WO2001014143A1

WO2001014143A1 - Method for producing paper compound materials and materials that are adhesive after humidification

Info

Publication number: WO2001014143A1
Application number: PCT/EP2000/008035
Authority: WO
Inventors: Thomas Möller
Original assignee: Henkel Kommanditgesellschaft Auf Aktien
Priority date: 1999-08-25
Filing date: 2000-08-17
Publication date: 2001-03-01
Also published as: DE19940261A1; AU6996700A

Abstract

The invention relates to a method for producing paper compound materials containing at least two layers. A water-soluble hot-melt-type adhesive is applied to a first layer of paper and at least a second layer of paper is laminated onto the adhesive side pertaining to the first layer of paper. The solubility of the hot-melt-type adhesive amounts to 3 wt. % in water at 20° C.

Description

Process for the production of paper composites and moisturizing sticky materials

The invention relates to a process for the production of at least two-day paper composites or of moisturizing-sticky materials using water-soluble hot-melt adhesives and the use of water-soluble high-molecular-weight polymers as hot-melt adhesive for the gluing of paper, in particular for the gluing of hygienic paper or for the production of moisturizing-sticky materials.

As a rule, hygiene papers should be particularly skin-friendly, ie they should cause as little skin irritation as possible when used on sensitive parts of the body. In addition to checking the migratable ingredients of the hygiene paper, the subjectively felt "softness" or "gentleness" of the hygiene paper plays a role in achieving this effect. A particularly soft and gentle impression is usually achieved in that the hygienic paper is composed of several thin layers. From the point of view of user-friendliness, however, there should be a noticeable liability between these individual layers so that the hygienic papers do not immediately dissolve into individual layers when they are used, and thus their handling deteriorates significantly. Another tendency in the field of hygienic paper is to reduce the number of layers that are necessary to achieve the softest possible effect as far as possible. The production and merging of several layers is generally more expensive than the production of a hygienic paper, for example reduced to only two layers. In order to achieve the required, velvety surface effect, the surface of the hygienic paper is usually modified by embossing or other treatments that influence, for example, the alignment of the fibers on the paper surface. If you now try to glue the individual layers of the hygienic paper using a water-soluble adhesive, this has several disadvantages. For example, water as a solvent for the adhesive has an adverse effect on the paper surface. This is expressed, for example, in the formation of wrinkles, shrinkage or smoothing of the paper surface. All of these effects have an adverse effect on the nature of the surface with regard to a "velvety" feeling for the user.

Similar phenomena such as wrinkling or shrinkage also occur in the manufacture of sticky materials such as stamps, envelopes or labels.

Furthermore, the use of water-soluble adhesives in the course of the bonding process requires a drying step in which water is removed from the bonded hygienic paper. Such drying stages are usually energy-intensive and lead to an increase in price and a time lag in the production process.

Another disadvantage of using water-soluble adhesives is that it usually takes a long time until the adhesion and cohesion values enable the individual layers of paper to adhere sufficiently. This has an adverse effect on the further processing of the bonded layers, i. that is, the bonded paper layers can usually only be subjected to sufficient mechanical loads after drying.

Another requirement for adhesives that are used to bond hygienic paper is that the adhesives should be as completely water-soluble as possible. This requirement is based on the high recycling rate in the production of hygienic paper, that is to say that production waste must be used again as directly as possible in the production of new paper layers. However, this requires that the bond between the individual layers of paper is completely removed from a recycled fiber pulp. Water-insoluble or poorly water-soluble adhesive components that get into the paper web from the recycled fiber material during the production of a new paper layer can lead to serious production downtimes. Such adhesive residues usually form so-called "stickies" in the recycled paper webs, ie sticky spots which can lead to the paper web sticking to rollers and similar guide elements for the paper web. This usually results in tearing off the paper web and lengthy production interruptions. It is therefore not only necessary that the bond can be detached again by water and thereby lead to a dispersion of the adhesive in the water, but the adhesive itself should be completely soluble in water. This prevents any adhesive residue that may have been discharged from becoming finely divided and leading to sticky agglomerates (stickies).

EP-A 0 705 895 relates to a method for bonding tissue or nonwovens, in which a hot-melt adhesive composition is used which consists of up to 60% of a starch ester, up to 40% of a polar wax, up to 50% of a plasticizer Contains 25% of a tackifier and up to 3% of an antioxidant. While this adhesive composition fulfills the basic requirements for an adhesive for bonding hygienic paper layers, not all components of the adhesive are completely water-soluble. This can lead to the disadvantages described above when recycling such hygienic paper.

In the older application DE 198 21 769, a method for producing at least two-layer paper composites is described, in which a water-soluble hot melt adhesive is applied to a first paper layer and at least a second paper layer is laminated onto the adhesive side of the first paper layer, the solubility of the hot melt adhesive in water 20 ° C at least 3% by weight is. In this document, the problem of visually assessing the spray pattern without a dye appearing in an optically disturbing manner is not addressed and also not solved.

The object was therefore to provide a hotmelt adhesive for bonding sanitary paper layers which can be applied as a melt, allows clean application even in the smallest application quantities (less than 0.1 g / m ² ), a firm, permanent and quick bond guaranteed after joining two paper webs to be glued and is also completely water-soluble, that is, is miscible with water in any amount. The application of the hot melt adhesive should be easy to control.

It has now been found that water-soluble polymers with a water solubility of at least 3% by weight at 20 ° C. do not have the disadvantages mentioned above.

The invention accordingly relates to a process for producing at least two-layer paper composites, in which a water-soluble hot-melt adhesive is applied to a first paper layer and at least a second paper layer is laminated onto the adhesive side of the first paper layer, the solubility of the hot-melt adhesive in water at 20 ° C. at least 3 Is wt .-% and the hot melt adhesive contains a UV-active fluorescent dye in a detectable amount.

The method according to the invention is particularly suitable for paper composites which are to be used as hygienic paper. In the context of the present invention, “hygiene paper” is used predominantly in households, in community facilities and for personal hygiene types of paper, eg. B. Household towels (kitchen paper), paper towels, paper handkerchiefs, paper napkins, toilet paper, children's diapers and the like are understood. The method according to the invention is particularly suitable for the production of paper composites from tissue. "Tissue" means a particularly thin, soft, predominantly wood-free material, possibly with fine (dry) crepe. The material is very absorbent and in a single layer usually has a basis weight of> 25 g / m ² (before the crepe). Such tissue composites, as can be obtained by the process according to the invention, are mainly used to produce toilet paper, paper tissues or facial tissues.

For the purposes of the present invention, “hot melt adhesives” are understood to mean adhesives which are solid at room temperature and are at least largely free of water and solvents. Hot melt adhesives are applied from the melt to the paper layers to be bonded and bind physically when they cool down and solidify. Suitable hot melt adhesives are, for example, organic polymers such as polyesters, polyurethanes, polyamides, polyalkylene oxides or polymers, for example polyacrylates. However, the hot melt adhesives must at least meet the above-mentioned requirements with regard to water solubility.

The terms “polyacrylate” as used in the context of the present text refer below to both polymers or copolymers of acrylic acid or their derivatives and to polymers or copolymers of methacrylic acid or their derivatives.

Polyacrylates suitable as hot-melt adhesive in the context of the present invention can be prepared by using acrylic acid or methacrylic acid or derivatives of acrylic acid or methacrylic acid, for example esters of acrylic or methacrylic acid with mono- or polyfunctional alcohols, in each case alone (in the case of acrylic acid or methacrylic acid) or as Mixture of two or more thereof, in a known manner, for example free-radical or ionic, polymerized. The polymers or copolymers should in any case have a proportion of free acid groups or their salts with alkali, alkaline earth or ammonium ions which is so high that the polymer has a water solubility of at least about 3% by weight at 20 ° C. For example, in the context of the present invention, polyacrylates in the form of homopolymers or copolymers can be used as the hotmelt adhesive, the latter also comprising styrene, styrene sulfonic acid, acrylonitrile, vinyl acetate, vinyl propionate, vinyl chloride, vinylidene chloride and / or butadiene in addition to the acrylic or methacrylic acid components or their mixture.

If appropriate, further acrylates or methacrylates or a mixture thereof with one or more functional groups may be present in the polymerization. For example, this maleic acid, itaconic acid, butanediol are diacrylate, hexanediol diacrylate, triethylene glycol diacrylate, tetraethylene glycol diacrylate, neopentyl glycol diacrylate, trimethylolpropane triacrylate, 2-hydroxyethyl acrylate, 2-hydroxyethyl methacrylate, hydroxypropyl acrylate, Propylenglycolmethacrylat, butane diol monoacrylate, ethyl diglycol acrylate and sulfonsäuregruppentragende monomers, such as 2-acrylamido-2-methylpropanesulfonic acid ,

In a preferred embodiment of the invention, the polyacrylates have a molecular weight of about 3,000 to about 50,000.

Also suitable for use as a hot melt adhesive in the context of the present invention are polyesters with a molecular weight of approximately 3,000 to approximately 50,000. For example, polyesters can be used which are formed by reacting low molecular weight alcohols, in particular ethylene glycol, diethylene glycol, neopentyl glycol, hexanediol, butanediol, propylene glycol, glycerol or trimethylol propane with corresponding at least difunctional acids. Also suitable as polyfunctional alcohols for the preparation of polyesters are 1,4-hydroxymethylcyclohexane, 2-methyl-1,3-propanediol, butanetriol-1, 2,4,

Triethylene glycol, tetraethylene glycol, polyethylene glycol, dipropylene glycol, polypropylene glycol, dibutylene glycol and polybutylene glycol.

Suitable polyester polyols can be produced, for example, by polycondensation. So difunctional or trifunctional alcohols or a mixture of two or more thereof, with dicarboxylic acids or tricarboxylic acids or a mixture of two or more thereof, or their reactive derivatives, to form polyester polyols. Suitable dicarboxylic acids are, for example, succinic acid and its higher homologues with up to 16 carbon atoms, furthermore unsaturated dicarboxylic acids such as maleic acid or fumaric acid and aromatic dicarboxylic acids, in particular the isomeric phthalic acids such as phthalic acid, isophthalic acid or terephthalic acid. Citric acid or trimellitic acid, for example, are suitable as tricarboxylic acids. Within the scope of the invention, polyester polyols from at least one of the dicarboxylic acids and glycerol mentioned, which have a residual OH group content, are particularly suitable. Particularly suitable alcohols are hexanediol, ethylene glycol, diethylene glycol or neopentyl glycol or mixtures of two or more thereof. Particularly suitable acids are isophthalic acid or adipic acid or a mixture thereof.

Polyols that can also be used as the polyol component for the production of the polyester are, for example, diethylene glycol or higher polyethylene glycols with a molecular weight (M _n ) of about 100 to about 22,000, for example about 200 to about 15,000 or about 300 to about 10,000, in particular about 500 to about 2,000.

Polyesters which can be used as hot-melt adhesive in the context of the present invention include in particular the reaction products of polyfunctional, preferably difunctional alcohols (optionally together with small amounts of trifunctional alcohols) and polyfunctional, preferably difunctional carboxylic acids. Instead of free polycarboxylic acids, the corresponding polycarboxylic acid anhydrides or corresponding polycarboxylic acid esters with alcohols with preferably 1 to 8 carbon atoms can be used (if they exist). The polycarboxylic acids can be aliphatic, cycloaliphatic, aromatic and / or heterocyclic. They can optionally be substituted, for example by alkyl groups, alkenyl groups, ether groups or halogens. Examples of polycarboxylic acids are succinic acid, adipic acid, suberic acid, azelaic acid, sebacic acid, phthalic acid, isophthalic acid, terephthalic acid, trimellitic acid, phthalic anhydride, tetrahydrophthalic anhydride, hexahydrophthalic Acid anhydride, tetrachlorophthalic anhydride, endomethylene tetrahydrophthalic anhydride, glutaric anhydride, maleic acid, maleic anhydride, fumaric acid, dimer fatty acid or trimer fatty acid or mixtures of two or more thereof. If necessary, minor amounts of monofunctional fatty acids can be present in the reaction mixture.

The polyesters can have, for example, carboxyl end groups. Polyesters obtainable from lactones, for example ε-caprolactone or hydroxycarboxylic acids, for example ω-hydroxycaproic acid, can likewise be used at least in part.

In any case, however, the polyesters must have a water solubility of at least 3% by weight at 20 ° C. Water solubility can be achieved, for example, by using suitable water-soluble comonomers in polyester production. To adjust the water solubility of the polyesters, it is advisable, for example, to use appropriate sulfonated polycarboxylic acids, for example sulfonated phthalic acid, isophthalic acid or terephthalic acid, or to use water-soluble polyether polyols such as polyethylene glycol with a molecular weight (M _n ) of at least about 100 in the polycondensation.

Also suitable as hot melt adhesive are, for example, polyalkylene glycols with a molecular weight (M _n ) of at least about 1,000, whose solubility in water at 20 ° C. is at least about 3% by weight.

Such polyalkylene glycols are generally produced by catalytically assisted ring-opening polymerization of alkylene glycols.

Usually, polymerization is started from a so-called starter molecule. In principle, all compounds are suitable as starter molecules which, if appropriate in the presence of a suitable catalyst, are capable of opening epoxy rings. For example, these are primary, secondary or tertiary amines, primary, secondary or tertiary alcohols, thiols or carboxylic acids. The polymerization usually takes place under basic catalysis. In the context of the present invention preferably polyalkylene glycols are used as oxides by polymerization of ethylene oxide, optionally in admixture with C _3- ι ₂ alkylene, is. The proportion of higher alkylene oxides in the polyalkylene glycol may, however, be such that the solubility in water (in the context of the present text also: water solubility) at 20 ° C. is at least about 3% by weight. Suitable are, for example, polyethylene glycols with a proportion of C ₃ or C ₄ units, or both, as can be obtained by copolymerizing ethylene oxide with propylene oxide or butylene oxide or a mixture thereof. However, polyethylene oxide is preferably used in the context of the present invention, as can be obtained by polymerizing ethylene oxide.

In a preferred embodiment of the invention, the hot-melt adhesive used is polyalkylene glycols which have been prepared using primary, secondary or tertiary alcohols or mixtures of two or more thereof as starting molecules.

Basically, all monofunctional or polyfunctional alcohols or mixtures thereof are suitable as starting molecules, but polyalkylene glycols are preferably used in the context of the present invention which are produced using a di- or trihydric alcohol, for example ethylene glycol, propylene glycol, butylene glycol, pentanediol, hexanediol, heptanediol, octanediol as well as their higher homologues, neopentylglycol, glycerol, trimethylolpropane, triethylolpropane, pentaerythritol, glucose, sorbitol, mannitol or a mixture of two or more thereof as the starting molecule.

The lower limit of the molecular weight of the polyalkylene glycols which can be used as hot melt adhesive in the context of the present invention is determined by the adhesive properties of the polyalkylene glycol. In any case, it is necessary that the molecular weight be so high that there is sufficient adhesion and cohesion of the hot melt adhesive. Furthermore, that should The molecular weight must be so high that the polyalkylene glycols no longer have any pressure-sensitive properties.

The polyalkylene glycols which can be used as hot melt adhesive in the process according to the invention therefore generally have a molecular weight (M _n ) of at least about 1,000, for example at least about 3,000 and in particular at least about 6,000.

The upper limit for the molecular weight is usually determined by the processing as a hot melt adhesive and by the water solubility. The result of this is that the upper limit of the molecular weight should be such that problem-free rolling or spraying of the molten polyalkylene oxide through conventional nozzles is possible within the framework of conventional application techniques. Furthermore, the molecular weight of the polyalkylene oxide should only be so high that the required water solubility of about 3% by weight is maintained. The upper limit of the molecular weight is therefore, for example, approximately 100,000, in particular up to approximately 50,000.

The polyalkylene glycols can be individually, i.e. H. can be used as a polyaddition product with molecular weight distributions usually formed in the case of base-catalyzed additions of alkylene oxides to water or other starter molecules. However, it is also possible to use mixtures of different polyalkylene glycols with different molecular weight distributions. It is also possible to use polyalkylene glycols which are formed by adding only one alkylene oxide compound to a starter molecule. However, it is also possible to use polyalkylene glycols which can be obtained by adding various alkylene oxides. It can be block copolymers as well as statistical copolymers.

Polyurethanes with a molecular weight (M _n ) of at least about 2,000, for example about 5,000 or more, which have a water solubility at 20 ° C. of have at least 3 wt .-%, are used. Both ionic and nonionic, water-soluble polyurethanes are suitable as hot melt adhesives.

Polyurethanes, such as can be used as hot melt adhesives in the context of the present invention, are usually produced by reacting at least one polyisocyanate, preferably a diisocyanate, and a polyol component, which preferably consists predominantly of diols. The polyol component can contain only one polyol, but a mixture of two or more different polyols can also be used as the polyol component. For example, polyalkylene oxides, in particular polyethylene oxide, are particularly suitable as the polyol component or at least as part of the polyol component.

The term "ionic" means that the polyurethane has ionic or at least ionizable groups in the context of an acid-base reaction as solubilizers, for example carboxylate, sulfonate, phosphonate or ammonium groups.

The term “nonionic” means accordingly that the polyurethane has no ionic groups as emulsifying groups, that is to say no carboxylate, sulfonate, phosphonate or ammonium groups. Rather, the water solubility is based on the hydrophilic nonionic groups of polyoxyethylene - [CH ₂ -CH ₂ -0-] _n -. These structural units are derived in particular from the polyethylene oxide which is preferably used as the polyol component. However, polyethylene oxide is not only to be understood as polyaddition products of ethylene oxide with water or ethylene glycol as the starting molecule, but also polyadditions of ethylene oxide with other dihydric alcohols, e.g. B. butanediol, hexanediol or 4,4'-dihydroxydiphenylpropane. Mixtures of two or more different polyethylene oxides can also be used which differ, for example, in the average molecular weight M _w or M _n or in both. Copolymers of ethylene oxide with higher alkylene oxides, e.g. B. with propylene oxide, as a polyol component, provided that they are sufficiently water-soluble, that is, more than about 3 g remain dissolved in about 100 g water at about 20 ° C for about 6 months.

The polyethylene oxide in the polyol component can be replaced by up to 10, preferably up to at most 5, in particular up to at most 2% by weight with other diols which contain a hydrophobic residue with a water solubility of at most 2 g / 100 g of water. The hydrophobic radical is, in particular, aliphatic or alicyclic structures with 2 to 44, in particular 6 to 36, carbon atoms. The residues can also contain aromatic structures. Diols with at least one primary OH group, in particular 1,2- or α, ω-diols, are preferred. Diols with the vicinal position of the OH groups are also suitable.

The polyethylene oxide in the polyol component preferably has a molecular weight (M _n ) of about 200 to about 20,000, in particular about 1,000 to about 15,000, for example about 1,550, 3,000, 6,000 or 12,000.

Furthermore, up to 10, preferably 0.5 to 5% of the polyethylene glycol can be replaced by hydrophobic homopolymeric polyalkylene glycols, the alkylene group having more than 2, preferably 3 or 4, carbon atoms. Their molecular weights are in particular 150 to 10,000 g / mol.

Specific examples of the hydrophobic diols with pure CH residues and with ether groups are polypropylene glycol (PPG), polybutylene glycol, polytetrahydrofuran, polybutadiene diol, hydroxyl-terminated ethylene-butylene copolymers (for example KRATON LIQUID polymer L-2203), hydrogenated polybutadiene 4-diol and alkane diol up to 44 carbon atoms. Preferred hydrophobic diols are polypropylene glycol, polyetrahydrofuran with a molecular weight of 150 to 10,000, in particular 200 to 4,500, particularly preferably 250 to 1,000, and 1, 10-decanediol, 1, 12-dodecanediol, 1, 12-octadecanediol, dimer fatty acid diol, 1, 2 Octane diol, 1, 2-dodecane diol, 1, 2-hexadecane diol, 1, 2-octadecane diol, 1,2-tetradecane diol, 4,4-isopropylidenedicyclohexanol and their isomer mixtures, 4,8-

Bis (hydroxymethyl) tricyclo [5,2,1, 0 ^2,6] decane and isomer mixtures thereof, 1, 4: 3,6- Dianhydro-D-mannitol, 1: 4: 3,6-dianhydro-D-sorbitol, 1, 16-hexadecanediol, bisphenol-A and their prop- or ethoxylation products or their mixtures, in particular with up to 30 EO units, and finally Mono fatty acid esters of glycerol with fatty acids containing up to 22 carbon atoms, eg glycerol monoesters of behenic acid, oleic acid, stearic acid, myristic acid. Mixtures of two or more of the hydrophobic diols mentioned can of course also be used.

The polyethylene glycol can also be replaced to a degree of 0 to 5, in particular 0.2 to 2% by higher functional alcohols, in particular by triols, e.g. by glycerin, trimethylolpropane, triethanolamine or their ethoxylated or propoxylated variants. Pentaerythritol is also useful. Ethoxylated or propoxylated variants of amines or amino alcohols are also possible, e.g. starting from ethylenediamine, diethylenetriamine, and their higher homologues, for example aminophenol, N-2-aminoethylpiperazine.

In order to obtain particularly high molecular weight polyurethanes, the purest possible diols should be used. For this purpose, the content of alkali and alkaline earth metal ions should be below 500 ppm, in particular below 150 ppm and preferably below 10 ppm. In addition, the water content should be below 0.5, in particular below 0.1, preferably below 0.05% by weight according to K. Fischer.

In addition to the diols of the polyol component, diisocyanates are essential components of the polyurethane that can be used as a hot melt adhesive. These are compounds of the general structure 0 = C = N-X-N = C = 0, where X is an aliphatic, alicyclic or aromatic radical, preferably an aliphatic or alicyclic radical with 4 to 18 C atoms.

Examples of suitable isocyanates are 1,5-naphthylene diisocyanate, 4,4'-diphenylmethane diisocyanate (MDI), hydrogenated MDI (H ₁₂ -MDI), xylylene diisocyanate (XDI), tetramethylxylylene diisocyanate (TMXDI), 4,4'-diphenyldimethylmethane diisocyanate, di and tetraalkyene diphenylmethane diisocyanate, 4,4'- Dibenzyl diisocyanate, 1,3-phenylene diisocyanate, 1,4-phenylene diisocyanate, the isomers of tolylene diisocyanate (TDI), 1-methyl-2,4-diisocyanato-cyclohexane, 1,6-diisocyanato-2,2,4-trimethylhexane, 1, 6-diisocyanato-2,4,4-trimethylhexane, 1-isocyanatomethyl-3-isocyanato-1, 5,5-trimethyicyclohexane (IPDI), chlorinated and brominated diisocyanates, phosphorus-containing diisocyanates, 4,4'-di-isocyanatophenylperfluoroethane, tetramethoxybutane 1,4-diisocyanate, butane-1,4-diisocyanate, hexane-1,6-diisocyanate (HDI), dicyclohexylmethane diisocyanate, cyclohexane-1,4-diisocyanate, ethylene diisocyanate, phthalic acid bis-isocyanato ethyl ester, and also diisocyanates reactive halogen atoms such as 1-chloromethylphenyl-2,4-diisocyanate, 1-bromomethylphenyl-2,6-diisocyanate or 3,3-bis-chloromethyl ether-4,4'-diphenyl diisocyanate. Sulfur-containing polyisocyanates are obtained, for example, by reacting 2 mol of hexamethylene diisocyanate with 1 mol of thiodiglycol or dihydroxydihexyl sulfide. Further usable diisocyanates are, for example, trimethylhexamethylene diisocyanate, 1,4-diisocyanatobutane, 1,2-diisocyanatododecane and dimer fatty acid diisocyanate. Particularly suitable are: tetramethylene, hexamethylene, undecane, dodecamethylene, 2,2,4-trimethylhexane, 1,3-cyclohexane, 1,4-cyclohexane, 1,3, or 1,4-tetramethylxylene -, Isophorone, 4,4- dicyclohexylmethane and lysine ester di-isocyanate. Tetramethylxylylene diisocyanate (TMXDI) is very particularly preferred, in particular the m-TMXDI available from Cyanamid.

To further increase the molecular weight, chain extension can be carried out, for example, in a known manner. To this end, prepolymers with excess diisocyanate are first produced, which are then subsequently extended with short-chain amino alcohols, diols, diamines or with water while increasing the molecular weight.

To this end, prepolymers with excess diisocyanate are first produced, which are then subsequently extended with short-chain diols or diamines or with water. As chain extenders, the following are specifically mentioned: saturated and unsaturated glycols such as ethylene glycol or condensates of ethylene glycol, 1,3-butanediol, 1,4-butanediol, 2-butene-1,4-diol, 1,4-butyne-1,4-diol, 1,2-propanediol, 2, propanediol -1, 3, neopentyl glycol, hexanediol, bis-hydroxymethylcyclohexane, dioxyethoxy hydroquinone, terephthalic acid bisglycol ester, succinic acid di-2-hydroxyethyl amide, succinic acid di-N-methyl- (2-hydroxyethyl) amide, 1,4-di (2-hydroxymethyl mercapto) -2,3,5,6-tetrachlorobenzene, 2-methylene-propanediol- (1, 3), 2-methyl-propanediol- (1, 3), 3-pyrrolidino-1,2-propanediol, 2-methylene-pentanediol-2,4 , 3-alkoxy-1,2-propanediol, 2-ethylhexane-1,3-diol, 2,2-dimethylpropanediol-1,3, 1,5-pentanediol, 2,5-dimethyl-2,5-hexanediol, 3rd -Phenoxy-1,2-propanediol, 3-benzyloxy-1,2-propanediol, 2,3-dimethyl-2,3-butanediol, 3- (4-methoxyphenoxy) -1, 2-propanediol and

hydroxymethylbenzyl; aliphatic, cycloaliphatic and aromatic diamines such as ethylene diamine, hexamethylene diamine, 1,4-cyclohexylene diamine, piperazine, N-methyl propylene diamine, diaminodiphenyl sulfone, diaminodiphenyl ether,

Diaminodiphenyldimethylmethane, 2,4-diamino-6-phenyltriazine, isophoronediamine, dimer fatty acid diamine, diaminodiphenylmethane or the isomers of phenylenediamine; also carbohydrazides or hydrazides of dicarboxylic acids; Amino alcohols such as ethanolamine, propanolamine, butanolamine, N-methylethanolamine, N-methylisopropanolamine, diethanolamine, triethanolamine and higher di- or tri (alkanolamines); aliphatic, cycloaliphatic, aromatic and heterocyclic mono- and diaminocarboxylic acids such as glycine, 1- and 2-alanine, 6-aminocaproic acid, 4-aminobutyric acid, the isomeric mono- and diaminobenzoic acids as well as the isomeric mono- and diaminonaphthoic acids.

However, the polyurethane is preferably produced in a one-step process. For example, all starting materials are first mixed in the presence of an organic solvent with a water content of less than 0.5% by weight. The mixture is heated to 60 to 200 ° C., in particular to 80 to 180 ° C. and preferably to 100 to 150 ° C., for about 1 to 30 hours. The reaction time can be shortened by the presence of catalysts.

In particular, tertiary amines are suitable, e.g. Triethylamine, 1,4-diazabicyclo [2,2,2] octane (= DABCO) dimethylbenzylamine, bis-dimethylaminoethyl ether and bis-methylaminomethylphenol. Particularly suitable are 1-methylimidazole, 2-methyl-1-vinylimidazole, 1-allylimidazole, 1-phenylimidazole, 1, 2,4,5-tetramethylimidazole, 1- (3-aminopropyl) imidazole, pyrimidazole, 4-dimethyiamino pyridine, 4-pyrrolidinopyridine, 4-morpholino-pyridine, 4-methylpyridine.

Organotin compounds can also be used as catalysts. These are understood to mean compounds which contain both tin and an organic radical, in particular compounds which contain one or more Sn — C bonds. Organotin compounds in the broader sense include, for example, salts such as tin octoate and tin stearate. Tin compounds in the narrower sense include above all compounds of tetravalent tin of the general formula R _n + ιSnX _3-n , where n stands for a number from 0 to 2, R stands for an alkyl group or an aryl group or both and X finally for one Oxygen, sulfur or nitrogen compound or a mixture of two or more of them. R expediently contains at least 4 carbon atoms, in particular at least 8. The upper limit is generally 12 carbon atoms. X is preferably an oxygen compound, that is to say an organotin oxide, hydroxide, carboxylate or an ester of an inorganic acid. However, X can also be a sulfur compound, ie an organotin sulfide, thiolate or a thiosate. In the case of the Sn-S compounds, thioglycolic acid esters are particularly suitable, for example compounds with the following radicals:

-S-CH ₂ -CH ₂ -CO-O- (CH ₂ ) ₁₀ -CH ₃ or -S-CH ₂ -CH ₂ -CO-0-CH ₂ -CH (C ₂ H ₅ ) -CH ₂ -CH ₂ -CH ₂ -CH ₃ . Such compounds fulfill a further selection rule: In a preferred embodiment of the invention, the molecular weight of the organotin compound should be over 250, in particular over 600.

Another preferred class of compounds are the dialkyltin (IV) carboxylates (X = 0-CO-R ¹ ). The carboxylic acids have 2, preferably at least 10, in particular 14 to 32, carbon atoms. Dicarboxylic acids can also be used. Suitable acids are, for example, adipic acid, maleic acid, fumaric acid, terephthalic acid, phenylacetic acid, benzoic acid, acetic acid, propionic acid and in particular caprylic, capric, lauric, myristic, palmitic and stearic acid. For example, dibutyltin diacetate and dilaurate and dioctyltin diacetate and dilaurate are particularly suitable.

Tin oxides and sulfides and thiolates are also suitable in the context of the present invention. Specific compounds are: bis (tributyltin) oxide, dibutyltin didodecylthiolate, dioctyltin dioctylhiolate, dibutyltin bis (2-ethylhexyl thioglycolate), octyltin tris- (thioglycolic acid-2-ethyl-bis-ethylhexylethyl) -di-2-ethylhexylthioethyl-dioctylhexyltinate ), Dibutyltin bis (thioethylene glycol laurate),

Dibutyltin sulfide, dioctyltin sulfide, bis (tributyltin) sulfide, dibutyltin bis (2-ethylhexyl thioglycolic acid), dioctyltin bis (2-ethylhexoate thioethylene glycol), trioctyltin 2-ethylhexyl ethyl acetate and 2-ethylhexyl ethyl acetate and 2-ethylhexyl ethyl acetate (S, S-methoxycarbonyl ethyl) tin bis (2-ethylhexyl thiolatoacetate), bis (S, S-acetylethyl) tin bis (2-ethyl thiolatoacetic acid), tin (II) octyl hiolate and tin ( ll) - thioethylene glycol 2-ethylhexoate.

The following may also be mentioned: dibutyltin diethylate, dihexyltin dihexylate, dibutyltin diacetylacetonate, dibutyltin diethylacetylacetate, bis (butyldichlorotin) oxide, bis (dibutylchlorotin) sulfide, tin (II) phenolate, tin (II) diacetyl acetonoyl acetonoyl, as well as other acetylacetonoyl acetonoyl acetylacetonate, Ethyl acetoacetate, n-propyl acetoacetate, α, α ^' -

Diphenylacetoacetic acid ethyl ester and dehydroacetoacetic acid. The catalyst is preferably added to the polyol. Its amount depends on its activity and the reaction conditions. It is preferably in the range from 0.001 to 0.5% by weight, based on the polyol.

However, preference is given to working without a catalyst. The solvent is also expediently omitted. In the context of the present text, “solvents” are understood as meaning inert organic liquid substances with a boiling point of less than 200 ° C. at normal pressure (1 bar).

The reaction is preferably carried out so that the ratio of OH groups in the polyol component to NCO groups in the polyisocyanate is from about 1.0 to about 2.0, in particular from about 1.05 to 1.8, for example from about 1.1 to 1 , 7 or about 1, 3 to 1, 6.

One possibility of introducing ion-forming structural elements is the reaction of OH-terminated polyurethane oligomers with dicarboxylic acid anhydrides. These can contain a total of 2 to 44, preferably 2 to 12, carbon atoms between the bisacyl groups such as alkylene, alkenylene or arylene grouping. Examples include succinic anhydride, glutaric anhydride, 1, 2,3,6-tetrahydrophthalic anhydride and its isomers, phthalic anhydride, trimellitic anhydride, 7-oxabicyclo [2,2,1] hept-5-en-2,3-dicarboxylic acid anhydride, 5-norbornene-2 , 3-dicarboxylic anhydride and its isomers, diglycolic anhydride, maleic anhydride, dimethyl maleic anhydride, citraconic anhydride, itaconic anhydride, alkenylsuccinic anhydride.de, preferably those whose alkenyl groups have more than 2 carbon atoms, in particular more than 5, particularly preferably more than 7, carbon atoms. Specifically mentioned are: n-octenylsuccinic anhydride, n-dodecenylsuccinic anhydride, tetra-propenylsuccinic anhydride, n-hexadecenylsuccinic anhydride and n-octadenylsuccinic anhydride. The alkenyl radical can be linear or branched. Mixtures of alkenyl groups can also be used - 19 - different numbers of carbon atoms occur. Mixtures of several anhydrides are also possible, but cyclic anhydrides are preferred.

However, it is also possible to use a molar excess of isocyanates, resulting in NCO-terminated oligomers.

In general, NCO groups are undesirable in the end product. However, they can be used to e.g. introduce hydrophobic or ionic structural elements.

Hydrophobic structural elements can be obtained, for example, by reacting NCO-terminated oligomers with monools or monofunctional amines with> 2 C atoms, in particular> 6,> 10 or> 16 C atoms. Specifically, the following may be mentioned: poly-ethylene / butylene with 1 OH group, e.g. with an OH equivalent weight of 3600 (Kraton L 1203) and 1-hexanol, 1-heptanol, 1-octanol, 1-nonanol, 1-decanol, 1-undecanol, 10-undecen-1-ol, 1-dodecanol, 1 - Tridecanol, 1-tetradecanol, 1-pentadecanol, 1-hexadecanol, 1-heptadecanol, 1-octadecanol, 9-cis-octadecen-1-ol, 9-trans-octadecen-1-ol, 9-cis-octadecen-1 , 12-diol, all-cis-9,12-octadecadien-1-ol, all-cis-9,12,15-octadecatrien-1-ol, 1-nonadecanol, 1-eicosanol, 9-cis-eicosen-1 -ol, 5,8,11, 14-eicosatetraen-1-ol, 1-heneicosanol, 1-docosanol, 13-cis-docosen-1-ol, 13-trans-docosen-1-ol. The corresponding fatty amines are also possible as hydrophobizing structural elements.

Another possibility for introducing ion-forming structures is finally the reaction of NCO-terminated oligomers with hydroxycarboxylic acids or aminocarboxylic acids with alkylene, alkenylene or arylene groups, as in the case of the dicarboxylic acid anhydrides. Examples include: glycolic acid, lactic acid, caproic acid and mandelic acid, and aminocaproic acid, aminododecanoic acid, glycine, alanine and phenylalanine. In a preferred embodiment of the invention, a nonionic polyurethane with a molecular weight (M _n ) of at least about 2,000 is used as the hot melt adhesive, in particular a nonionic polyurethane which can be obtained by reacting at least one polyisocyanate with at least one polyalkylene glycol with a molecular weight of at least 1,000.

The hotmelt adhesive can contain further additives, for example plasticizers, theological additives, antioxidants, UV stabilizers, dyes, tackifier resins or pigments (filler).

For example, hydrocarbon resins are used as tackifiers, in particular C5 or C9 resins or C9 resins modified with C5 resins. Resins based on pure hydrocarbon monomers, for example resins such as are obtainable from the polymerization of mixtures of styrene, α-methylstyrene and vinyltoluene, are also suitable for use as tackifiers. The hydrocarbon resins mentioned can be partially hydrogenated or fully hydrogenated.

Also suitable for use as a tackifier are natural resins such as balsam resin, such as that obtained from trees, or tall resin, which is produced in paper production. The natural resins can be used in the form mentioned above as tackifiers, but it is also possible to use the resins mentioned after esterification with corresponding polyfunctional alcohols as pentaerythritol esters, glycerol esters, diethylene glycol esters, triethylene glycol esters or methyl esters.

The polyterpene resins are also suitable as tackifiers. Terpenes are obtained when resin acids are separated from their natural solvents and can be polymerized to polyterpene resins. Also suitable for use as tackifiers are the terpene phenol resins which can be obtained from polyterpene resins by phenol modification. The additives can be present individually or as a mixture of two or more of the substances mentioned in the hot melt adhesive. The amount of additives should not exceed about 20% by weight (based on the total hot melt adhesive). For example, amounts of about 0.1 to about 15% by weight are suitable, or about 1 to about 10% by weight in a preferred embodiment of the invention, for example about 2, 3, 4, 5, 7 or 9% by weight. % Additives used.

In order to enable a visual assessment of the spray pattern, but without visually disturbing the adhesive, a UV-active fluorescent dye is added to the hot melt adhesive. These are so-called optical brighteners of the following classes of substances: benzoxazole, benzoxazole-stilbene, stilbene, biphenyl, coumarin, pyrazoline, pyrazine and benzimidazole derivatives. Specifically, the following may be mentioned as examples: bis (5-tert-butyl-2-benzoxazolyl) thiophene ^* 2.5-, bis (2-benzoxazolyl) thiophene ^* 2.5-, bis (benzoxazolyl) stilbene ^* 4,4'-, diphenylstilbene Derivative, [bis (2-methoxy-4-anilinocyanurato) 4,4'-diamino] stilbene-2,2'-disulfonic acid di-sodium salt, bis [(4-anilino-6-methoxy-1 , 3,5-triazin-2-yl) amino] -2,2'- stilbenedisulfonic acid di-sodium salt ^* 4,4'-, diphenyldistyryl derivative, distyrylbiphenyl derivative anionic, stilbenedisulfonic acid derivative, bis [(4th , 6-dianilino-s-triazin-2-yl) amino] -stilbene-2,2'-disulfonic acid di-sodium salt ^* 4,4'-, stilbene disulfonic acid derivative, stilbene triazine derivative, bis (styryl) biphenyl Derivative, bis- (2-methylstyryl) biphenyl ^* 4,4'-, dibenzofuranylbiphenyl derivative, coumarin derivative dispersion in benzyl butyl phthalate, 2 (4- (3- (4-chlorophenyl) -4,5-dihydropyrazolyl) phenylsulfonyl ) ethyldimethylammonium hydrogenphosphonate, chlorophenyl-3 (4-chlorophenyl) -4,5-dihydro-1 H-pyrazole-1 (3-chloro-3-phenyl-4,5-dihydro-1 H-pyrazole mixture ^* 1 (3rd - Sulfamidophenyl) -3 (4-chlorophenyl) pyrazoline- ^* 1 (4-, diphenylpyrazoline derivative * 1, 3 non-ionic, diphenylpyrazoline derivative * 1, 3-, diphenylpyrazoline derivative-ketone-aldehyde condensation resin mixture ^* 1, 3-,

Sulfamidophenyl) -3 (4-chlorophenyl) pyrazoline ^* 1 (4-, chlorophenyl) -1 (4-amidosulfonylphenyl) pyrazoline * 3 (4-, N, N-dimethyl-2 (3- (4-chlorophenyl) -4, 5-dihydropyrazol-1-ylphenylsulfonyl) ethylamine. Such products can come, for example, from the Uvitex or Tinopal product series from Ciba Geigy, Blankophor from Bayer, Leukophor from Sandoz, Hostalux from Hoechst or Eastobrite from Eastman. Specifically, the following should be mentioned: Uvitex-OB, -ERN-P, -SOF, -EFT, -CBS, -3257, -CF, -CFkonz., -3692, -NFW-liquid, -CK, -SOP, -MST, - FP, -SWN-conc. and -4457, Tinopal-SOF, -CBS, -3257, -SOP, -DMSIX, -3859, -PLC, -SWN-conc, -FS, -CH-3566 and -LS, Eastobrite-OB-1, Blankophor- CA-4499, -CA-4601, -FBW, -MAR, -MAN, -K-2002-SK, FB-766 and -FB, Lenkophor-CRL-20/119, -EFR and Hostalux-VP-3481. Uvitex-OB is preferred.

The UV-active fluorescent dyes are used in an amount of up to 10, preferably up to 1 and in particular up to 0.05% by weight, based on the hotmelt adhesive as a whole. The lower limit results from the effectiveness of the dyes used and the desired color intensity of the UV light.

It is advisable to check the spray pattern in the following way:

A sample of the hot melt adhesive loaded paper composite is delaminated and preferably in a darkened room (e.g.

Sample box) the light of a UV radiation source with a wavelength of e.g. Exposed 254 mm. It is important that the wavelength is able to excite the dye.

The qualitative assessment of the application picture of the adhesive is done visually.

There is also the possibility of a quantitative assessment of the spray pattern by using the fluorescent light via suitable photoreceptors (photometers,

Cameras) and recorded using the image analysis methods connected to it. In addition to an analysis of the adhesive distribution, there is also the

Possibility of a statement about the amount of adhesive.

The polyalkylene glycol advantageously has a melt viscosity of not more than 20,000 mPas (Brookfield Thermosel, spindle 27, 180 ° C.). In a preferred embodiment, however, the melt viscosity is below this value, for example at about 1,000 mPas to about 10,000 mPas, for example about 2,000 to about 8,000 mPas. Good results can be achieved, for example, at around 5,000 to 6,000 mPas at a melting temperature of around 150 ° C (Brookfield Thermosel, spindle 27).

The hotmelt adhesives used in the process according to the invention should generally have a viscosity which allows the hotmelt adhesives to be used in the course of customary application processes. The hot melt adhesives therefore advantageously have a viscosity (Brookfield Thermosell, spindle 27) which is in a range from approximately 400 mPas at 100 ° C. to approximately 20,000 mPas at approximately 180 ° C. In a preferred embodiment of the present invention, the hotmelt adhesives have a viscosity in the range mentioned above in a temperature range from about 120 ° C. to about 150 ° C. Suitable viscosities are, for example, about 1,000 to about 15,000 mPas or about 3,000 to about 8,000 mPas.

The method according to the invention for producing at least two-ply paper composites generally includes at least one process step in which hot melt adhesive is applied to a first ply and a second paper ply is laminated onto the first paper ply at a certain time and space. In order for there to be sufficient adhesion between the first and second paper layers, the hotmelt adhesive must still be sufficiently tacky at the time the second paper layer is laminated on, i.e. it must not yet be physically hardened. The time after the application of the hot melt adhesive, in which the adhesive has sufficient tack to laminate on a second layer of paper, is hereinafter referred to as "open time". “Sufficiently tacky” is understood to mean tackiness that creates a connection between the paper layers that has a peeling force of more than 0 N / cm.

At conventional machine speeds of up to 600 m / min, for example, it is generally sufficient if the hot melt adhesive has an open time of approximately 0.1 to about 1 second, for example about 0.2 to about 0.5 seconds. If the hot melt adhesive is only to be used when the full machine speed has been reached, an open time of the order of magnitude mentioned above is usually sufficient. However, if, for example, the hotmelt adhesive is to lead to a connection of at least two layers of paper already during the start-up phase of the machine, the open time should include a longer period than that specified above. Open times of approximately 1 to approximately 10 seconds, for example approximately 2 to approximately 8 or approximately 4 to approximately 6 seconds, are then advantageous.

In a preferred embodiment of the invention the hot melt adhesive has no pressure sensitive properties, i.e. the surface of the hot melt adhesive is no longer tacky after the end of the open time.

The hot melt adhesive to be used in the process according to the invention is water-soluble, so that at 20 ° C. at least an amount of about 3% by weight completely dissolves in water. “Complete dissolution” is understood to mean the formation of a dispersion which is not tacky in the subsequent recycling process, but preferably a molecularly dispersed solution of the adhesive in water.

As already mentioned at the outset, the hot melt adhesives used in the process according to the invention serve, for example, to simplify the return of already bonded paper layers into the material cycle for the production of new paper layers. For this purpose, the already glued paper layers are usually mixed with water, which dissolves the hot melt adhesive and at the same time produces a pulp suitable for further processing. This water generally has a temperature which is higher than the ambient temperature, for example from about 25 to about 80.degree. In this connection, it can happen that certain polymers suitable as hot melt adhesives no longer have sufficient solubility in water at elevated temperature. The property of certain macromolecular compounds to precipitate out when a solution of the macromolecular compounds is heated is called generally "upper critical solution temperature" (UCST). As a rule, this phenomenon manifests itself in that a visible cloudiness is created by the clustering of molecules which are no longer in solution.

Similarly, certain macromolecular compounds can also show a "lower critical solution temperature" (LCST). This means that dissolved macromolecular compounds precipitate out of the solution as the temperature of the solution decreases. This also causes the solution to become cloudy.

For reasons of better observability, the term "cloud point" is used in the context of the present text, i.e. the point at which a measurable cloudiness of the aqueous solution of the hot-melt adhesive can be observed. The “upper cloud point” is understood to mean both the turbidity that results from a UCST of the hot melt adhesive, and the “lower cloud point” is a turbidity that is based on an LCST.

For example, if a hot melt adhesive consisting of different polymers is used and at least one of the polymers has a UCST and at least one of the polymers has an LCST, there is both a lower cloud point (caused by the LCST) for an aqueous solution of such a hot melt adhesive also an upper cloud point (caused by the UCST). The cloud points are given as the temperature at which a solution of the hot melt adhesive shows a cloudiness which is perceptible to the eye.

In a preferred embodiment, the water-soluble hot melt adhesive has an upper cloud point of at least about 60 ° C. with a 0.3% by weight solution of the hot melt adhesive. The cloud point is preferably 60 ° C. for a 1% by weight and in particular for a 3% by weight solution. The lower cloud point should advantageously be less than about 20 ° C with a 0.3% by weight solution of the hot melt adhesive. The cloud point is preferably less than about 20 ° C. for a 1% by weight and in particular for a 3% by weight solution. For example, the lower cloud point may be about 10 ° C or below, about 5 ° C or about 3 ° C, for the above concentrations.

In a preferred embodiment of the invention, hot-melt adhesives are used which are essentially infinitely miscible with water, ie which are at a concentration of at least about 10% by weight or more, for example about 20% by weight or about 50% by weight. or above, have no miscibility gap.

The hot melt adhesives which can be used in the context of the present invention are generally solid at room temperature and are at least partially crystalline. The degree of crystallization varies widely depending on the starting materials and the crystallization conditions. It is, for example, at least about 20 to about 100%, in particular at least about 30%, based on the degree of crystallization, of polyethylene glycol 6,000 (measured by DSC). The melting point of the hot-melt adhesives is at least about 60 ° C., however, can also be, for example, about 70 to about 100 ° C., provided that the required viscosity values of the melt are met at the processing temperature.

100% amorphous systems can also be used. However, their glass transition temperature (Tg) should be at least about 30 ° C, preferably at least about 50 ° C.

The hotmelt adhesive is generally processed by applying the adhesive to the paper layers using conventional application methods in the molten state. Suitable application methods are, for example, application by rollers, slot nozzles or spray nozzles. If a roller is used, only very high basis weights of adhesive can usually be achieved. The roller application therefore usually serves for a firm connection of the individual paper layers. Hot melt adhesives are suitable for roller application, for example, which have a melt viscosity (Brookfield Thermosel, spindle 27) of approximately 1,000 to approximately 6,000, in particular approximately 2,000 to approximately 3,000 mPas at approximately 120 to approximately 150 ° C. By means of roller application, for example, the production of moisturizing sticky materials is possible.

"Moisture-sticky materials" are understood to mean materials that can be converted into self-adhesive systems by moistening. These generally include materials that have a layer on at least one side that can be made sticky by moistening with water and applied, for example, to a second material. After the water has evaporated, the materials adhere to one another. Examples of such materials are stamps, envelopes, labels and the like.

If the hot melt adhesive is applied by means of a slot nozzle, a hot melt adhesive is generally used for this purpose, which has a melt viscosity (Brookfield Thermosel, spindle 27) of about 400 to about 20,000 mPas, in particular about 600 to about 5,000, at about 120 to about 150 ° C has mPas.

For the bonding of tissues, it is preferred to apply the hot melt adhesive by means of a spray nozzle, with no full-area application being produced. Tissue bonding can be carried out by means of atomizing as well as non-atomizing spray nozzles, in the latter case one also speaks of spin spraying.

Atomizing spray nozzles generally require a hot melt adhesive that has a melt viscosity (Brookfield Thermosel, spindle 27) of approximately 400 to approximately 10,000, in particular approximately 600 to approximately 5,000 mPas at approximately 120 to approximately 150 ° C. having. Non-atomizing spray nozzles require hot melt adhesives with a slightly higher viscosity to ensure the required thread cohesion. For example, hot melt adhesives with a melt viscosity (Brookfield Thermosel, spindle 27) of about 3,000 to about 10,000 mPas at a temperature of about 120 to about 150 ° C. are suitable.

Another object of the invention is a process for the production of moisture-sticky materials, in which a hotmelt adhesive with a solubility in water at about 20 ° C. of at least about 3% by weight is applied to a material, in particular to paper. The application is carried out by spraying or rolling processes, in particular by means of a roller.

Another object of the present invention is the use of polyalkylene glycol with a molecular weight of at least 1000 and a water solubility of at least 3 wt .-% at 20 ° C as a hot melt adhesive, in particular for the production of at least two-ply hygiene paper or moisturizing sticky materials.

Another object of the invention is the use of a nonionic polyurethane with a molecular weight (M _n ) of at least 2000 as a hot melt adhesive, in particular for the production of at least two-ply hygienic paper or moisturizing sticky materials.

The process according to the invention is explained in more detail below by examples.

Examples

Manufacture of hot melt adhesives

Examples 1 to 4

97.3 parts by weight of polyethylene glycol with an OH number of 19 (PEG 6000) were dewatered for two hours at 90 ° C. and a pressure of 1 mbar. After adding 2.7 parts by weight of TMXDI, the reaction temperature was raised to 140 ° C. while feeding in nitrogen. After a reaction time of about 2 hours, the NCO value was 0%. The substance had a melt viscosity of approx. 5,500 mPas at 150 ° C. 1, 01, 0.05 and 0.02% by weight of the UV-active fluorescent dye Uvitex OB, the finished hot melt adhesive, were mixed in the melt at 140 ° C.

Examples 5 to 11

The polyurethanes listed in Table 1 below were prepared analogously to the process described in Example 1.

The following fluorescent dyes were added to the hot melt adhesives in an amount of 0.05% by weight, based on the hot melt adhesive as a whole:

The above hot melt adhesives were used to produce two-ply paper composites, namely by spraying the melt on nozzles at 150 ° C.

The spray pattern was checked by exposing a sample of the delaminated paper composite to which the hot melt adhesive had been applied in a darkened box to the light of a UV lamp (254 nm). The distribution of the adhesive was assessed visually. Table 1

Claims

claims

1. A process for producing at least two-day paper composites, in which a water-soluble hot melt adhesive is applied to a first paper layer and at least one second paper layer is laminated onto the adhesive side of the first paper layer, the solubility of the hot melt adhesive in water at 20 ° C. being at least 3% by weight. is and the hot melt adhesive contains a UV-active fluorescent dye in a detectable amount.

2. The method according to claim 1, characterized in that a 0.3 wt .-% solution of the hot melt adhesive in water has an upper cloud point of at least 60 ° C.

3. The method according to any one of claims 1 or 2, characterized in that the hot melt adhesive at a temperature of 100 to 180 ° C has a melt viscosity (Brookfield Thermosel, spindle 27) of 400 to 20,000 mPas.

4. The method according to any one of claims 1 to 3, characterized in that the hot melt adhesive has an open time of at least 0.2 seconds.

5. The method according to any one of claims 1 to 4, characterized in that the hot melt adhesive has a crystallinity (measured by means of DSC) of at least about 20% of the value measured for polyethylene glycol with a molecular weight (M _n ) of 6,000.

6. The method according to any one of claims 1 to 5, characterized in that a polyalkylene glycol with a molecular weight (M _n ) of 1,000 to 100,000 is used as the hot melt adhesive.

7. The method according to any one of claims 1 to 6, characterized in that at least one nonionic polyurethane with a molecular weight (M _n ) of at least 2,000 or a polyester with a molecular weight of at least about 3,000 is used as the hot melt adhesive.

8. The method according to claim 7, characterized in that the nonionic polyurethane is obtainable by reacting at least one polyisocyanate with at least one polyalkylene glycol with a molecular weight of at least 1,550.

9. Use of polyalkylene glycol with a molecular weight of at least 1,000 and a water solubility of at least 3% by weight at 20 ° C. as a hot melt adhesive.

10. Use of a nonionic polyurethane with a molecular weight (M _n ) of at least 2,000 as a hot melt adhesive.

11. Use according to claim 9 or 10, characterized in that the hot melt adhesive is used in the production of at least two-ply hygienic paper or in the production of moisturizing sticky materials.

12. The method according to claim 1, characterized by the concentration of the UV-active fluorescent dye in a range from 0.0001 to 10, in particular 0.001 to 1, 0 wt .-%, based on the hot melt adhesive as a whole.

13. The method according to claim 1, characterized by at least one UV-active fluorescent dye from the group of benzoxazole derivatives.