EP3966379B1 - Bituminöse membranen mit biologisch abbaubarem bindemittel - Google Patents

Bituminöse membranen mit biologisch abbaubarem bindemittel Download PDF

Info

Publication number
EP3966379B1
EP3966379B1 EP21713059.0A EP21713059A EP3966379B1 EP 3966379 B1 EP3966379 B1 EP 3966379B1 EP 21713059 A EP21713059 A EP 21713059A EP 3966379 B1 EP3966379 B1 EP 3966379B1
Authority
EP
European Patent Office
Prior art keywords
starch
binder
nonwoven
polyvinyl alcohol
carrier
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
EP21713059.0A
Other languages
English (en)
French (fr)
Other versions
EP3966379A1 (de
Inventor
Luca ASSUMMA
Maria CONVERSO
Laura D'ANDRIA
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Freudenberg Performance Materials GmbH and Co KG
Original Assignee
Freudenberg Performance Materials GmbH and Co KG
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Freudenberg Performance Materials GmbH and Co KG filed Critical Freudenberg Performance Materials GmbH and Co KG
Publication of EP3966379A1 publication Critical patent/EP3966379A1/de
Application granted granted Critical
Publication of EP3966379B1 publication Critical patent/EP3966379B1/de
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • D—TEXTILES; PAPER
    • D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04H—MAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H1/00—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
    • D04H1/40—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
    • D04H1/58—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties by applying, incorporating or activating chemical or thermoplastic bonding agents, e.g. adhesives
    • D04H1/587—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties by applying, incorporating or activating chemical or thermoplastic bonding agents, e.g. adhesives characterised by the bonding agents used
    • D—TEXTILES; PAPER
    • D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04H—MAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H1/00—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
    • D04H1/40—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
    • D04H1/58—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties by applying, incorporating or activating chemical or thermoplastic bonding agents, e.g. adhesives
    • D04H1/64—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties by applying, incorporating or activating chemical or thermoplastic bonding agents, e.g. adhesives the bonding agent being applied in wet state, e.g. chemical agents in dispersions or solutions
    • D—TEXTILES; PAPER
    • D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04H—MAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H3/00—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
    • D04H3/08—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating
    • D04H3/12—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating with filaments or yarns secured together by chemical or thermo-activatable bonding agents, e.g. adhesives, applied or incorporated in liquid or solid form
    • D—TEXTILES; PAPER
    • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06N—WALL, FLOOR, OR LIKE COVERING MATERIALS, e.g. LINOLEUM, OILCLOTH, ARTIFICIAL LEATHER, ROOFING FELT, CONSISTING OF A FIBROUS WEB COATED WITH A LAYER OF MACROMOLECULAR MATERIAL; FLEXIBLE SHEET MATERIAL NOT OTHERWISE PROVIDED FOR
    • D06N5/00—Roofing materials comprising a fibrous web coated with bitumen or another polymer, e.g. pitch
    • D06N5/003—Roofing materials comprising a fibrous web coated with bitumen or another polymer, e.g. pitch coated with bitumen

Definitions

  • the invention relates to a nonwoven carrier comprising a nonwoven consolidated with a binder, wherein the binder comprises starch and polyvinyl alcohol, wherein the binder does not comprise a crosslinker or a filler.
  • Subject of the invention are also uses of the nonwoven carrier, production methods, bituminous membranes and building materials.
  • Bituminous membranes having waterproofing and shielding properties are used in building applications, especially as roofing materials.
  • Bituminous membranes comprise a textile carrier, which is impregnated with bitumen.
  • the bitumen is applied to the textile carrier in a bath of molten bitumen at approximately 180°C to 200°C, followed by cooling and solidification.
  • the main function of the carrier is to confer mechanical stability, and in this regard especially mechanical resistance and dimensional stability, to the bituminous membrane and to "keep the bitumen together".
  • the textile fabric can be a nonwoven, which is consolidated with aqueous binder, such as an acrylic, SBR, polyurethane or natural polymer binder.
  • aqueous binder such as an acrylic, SBR, polyurethane or natural polymer binder.
  • the binder shall increase the mechanical resistance and dimensional stability of the nonwoven.
  • the stability of the nonwoven is increased further by a reinforcement, for example glass fiber yarns or a scrim.
  • the nonwoven is impregnated with the aqueous binder solution, followed by drying and solidification, thereby obtaining a nonwoven carrier for bitumen impregnation.
  • the nonwoven carriers and bituminous membranes are generally provided in the form of relatively thin flexible sheets, typically with a thickness of a few millimeters, which can be rolled up and unrolled.
  • Such binder consolidated nonwoven carriers for bituminous membranes should have special properties, which render them suitable for producing bituminous membranes.
  • the nonwoven carrier should not develop dimensional shrinking or stretching when subjected to temperature or mechanical forces. It should easily follow all stresses in the bituminization process (at about 180°C to 200 °C), thereby having a high initial modulus and high dimensional stability (low deformation). Further the nonwoven carrier should have a high tearing resistance and elongation at break (determined from tensile test at room temperature). This requirement is important because it is determinant for the technical specification of the membrane like tearing resistance and elongation at break.
  • Bituminous membranes are produced in large amounts for building applications. Therefore, they are often produced at large scale in an automated production line, wherein a roll of nonwoven carrier is continuously unwound and guided through a bath of molten bitumen. Subsequently, the product is cooled until the bitumen solidifies and the bituminous membrane product is rolled up. In such a process, it is important that the nonwoven carrier is dimensionally stable, thus being deformed as little as possible. The nonwoven carrier should not be deformed at about 180°C, when it is processed and guided through the hot bath. Otherwise, the sheet material could be damaged or a nonuniform product could be obtained. The binder must remain stable at around 180°C.
  • bituminous membranes must meet high quality standards for the building applications. Generally, they are used as building and roofing membranes, such as sarking, shielding or waterproofing membranes. In such applications, they must shield the roof and building from moisture over many years. Therefore, it is very important that bituminous membranes are homogenous and have no defects such as cracks and punctures, or even structural irregularities which could lead to damages over time. Even minor defects can lead to leakage of moisture or other problems at a building site over extended time periods. Therefore, the relatively thin bituminous roofing membranes and nonwoven carriers embedded therein should have good mechanical properties and high dimensional stability, such that they can be applied to a building or roofing site conveniently without being damaged. High stability is also required after application to the construction site, because a building site or roof can be subjected to stress and strain over the years.
  • nonwoven carriers for bituminous membranes are flexible, and at the same time have good mechanical properties and high dimensional stability at cold and hot temperature. Even minor improvements of mechanical stability of the nonwoven carriers at cold or hot temperature can provide a significant reduction of damages, such that a more accurate and reliable material is obtained.
  • various synthetic binders are used for consolidating nonwovens, such as acrylic, SBR or polyurethane polymers.
  • starch-based binders for consolidating nonwoven carriers for bituminous membranes have been described in the art.
  • Starch as a binder is available in large amounts and relatively inexpensive.
  • Conventional starch based binders for nonwovens are often provided in a mixture with another binder polymer.
  • Such compositions also comprise a crosslinker which covalently links the binder molecules, such that a three dimensional polymer matrix is formed. It is also assumed in the art that a high dimensional stability is achieved by crosslinking the polymer binder.
  • EP 0 354 023 A2 relates to a binder composition for fiber mats, wherein the binder comprises starch, a starch crosslinking agent and an anti-wicking agent.
  • the crosslinker can be melamine-formaldehyde or urea-glyoxal condensate.
  • the binder may comprise a polymer strength additive, such as polyvinyl alcohol or acrylic polymer.
  • the anti-wicking agent is typically a surfactant.
  • WO 2006/120523 A1 discloses a curable aqueous binder composition comprising polyvinyl alcohol, starch or sugar, a multi-functional crosslinking agent and a catalyst. It is suggested to use the binder for impregnating glass fiber products.
  • WO 2015/084372 A1 discloses aqueous binders for impregnating nonwovens, which comprise a polyol in colloid form, such as starch, and a crosslinker.
  • the binder may comprise additional polymers.
  • the crosslinker is a polyfunctional small molecule, such as glyoxal or citric acid.
  • WO2019/050439A2 relates to a heat and sound-insulating material made from mineral fiber.
  • the product is a mat obtained from mineral fibers and a binder, which is crosslinked with heavy metal or boron compounds and heavy metal salts.
  • DE 1 619 127 relates to methods for impregnating fiber products with resins.
  • a fibrous substrate is impregnated with an intermediate first binder (A), which is washed away after subsequent impregnation with a binder (B).
  • the intermediate products are instable and not suitable for producing bituminous membranes.
  • EP 3 299 514 A1 relates to textile fabrics impregnated with a binder system comprising ⁇ 30% polyvinyl alcohol, ⁇ 70% starch, a crosslinker, fillers and additives.
  • a binder system comprising ⁇ 30% polyvinyl alcohol, ⁇ 70% starch, a crosslinker, fillers and additives.
  • specific binder compositions or working examples are not disclosed.
  • starch-based binder compositions and nonwovens consolidated therewith which have been described in the art, could still be improved. Often, the binder compositions require various additives and are thus relatively complex. All concrete binder compositions include a crosslinker, and frequently also a catalyst for controlling the crosslinking reaction. The reaction between starch, polyvinyl alcohol and crosslinker has to be initiated, controlled and monitored. An insufficient degree of crosslinking may result in lead low product stability, whereas an overly high degree could render the product too rigid. Thus, it would generally be desirable to consolidate such nonwoven carriers with more simple and reliable binder systems.
  • nonwoven carriers impregnated with such binders could still be improved.
  • binder-consolidated nonwoven carriers which are flexible and have good mechanical properties at cold and hot temperature; and which are thus suitable for producing bituminous membranes.
  • most prior art documents do not address this problem, and especially not mechanical properties at hot temperature.
  • binders for nonwoven fabrics often comprise formaldehyde-based crosslinkers, such as melamine-formaldehyde. Since aldehyde based binders, such as those derived from formaldehyde and glyoxal, can cause health problems, this is not desirable for safety and environmental reasons.
  • binder compositions are often relatively expensive, because components or additives are not easily available in large amounts. Since bituminous membranes are industrial products, which are used in large amounts in building applications, less costly binders would be desirable.
  • binder compositions that they comprise components or additives, which are not obtainable from natural sources and/or which are not biodegradable. It would be desirable to provide easily available binder compositions which are obtainable from natural sources or biodegradable.
  • the problem underlying the invention is to provide nonwoven fabrics, uses, methods and bituminous membranes which overcome the above mentioned problems.
  • a specific problem is to provide nonwoven carriers which are impregnated and consolidated with binders in a relatively simple, efficient and inexpensive manner.
  • the binder compositions shall be provided and processed simply and reliably.
  • the binder should be formaldehyde-free and/or shall be available, as much as possible, from natural sources or biodegradable. Overall, the nonwoven carrier shall be produced as sustainable as possible.
  • nonwoven carriers consolidated with a binder which are highly suitable for producing bituminous membranes.
  • the nonwoven carriers shall have good mechanical properties at room temperature, especially with regard to maximum tensile strength before break and tenacity.
  • the nonwoven carriers shall have high dimensional stability at hot temperature of about 180°C. Accordingly, the nonwoven carrier shall be suitable for producing bituminous membranes in roll form with standard machinery in an automated process.
  • Subject of the invention is the use of a nonwoven carrier as a substrate for bituminous membranes, wherein the nonwoven comprises organic polymer fibers and is consolidated with an aqueous binder, wherein the binder comprises
  • Subject of the invention is also a nonwoven carrier for bituminous membranes, wherein the nonwoven comprises organic polymer fibers and is consolidated with an aqueous binder, wherein the binder comprises
  • the nonwoven carrier comprises a nonwoven consolidated with a binder.
  • the nonwoven is a sheet of staple fibers or of continuous filaments that has been formed into a web by any means and bonded together by any means with the exception of weaving or knitting.
  • the fibers forming the nonwoven are randomly orientated.
  • they are bonded by friction, cohesion and/or adhesion.
  • the nonwoven carrier is a substrate for producing bituminous membranes. Bituminous membranes are often used for building applications, especially roofing applications. In a typical production process, the nonwoven carrier is impregnated with molten bitumen.
  • the nonwoven carrier which is consolidated with the binder, is porous.
  • the void fraction of the nonwoven carrier and/or of the nonwoven before binder impregnation is between 60% and 95%, more preferably between 75% and 93%, especially between 80% and 90%.
  • the porosity can be calculated from the weight and density of the product and components.
  • the molten bitumen can permeate the pores from one side of the nonwoven carrier sheet to the other, such that an intimate and stable composite is obtainable after bitumen solidification.
  • the average pore diameter is between 50 ⁇ m and 300 ⁇ m, preferably between 80 ⁇ m and 200 ⁇ m, as preferably determined by ISO 15901-1:2016.
  • the nonwoven carrier is a sheet material. Preferably, it is flexible and/or rollable.
  • Subject of the invention is also a roll of the nonwoven carrier and/or of the bituminous membrane. Such a roll can be unrolled and rolled up again conveniently by a user. Flexibility and roll form of the nonwoven carrier are advantageous for efficient processing in an automated, continuous process. Flexibility and roll form of the bituminous membrane are advantageous for application and processing at a building site or the like.
  • the nonwoven carrier is consolidated with an aqueous binder.
  • aqueous binder This is a solution or dispersion of the polymers and optionally additives in water, which is applied to the nonwoven, typically by impregnation in a bath, dried and solidified, and bonds the nonwoven fibers together.
  • the nonwoven binder enhances the stability of the nonwoven.
  • the binder comprises starch and polyvinyl alcohol.
  • Nonwoven binders comprising starch and polyvinyl alcohol have been described in the art.
  • the binder for use in the present invention is different, because it does not comprise a crosslinker.
  • crosslinker-free binders comprising starch and polyvinyl alcohol as structural polymers are applicable for producing nonwoven carriers for bituminous membranes, which meet the high requirements regarding mechanical resistance and dimensional stability at cold and even at hot temperature around 180°C. It was unexpected that such nonwoven carriers would have sufficient stability even at hot temperature in the absence of a crosslinker, which is used in conventional binders for forming a three-dimensional matrix of covalently linked binder polymers. More surprisingly, it was also found that the crosslinker free binders can have even better mechanical properties at cold and hot temperature, and especially better dimensional stability, than respective binders with crosslinker.
  • crosslinker refers to a compound which is specifically added to the aqueous binder, and which forms covalent linkages of binder polymers in the binder composition upon consolidation. According to the invention, no such compound is present which would form covalent bonds between starch and polyvinyl alcohol molecules.
  • Polyvinyl alcohol and starch are polyols, which are characterized by repetitive hydroxyl functional groups on the polymer backbones.
  • crosslinkers for binders comprising starch and/or polyvinyl alcohol are often compounds having two or more functional groups, which can react with hydroxyl groups, often carboxylic groups, but also amine or aldehyde groups.
  • Starch can also be chemically modified, for example by partial oxidation in which some hydroxyl groups are converted into carboxyl groups. Such modified starch may be crosslinked with crosslinkers having hydroxyl and carboxyl groups.
  • the aqueous binder used according to the present invention does not comprise a crosslinker compound, which would covalently link the specific starch to the polyvinyl alcohol during consolidation of the binder.
  • the aqueous binder does not comprise a crosslinker.
  • Typical crosslinkers for respective binders in the art are formaldehyde or formaldehyde resins, such as urea-formaldehyde resin, melamine-formaldehyde resin or acetone-formaldehyde resin, glyoxal or glyoxal resins, urea or urea resins, or non-polymeric polycarboxylic acids or non-polymeric polycarboxylic acid anhydrides comprising two, three or more carboxylic groups, such as citric acid.
  • the aqueous binder does not comprise an additional compound which comprises two or more functional groups for crosslinking the specific starch and polyvinyl alcohol in the binder, and especially for crosslinking hydroxyl groups of the starch and polyvinyl alcohol; such as functional groups selected from carboxyl, isocyanate, amine, aldehyde, epoxide or keto groups.
  • the binder also does not comprise crosslinkers in the form of heavy metal or boron salts or compounds.
  • the binder does not comprise a catalyst, especially a crosslinking catalyst, because no chemical reaction needs to be catalyzed.
  • the nonwoven is not consolidated with the aqueous binder in a manner such that the binder is crosslinked.
  • Crosslinking of starch and polyvinyl alcohol does not occur in a crosslinker-free binder under standard conditions, at which a nonwoven is impregnated, dried and the binder is solidified.
  • at least some degree of crosslinking may occur although no crosslinker is present. Therefore, it is preferred that the nonwoven carrier, during or after binder consolidation, is not subjected to conditions at which crosslinking would occur.
  • a very high or very low pH, pressure, temperature and/or water depletion is/are not adjusted; that the aqueous binder does not comprise highly reactive additives; or that the nonwoven carrier is not subjected to a highly reactive environment, such as reactive radiation or plasma.
  • the starch and polyvinyl alcohol are not crosslinked, or at least not substantially crosslinked.
  • substantially means that although conditions are adjusted such that no crosslinking should occur, an unavoidable and negligible small number of covalent bonds may be formed, for example due to impurities or structural anomalies of the raw materials.
  • not substantially crosslinked could mean that less than 2% or less than 0.5 % of the starch and/or polyvinyl alcohol molecules are covalently bonded to each other.
  • the amount of crosslinking can be determined by removing the binder from the nonwoven carrier, molecular analysis, for example by MALDI TOF, and comparison to the aqueous binder solution.
  • the starch can be modified starch or native (natural) starch.
  • Native starch is directly obtained from natural origin without any physical or chemical treatment.
  • the origin of the modified or native starch is natural.
  • the origin is plants, preferably vegetables.
  • the starch origin is tubers, such as potatoes, manioc, maranta, batata, grain such as wheat, corn (maize), rye, rice, barley, millet, oats, sorghum, fruits such as chestnuts, acorns, beans, peas, and other legumes, bananas, or plant pulp, e.g. sago palm.
  • the starch is corn starch, which is preferably modified.
  • the starch is not native starch.
  • the starch is modified starch. It is highly preferred that the starch is physically and/or chemically modified. Modified starch is obtainable by physical and/or chemical treatment of natural starch, typically in order to change its properties. According to the invention, it was found that modified starch can confer high stability to the nonwoven carriers. In contrast, it can be more difficult to provide a uniform binder with native starch in the absence of a crosslinker, which can result to lower stability of the nonwoven carrier.
  • the starch is chemically modified.
  • the term "chemically modified” refers to partly hydrolysed starch and starch with chemically modified side chains and/or functional groups.
  • the chemically modified starch can be alkaline-modified starch, bleached starch, oxidized starch, acetylated starch, hydroxypropylated starch, starch ether, hydroxyethyl starch, cationic starch or carboxymethylated starch.
  • the starch can be a dextrin, such as maltodextrin or cyclodextrin.
  • Dextrins are low-molecular-weight carbohydrates obtained by hydrolysis of starch, which are characterized by a dextrose equivalent between 3 to 20.
  • the starch is not dextrin. Since molecular weights of dextrins are relatively low, it can be preferred to use starch having a higher molecular weight for obtaining a highly stable product.
  • the chemically modified starch is partly hydrolysed starch.
  • Partly hydrolysed starch is characterized by lower polysaccharide chain lengths compared to the corresponding natural starch. It was found that partly hydrolysed starch can confer advantageous properties to the nonwoven carriers.
  • the starch may have an average molecular weight between 500 g/mol and 25,000 g/mol, especially between 2,500 g/mol and 20,000 g/mol, as determined by MALDI-TOF.
  • the starch does not comprise chemically modified side chains, i.e. hydroxyl groups which have been converted into other functional group by chemical reaction.
  • the starch comprises the hydroxyl groups as its starch precursor from natural origin. Native starches, physically modified and partly hydrolysed starches have a characteristic structure, in which all functional groups on the polymer backbone are hydroxyl groups. In these starches, the amount of other functional groups is negligible, for example less than 2%, less than 0.5% or less than 0.2% of the total hydroxyl groups and/or total of non-terminal hydroxyl groups. It was found that the stability of the nonwoven carrier at cold and hot temperature can be especially high when the starch hydroxyl groups are not chemically modified.
  • the average size of the starch particles in the aqueous binder dispersion is at least 0.1 ⁇ m, preferably at least 1 ⁇ m, more preferably at least 2 ⁇ m or at least 5 ⁇ m.
  • the average size can be in the range of 0.1 ⁇ m to 50 ⁇ m, preferably 1 ⁇ m to 50 ⁇ m, especially between 5 ⁇ m and 25 ⁇ m.
  • the average particle size can be determined by dynamic light scattering (DLS), for example according to ISO 22412:2017.
  • the term "starch particles” refers to the starch aggregates observed, which may also include some PVOH. It was found that such a relatively high particle size can correlate with high dimensional stability to the nonwoven carrier at hot temperature and higher mechanical resistance at cold temperature.
  • the starch may have a viscosity of 50 mPa*s to 800 mPa*s, preferably 150 mPa*s to 600 mPa*s, or more preferably 250 mPa*s to 600 mPa*s, as determined according to ISO 2555 at a concentration of 25 wt.% and 23°C.
  • the starch viscosity may be at least 50 mPa*s, preferably at least 150 mPa*s, or more preferably at least 250 mPa*s. It was found that the mechanical stability of the nonwoven carrier at cold and hot temperature can be improved significantly, if the viscosity of the starch is adjusted accordingly.
  • viscosity may be a more suitable parameter for selecting the type of starch in the binder composition than molecular weight, because viscosity depends not only from molecular weight, but also other properties such as the three dimensional structure of the starch molecules.
  • Starch is a polysaccharide, which consist essentially of amylose and/or amylopectin.
  • the ratio of amylose in the starch is between 10% and 50%, more preferably between 15% and 30% (dry weight, of total amount amylose and amylopectin). It was found that such a starch comprising a relatively high degree of amylopectin, such as corn starch, can confer high dimensional stability to the nonwoven carrier.
  • the starch is to-be-cooked type.
  • the starch is insoluble in water at 23°C and/or is not pre-gelatinized.
  • the starch is not soluble when 5 wt.% is added to cold water at and stirred for 2 minutes.
  • Starch is commercially available in soluble or insoluble form.
  • soluble starch such as pre-gelatinized starch is more convenient to use. Soluble starch can be dissolved easily in water at cold temperature.
  • native starch is rendered soluble by physical treatment, such as heating, mechanical shearing, drying and grinding.
  • Soluble starch can be provided in dry powder form, is instantaneously soluble in cold water and has thickening/gelling capability.
  • Pre-gelatinized soluble starch particles exhibit a lack of birefringence and retain little, if any, of the original native granule structure.
  • to be cooked type starch can provide high stability to the nonwoven carrier at cold and hot temperature. Since starch to be cooked cannot be simply dissolved in cold water, it should be subjected to a pretreatment before applying the binder of the present invention to the nonwoven.
  • the pre-treatment comprises heating and stirring, for example to at least 80°C, preferably at least 90°C. After cooling, the uniform starch dispersion obtained can be added to the binder.
  • the starch is physically modified.
  • Starch can be subjected to a physical treatment, for example under heat and/or mechanical shearing, which changes the physical structure.
  • a modification is considered physical, if no chemical reaction occurs, such as cleavage of polysaccharide chains. Physical modification can render the starch more homogeneous, which can improve the binder properties.
  • the starch is a partly hydrolyzed starch from natural origin, which preferably comprises 10% to 50% amylose (dry weight, of total of amylose and amylopectin), and which has an average molecular weight between 1000 and 2500 g/mol.
  • the average size of the starch particles in the starch dispersion and/or aqueous binder dispersion is at least 0.1 ⁇ m, preferably at least 1 ⁇ m, as determined by dynamic light scattering (DLS) and/or the viscosity of the starch is at least 150 mPa*s, preferably at least 250 mPa*s, determined according to ISO 2555 at a concentration of 25 wt.% at 23°C. It was found that stability of the nonwoven carrier at hot temperature can be especially high when using starch having such properties.
  • DLS dynamic light scattering
  • the starch is chemically modified starch, wherein functional groups are chemically modified. Hydroxyl groups of the starch substrate can be converted at least in part to different functional groups, for example by etherification, esterification, amidation or oxidation.
  • Chemically modified starches include starch esters, such as xanthogenates, acetates, phosphates, sulfates, nitrates; starch ethers, such as methyl- or ethyl- ethers, nonionic, anionic or cationic starch ethers, and oxidized starches such as carboxylic starch.
  • the starch comprises at least 90%, preferably at least 95%, more preferably at least 98%, or even at least 99% hydroxyl groups, which are not chemically modified. Most preferably, the starch does not comprise chemically modified hydroxyl groups. A high level of hydroxyl groups could be advantageous for binder stability, which could be mediated at least in part by hydrogen bonds.
  • the starch is partly oxidized. Preferably, the oxidation degree of the hydroxyl groups is low, for example between 0.1 and 10%, or between 0.5 and 5%. The partly oxidized starch could comprise more than 90% amylopectin. In an embodiment, the starch comprises about 99% amylopectin and has an oxidation degree of about 0.5 to 2%.
  • the aqueous binder comprises polyvinyl alcohol, which may comprise up to 5 mol.% of other monomer units.
  • Polyvinyl alcohol is a linear polymer consisting of monomeric building blocks with hydroxyl groups. It is assumed that starch has good compatibility with polyvinyl alcohol, also because both polymers comprise hydroxyl groups and are capable of forming intramolecular hydrogen bonds. It is a further advantage of polyvinyl alcohol that it is biodegradable, although relatively slow.
  • the viscosity of the polyvinyl alcohol is at least 25 mPa*s, more preferably at least 30 mPa*s.
  • the viscosity is in the range of 25 to 100 mPa*s, more preferably between 30 and 75 mPa*s. It was found that the mechanical properties of the nonwoven carrier are especially good at cold and hot temperature, if the viscosity of the polyvinyl alcohol is adjusted accordingly. If the viscosity is too low, the mechanical stability of the nonwoven can decrease. If the viscosity is too high, the workability may be lower and formation of an intimate mixture of starch and polyvinyl alcohol may be impaired.
  • viscosities of polyvinyl alcohol are determined according to ISO 2555 at a concentration of 4 wt.% at 23°C.
  • the polyvinyl alcohol has a saponification degree (degree of hydrolysis) of at least 90 mol%, more preferably of at least 95 mol% or at least 98 mol%.
  • the degree of saponification indicates which degree of acetate groups from a precursor polymer is converted into hydroxyl groups.
  • a high degree of saponification is advantageous, because the binder is more uniform and can thereby confer higher stability to the nonwoven carrier.
  • the polyvinyl alcohol may comprise up to 5 mol.% of other monomer units, preferably up to 2 mol.%. Such other monomer units are incorporated intentionally into the polymer chain during polymerization. Thus, the other monomers are part of the monomer mixture from which the polyvinyl alcohol or polyvinyl alcohol precursor, typically polyvinyl acetate, is polymerized. Thus, the monomer is not vinyl alcohol or residual vinyl acetate, which has not been hydrolysed when converting polyvinyl acetate to polyvinyl alcohol. Polyvinyl alcohol derivatives with other monomer units are known in the art and commercially available.
  • the polyvinyl alcohol does not comprise other monomer units and/or groups, except for residual acetate groups. This can be advantageous, because the polymer is homogenous and may confer high stability to the nonwoven carrier.
  • the polyvinyl alcohol has a polymerization degree of at least 600, more preferably at least 1000.
  • a relatively high polymerization degree which correlates to a relatively high polymer chain length, may provide good mechanical stability to the nonwoven carrier.
  • the starch and/or the polyvinyl alcohol are produced from natural raw materials.
  • Starch can be produced from natural origin and polyvinyl alcohol from natural building blocks, for example based on bioethanol. Accordingly, a sustainable binder can be produced, which is also biodegradable.
  • the nonwoven fibers are from recycled PET, for example from used PET bottles. Thereby, a sustainable nonwoven carrier can be provided.
  • the amount of polyvinyl alcohol in the binder is less than 30 wt.%, less than 25 wt.% or less than 20% wt.%. It is an advantage that the ratio of starch in the composition can be significantly higher than the ratio of polyvinyl alcohol, because commercially available starch is less expensive than polyvinyl alcohol. Since crosslinkers are excluded, the additives, if present, do not comprise crosslinkers.
  • the binder comprises only starch and polyvinyl alcohol as solid components.
  • a binder which consists completely or predominantly of starch and polyvinyl alcohol.
  • it is highly advantageous if such a binder consists of a low number of components. At first, it can be prepared easily and is inexpensive. Further, both polymer components are biodegradable. It is another advantage of a binder without crosslinker that no chemical reaction is carried out during or after impregnation of the nonwoven. In contrast, reactive binders used in the art require control of the chemical reaction. If the reaction is incomplete or excessive, the product can have undesired properties.
  • a simple binder composition can improve product uniformity, reproducibility and quality control.
  • Another advantage of binders without crosslinker is that excessive aqueous binder from the production process can be reused. In contrast, an aqueous binder which is crosslinked cannot be used again and has to be discarded.
  • the invention can reduce waste and provides a more sustainable nonwoven carrier.
  • binder without crosslinker can confer even better mechanical properties, including dimensional stability, to a substrate than a comparable binder with crosslinker. For example, it was found that a binder without crosslinker can have lower hot deformation, which is especially important for the bituminization process. This was unexpected, because it is generally assumed in the art that crosslinkers increase the dimensional stability by formation of a polymer network.
  • the binder does not comprise structural polymers different from starch and polyvinyl alcohol.
  • the binder does not comprise an additional structural polymer which is commonly used in nonwoven binders, such as acrylic polymers, SBR, polyurethane, polyamides, polyester, or copolymers thereof, or other natural polymers, such as proteins, gelatin or alginate.
  • the binder does not comprise other polymers at all, and thus also not as functional additives. Since nonwoven carriers with high mechanical stability can be obtained only with starch and polyvinyl alcohol as structural polymers, it is not necessary to include additional structural polymers. This is also advantageous for ease of the production process, quality control and cost reasons.
  • the binder may comprise additives.
  • the total amount of additives is relatively low. Preferably, it is less than 15 wt.%, more preferably less than 10 wt.%, or less than 5 wt.%, all wt.% relating to total binder dry weight. It is especially preferred that the amount of additives is less than 2 wt%, less than 1 wt.%, or that no additives are present at all. Accordingly, it is preferred that the binder consists fully or substantially of starch and polyvinyl alcohol as the solid components.
  • the additives can be functional additives, which confer a desired property to the binder.
  • Such functional additives are known in the art and include UV stabilizers, adhesion promoters, colorants and processing aids.
  • the additives are not polymers.
  • only additives are additives in the aqueous binder solution, which do not become part of the consolidated binder on the nonwoven carrier, such as salts and buffer substances.
  • the total amount of additives is low.
  • a very simple binder composition based essentially or solely on starch and polyvinyl alcohol can confer highly advantageous properties to the nonwoven carrier.
  • the binder solution can be very simple, which is advantageous for large scale production and processing.
  • a low amount of additives can also be advantageous for environmental reasons.
  • a binder without additives or with only low amount of additives can be recycled more efficiently.
  • Such a binder can be recycled from the binder bath and/or can be stripped from the nonwoven carrier and recycled.
  • crosslinked binders or binders comprising high levels of synthetic additives cannot be recycled efficiently.
  • the binder does not comprise a filler. This can be advantageous, because fillers are often applied in relatively high amounts and can significantly impair the stability of the polymer matrix formed from starch and polyvinyl alcohol. Especially since the binder is not crosslinked, nonwoven carrier stability could be decreased by a filler.
  • the binder does not comprise a surfactant, detergent, wetting agent, emulsifier, protective colloid and/or dispersant, preferably none of these additives.
  • the binder does not comprise an additive, which is an amphipathic molecule or a non-ionic surfactant. More preferably, the binder does not comprise a hydrocarbon containing 8 to 18 carbon atoms, which is attached to a polar or ionic portion, and/or an ethoxylated surfactant, such as an ethoxylated sorbitan ester.
  • the binder may comprise unavoidable impurities, such as salts, which have no relevant impact on the consolidated binder structure.
  • the polyvinyl alcohol is provided to the binder in form of an aqueous solution.
  • the polyvinyl alcohol it is not provided in the form of a dispersion. In this embodiment, it is provided without additives required for preparing such a dispersion, such as emulsifiers or protective colloids.
  • the binder does not comprise an additive which comprises hydrophilic groups, such as hydroxyl groups, carboxyl groups, amine groups, aldehyde or keto groups and/or ionic groups. More preferably, the binder does no comprise an additive which comprises hydroxyl groups.
  • hydrophilic groups may affect hydrogen bonds in the binder structure and thus reduce the stability of the nonwoven carrier.
  • the binder comprises
  • the binder comprises 50 to 95 wt.%, preferably 72 to 95 wt.% starch, 5 to 50 wt.%, preferably 5 to 28% wt.% polyvinyl alcohol, and 0 to 15 wt.% preferably 0 to 2 wt.% additives, wherein the total of all percentages is 100 wt.% (dry weight). It was found that binder compositions comprising such relatively high amounts of starch can confer high dimensional stability to the nonwoven carrier.
  • the binder comprises 5 to 69 wt.% starch, 31 to 95 wt.% polyvinyl alcohol and 0 to 15 wt.%, preferably 0 to 2 wt.% additives, wherein the total of all percentages is 100 wt.% (dry weight). It was found that binder compositions comprising such relatively high amounts of polyvinyl alcohol can confer high mechanical resistance to the nonwoven carrier.
  • the binder comprises 30 to 70 wt.% starch, 30 to 70 wt.% polyvinyl alcohol and 0 to 15 wt.%, preferably 0 to 2 wt.% additives, wherein the total of all percentages is 100 wt.% (dry weight). It was found that binder compositions comprising relatively similar amounts of polyvinyl alcohol and starch can confer high dimensional stability to the nonwoven carrier, especially at hot temperature.
  • the binder comprises 60 to 90 wt.% starch, 10 to 40 wt.% polyvinyl alcohol and 0 to 5 wt.% additives, wherein the total is 100 wt.% (dry weight).
  • the binder comprises 70 to 90 wt.% starch, especially 72 to 90 wt.% starch, 10 to 30 wt.% polyvinyl alcohol and 0 to 5 wt.% additives, wherein the total is 100 wt.% (dry weight).
  • the nonwoven can be spunlaid, spunlace, melt-spun or staple fiber nonwoven.
  • fiber includes staple fibers and filaments. Staple fibers have a defined length, whereas filaments can be "endless" filaments. Staple fibers can be processed and laid by conventional means, such as carding. Preferably, the length of staple fibers is between 20 mm to 200 mm, more preferably between 60 mm to 100 mm.
  • the nonwoven comprises organic polymer fibers.
  • the organic fibers are synthetic fibers.
  • the nonwoven consists of organic polymer fibers, preferably synthetic fibers.
  • the nonwoven does not comprise nonwoven inorganic and/or mineral fibers, such as nonwoven glass fibers.
  • Nonwovens from organic and polymer fibers are advantageous, because they are lighter than glass fiber and the binder can provide high stability to such nonwovens.
  • the organic polymer is polyester.
  • the polyester can be selected from polyethylene terephthalate, polybutylene terephthalate and polyester copolymers. It is preferred that the polyester is polyethylene terephthalate (PET).
  • the nonwoven fibers are only polyester fibers.
  • the nonwoven may comprise monocomponent and/or multicomponent fibers, such as bicomponent fibers.
  • the nonwoven may optionally comprise additional reinforcing inorganic fibers. If the nonwoven consists of organic polymer fibers, preferably synthetic fibers, preferably polyester fibers, especially PET fibers, it may optionally comprise a reinforcement, which is not made from nonwoven fibers.
  • the nonwoven fibers are a mixture of organic fibers and inorganic fibers.
  • the nonwoven may comprise a mixture of polyester fibers and other nonwoven fibers, for example less than 50%, less than 20% or less than 10% by weight of all fibers.
  • the nonwoven may comprise other fibers which are relatively stable at hot temperature, such as natural fibers or inorganic nonwoven fibers.
  • the linear density of the nonwoven fibers is from 0.5 to 20 dtex, more preferably from 1 to 10 dtex, especially in the range of 2 to 6 dtex.
  • Nonwovens of such fibers can provide strength and flexibility to bituminous membranes.
  • the diameter of the nonwoven fibers is in the range of 5 ⁇ m to 50 ⁇ m, preferably 10 to 30 ⁇ m.
  • the fiber titer is at least 2.5 dtex.
  • the nonwoven comprises a reinforcement.
  • the reinforcement relates to any fibrous structure, i.e. fibers, filaments, yarns, wires or other elongated structures. Reinforcing fibers are different from the nonwoven fibers, because they are not randomly laid into the fleece (nonwoven precursor) in the nonwoven production process, as the other nonwoven fibers. In contrast, the reinforcing fibers are incorporated in a different manner during or after the nonwoven production process.
  • a reinforcement is directional, i.e. it especially reinforces the nonwoven in a specific direction.
  • the reinforcement can be linear yarns or a discrete layer, such as a scrim.
  • the reinforcing fibers are not part of the fiber raw material, which is laid to form the nonwoven or fleece precursor.
  • the reinforcement is embedded in interior of the nonwoven carrier.
  • the reinforcement can be multi- and/or monofilaments.
  • the reinforcement can be from aramids, preferably so-called high-module aramids, carbon, glass, glass rovings, mineral fibers (basalt), high-strength polyester monofilaments or multifilaments, high-strength polyamide monofilaments or multifilaments, as well as yarns, such as hybrid multifilament yarns (yarns containing reinforcing filaments and lower melting binder fibers), or wires (monofilaments) made of metals or metallic alloys.
  • the reinforcement is made from inorganic fiber, such as glass fibers or glass fiber yarns.
  • the reinforcement is yarns, preferably glass fiber yarns.
  • the amount of glass fiber yarns in the nonwoven carrier is 2 to 20 wt.%, preferably 5 to 15 wt.%. Such levels are normally sufficient for increasing the strength without impairing the nonwoven properties.
  • the yarns are aligned to each other, preferably in parallel. Glass fiber yarns can increase the mechanical strength of the nonwoven carrier.
  • the nonwoven carrier consists of the nonwoven, which is consolidated with the binder and which optionally comprises the reinforcement.
  • the nonwoven carrier is a composite substrate which comprises an additional, separate layer of inorganic fibers.
  • the additional layer can be a nonwoven, a woven, a net or scrim, or a layer of fibers and/or yarns.
  • the nonwoven does not comprise an additional layer.
  • the base weight of the nonwoven, before impregnation with the binder is from 50 to 500 g/m 2 , more preferably from 100 to 300 g/m 2 , especially from 150 to 250 g/m 2 .
  • Such base weights are especially suitable for bituminous membranes.
  • the nonwoven can be pre-consolidated before impregnation with the binder, especially mechanically, for example by hydroentangling or pre-needling.
  • the load of binder (add-on) is from 1% to 50 wt.%, preferably from 5% to 40 wt.%, more preferably from 10% to 30 wt.%, of the nonwoven (dry weight without binder).
  • water is the only solvent in the aqueous binder.
  • the thickness of the nonwoven carrier is between 0,25 mm and 6 mm, more preferably between 0,5 mm and 4 mm, and especially between 0.8 mm and 2 mm, as determined according to ISO 9073-2, 1997, section 5.1, normal nonwovens.
  • the nonwoven carrier has a hot tensile deformation at 180°C and 120 N of less than 1.8 %, more preferably less than 1.5%, preferably determined at a base weight of 180 g/m 2 . Due to this high dimensional stability, the nonwoven carrier can be advantageously used for producing bituminous membranes with standard machinery. Further, the high stability at hot temperature indicates that the bituminous membranes remain stable for long time periods in building and roofing applications. Even in moderate climate, roof temperatures can raise up to 100°C, for example when the sun shines directly on metal parts of a roof. In hot geographical regions and for specific applications, temperatures may raise even higher. Therefore, high dimensional stability at hot temperature is also advantageous for building and roofing applications.
  • the nonwoven carrier has a maximum glass tensile strength at 180°C of at least 150 N/50 mm, more preferably at least 200 N/50 mm, especially when comprising reinforcing glass fiber yarns.
  • the maximum glass tensile strength is correlated to dimensional stability. It defines the threshold, at which the nonwoven collapses because of the breaking of the reinforcement, typically the glass fibers. This is defined by a defined peak in the tensile strength vs. elongation diagram. High maximum glass hot tensile strength is desirable, because it indicates that the material can withstand higher tension and pulling forces at 180°C on the bitumen production line, especially at higher speed.
  • the nonwoven carrier When a higher force than the maximum glass tensile strength is exerted on the nonwoven carrier, it loses its shape (collapses) and cannot be processed any more.
  • the high maximum glass tensile strength indicates that the nonwoven carrier is suitable for efficiently producing high quality bituminous membranes in an industrial process.
  • bituminous membranes are used for building applications and are subjected to mechanical forces, for example bent to covering irregular building parts, nailed or subjected to stress and strain.
  • mechanical forces for example bent to covering irregular building parts, nailed or subjected to stress and strain.
  • the material is mechanically stable at low temperature to avoid punctures, ruptures and the like.
  • the total maximum tensile strength of the nonwoven carrier at room temperature is at least 600 N/5 cm, more preferably at least 625 N/5 cm, determined according to ISO 9073-3.
  • the peak tenacity at room temperature is at least 0.28 daN/5 cm/g/m 2 .
  • the elongation at break is at least 40%, determined according to ISO 9073-3.
  • the above parameters regarding mechanical stability are determined in machine direction, preferably in machine direction and cross-direction.
  • the properties are determined for a base weight of 180 g/m 2 spunbond with additional 20% binder add-on.
  • the air permeability of the nonwoven carrier is 250 ⁇ 2500 l/m 2 , as determined by ISO 9037-15.
  • Subject of the invention is also a method for producing the nonwoven carrier of the invention, comprising the steps of
  • the solidification may be achieved by drying. Since no crosslinker is present, it is not necessary to induce, monitor and/or terminate a crosslinking reaction.
  • Subject of the invention is also a bituminous membrane, which comprising the nonwoven carrier as defined above.
  • Subject of the invention is also a method for producing a bituminous membrane, comprising the steps of
  • the impregnation of the nonwoven carrier with bitumen is performed in a bath comprising molten bitumen in which the nonwoven carrier is immersed.
  • the nonwoven carrier with the bitumen attached to it is subsequently removed from the bath and dried.
  • the method is carried out as an automated process, preferably a continuous process, in which "endless" rolls of the nonwoven carrier are fed into the process and rolls of the bituminous membrane are obtained as the final product.
  • the nonwoven carrier and the bituminous membranes should be flexible. Accordingly, the nonwoven carriers and/or bituminous membranes are rollable. In contrast, the nonwoven carriers and/or bituminous membranes are not rigid.
  • the bituminous membrane is obtainable in a conventional process, in which nonwoven carrier, which is bonded with the binder, is impregnated with molten bitumen in a bath.
  • the nonwoven carrier is provided in roll form to a production line where it is unrolled and directed through the hot bitumen bath by standard machinery, led out of the bath, followed by cooling and solidification of the bitumen adhered to the carrier. After solidification, the bituminous membrane is rolled up, such that it can be stored, shipped and provided to the building site.
  • the bituminous membrane can be used in building and roofing applications.
  • the bituminous membrane is unrolled at the building site, optionally cut to a desired shape, subjected to temporary heat by flaming in order to soften at least a bituminous surface, laid on the application site, and optionally deformed and thus aligned with the surface of the application site. Subsequently, additional layers, such as insulating layers or tiles, are laid over the bituminous membranes.
  • Methods for applying bituminous membranes in building applications are standardized in DIN V 20000-201.
  • the proportion of bitumen to the nonwoven carrier is preferably 60 to 97% by weight to 3 to 40% by weight.
  • Subject of the invention is also a roof, building material or building, which comprises a bituminous membrane of the invention.
  • the bituminous membrane can be used as a sarking membrane, sealing membrane or waterproofing sheet.
  • the nonwoven carrier can also be used for other applications, such as a reinforcing insert, optionally in combination with further textile fabrics, for sarking membranes, as a textile backing or textile reinforcement, in flooring, in particular fitted carpets and PVC flooring, as a facer in wall coatings for the interior and exterior of buildings, or in decorative surfaces.
  • a reinforcing insert optionally in combination with further textile fabrics, for sarking membranes, as a textile backing or textile reinforcement, in flooring, in particular fitted carpets and PVC flooring, as a facer in wall coatings for the interior and exterior of buildings, or in decorative surfaces.
  • the nonwoven carrier, bituminous membranes, uses and methods of the invention solve the problem underlying the invention.
  • a nonwoven carrier for producing bituminous membranes is provided which is easily available, easy to produce, inexpensive and has excellent mechanical properties.
  • the nonwoven carriers have high mechanical resistance and especially dimensional stability at room temperature and also at hot temperature, which can be even better than for comparable binders which comprise a crosslinker. This was unexpected, because the stability of many thermoplastic polymer binders deteriorates at hot temperature.
  • the nonwoven carriers are suitable for producing high quality bituminous membranes in an efficient high-speed automated process.
  • the high dimensional stability at hot temperature and also the very good mechanical properties at room temperature render the nonwoven carriers especially suitable for building and roofing applications.
  • the invention also provides guidance how to provide specific crosslinker-free starch/polyvinyl alcohol binders having especially advantageous properties. It is a further advantage that the binder is biodegradable and formaldehyde-free, and can be based on natural sources, such that a sustainable product can be provided.
  • RPET bottle recycled polyester
  • the average particle size of solutions were determined by dynamic light scattering (DLS) using a 90 Plus Particle Size Analyzer (Brookhaven Instruments Corporation, US) at 25.0 ⁇ 0.1°C.
  • the autocorrelation function was measured at 90°, while the laser beam was operating at 658 nm.
  • the mean size and standard deviation ( ⁇ S.D.) were directly obtained from the instrument fitting data by the inverse "Laplace transformation” method and by Contin. All analyses were done in triplicate and expressed as mean ⁇ standard deviation. The S.D. was found to be 10 nm.
  • Starch A is constituted by 99% of amylopectin, which is partly oxidized at low degree.
  • Starch B and starch C comprise about 20 to 25% (dry weight) amylose and are partly hydrolyzed to decrease the M w .
  • Starch D comprises about 20 to 25% (dry weight) amylose, is pre-gelatinized and water soluble. It has been pre-treated by the supplier by cooking and water removal, which renders the starch water soluble such that no cooking step is required before use.
  • Polyvinyl alcohols were used in various grades, which are characterized by different molecular weights. The higher the molecular weight, the higher is the viscosity of the polymer in aqueous solution. All grades are characterized by 98% of hydrolysis (of acetate groups). The pH of PVOH aqueous solutions is 6, as determined according to ISO 976. Viscosities were determined according to ISO 2555 at 23°C with 4% (w/w) aqueous solution and are summarized in table 2.
  • Table 2 Viscosity of PVOH grades Type PVOH 498 PVOH 698 PVOH 1098 PVOH 2098 Viscosity (mPa*s) 22 26 32 50 Degree of hydrolysis (saponification) 98 - 98.8 98 - 98.8 98 - 98.8 98 - 98.8 98 - 98.8
  • Binders were prepared by mixing the starch dispersion (20% solid content) and PVOH solution (10% solid content).
  • the starch dispersion 500 g - 20% solid content
  • the starch dispersion was heated to 90°C and left at this temperature for 15 minutes keeping the system under mechanical stirring. Finally, the system was cooled to 60 °C.
  • the PVOH water solution (10% solid content) was prepared by introducing 60 g PVOH and 540 g water into a three-necked flask equipped with mechanical stirrer. Then the mixture was heated up to 95 °C and kept at this temperature for at least 40 minutes. Afterwards, the temperature was cooled down to 60 °C.
  • 500 g binder formulation with a solid content of 12.5% was prepared by mixing 219 g of the starch dispersion, 187 g of the PVOH solution and 94 g water. 1 g wetting agent was added if indicated. Finally, the mixture was stirred at 60 °C for 10 minutes and used for nonwoven impregnation.
  • the nonwoven substrate was a spunbond nonwoven fabric from recycled polyethylene terephthalate (PET) fibers (4,4 dtex; reinforced with glass yarns 68 tex, base weight 180 g/m 2 , pre-consolidated by needle-punching and thermosetting).
  • PET polyethylene terephthalate
  • the nonwoven substrates were impregnated with the binder formulation using Mathis Foulard settings (speed: 2.5 m/min; cylinder pressure: 3.5 bar). Specimens (33 cm x 44 cm) of the nonwoven were impregnated in a bath containing the binder formulation. A final add-on of 20% on a dry basis following oven drying was adjusted.
  • the binder applied on nonwoven fabric samples was oven dried at 200°C for 3 minutes and 45 seconds.
  • a set of 15 specimens was obtained from the samples produced, which were subjected to mechanical tensile tests with a dynamometer (Instron).
  • a dynamometer Instron
  • 5 specimens of 50 mm x 300 mm were used in MD and in CD, respectively.
  • hot temperature (180°C) 5 specimens of 50 mm x 180 mm were used.
  • the hot tensile deformation is the elongation at a specific tensile strength. The lower the value, the more dimensionally stable is the material, and thus the better is the product.
  • the tensile stress test at 180°C was performed based on US2008/0214716 under modified conditions.
  • the clamping length is 80 mm and the take-off speed is 100 mm/min.
  • the elongation of the nonwoven was determined in machine direction (MD) with increasing tensile force at loads of 80 N, 100 N and 120 N, whereby the maximum tensile strength was also determined.
  • Example 1 to 5 Impact of different types of corn starches on mechanical properties
  • nonwovens were consolidated with binders comprising different types of starch and the same PVOH (grade 1098).
  • the products were thin porous sheets, which were flexible and rollable.
  • the binder compositions and results are summarized in table 3.
  • a conventional binder for nonwoven carriers for bituminous roofing membranes was used, which consists of 70% acrylic/melamine/formaldehyde binder (63% acrylic resin, trademark Acronal S888S, BASF, DE, 7% melamine-formaldehyde crosslinker, trademark Saduren 163, BASF, DE) and 30% starch C, all percentages dry wt.%).
  • the starch/PVOH binder is formaldehyde free, which is advantageous for safety and environmental reasons. Further, the starch/PVOH binder is significantly less costly, which is relevant for industrial products which are produced at large scale. Thirdly, the starch/PVOH binder can be produced without crosslinker and crosslinking catalyst. Thus, the composition and production process is much simpler than a crosslinking composition, in which reactive components have to be adapted to each other and reaction control is required.
  • the results provide evidence that the starch/PVOH binder, although not crosslinked, can confer improved mechanical properties to the product, which render it highly suitable as a carrier for bituminous membranes.
  • the nonwoven carrier is dimensionally stable at 180°C.
  • the results show that the starch/PVOH binder consolidated nonwovens can have a much lower deformation and higher maximum glass tensile strength than the comparative standard nonwoven with crosslinked melamine acrylic binder. This represents a great advantage when the nonwoven carrier is impregnated with bitumen in an industrial process.
  • the low hot tensile deformation indicates that the nonwoven carrier can maintain its shape when being pulled through the production line under significant tensile force and loaded with high amounts of bitumen.
  • a high maximum glass tensile strength suggests that the nonwoven carrier can withstand a comparably high maximum force in the bitumen impregnation line.
  • bituminous membranes can be produced from inventive nonwoven carriers at higher speed and productivity, but also with higher product quality, i. e. less failures, product irregularities and damages.
  • Especially high dimensional stability at hot temperature was observed in example 3 with starch B. Only example 4 provides a level of deformation at hot temperature, which is comparable to the standard binder. However, this is still a good and unexpected result for a binder without crosslinker.
  • the results indicate that the mechanical properties at low temperature are advantageous.
  • the cold tenacity of the starch/PVOH consolidated nonwovens was comparable to comparative example 1 with the standard binder.
  • the binders in example 4 and 5 were not able to provide the same tensile strength and tenacity as the conventional binder, but the results are still good and also unexpected for a natural binder which does not comprise a crosslinker.
  • the nonwoven carriers can also be stretched and elongated, as required for building and roofing applications.
  • the results at cold temperature demonstrate that the nonwoven carriers also confer good mechanical properties to bituminous membranes in the final building or roofing application.
  • starch aggregates in starch only dispersions and in starch/PVOH binder dispersions was determined by DLS. As seen in table 4, the size of starch aggregates present in the dispersion was different for different aqueous starch dispersions and aqueous starch/PVOH dispersions. Specifically, starch B and starch B /PVOH dispersion are characterized by relatively large particles. Further, the average particle size of starch B/PVOH dispersion is significantly higher than in the dispersion with starch B only. In contrast, the dispersions of starch A or C mixed with PVOH show similar aggregates dimension as starch A or C only.
  • starch A and starch B displayed the best values, comparable or even slightly better than the melamine/acrylic binder standard (total tenacity and tensile strength).
  • starch B provides the lowest MD deformation at 120 N.
  • the rheological characterization demonstrated the highest G* value for the mixture starch B/PVOH (data not shown), which is an indication of a stronger bio-polymer network for this binder.
  • the size of aggregates measured by DLS was the highest compared to the others binders. The largest aggregates could lead to a better adhesion to the fibers and better thermo-mechanical properties.
  • the pre-gelatinized starch used in example 5 is water soluble and can be instantaneously solubilized in cold water. The results demonstrate that these modifications of starch structure may cause a decrease in binding properties compared to the to-be-cooked starch.
  • the aqueous binder was heated to 200°C for 3 minutes and the size of the binder molecules was analyzed by MALDI-TOF. It was observed that the size of binder molecules is not affected by the heating treatment. Thus, it can thus be excluded that an esterification reaction between starch and PVOH occurs. This confirms that the good mechanical properties of the binder consolidated nonwovens of examples 2 to 5 are obtained although the binders are not crosslinked.
  • the viscosity of polyvinyl alcohol having linear polymer chains is directly related to the average molecular weight.
  • PVOH 498 and 698 are characterized by low molecular weight and viscosity.
  • the hot tensile deformations for PVOH 698, 1098 and 2098 are lower than for the conventional binder.
  • the hot glass tensile strength is always significantly higher than with the standard binder.
  • the products are highly suitable as nonwoven carriers for producing bituminous membranes. Overall, the results show that the binding properties can be improved, if the PVOH has a higher molecular weight.
  • starch / PVOH binder compositions were prepared with additional wetting agents, which are used in the art as additives for improving workability of the binder and properties of nonwovens.
  • a silicon free non-ionic ethoxylated surfactant was used (example 14), which is characterized by low tendency to create foam and high efficiency in decreasing the surface tension of water based solution and dispersion. Adding 0.2% (v/v %) of this substance to an aqueous dispersion allows decreasing the surface tension to below 30 mN/m.
  • a polyethoxylated monoester of 3,6-sorbitan (example 16) was also used, which is hydrophilic and soluble or dispersible in water and dilute solutions of electrolytes. The solubility in aqueous solution increases with the degree of ethoxylation.
  • the binders with the wetting agents were compared to inventive binders without the additive, respectively (examples 13, 15).
  • MD and CD cold tensile strength
  • Example 14 cold glass tensile strength
  • ethoxylated wetting agent a decrease in cold tensile properties was also observed (example 16).
  • both wetting agents also affected hot tensile deformation in an undesired manner, since higher deformation was observed compared to the binders without the additive, respectively.
  • the high tensile strength of a starch/PVOH binder could be due to the high number of hydrogen bond between the molecules and/or the high compatibility between both polymers.
  • surfactants have the tendency to migrate at the interfaces, causing a decreasing in adhesion force between the binder and the surface of the PET fibers. This could be confirmed by electron microscopy images of the products.
  • the wetting agent has an adverse effect on binder microstructure, since an undesired phase separation in the binder film was observed.
  • a homogenous binder film was observed in comparative example 15. This could explain the lower tensile strength of the nonwoven samples in examples 14 and 16.
  • standard additives such as surfactants can significantly reduce the stability of the nonwoven carriers.
  • nonwovens were consolidated with binders as described in example 2 above, which additionally comprised a crosslinker.
  • Three specific types of crosslinker were selected which are preferred in the art, such as EP 3 299 514 A1 , for crosslinking starch based binders for nonwoven substrates (see table 6).
  • the binders were prepared as described above for example 2, whereby 5% (solid content) of starch B was replaced by 5% (solid content) crosslinker, respectively.
  • Nonwovens were impregnated as described above.
  • the products were thin porous sheets, which were flexible and rollable.
  • the binder compositions and results are summarized in table 7.
  • Comparative example 17 is the conventional binder for nonwoven carriers for bituminous roofing membranes, which consists of 70% acrylic/melamine/formaldehyde binder (63% acrylic resin, 7% melamine-formaldehyde crosslinker 1) and 30% starch C, all percentages dry wt.%).
  • the results were compared with those obtained for respective binder without crosslinker and melamine/acrylic standard binder.
  • Example 17 to 21 Example 17 (comp.) 18 19 (comp) 20 (comp) 21 (comp) starch 30% starch C 70% starch B 65% starch B 65% starch B 65% starch B PVOH - 30% PVOH 1098 30% PVOH 1098 30% PVOH 1098 30% PVOH 1098 crosslinker melamine FA + acrylic resin - 5% crosslinker 1 5% crosslinker 2 5% crosslinker 3 starch viscosity (mPa*s) 100 370 370 100 200 start nonwoven grammage (g/sqm) 182 181 181 180 180 binder add-on (%) 20 20 20 20 20 cold tensile tests MD max tensile strength (N/50mm) 660 650 665 616 587 MD elongation (%) 22 29 17 28 22 MD tenacity (daN/gsqm/50mm) 0,30 0,30 0,30 0,28 0,27 CD max tensile strength (N/50mm) 450 438 440 423 358 CD elong
  • PVOH can be very effecting in aggregating starch particles that are responsible for the very good hot and cold tensile performances. Without being bound to theory, it is possible that the crosslinker interferes with the aggregation phenomena, which leads to a decline of tensile properties.
  • Nonwoven carriers were produced at large scale with binders comprising starch B and PVOH (98% hydrolysis degree, pH 6, 32 mPa*s viscosity at 23°C, determined according to DIN EN ISO 2555 with 4% (w/w) aqueous solution).
  • Binders were prepared at large scale by mixing the starch dispersion (25% solid content) and PVOH solution (15% solid content).
  • the starch dispersion 500 Kg - 25% solid content
  • the starch dispersion was heated to 90°C - 100 °C through a jet cooker system. Finally, the system was cooled to 60 °C.
  • the PVOH water solution (15% solid content) was prepared by introducing 90 Kg PVOH and 510 kg water into a heated tank equipped with a mechanical stirrer. Then the mixture was heated up to 95 °C and kept at this temperature for at least 40 minutes. Afterwards, the temperature was cooled down to 60 °C.
  • Binder compositions examples 23 to 25 Example Binder Recipe Starch quantity [kg] PVOH quantity [kg] Water [kg] 23 69% Starch - 31% PVOH 210 150 140 24 50% Starch - 50% PVOH 150 250 100 25 33% Starch - 66% PVOH 99 330 71
  • the starch/PVOH binder can confer mechanical properties to the product, which render it highly suitable as a carrier for bituminous membranes.
  • the binder does not comprise crosslinker
  • the inventive nonwoven carriers have improved properties compared to the standard with conventional crosslinked acrylic/melamine formaldehyde binder.
  • Especially binder formulations comprising at least 50% PVOH can have advantageous mechanical properties.
  • the nonwoven carrier is mechanically stable at 180°C.
  • the results show that the starch/PVOH binder consolidated nonwovens have a lower deformation and significantly higher glass tensile strength than the standard. This represents a great advantage at the customer line, because lower hot tensile deformation means lower deformation during bitumen impregnation and therefore higher speed and productivity, but also less failures, product irregularities and damages.
  • Especially low deformation at hot temperature was observed in examples 24 and 25 with at least 50% of PVOH.
  • starch/PVOH binder formulation can display especially better values than standard binder, especially when the quantity of PVOH is higher than 30% wt.

Claims (15)

  1. Verwendung eines Vliesstoffträgers als Substrat zur Herstellung von bituminösen Membranen, wobei der Vliesstoff organische Polymerfasern umfasst und mit einem wässrigen Bindemittel verfestigt ist, wobei das Bindemittel umfasst
    (a) Stärke, und
    (b) Polyvinylalkohol, der bis zu 5 Mol-% anderer Monomereinheiten umfassen kann, wobei
    (c) das Bindemittel keinen Vernetzer umfasst, und
    (d) das Bindemittel keinen Füllstoff umfasst.
  2. Verwendung nach Anspruch 1, wobei die Stärke physikalisch und/oder chemisch modifizierte Stärke natürlichen Ursprungs ist.
  3. Verwendung nach mindestens einem der vorhergehenden Ansprüche, wobei die Stärke teilweise hydrolysiert ist.
  4. Verwendung nach mindestens einem der vorhergehenden Ansprüche, wobei das Bindemittel weniger als 2% Zusatzstoffe, vorzugsweise 0% Zusatzstoffe umfasst (bezogen auf das Gesamttrockengewicht).
  5. Verwendung nach mindestens einem der vorhergehenden Ansprüche, wobei die durchschnittliche Größe der Stärkepartikel in der wässrigen Bindemitteldispersion mindestens 0,1 µm beträgt, wie durch dynamische Lichtstreuung (DLS) bestimmt, und/oder wobei die Viskosität der Stärke mindestens 150 mPa*s beträgt, bestimmt nach ISO 2555 bei einer Konzentration von 25 Gew.-% bei 23°C.
  6. Verwendung nach mindestens einem der vorhergehenden Ansprüche, wobei die Stärke bei 23°C wasserunlöslich und/oder nicht vorgelatiniert ist, und/oder wobei die Stärke 10% bis 50% Amylose umfasst (Trockengewicht, von Amylose und Amylopektin insgesamt).
  7. Verwendung nach mindestens einem der vorhergehenden Ansprüche, wobei die Stärke und der Polyvinylalkohol im Wesentlichen nicht vernetzt sind, und/oder wobei die Viskosität des Polyvinylalkohols mindestens 25 mPa*s beträgt, bestimmt nach DIN EN ISO 2555 bei einer Konzentration von 4 Gew.-% bei 23°C.
  8. Verwendung nach mindestens einem der vorhergehenden Ansprüche, wobei das Bindemittel 5 bis 95 Gew.-% Stärke, 5 bis 95 Gew.-% Polyvinylalkohol und 0 bis 15 Gew.-% Zusatzstoffe umfasst, wobei sich alle Prozentangaben auf das Trockengewicht beziehen und die Summe aller Prozentangaben 100 Gew.-% beträgt.
  9. Verwendung nach mindestens einem der vorhergehenden Ansprüche, wobei das Bindemittel keine von Stärke und Polyvinylalkohol verschiedenen Strukturpolymere umfasst, und/oder wobei das Bindemittel keinen Zusatzstoff umfasst, der Hydroxygruppen umfasst.
  10. Verwendung nach mindestens einem der vorhergehenden Ansprüche, wobei der Vliesstoff aus organischen Polymerfasern, vorzugsweise Polyesterfasern, besteht, und/oder wobei der Vliesstoff eine Verstärkung, wie anorganische Fasergarne, umfasst.
  11. Vliesstoffträger für bituminöse Membranen, wobei der Vliesstoff organische Polymerfasern umfasst und mit einem wässrigen Bindemittel verfestigt ist, wobei das Bindemittel umfasst
    (a) Stärke, und
    (b) Polyvinylalkohol, der bis zu 5 Mol-% anderer Monomereinheiten enthalten kann, wobei
    (c) das Bindemittel keinen Vernetzer umfasst, und
    (d) das Bindemittel keinen Füllstoff umfasst,
    wobei die durchschnittliche Größe der Stärkepartikel in der wässrigen Bindemitteldispersion mindestens 0,1 µm beträgt, wie bestimmt durch dynamische Lichtstreuung (DLS), und/oder wobei die Viskosität der Stärke mindestens 150 mPa*s beträgt, bestimmt nach ISO 2555 bei einer Konzentration von 25 Gew.-% bei 23°C.
  12. Verfahren zur Herstellung eines Vliesstoffträgers nach Anspruch 11, umfassend die Schritte
    (a) Bereitstellen eines Vliesstoffs,
    (b) Imprägnieren des Vliesstoffes mit dem wässrigen Bindemittel, und
    (c) Trocknen und Verfestigen des Bindemittels, um den Vliesstoffträger zu erhalten.
  13. Verfahren zur Herstellung einer bituminösen Membran, umfassend die Schritte
    (A) Bereitstellen eines Vliesstoffträgers wie in einem der Ansprüche 1 bis 11 definiert, und
    (B) Imprägnieren des Vliesstoffträgers mit Bitumen.
  14. Bituminöse Membran, umfassend einen Vliesstoffträger wie in mindestens einem der Ansprüche 1 bis 11 definiert.
  15. Dach, Baumaterial oder Gebäude umfassend eine bituminöse Membran nach Anspruch 14.
EP21713059.0A 2020-03-30 2021-03-25 Bituminöse membranen mit biologisch abbaubarem bindemittel Active EP3966379B1 (de)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
EP20166708 2020-03-30
EP20170583 2020-04-21
EP20211895 2020-12-04
PCT/EP2021/057696 WO2021197999A1 (en) 2020-03-30 2021-03-25 Bituminous membranes with biodegradable binder

Publications (2)

Publication Number Publication Date
EP3966379A1 EP3966379A1 (de) 2022-03-16
EP3966379B1 true EP3966379B1 (de) 2022-10-26

Family

ID=75108349

Family Applications (1)

Application Number Title Priority Date Filing Date
EP21713059.0A Active EP3966379B1 (de) 2020-03-30 2021-03-25 Bituminöse membranen mit biologisch abbaubarem bindemittel

Country Status (3)

Country Link
EP (1) EP3966379B1 (de)
CN (1) CN115279961A (de)
WO (1) WO2021197999A1 (de)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2024050810A1 (zh) * 2022-09-09 2024-03-14 宁德时代新能源科技股份有限公司 一种粘结剂组合物及由其制备的电极极片

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3779015A1 (de) * 2018-08-17 2021-02-17 Johns Manville Binderverfestigtes textilgewebe, verfahren zu dessen herstellung und dessen verwendung

Family Cites Families (29)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR767590A (de) * 1933-05-20 1934-07-19
US3358640A (en) * 1963-04-12 1967-12-19 Kurashiki Rayon Co Device for treating cigarette filter plugs
DE1444068A1 (de) * 1963-10-31 1968-10-17 Bayer Ag Verfahren zur Herstellung von Vliesstoffen
NL135509C (de) * 1967-11-01 Gelder Zonen Papierfab Van
DE1619127A1 (de) 1967-11-22 1971-07-08 Nippon Cloth Industry Co Ltd Verfahren zur Herstellung eines verbundenen Fasermaterials
US4613627A (en) * 1982-12-13 1986-09-23 Usg Acoustical Products Company Process for the manufacture of shaped fibrous products and the resultant product
JPH0299655A (ja) 1988-08-03 1990-04-11 Sequa Chemicals Inc 繊維マット用澱紛系バインダー組成物およびその製造方法
JP2599793B2 (ja) * 1989-07-14 1997-04-16 株式会社クラレ 紙製のラベル用アルカリ洗浄性接着剤
JP3403415B2 (ja) * 1995-12-04 2003-05-06 花王株式会社 アスファルト乳剤
SE513632C2 (sv) * 1998-07-06 2000-10-09 Borealis Polymers Oy Multimodal polyetenkomposition för rör
US6713156B1 (en) * 2003-05-05 2004-03-30 National Starch And Chemical Investment Holding Corporation Polymer-treated abrasive substrate
CN101203555A (zh) 2005-05-06 2008-06-18 太尔公司 基于聚乙烯醇且不含甲醛的可固化含水组合物
US7592049B2 (en) * 2005-07-14 2009-09-22 Wacker Chemical Corporation Dry chemically bound nonwovens which are flushable and dispersible
DE102005037113A1 (de) 2005-08-03 2007-02-08 Basf Ag Verwendung einer thermisch härtbaren wässrigen Zusammensetzung als Bindemittel für Substrate
RU2436882C2 (ru) * 2006-02-23 2011-12-20 Мидвествако Корпорейшн Способ обработки субстрата
US20090022983A1 (en) * 2007-07-17 2009-01-22 David William Cabell Fibrous structures
US8946348B2 (en) * 2007-11-30 2015-02-03 Sekisui Specialty Chemicals America, Llc Method for dissolving polyvinyl alcohol particles into aqueous media using high shear
DE102007060494A1 (de) * 2007-12-14 2009-06-18 Johns Manville Europe Gmbh Trägereinlage, Verfahren zu deren Herstellung und deren Verwendung
WO2010103050A1 (en) * 2009-03-10 2010-09-16 Corrutech Improved adhesive composition
AU2011208841B2 (en) * 2010-01-19 2015-05-14 C-Ip S.A. Improved adhesive composition
FR2957610B1 (fr) * 2010-03-17 2012-03-23 Freudenberg Politex Sa Produit non-tisse contenant des particules organiques et/ou minerales et son procede de fabrication
BR112013025244A2 (pt) * 2011-04-04 2016-12-20 Basf Se composição de aglutinante aquosa, uso de uma composição de aglutinante aquosa, processo para a produção de um artigo moldado, artigo moldado, uso de um artigo moldado, e, membrana de telhado betumizada
DE102011112267A1 (de) * 2011-09-02 2013-03-07 Carl Freudenberg Kg Fixiereinlage
JP2014205825A (ja) * 2013-03-18 2014-10-30 日本合成化学工業株式会社 架橋方法、並びにその架橋方法により得られる架橋高分子
US11453798B2 (en) 2013-12-05 2022-09-27 Ecosynthetix Ltd. Formaldehyde free binder and multi-component nanoparticle
US9494810B2 (en) * 2015-03-24 2016-11-15 Finisar Corporation Automatic bias stabilization of dual-polarization in-phase and quadrature optical modulator
US10259190B2 (en) * 2015-03-31 2019-04-16 Freudenberg Performance Materials Lp Moldable composite mat
DE102016011586A1 (de) * 2016-09-24 2018-03-29 Johns Manville Europe Gmbh Binderverfestigtes, textiles Flächengebilde, Verfahren zu dessen Herstellung und dessen Verwendung
RU2688549C2 (ru) * 2017-09-06 2019-05-21 Общество с ограниченной ответственностью "НИКОЛЬ" Тепло- и звукоизоляционный материал из минерального волокна на основе нефенолформальдегидного связующего

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3779015A1 (de) * 2018-08-17 2021-02-17 Johns Manville Binderverfestigtes textilgewebe, verfahren zu dessen herstellung und dessen verwendung

Also Published As

Publication number Publication date
EP3966379A1 (de) 2022-03-16
CN115279961A (zh) 2022-11-01
WO2021197999A1 (en) 2021-10-07

Similar Documents

Publication Publication Date Title
EP2192153B1 (de) Mit Bindemittel verfestigtes Textilgewebe, Verfahren zu dessen Herstellung und dessen Verwendung
RU2682632C2 (ru) Уплотненная связующим ткань, способ ее производства и ее использование
CN107869054B (zh) 粘合剂加固的纺织物、其制造方法及其用途
US20100015425A1 (en) Method for making a reinforcement frame and sealing membrane including such frame, and products thus obtained
CN101903589B (zh) 基础内衬、其生产方法和应用
RU2622308C2 (ru) Укрепленный связующим текстильный материал, способ его изготовления и его применение
EP3966379B1 (de) Bituminöse membranen mit biologisch abbaubarem bindemittel
EP2199333B1 (de) Binderverfestigtes, textiles Flächengebilde, Verfahren zu dessen Herstellung und dessen Verwendung
CA3169143A1 (en) Bituminous membranes with biodegradable binder
US20210355629A1 (en) Formaldehyde-free binder composition
EP3632867B1 (de) Mit beschichtung mit teilweise löslichem dextrin beschichtetes glastextil
EP4244419B1 (de) Bituminöse membranen mit biologisch abbaubarem bindemittel
US20220220646A1 (en) Formaldehyde-free binder composition
EP2360304B1 (de) Vorkonfektionierte Trägereinlage und beschichtete Dachbahnen
CN114182439A (zh) 固结非织造布
EP4259869A1 (de) Textile flächengebilde

Legal Events

Date Code Title Description
STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: UNKNOWN

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE INTERNATIONAL PUBLICATION HAS BEEN MADE

PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE

17P Request for examination filed

Effective date: 20211209

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: EXAMINATION IS IN PROGRESS

17Q First examination report despatched

Effective date: 20220330

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: GRANT OF PATENT IS INTENDED

INTG Intention to grant announced

Effective date: 20220520

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE PATENT HAS BEEN GRANTED

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

DAV Request for validation of the european patent (deleted)
DAX Request for extension of the european patent (deleted)
REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

REG Reference to a national code

Ref country code: AT

Ref legal event code: REF

Ref document number: 1527091

Country of ref document: AT

Kind code of ref document: T

Effective date: 20221115

REG Reference to a national code

Ref country code: DE

Ref legal event code: R096

Ref document number: 602021000638

Country of ref document: DE

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

REG Reference to a national code

Ref country code: SE

Ref legal event code: TRGR

REG Reference to a national code

Ref country code: NL

Ref legal event code: FP

REG Reference to a national code

Ref country code: LT

Ref legal event code: MG9D

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: PT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230227

Ref country code: NO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230126

Ref country code: LT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20221026

Ref country code: FI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20221026

Ref country code: ES

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20221026

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 20230316

Year of fee payment: 3

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: RS

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20221026

Ref country code: PL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20221026

Ref country code: LV

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20221026

Ref country code: IS

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230226

Ref country code: HR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20221026

Ref country code: GR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20230127

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: TR

Payment date: 20230322

Year of fee payment: 3

Ref country code: SE

Payment date: 20230314

Year of fee payment: 3

Ref country code: DE

Payment date: 20230316

Year of fee payment: 3

Ref country code: BE

Payment date: 20230317

Year of fee payment: 3

P01 Opt-out of the competence of the unified patent court (upc) registered

Effective date: 20230515

REG Reference to a national code

Ref country code: DE

Ref legal event code: R097

Ref document number: 602021000638

Country of ref document: DE

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SM

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20221026

Ref country code: RO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20221026

Ref country code: EE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20221026

Ref country code: DK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20221026

Ref country code: CZ

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20221026

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: IT

Payment date: 20230331

Year of fee payment: 3

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20221026

Ref country code: AL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20221026

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed

Effective date: 20230727

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MC

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20221026

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20221026

REG Reference to a national code

Ref country code: AT

Ref legal event code: UEP

Ref document number: 1527091

Country of ref document: AT

Kind code of ref document: T

Effective date: 20221026

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20230325

REG Reference to a national code

Ref country code: IE

Ref legal event code: MM4A

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20230325

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 20240311

Year of fee payment: 3

Ref country code: NL

Payment date: 20240311

Year of fee payment: 4