter content which is advantageous for the subsequent nonwoven laying and thermal bonding. This dry matter content is preferably 60-85% of the total weight of the fibers. In this state, the fibers are still elastic and can withstand mechanical processing well. In addition, the fibers are less prone to sticking in cards or similar, possibly used for web forming equipment. Furthermore, the fibers have limited self-weight at this moisture content and can therefore be laid to a non-woven with the largest possible volume or the lowest possible density.

Die Trocknung bzw. Vortrocknung 8 kann mit verschiedenen Trocknungstechniken erzielt werden, z.B. Flugschichttrockner, Trommeltrockner oder Bandtrockner.The drying or pre-drying 8 can be achieved with various drying techniques, e.g. Air-layer dryer, drum dryer or belt dryer.

Es sind grundsätzlich verschiedene Reihenfolgen der Verarbeitungsschritte Mischung 9 mit Bindefasern, Zudosierung der Additive 10 und Trocknung bzw. Vortrocknung 8 möglich. Dabei ist zu beachten, dass auch der Transport der Fasern im Luftstrom zu einem nicht unbedeutenden Trocknungseffekt führen kann und dazu auch gezielt genutzt werden kann.In principle, different sequences of the processing steps mixture 9 with binder fibers, metered addition of the additives 10 and drying or pre-drying 8 are possible. It should be noted that the transport of the fibers in the air stream can lead to a not insignificant drying effect and can also be used selectively.

Alternativ zur Vortrocknung 8 ist es auch möglich, die mit Bindefasern und Additiven ausgerüsteten Fasern ohne eigentliche Vortrocknung 8, d.h. mit einem Trockensubstanzgehalt von 36-50% der Vliesbildung zu übergeben.As an alternative to pre-drying 8, it is also possible to use the fibers provided with bonding fibers and additives without actual pre-drying 8, i. with a dry matter content of 36-50% of the web formation.

Als weitere Alternative zur Vortrocknung 8 ist es auch möglich, die Fasern vor der Vliesbildung vollständig, d.h. auf einem Trockensubstanzgehalt von über 85% zu trocknen.As a further alternative to pre-drying 8, it is also possible to completely remove the fibers prior to web formation, i. to dry to a dry matter content of over 85%.

Für die Vlieslegung bietet die Industrie verschiedene Verfahren an, z.B. air lay, direkte Vliesbildung 11, Aufstreuen, Krempel, oder ähnliche, welche für die vorliegende Aufgabenstellung geeignet sind.For nonwoven laying, the industry offers various methods, e.g. Air lay, direct web formation 11, scattering, carding, or the like, which are suitable for the present task.

Beim Thermobondieren 12 des Vlieses (oder Aktivieren der Bindefasern) erfolgen die Erhitzung des Vlieses auf die Schmelztemperatur der Mantelkomponente der Stützfasern sowie die Einstellung der gewünschten Plattendicke bzw. -dichte. Die Plattendichte bzw. -dicke wird mit einem überlaufenden Band eingestellt, welches das Faservlies auf eine Dicke von ca. 3 mm bis 250 mm verdichtet und ihm dabei eine gleichmässige Oberfläche verleiht. Die Erhitzung des Vlieses erfolgt mit einer Zuluft-Temperatur von 120-180°C, vorzugsweise von 140-170°C. Der Thermobondierofen ist auch zur Entnahme der Restfeuchte im Faservlies geeignet.In the case of thermobonding 12 of the nonwoven fabric (or activation of the binder fibers), the heating of the nonwoven fabric takes place at the melting temperature of the sheath component of the support fibers and the setting of the desired plate thickness or density. The plate density or thickness is adjusted with an overflowing band, which compresses the nonwoven fabric to a thickness of about 3 mm to 250 mm, thereby giving it a uniform surface. The heating of the web takes place with a supply air temperature of 120-180 ° C, preferably 140-170 ° C. The Thermobondierofen is also suitable for removing the residual moisture in the nonwoven fabric.

Nach der Erhitzung wird das Faservlies gekühlt, auf die gewünschten Masse der Fasermatten zugeschnitten 13, palettiert und verpackt.After heating, the nonwoven fabric is cooled, cut to the desired mass of fiber mats 13, palletized and packaged.

Figur 2 zeigt übersichtsmässig die Struktur einer Anlage zur Vliesherstellung: eine Vorverarbeitungseinheit 21 weist die Vorrichtungen zum Zerreissen, Zerfasern und Entwässern auf, also zur Bereitstellung der Pflanzenfasern 101. Eine Kerneinheit 22 weist die Vorrichtungen zum Mischen 9, Aufsprühen 9 von Additiven und Trocknen 8 und somit zur Bildung des Fasergemisches 102 auf. Eine Vlieserzeugungseinrichtung 23 weist die Vorrichtungen zur Vlieslegung, Thermobondierung und zum Zuschneiden zum Bilden von Vlieselementen 103 auf. Eine optionale Konzentrationseinrichtung 24 weist die Mittel zum Aufkonzentrieren der aus der Suspension abgetrennten verdaulichen Bestandteile 104 zu Nahrungsstoffen 105 auf. FIG. 2 shows an overview of the structure of a plant for nonwoven production: a pre-processing unit 21 has the devices for tearing, fraying and dewatering, so to provide the plant fibers 101. A core unit 22 has the means for mixing 9, spraying 9 of additives and drying 8 and thus to Forming the fiber mixture 102 on. A web-forming device 23 comprises the devices for fleece laying, Thermobondierung and for cutting to form nonwoven elements 103. An optional concentrator 24 has means for concentrating the digestible constituents 104 separated from the suspension into feeds 105.

Mit dem erfindungsgemässen Verfahren wurden aus Gras Vliese mit einer Dichte von 25-90 kg/m3 hergestellt. Die Platten mit geringer Dichte sind leicht flexibel, etwas stauchfähig und angenehm zu handhaben. Es wurden eine Wärmeleitfähigkeit von 0,034-0,040 W/(m,K) gemessen.Nonwovens having a density of 25-90 kg / m 3 were produced from grass using the method according to the invention. The low density panels are slightly flexible, somewhat compressible and comfortable to handle. A thermal conductivity of 0.034-0.040 W / (m, K) was measured.

Für die Platten mit höherer Dichte können die Bindefasern so ausgewählt werden, dass das Produkt eine erhöhte mechanische Druckfestigkeit aufweist und so auch für Anwendungen als Trittschallisolation sowie für direkt verputzte Aussenfassaden geeignet ist.For the higher density panels, the binder fibers can be selected so that the product has increased mechanical compressive strength and is thus also suitable for impact sound insulation as well as directly plastered exterior facades.

Die Anwendung des Vlieses zur Herstellung von Matratzen können spezielle Bindefasern eingesetzt werden, welche das Rückstellverhalten des Vlieses beeinflussen.The use of the fleece for the production of mattresses special binding fibers can be used, which influence the recovery behavior of the fleece.

Weitere Eigenschaften, z.B. Geruchsfreiheit und Wasserabstossung, können durch gezielte Beeinflussung der Fasern erreicht werden, beispielsweise indem sie mit einem Oxidationsmittel oder mit einem Hydrophobierungsmittel behandelt werden.Other properties, e.g. Odorlessness and water repellency can be achieved by targeted influencing of the fibers, for example by being treated with an oxidizing agent or with a hydrophobing agent.

Das Verfahren ermöglicht die Nutzung eines bisher industriell kaum genutzten Rohstoffs zur Herstellung eines hochwertigen Produktes. Damit verbunden sind bedeutende ökologische Vorteile bei der Rohstoffbereitstellung (nachwachsender Rohstoff), der Verarbeitung (geringer Energieaufwand), der Produktnutzung (optimale Kombination von Kälteschutz, Wärmeschutz und Schallschutz) sowie der Produktentsorgung (Rezyklierbarkeit).The process allows the use of a hitherto barely used raw material for the production of a high quality product. Associated with this are significant ecological advantages in the provision of raw materials (renewable raw material), the processing (low energy consumption), product use (optimal combination of cold protection, thermal insulation and sound insulation) and product disposal (recyclability).

Claims (17)

  1. A method of manufacturing an insulation mat from a raw material comprising grass plants, characterized in that:
    i. the raw material grass is mowed in the field,
    ii. the mowed grass is withered in the field meaning to pre-dry the grass to a dry substance content of 25-40%,
    iii. the raw material is being collected (1)and pressed in a silo under the exclusion of air,
    iv. the raw material is removed from the silo, being loosened (1) and moved to a metering device (2),
    v. the device moves the raw material into one or more hammer mills, where it is ripped apart 3 and reduced into parts of an approx. 10-30 mm in length and 1-3 mm in thickness,
    vi. by adding water to the de-fibered plant matter, a raw material suspension, which can be stirred or pumped, is manufactured (4),
    vii. the raw material suspension is moved to a mechanical de-fibering (5),
    viii. the fibers are withdrawn (6) from the suspension,
    ix. then, the fibers are being mechanically drained (7), to obtain a first intermediate product (101) made of moist, natural grass fibers which have a dry substance component of 30% to 50%, preferably nearly 40%,
    x. and a second intermediate product (102) is obtained from a first intermediate product (101) by implementing the following steps:
    • pre-drying (8) of the grass fibers to a dry substance content of 60-85% of the total weight of the fibers or drying up to a dry substance content greater than 85 %, of the total weight of the fibers,
    • adding (9) of binding fibers up to a content by weight of 4-25%, preferably 5-15% of the product's weight,
    • spraying (10) of the additives.
  2. The method according to claim 1, characterized in that the binding fibers added to the natural fibers (9) are in a watery suspension which dry substance content is under 10%.
  3. The method according to one of the above claims, characterized in that the step of the pre-drying (8) is at least partially occurring in at least one conveying section in which the fibers are exposed a hot air flow.
  4. The method according to claim 1, characterized in that, to manufacture the first intermediate product, the digestible parts of the raw material (100) are being separated from the raw material (100).
  5. The method according to claim 1, characterized in that, the vegetable raw material (100) is being de-fibered (5), in a watery suspension (4) by means of a mechanical de-fibering system, preferably a macerator and/or deflaker.
  6. The method according to claim 5, characterized in that, a macerator as well as a deflaker are used, with the macerator positioned in front of the deflaker.
  7. The method according to one of the claims 4 to 6, characterized in that, the separation of the digestible parts is done by separating the vegetable grass fibers from the suspension (4), after the de-fibering (5), with the digestible parts remaining in the suspension.
  8. The method according to claim 7, characterized in that, the digestible parts (104) contain mainly acids, proteins and minerals and are concentrated into a special feeding stuff or to a nutrient additive (105).
  9. The method according to claim 7, characterized in that, the digestive parts (104) further comprise at least one of enzymes, vitamins, similar hormone matter and vitamin D3 hormone.
  10. The method according to one of the above claims, , characterized in that an insulation mat is manufactured from the second intermediate product (102), by the additional steps of:
    • forming (11) a fleece from the second intermediate product (102),
    • activating (12) of the binding fibers through the heating of the fleece, whereby the binding fibers and natural fibers are bonding together.
  11. The method according to claim 10, characterized in that, the second intermediate product (102) has a dry substance content of approximately 60% to 85% for manufacture of the fleece, wherein a residual drying is provided by heating the fleece in order to activate (12) the binding fibers.
  12. The method according to claim 10, characterized in that, the second intermediate product (102) has a dry substance content of approximately 40% to 60%, is positioned on a conveyor belt, is post-dried, and is loosened up, the activation (12) of the binding fibers then occurring.
  13. An insulation mat produced according to the method according at least one the claims 1 to 12.
  14. An insulation mat according to claim 13 with a density of 25-90 kg/m3.
  15. A device for the manufacturing of an insulation mat from grass plants by the method according at least one the claims 1 to 12 comprising a core unit (22) for producing a second intermediate product (102) from a first intermediate product (101), whereby the core unit (22) comprises: a hot air based drying unit, a mixer unit for mixing natural fibers with binding fibers, which may be thermally activated, and a provider unit for providing additives to the fibers.
  16. A device according to claim 15 comprising a pre-processing system (21), having equipment for de-fibering the grass plants and separating the digestible parts from the fiber for manufacturing the first intermediate product (101).
  17. A device according to claim 15 or 16 comprising a fleece production system (23), further comprising units for fleece laying of the second intermediate product (102), and having units for heating the fleece, above a binding fiber activation temperature, for activating the binding fibers.
EP20080714781 2007-03-26 2008-03-25 Production of non-woven elements made of natural fibres Active EP2139655B1 (en)

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PCT/CH2008/000131 WO2008116340A1 (en) 2007-03-26 2008-03-25 Production of non-woven elements made of natural fibres

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FI20105125A (en) * 2010-02-09 2011-08-10 Ekovilla Oy Wood fiber insulation and a method of making it
US8795469B2 (en) * 2010-06-25 2014-08-05 Prairie Paper Ventures Inc. Method for preparing nonwood fiber paper
CH704022A2 (en) 2010-10-22 2012-04-30 Gramitech S A METHOD AND DEVICE FOR OBTAINING AND TREATMENT Plant Fibers.
DE102011010140B4 (en) * 2011-02-02 2016-06-16 Biowert Ag Process for the supply and preparation of natural fibers and their use for the production of fiber-reinforced plastic material and insulating material
DE102011010192B4 (en) * 2011-02-02 2016-06-16 Biowert Ag Process for the supply and preparation of natural fibers and their use for the production of fiber-reinforced plastic material and insulating material
WO2012107054A1 (en) * 2011-02-07 2012-08-16 Naporo Klima Dämmstoff Gmbh Flexible nonwoven elements based on reed fibres for insulation purposes
BR112014014381A2 (en) * 2011-12-13 2017-06-13 Federal-Mogul Powertrain Inc moisture resistant, flame retardant, non-woven panel, and method to build the same
CN102561095B (en) * 2012-02-26 2014-05-21 昆山华阳复合材料科技有限公司 Degradable straw fiber
PL3006174T3 (en) * 2014-10-08 2019-01-31 SWISS KRONO Tec AG Method and system for manufacturing a wood fibre board
DE102017129489A1 (en) * 2017-11-10 2019-05-16 Creapaper Gmbh Process and device for the treatment of grass fibers
UY38825A (en) * 2019-08-08 2021-02-26 Feltwood Ecomateriales S L METHOD FOR THE PRODUCTION OF SOLID MOLDED ARTICLES MADE OF NON-WOOD PLANT MATERIALS
GB2586687B (en) 2020-05-15 2021-09-08 George Omalley A process for producing a non-woven grass fibre product

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FR2765773B1 (en) 1997-07-10 1999-08-27 Abc Equip Snc AGRICULTURAL MACHINE OF THE WASHER OR SLURRY TYPE
DE20023167U1 (en) 2000-06-02 2003-06-18 Steico Ag Process for production of wood fiber insulating panels, useful in the automobile industry. gives thicker insulating panels than previously obtainable
AT411270B (en) 2002-03-26 2003-11-25 Schober Rudolf Making non-woven from renewable material (e.g. reed) and binder fibers includes spreading chopped reed on laid material mixture
WO2005017251A1 (en) 2003-08-18 2005-02-24 Stefan Grass Method for the production of fiberboards made of moist biomass
US20070044891A1 (en) 2005-09-01 2007-03-01 Sellars Absorbent Materials, Inc. Method and device for forming non-woven, dry-laid, creped material

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US20100147474A1 (en) 2010-06-17
WO2008116340A1 (en) 2008-10-02
US8110070B2 (en) 2012-02-07
CA2686515A1 (en) 2008-10-02
CA2686515C (en) 2014-11-25

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