WO2024251528A1

WO2024251528A1 - Use of polyurethane elastomers based on or use of kit-of-parts comprising mdi-polyadipate prepolymers and polyamine chain-extenders in pulp and paper applications, preferably in the manufacture of die cutting pads, anvil covers, rollers and zero crush wheels

Info

Publication number: WO2024251528A1
Application number: PCT/EP2024/064185
Authority: WO
Inventors: Helene VIGOUROUX; Eric BONANAD; Anne-Marie MONNET; David Leger; Cedric Vartabedian; Clementine DIMECK
Original assignee: Covestro Deutschland AG
Current assignee: Covestro Deutschland AG
Priority date: 2023-06-07
Filing date: 2024-05-23
Publication date: 2024-12-12
Anticipated expiration: 2025-12-07
Also published as: EP4474401A1; CN121195002A; EP4724510A1

Abstract

The present invention relates to the use of polyurethane elastomers based on and to the use of kit-of- parts comprising MDI-polyadipate prepolymers and polyamine chain-extenders in pulp and paper applications, especially in the manufacture of die cutting pads, anvil covers, zero crush wheels and rollers, wherein the resulting products exhibit good dynamic performances, especially in terms of elongation and tear resistance.

Description

2022PF30241 – Foreign Countries 1 Use of polyurethane elastomers based on or use of kit-of-parts comprising MDI-polyadipate prepolymers and polyamine chain-extenders pulp and paper applications, preferably in the manufacture of die cutting pads, anvil covers, and zero crush wheels In 2004, the European Committee issued a directive (2004/37/EC) on the protection of employees from the risks related to exposure to carcinogens or mutagens at work. This directive was tightened in 2017 (2017/2389) to work towards a point where the use of these agents will be prohibited.4,4’-methylenebis (2-chloroaniline) (MOCA or MBOCA) has been labelled as a carcinogen under this directive. MOCA is mainly used as a hardener for polyurethane prepolymers in the manufacture of castable polyurethane products such as anvil covers, die cutting pads and zero crush wheels. These products have so far been manufactured predominantly from TDI-based prepolymers and MOCA as curative (chain extender). Other diamines have been used in combination with these prepolymers, such as 3- (Aminomethyl)-3,5,5-trimethylcyclohexan-1-amine (IPDA), 2,4-Diethyl-6-methylbenzene-1,3- diamine (DETDA), 3,5-dimethylthio-2,4-toluenediamine and 3,5-dimethylthio-2,6-toluenediamine (DMTDA). However, the direct replacement of MOCA by these diamines does not lead to the same performance in these applications, which puts a dynamic strain on the material (see experimental part). Therefore, an alternative polyurethane system had to be developed to replace MOCA without losing the dynamic performance of the material. In accordance with the present invention it has been surprisingly found that the use of polyurethane elastomers based on MDI-polyadipate prepolymers and polyamine chain-extenders in the manufacture of die cutting pads, anvil covers, rollers and zero crush wheels to good dynamic performances of these products, in particular in terms of elongation and tear resistance. US2009/076239A1 discloses in Example 30 the use of a PU elastomer, which is based on a MDI- polyadipate-prepolymer and trimethylene glycol di-p-amino-benzoate diamine as chain extender, for producing wheels. Claim 15 mentions DMTDA (dimethylthio-toluene diamine) as a further suitable chain extender. The use of PU elastomers in pulp and paper applications is not disclosed in the document. EP1950234A1 discloses a PU elastomer based on a MDI-polyadipate-prepolymer in combination with 3,5-diamino-4-chlorobenzoacid isobutylester as chain extender (examples 8 and 9). In [0029] the use of DMTDA as a further suitable chain extender is mentioned. Furthermore the document discloses the use of the PU elastomer for producing wheels (claim 4), but does not disclose its use in pulp and paper applications. US2014/194588A1 discloses a PU elastomer based on a MDI-polyadipate-prepolymer in combination with methylenedianiline as chain extender (example 3A). No other suitable chain-extenders are mentioned in this document. The elastomer can be used for producing wheels, tires and die cutting pads. 2022PF30241 – Foreign Countries 2 WO2022/238285A1 discloses polyurethane elastomers obtainable from NCO-terminated prepolymers, which are preferably derived from TDI or MDI from polyethers or polyesters, wherein in the latter case polyadipates are preferred. Apart from the NCO-terminated prepolymers the reaction mixture obligatorily contains polyether carbonate polyols and optionally polyamine and/or polyol chain extenders. The use of MDI-polyadipate-prepolymers in combination with exclusively polyamine chain- extenders or polyamine/polyol chain extenders as the main components is not disclosed. The International Application with the number PCT/EP2022/084392 (priority date December 8, 2021) discloses polyurethane elastomers obtainable from NCO-terminated prepolymers, which are preferably derived from TDI or MDI and from polyethers or polyesters. Apart from the NCO-terminated prepolymers the reaction mixture obligatorily contains a polyol mixture, obtainable by mixing polyester polyols and carbodiimides, and as a further component polyamine and/or polyol chain extenders. This International Application does not disclose the use of NCO-terminated prepolymers which are based on polyadipate polyols and have a residual monomeric diisocyanate content of at most 8 weight %. The present invention relates to the use of a polyurethane elastomer, obtained from (embodiment I) or obtainable from (embodiment II) the reaction (RE) of (A) at least one NCO-terminated prepolymer, obtainable or obtained from the reaction (RP) of (A1) at least one diphenylmethane diisocyanate, optionally modified by urethane- and/or carbodiimide-groups, (A2) at least one polyadipate polyol, with a number-average molar mass Mn of from 800 to 4000 g/mol, determined by gel permeation chromatography as specified below, and a functionality of 2 to 4, (A3) optionally at least one lactone-based polyester polyol and (A4) optionally at least one catalyst and/or at least one additive, (B) at least one chain extender, which is one of i) at least one polyamine, selected from the group consisting of isophoronediamine, ethylenediamine, 1,2-propylenediamine, 1,3-propylenediamine, N-methylpropylene- 1,3-diamine, N,N'-dimethylethylenediamine, 4,4’-methylenebis (2-chloroaniline), 2,4-toluenediamine, 2,6-toluenediamine, 6-methyl-2,4-bis(methylthio)phenylene-1,3- diamine, 2-methyl-4,6-bis(methylthio) phenylene-1,3-diamine, 3,5-diethyl-2,4- toluenediamine, 3,5-diethyl-2,6-toluenediamine, and primary mono-, di-, tri-, or tetraalkyl-substituted 4,4'-diaminodiphenylmethanes, or ii) a mixture of at least one polyamine with a functionality of at least 2 and at least one polyol with a functionality of at least 2, (C) optionally at least one catalyst, (D) optionally at least one additive and 2022PF30241 – Foreign Countries 3 (E) optionally at least one filler, with the provisio that no polyether polyols are present in the reaction (RE), and with the provisio that in embodiment II component (A) has a monomeric diisocyanate content of ≤ 8 weight %, preferably ≤ 6 weight %, determined by gas chromatography with an internal standard to DIN EN ISO 10283:2007-11, in pulp and paper applications. The present invention also relates to the use of a kit-of-parts, consisting of (embodiment III) or comprising (embodiment IV) (A) at least one NCO-terminated prepolymer, obtainable or obtained from the reaction (R_P) of (A1) at least one diphenylmethane diisocyanate, optionally modified by urethane- and/or carbodiimide-groups, (A2) at least one polyadipate polyol, with a number-average molar mass Mn of from 800 to 4000 g/mol, determined by gel permeation chromatography as specified below, and a functionality of 2 to 4, (A3) optionally at least one lactone-based polyester polyol and (A4) optionally at least one catalyst and/or at least one additive, (B) at least one chain extender, which is one of i) at least one polyamine, selected from the group consisting of isophoronediamine, ethylenediamine, 1,2-propylenediamine, 1,3-propylenediamine, N-methylpropylene- 1,3-diamine, N,N'-dimethylethylenediamine, 4,4’-methylenebis (2-chloroaniline), 2,4-toluenediamine, 2,6-toluenediamine, 6-methyl-2,4-bis(methylthio)phenylene-1,3- diamine, 2-methyl-4,6-bis(methylthio) phenylene-1,3-diamine, 3,5-diethyl-2,4- toluenediamine, 3,5-diethyl-2,6-toluenediamine, and primary mono-, di-, tri-, or tetraalkyl-substituted 4,4'-diaminodiphenylmethanes, or ii) a mixture of at least one polyamine with a functionality of at least 2 and at least one polyol with a functionality of at least 2, (C) optionally at least one catalyst, (D) optionally at least one additive and (E) optionally at least one filler, with the provisio that no polyether carbonate polyols are present in the kit-of-parts,and with the provisio that in embodiment IV component (A) has a monomeric diisocyanate content of ≤ 8 weight %, preferably ≤ 6 weight %, determined by gas chromatography with an internal standard to DIN EN ISO 10283:2007-11, in pulp and paper applications. 2022PF30241 – Foreign Countries 4 In a preferred embodiment of embodiment I and in a preferred embodiment of embodiment III component (A) has a monomeric diisocyanate of ≤ 8 weight %, preferably ≤ 6 weight %, determined by gas chromatography with an internal standard to DIN EN ISO 10283:2007-11. According to the present invention the wording “elastomeric” or “elastomer” means a polyurethane having/alternance of polyols macromolecular chains corresponding to “soft segment”, with urethane reticulation bonding to short segments called “hard segment” composed of urethane bonding. The single components of the polyurethane elastomer and/or the kit-of-parts used according to the present invention will be described in detail in the following. NCO-terminated prepolymer(s) (A): Optionally modified diphenylmethane diisocyanate(s) (A1): The at least one diphenylmethane diisocyanate, optionally modified by urethane- and/or carbodiimide- groups, is preferably selected from the group consisting of diphenylmethane-4,4'-diisocyanate (4,4’- MDI), diphenylmethane-2,4'-diisocyanate (2,4’-MDI), diphenylmethane-2,2'-diisocyanate (2,2’-MDI), diphenylmethane-2,4'-diisocyanate (2,4’-MDI)/diphenylmethane-4,4'-diisocyanate (4,4’-MDI) mixtures, urethane-modified liquid diphenylmethane-4,4'-diisocyanates and diphenylmethane-2,4'- diisocyanates and carbodiimide-modified diphenylmethane-2,2'-diisocyanates, diphenylmethane-2,4'- diisocyanates and diphenylmethane-4,4'-diisocyanates. The diisocyanates mentioned can be used individually or in the form of mixtures with one another. Component (A1) is in general used in an amount of 2 to 30 wt. % based on the total weight of the at least one NCO-terminated prepolymer (A). Polyadipate polyol(s) (A2): The at least one polyadipate polyol has a number-average molar mass Mn of from 800 to 4000 g/mol and preferably from 1500 to 2500 g/mol, wherein Mn has been determined by gel permeation chromatography. The number-average molecular weight (Mn) was determined by gel permeation chromatography (GPC) in tetrahydrofuran at 23°C. The procedure is according to DIN 55672-1: "Gel permeation chromatography, Part 1 - Tetrahydrofuran as eluent" (SECurity GPC System from PSS Polymer Service, flow rate 1.0 ml/min; columns: 2×PSS SDV linear M, 8×300 mm, 5 µm; RID detector). Polystyrene samples of known molar mass are used for calibration. The number-average molecular weight is calculated with software support. Baseline points and evaluation limits are fixed in accordance with DIN 55672 Part 1. 2022PF30241 – Foreign Countries 5 The at least one polyadipate polyol has a functionality of 2 to 4 and preferably of 2. Suitable polyadipate polyols can by way of example be produced from adipic acid and from polyhydric alcohols. For the production of the polyester polyols it can optionally be advantageous to use, instead of the adipic acid, the corresponding adipic acid derivatives, for example the carboxylic diesters having from 1 to 4 carbon atoms in the alcohol moiety, adipic acid anhydride, adipoyl chloride or mono carboxylic ester adipoyl chloride, having from 1 to 4 carbon atoms in the alcohol moiety, and mixtures thereof. Examples of polyhydric alcohols are glycols having from 2 to 10, preferably from 2 to 6, carbon atoms, for example ethylene glycol, diethylene glycol, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, 1,10- decanediol, 1,12-dodecanediol, 2,2-dimethyl-1,3 propanediol (neopentyl glycol), 1,3-propanediol, and dipropylene glycol. The polyhydric alcohols can be used alone or optionally in a mixture with one another, as required by the desired properties. Preferred polyadipate polyols used are ethanediol polyadipates, 1,4-butanediolpolyadipates, ethanediol- 1,4-butanediol-polyadipates, 1,6-hexanediol neopentyl glycol polyadipates and 1,6-hexanediol-1,4- butanediol polyadipates. The polyadipate polyols can be used individually or in the form of mixtures with one another. Component (A2) is in general used in an amount of 70 to 98 wt. % based on the total weight of the at least one NCO-terminated prepolymer (A). Lactone-based polyester polyol(s) (A3): Lactone-based polyester polyols comprise the polymerization products of lactones, for example of optionally substituted caprolactones. Preferred lactone-based polyester polyols are polycaprolactones. Component (A3) is in general used in an amount of 0 to 15 wt. %, based on the total weight of the at least one NCO-terminated prepolymer (A). Catalyst(s) and/or at least one additive(s) (A4): The at least one diphenylmethane diisocyanate-terminated prepolymer (A) according to the present invention is obtainable in the presence of optionally at least one catalyst and / or at least one additive. Suitable catalysts can optionally be used in the process of the invention. The conventional tertiary amines known from the prior art, e.g. triethylamine, dimethylcyclohexylamine, N-methylmorpholine, N,N‘-dimethylpiperazine, 2-(dimethylaminoethoxy)ethanol, diazabicyclo[2.2.2]octane (DABCO), diethylethanolamine, N-cocomorpholine, N,N-diethyl-3-diethylaminopropylamine 2022PF30241 – Foreign Countries 6 dimethylbenzylamine, 1,8-Diazabicycloundec-7-ene (DBU),triazabicyclodecene (TBD) and N- methyltriazabyclodecene (MTBD). compounds, for example titanium compounds, iron compounds, bismuth compounds, zinc compounds, or tin compounds, for example tin diacetate, tin dioctanoate, tin dilaurate, or the dialkyltin salts of aliphatic carboxylic acids, for example dibutyltin diacetate or dibutyltin dilaurate, are suitable catalysts for the production of PU elastomers. Preferred catalysts are amine compounds and/or organometallic compounds, in particular tin compounds. Suitable additives may be lubricants, for example fatty acid esters, metal soaps of these, fatty acid amides, fatty acid ester amides, and silicone compounds, anti-foaming agents, rheological agents such as viscosity regulator, jellification agents, antiblocking agents, inhibitors, stabilizers with respect to hydrolysis, UV or other light, heat, and discoloration. In another preferred embodiment, additives used in small amounts may also be customary mono-, di-, tri- or polyfunctional compounds reactive toward isocyanates in proportions of 0.001 mol% up to 2 mol%, preferably of 0.002 mol% to 1 mol%, based on the total molar amount of component A, for example as chain terminators, auxiliaries or demoulding aids. Examples include alcohols such as methanol, ethanol, n-propanol, isopropanol, n-butanol, isobutanol, sec-butanol, the isomeric pentanols, hexanols, octanols and nonanols, n-decanol, n-dodecanol, n-tetradecanol, n-hexadecanol, n-octadecanol, cyclohexanol and stearyl alcohol. Examples of suitable triols are trimethylolethane, trimethylolpropane or glycerol. Suitable higher-functionality alcohols are ditrimethylolpropane, pentaerythritol, dipentaerythritol or sorbitol. Amines such as butylamine and stearylamine or thiols. Component (A4) is in general used in an amount of 0 to 3 wt. %, preferably 0 to 1 wt. %, based on the total weight of the at least one NCO-terminated prepolymer (A). Most preferably no catalyst (A4) is used. Synthesis of the prepolymer (A): The NCO-terminated prepolymer (A) is obtained from the components as mentioned before. The preparation of a prepolymer is in general known to the skilled artisan in the art. The NCO-terminated prepolymer (A) can be obtained as follows: The provision of component (A1) is in general done in a suitable reactor under suitable conditions known to the skilled artisan, for example under vacuum, with a stirrer, and at a temperature of preferably 40 to 100 °C. Then the provision of the component (A2) and optionally (A3) and optionally (A4) is done in the same reactor under vacuum. The mixture is stirred preferably during 2 to 3 hours at a temperature between 40 and 100°C. Then the product is extracted and stored in a drum under nitrogen or vacuum. 2022PF30241 – Foreign Countries 7 Components (A1), (A2) and optionally (A3) are used in a molar ratio of isocyanate-groups of component (A1) to isocyanate-reactive groups of (A2) and optionally (A3) (sum of both, if (A3) is present) of preferably 1.5 to 4 and more preferably 1.6 to 3. The proportion of component (A), based on the total mass of the polyurethane elastomer is preferably 80% to 98% % by weight, particularly preferably 88% to 93% by weight, with the provision that the sum of components (A) and (B) in the polyurethane elastomer is 100% by weight. Component (B): Component (B) according to the present invention is at least one chain extender, which is one of i) at least one polyamine, selected from the group consisting of isophoronediamine, ethylenediamine, 1,2-propylenediamine, 1,3-propylenediamine, N-methylpropylene-1,3- diamine, N,N'-dimethylethylenediamine, 4,4’-methylenebis (2-chloroaniline), 2,4- toluenediamine, 2,6-toluenediamine, 6-methyl-2,4-bis(methylthio)phenylene-1,3-diamine, 2- methyl-4,6-bis(methylthio) phenylene-1,3-diamine, 3,5-diethyl-2,4-toluenediamine, 3,5- diethyl-2,6-toluenediamine, and primary mono-, di-, tri-, or tetraalkyl-substituted 4,4'- diaminodiphenylmethanes, or ii) a mixture of at least one polyamine with a functionality of at least 2 and at least one polyol with a functionality of at least 2. The functionality of the polyamines and polyols (B)ii) is preferably 2 or 3, and more preferably 2. In one embodiment the chain extender component (B)ii) can comprise low-molecular-weight compounds with a molar mass of 60 to 490 g/mol, preferably 62 to 400 g/mol, and particularly preferably 62 to 300 g/mol. Suitable polyamines (B)ii) are (cyclo)aliphatic diamines, for example isophoronediamine, ethylenediamine, 1,2-propylenediamine, 1,3-propylenediamine, N-methylpropylene-1,3-diamine, N,N'- dimethylethylenediamine, and aromatic diamines, for example 4,4’-methylenebis (2-chloroaniline), 2,4- toluenediamine and 2,6-toluenediamine, 6-methyl-2,4-bis(methylthio)phenylene-1,3-diamine and 2- methyl-4,6-bis(methylthio)phenylene-1,3-diamine, 3,5-diethyl-2,4-toluenediamine, and 3,5-diethyl- 2,6-toluenediamine, and primary mono-, di-, tri-, or tetraalkyl-substituted 4,4'- diaminodiphenylmethanes. In preferred embodiments 4,4’-methylenebis (2-chloroaniline) is excluded from the chain extenders according to i) and ii). 2022PF30241 – Foreign Countries 8 The at least one polyamine is preferably selected from the group consisting of isophoronediamine, 6- methyl-2,4-bis(methylthio)phenylene-1,3- and 2-methyl-4,6-bis(methylthio)phenylene-1,3- diamine. Suitable polyols are diols, such as ethanediol, 1,2-ethanediol, 1,2-propanediol, 1,3-propanediol, 1,2- butanediol, 1,3-butanediol, 1,4-butanediol, 1,5-pentanediol, 2,2-dimethylpropane-1,3-diol, 2-butyl-2- ethyl propane-l,3-diol, 2-methyl-2,4-pentane diol, 2-ethyl-1,3-hexane diol, 2-methyl-1,3-propane diol, 1,5-hexanediol, 1,6-hexanediol, 1,8-octanediol, 1,10-decanediol, 1,12-dodecanediol, 2,2,4,4- tetramethylcyclobutane-l,3-diol, 1,3-cyclopentanediol, 1,2-cyclohexanediol, 1,3-cyclohexanediol, 1,4- cyclohexanediol, 1,2-cyclohexanedimethanol, 1,3-cyclohexanedimethanol, 1,4- cyclohexanedimethanol, 1,4-cyclohexanediethanol, isosorbide, triisopropanolamine, glycerol monoesters, glycerol monoethers, trimethylolpropane monoesters, trimethylolpropane monoethers, pentaerythritol diesters, pentaerythritol diethers, and alkoxylated derivatives of any of these, diethylene glycol, triethylene glycol, tetraethylene glycol, higher poly(ethylene glycol), for example having number average molecular weights of from 220 to 2000 g/mol, dipropylene glycol, tripropylene glycol, and higher poly(propyleneglycols), alkoxylated derivative of a compound selected from the group consisting of a diacid, a diol, and a hydroxy acid, polymeric diol, preferably wherein the polymeric diol is selected from the group consisting of polyethers, polyesters, hydroxy-terminated polyolefins, polyether- copolyesters, polycarbonate-copolyesters, polyoxymethylene polymers, and alkoxylated analogs thereof, diesters of terephthalic acid with glycols having from 2 to 4 carbon atoms, for example bis(ethylene glycol)terephthlate or bis(1,4-butanediol)terephthlate, hydroxyalkylene ethers of hydroquinone, for example 1,4-di(hydroxyethyl)hydroquinone, and ethoxylated bisphenols, and also reaction products of these with ɛ caprolactone. The at least one polyol is preferably selected from the group consisting of 1,2-ethanediol, 1,3- propanediol, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, 1,8-octanediol, 1,10-decanediol, 1,12- dodecanediol, diethylene glycol, dipropylene glycol, neopentyl glycol, trimethylolpropane and 1,4- di(hydroxyethyl)hydroquinone and is more preferably selected from the group consisting of 1,3- propanediol, 1,4-butanediol, 1,6-hexanediol and trimethylolpropane. Relatively small quantities of triols may also be added. In embodiment ii) the at least one polyol (total amount of the polyols of Component (B)) is used in an maximum amount of preferably 80 wt. %, more preferably 50 wt. %, most preferred 20 wt. % based on the total weight of Component (B). Embodiment i) is preferred over embodiment ii). 2022PF30241 – Foreign Countries 9 The proportion of component (B), based on the total mass of the polyurethane elastomer is preferably 2 to 20 % by weight, particularly preferably 7 to % by weight, with the provision that the sum of components (A) and (B) in the polyurethane elastomer is 100% by weight. Catalyst(s) (C): Suitable catalysts can optionally be used in the process of the invention. The conventional tertiary amines known from the prior art, e.g. triethylamine, dimethylcyclohexylamine, N-methylmorpholine, N,N‘-dimethylpiperazine, 2-(dimethylaminoethoxy)ethanol, diazabicyclo[2.2.2]octane (DABCO), diethylethanolamine, N-cocomorpholine, N,N-diethyl-3-diethylaminopropylamine dimethylbenzylamine, 1,8-Diazabicycloundec-7-ene (DBU),triazabicyclodecene (TBD) and N- methyltriazabyclodecene (MTBD). Organometallic compounds, for example titanium compounds, iron compounds, bismuth compounds, zinc compounds, or tin compounds, for example tin diacetate, tin dioctanoate, tin dilaurate, or the dialkyltin salts of aliphatic carboxylic acids, for example dibutyltin diacetate or dibutyltin dilaurate, are suitable catalysts for the production of PU elastomers. Preferred catalysts are amine compounds and/or organometallic compounds, in particular tin compounds. The total quantity of catalysts based on the total mass of the polyurethane elastomer is generally about 0 to 5% by weight, preferably 0.0001 to 1% by weight, and particularly preferably 0.0002 to 0.5% by weight. Additive(s) D: Suitable additives may be lubricants, for example fatty acid esters, metal soaps of these, fatty acid amides, fatty acid ester amides, and silicone compounds, anti-foaming agents, rheological agents such as viscosity regulator, jellification agents, antiblocking agents, inhibitors, stabilizers with respect to hydrolysis, UV or other light, heat, and discoloration, flame retardants, dyes, pigments, inorganic and/or organic fillers, and reinforcing agents. Reinforcing agents are in particular fibrous reinforcing materials, e.g. inorganic fibers, where these are produced in accordance with the prior art and can also have been treated with a size. In a preferred embodiment, additives (D) used in small amounts may also be customary mono-, di-, tri- or polyfunctional compounds reactive toward isocyanates in proportions of 0.001 mol% up to 2 mol%, preferably of 0.002 mol% to 1 mol%, based on the total molar amount of component (A), for example as chain terminators, auxiliaries or demoulding aids. Examples include alcohols such as methanol, ethanol, n-propanol, isopropanol, n-butanol, isobutanol, sec-butanol, the isomeric pentanols, hexanols, octanols and nonanols, n-decanol, n-dodecanol, n-tetradecanol, n-hexadecanol, n-octadecanol, cyclohexanol and stearyl alcohol. Examples of suitable triols are trimethylolethane, trimethylolpropane 2022PF30241 – Foreign Countries 10 or glycerol. Suitable higher-functionality alcohols are ditrimethylolpropane, pentaerythritol, dipentaerythritol or sorbitol. Amines such as and stearylamine or thiols. The total quantity of additives based on the total mass of the polyurethane elastomer is generally about 0 to 5 % by weight, preferably 0 to 3 % by weight, and particularly preferably 0,2 to 1 % by weight. Filler(s) (E): Suitable filler are preferable mineral filler selected from the group consisting of CaCO₃, SiO₂, Al(OH)₃, Al₂O₃, CaO, MgO, Na₂O, K₂O, B₂O₃, Fe₂O₃, P₂O₅, zirconia, cerium oxide, TiO₂, silicates, in particular sodium silico-aluminate, calcium silicate, magnesium silicate, mixtures thereof as well hydrated modifications of the mentioned fillers. The at least one filler which is used according to the present invention has preferably a particle size of 1 to 10 µm, particularly preferably 2 to 8 µm, for example 5 µm. The total quantity of fillers based on the total mass of the polyurethane elastomer is generally 0 to 30 % by weight, preferably 0 to 20 % by weight, and particularly preferably 0 to 10 % by weight. Components (A) and (B) are used in a molar ratio of isocyanate-groups of component (A) to isocyanate- reactive groups of component (B) of preferably 0.90 to 1.10 and more preferably 0.95 to 1.05. The polyurethane elastomer used according to the present invention is obtained from the components as mentioned before. The preparation of the polyurethane elastomer is in general known to the skilled artisan in the art. The polyurethane elastomer can be obtained as follows: In a preferred embodiment component (A) is provided in a suitable reactor and component (B), optionally (C), optionally (D) and optionally (E) are added to component (A), wherein components (C), (D) and (E) can be added, independently of each other, before or after component (B) is added or in admixture with component (B). In an preferred embodiment of the foregoing embodiment component (A) is preheated at 60 to 100°C, preferably 60 to 85°C, before components (B) optionally (C), optionally (D) and optionally (E) are added. The provision, the measuring and the metering of the single components (A) to (E) can be done by any method that is known to the skilled artisan, for example by hand, with the use of a balance, by syringes, pumps, automatic weighing in the reactor, low pressure dispensing machine etc. 2022PF30241 – Foreign Countries 11 After all components (A), (B), optionally (C), (E) are present in the reactor, preferably under an inert atmosphere, mixing is done for a time of for example 10 seconds to 3 minutes, preferably 30 to 90 seconds. In parallel to the mixing or after the mixing, the mixture is preferably degassed in a vacuum chamber, in particular according to methods known to the skilled artisan, until the mixture is bubble free, for example for 10 seconds to 2 minutes. Next, the mixture is preferably poured into an open or closed mold, preferably at a temperature of 20 to 120 °C, and then cured for 0.1 to 48 hours, preferably at a temperature of 20 to 120 °C. The mold as such is also known to the skilled artisan. The polyurethane elastomer is preferably demolded after a certain demolding time, for example 1 minutes to 2 hours, preferably 1 minute to one hour. Optionally, a so-called maturation step can then be conducted to complete curing and reticulation. This is for example done by setting the cast polyurethane elastomer for 2 to 14 days at a temperature of 10 to 40 °C at 30 to 70% air humidity. The polyurethane cast elastomers according to the present invention have good mechanical properties. The tensile strength of the polyurethane elastomers according to the present invention is at least 40 MPa, preferably at least 45 MPa, each acquired according to DIN 53504 (2009). The tear strength of the polyurethane elastomers according to the present invention is at least 100 kN/m, preferably at least 120 kN/m, each acquired according to ISO 34-1 (2010). The elongation of the polyurethane elastomers according to the present invention is at least 600 %, preferably at least700 %, each acquired according to DIN53504 (2009). The abrasion loss of the polyurethane elastomers according to the present invention is at most 50 mm3, preferably at most 35 mm3, each acquired according to ISO 4649 (2017). The present application relates to the use of a polyurethane elastomers as described above or the kit-of- parts as described above in pulp and paper applications. The pulp and paper applications, which the elastomers and kit-of parts described above may be used in, are preferably die cutting pads, anvil covers, rollers and zero crush wheels, preferably anvil covers. 2022PF30241 – Foreign Countries 12 Therefore the present application also relates to the use of a polyurethane elastomers as described above or the kit-of-parts as described above in the of die cutting pads, anvil covers, zero crush wheels and rollers, preferably in the manufacture of anvil covers. The present application also relates to die cutting pads, anvil covers, rollers and zero crush wheels produced by use of a polyurethane elastomer as described above or of a kit-of-parts as described above. The present application also relates to die cutting pads, anvil covers, zero crush wheels and rollers , preferably anvil covers, comprising or consisting of a polyurethane elastomer as described above or a kit-of-parts as described above. Zero crush wheels do not have a compact structure and therefore are not suitable for transport. Examples of industrial uses of zero crush wheels are: - Hold-Down Wheels for the corrugated cardboard and packaging industry - Bottle Spacing Wheels to allow for bottles and other containers to pass by - Labeling Wheels to provide pressure for labels to be applied to objects - Flex-Grip Wheels to give maximum surface area onto objects being moved - Metering Wheels to only allow objects to pass by at the proper time The present invention is elucidated by the following examples.

2022PF30241 – Foreign Countries 13 Examples Hydroxyl Commercial molecu Supplier Type value or Amine lar weight f initiato name amine number (mmol/g) unctionality ) (g rs (mgKOH/g /mol) DESMODUR® T80 Covestro Toluene-2,4-diisocyanate 80% Toluene-2,6-diisocyanate 20% - - 174,2 2 - DESMODUR® T100 Covestro Toluene-2,4-diisocyanate 100% - - 174,2 2 - 4,4'-Methylene diphenyl DESMODUR® diisocyanate : ≥ 99% 0118 T Covestro / 2,4-Methylene diphenyl - - 250,25 2 - diisocyanate: ≤ 1% DESMOPHEN® Covestro Polyadipate p Adipic 20555-1A olyol 56 - - 2 acid DESMOPHEN® Covestro Polyad Adipic 1000 EING. ipate polyol 112 - - 2 acid BAYTEC® XL1705 Covestro Dimethylthiotoluenediamine (DMTDA) 531 214,4 2 - MOCA Suzhou 4,4′-Methylenebis(2-chloroaniline) - 7,5 267,15 2 - CATALYST SD2.4 Covestro Tin based catalyst - - - - - Test methods: Hydroxyl value : Measurements of Hydroxyl value (mgKOH/g) were done in accordance with norm ISO 4629-2 (2016). Mn determination : The number-average molecular weight (Mn) was determined by gel permeation chromatography (GPC) in tetrahydrofuran at 23°C. The procedure is according to DIN 55672-1: "Gel permeation chromatography, Part 1 - Tetrahydrofuran as eluent" (SECurity GPC System from PSS Polymer Service, flow rate 1.0 ml/min; columns: 2×PSS SDV linear M, 8×300 mm, 5 µm; RID detector). Polystyrene samples of known molar mass are used for calibration. The number-average molecular weight is calculated with software support. Baseline points and evaluation limits are fixed in accordance with DIN 55672 Part 1. Isocyanate value : Measurements of Isocyanate value (%) were done in accordance with ISO 14896:2009 Isocyanate monomers determination : Measurements of Isocyanate monomers value (%m) were done in accordance with DIN EN ISO 10283:2007-11 “Determination of monomeric diisocyanates in isocyanate resins”. Elongation: Measurements of elongation were done in accordance with DIN 53504 (2009) at a pulling rate of 500 mm/min. 2022PF30241 – Foreign Countries 14 Tensile strength : Measurements of the tensile strength were done accordance with DIN 53504 (2009) at a pulling rate of 500 mm/min. Tear resistance : Measurements of Tear resistance were done in accordance with ISO 34-1 (2010). Abrasion : Measurements of Abrasion were done in accordance with ISO 4649 (2017). Preparation of Prepolymers from A to D Prepolymer A: The components were first preheated to 50°C. In a reactor heated to 80°C under stirring and vacuum, 141 g of DESMODUR® T100 and 33g of DESMODUR® T80 were incorporated. 723 g of DESMOPHEN® 20555-1A and 103 g of DESMOPHEN® 1000 EING. were added, the mixture was homogenized during 16 at 80°C. Then the isocyanate value was measured in accordance with ISO 14896:2009 and 4,3% was found. The obtained material was then stored under nitrogen in a container and put aside. Prepolymer B: The components were first preheated to 50°C. In a reactor heated to 80°C under stirring and vacuum, 351 g of DESMODUR® 0118T were incorporated. 432 g of DESMOPHEN® 20555-1A and 216 g of DESMOPHEN® 1000 EING. were added, the mixture was homogenized during 2 hours at 80°C. Then the isocyanate value was measured in accordance with ISO 14896:2009 and 8,0% was found. The obtained material was then stored under nitrogen in a container and put aside. Prepolymer C: The components were first preheated to 50°C. In a reactor heated to 80°C under stirring and vacuum, 331 g of DESMODUR® 0118T were incorporated.669 g of DESMOPHEN® 20555-1A were added, the mixture was homogenized during 2 hours at 80°C. Then the isocyanate value was measured in accordance with ISO 14896:2009 and 8,2% was found. The obtained material was then stored under nitrogen in a container and put aside. Prepolymer D: The components were first preheated to 50 °C. In a reactor heated to 80°C under stirring and vacuum, 217 g of DESMODUR® 0118T were incorporated.778 g of DESMOPHEN® 20555-1A were added, the mixture was homogenized during 2 hours at 80°C. Then the isocyanate value was measured in accordance with ISO 14896:2009 and 4,0% was found. The obtained material was then stored under nitrogen in a container and put aside. The isocyanate monomers of the prepolymers were measured in accordance with ISO 10283:2007 and the values are shown in the table below. 2022PF30241 – Foreign Countries 15 Prepolymer A B C D Isocyanate monomers 2,7% TDI MDI 12,2% MDI 4,0% MDI content (in mass %) In the state of the art, it is known that MDI prepolymers with standard free monomer content (above 10% approximately) are extended with alcohol chain extenders to avoid too short pot lives, and then not castable products. Preparation of polyurethane elastomers Example 1 (PU A1 : comparative example): 100 g of Prepolymer A preheated at 80°C was weighted in a flask.13 g of MOCA was added and the mixture was stirred during 30 seconds to 1 minute. Then vacuum was applied to degas the reaction mixture until bubble free. The mixture was poured into a closed mold at a temperature of 110°C for 30 minutes. Then, the part was demolded and post cured at 110°C for 16 hours. The sheet was matured 7 days at 23°C and 50% relative humidity. Example 2 (PU A2 : comparative example) 100 g of Prepolymer A preheated at 80°C was weighted in a flask. 10,4 g of BAYTEC® XL1705 was added and the mixture was stirred during 30 seconds to 1 minute. Then vacuum was applied to degas the reaction mixture until bubble free. The mixture was poured into a closed mold at a temperature of 110°C for 30 minutes. Then, the part was demolded and post cured at 110°C for 16 hours. The sheet was matured 7 days at 23°C and 50% relative humidity. Example 3 (PU B : comparative example) 0,05 g of CATALYST SD2.4 was weighted in a flask and 8,4 g of BAYTEC XL® B was added. Then 100 g of Prepolymer B preheated at 80°C was weighted and the mixture was stirred during 30 seconds to 1 minute. Then vacuum was applied to degas the reaction mixture until bubble free. The mixture was poured into a closed mold at a temperature of 110°C for 30 minutes. Then, the part was demolded and post cured at 100°C for 24 hours. The sheet was matured 7 days at 23°C and 50% relative humidity. Example 4 (PU C : comparative example) 100 g of Prepolymer C preheated at 80°C was weighted in a flask.8,6 g of BAYTEC® XL B was added and the mixture was stirred during 30 seconds to 1 minute. Then vacuum was applied to degas the reaction mixture until bubble free. The mixture was poured into a closed mold at a temperature of 110°C for 30 minutes. Then, the part was demolded and post cured at 110°C for 16 hours. The sheet was matured 7 days at 23°C and 50% relative humidity. Example 5 (PU D : according to the invention) 100 g of Prepolymer D preheated at 80°C was weighted in a flask. 9,8 g of BAYTEC® XL 1705 was added and the mixture was stirred during 30 seconds to 1 minute. Then vacuum was applied to degas the reaction mixture until bubble free. The mixture was poured into a closed mold at a temperature of 100°C for 30 minutes. Then, the part was demolded and post cured at 110°C for 24 hours. The sheet was matured 7 days at 23°C and 50% relative humidity. 2022PF30241 – Foreign Countries 16 Results : Elastomers properties Property Standard Unit PU A1 PU A2 PU B PU C PU D Tensile strength DIN 53504 MPa 49 52 52 52 52 Elongation DIN 53504 % 510 660 620 630 750 Tear strength ISO 34-1 kN/m 114 107 125 147 130 Abrasion loss ISO 4649 mm³ 35 55 35 30 33

Claims

2022PF30241 – Foreign Countries 17 Claims: 1. Use of a polyurethane elastomer, obtained from (embodiment I) or obtainable from (embodiment II) the reaction (R_E) of (A) at least one NCO-terminated prepolymer, obtainable or obtained from the reaction (R_P) of (A1) at least one diphenylmethane diisocyanate, optionally modified by urethane- and/or carbodiimide-groups, (A2) at least one polyadipate polyol, with a number-average molar mass Mn of from 800 to 4000 g/mol, wherein Mn has been determined by gel permeation chromatography as referred to in the specification, and a functionality of 2 to 4, (A3) optionally at least one lactone-based polyester polyol and (A4) optionally at least one catalyst and/or at least one additive, (B) at least one chain extender, which is one of i) at least one polyamine, selected from the group consisting of isophoronediamine, ethylenediamine, 1,2-propylenediamine, 1,3-propylenediamine, N-methylpropylene- 1,3-diamine, N,N'-dimethylethylenediamine, 4,4’-methylenebis (2-chloroaniline), 2,4-toluenediamine, 2,6-toluenediamine, 6-methyl-2,4-bis(methylthio)phenylene-1,3- diamine, 2-methyl-4,6-bis(methylthio) phenylene-1,3-diamine, 3,5-diethyl-2,4- toluenediamine, 3,5-diethyl-2,6-toluenediamine, and primary mono-, di-, tri-, or tetraalkyl-substituted 4,4'-diaminodiphenylmethanes, or ii) a mixture of at least one polyamine with a functionality of at least 2 and at least one polyol with a functionality of at least 2, (C) optionally at least one catalyst, (D) optionally at least one additive and (E) optionally at least one filler, with the provisio that no polyether carbonate polyols are present in the reaction (RE), and with the provisio that in embodiment II component (A) has a monomeric diisocyanate content of ≤ 8 weight %, preferably ≤ 6 weight %, determined by gas chromatography with an internal standard to DIN EN ISO 10283:2007-11, in pulp and paper applications. 2. Use of a kit-of-parts, consisting of (embodiment III) or comprising (embodiment IV) (A) at least one NCO-terminated prepolymer, obtainable or obtained from the reaction (R_P) of (A1) at least one diphenylmethane diisocyanate, optionally modified by urethane- and/or carbodiimide-groups, 2022PF30241 – Foreign Countries 18 (A2) at least one polyadipate polyol, with a number-average molar mass Mn of from 800 to 4000 g/mol, Mn has been determined by gel permeation chromatography as referred to in the specification, and a functionality of 2 to 4, (A3) optionally at least one lactone-based polyester polyol and (A4) optionally at least one catalyst and/or at least one additive, (B) at least one chain extender, which is one of i) at least one polyamine, selected from the group consisting of isophoronediamine, ethylenediamine, 1,2-propylenediamine, 1,3-propylenediamine, N-methylpropylene- 1,3-diamine, N,N'-dimethylethylenediamine, 4,4’-methylenebis (2-chloroaniline), 2,4-toluenediamine, 2,6-toluenediamine, 6-methyl-2,4-bis(methylthio)phenylene-1,3- diamine, 2-methyl-4,6-bis(methylthio) phenylene-1,3-diamine, 3,5-diethyl-2,4- toluenediamine, 3,5-diethyl-2,6-toluenediamine, and primary mono-, di-, tri-, or tetraalkyl-substituted 4,4'-diaminodiphenylmethanes, or ii) a mixture of at least one polyamine with a functionality of at least 2 and at least one polyol with a functionality of at least 2, (C) optionally at least one catalyst, (D) optionally at least one additive and (E) optionally at least one filler, with the provisio that no polyether carbonate polyols are present in the kit-of-parts,and with the provisio that in embodiment IV component (A) has a monomeric diisocyanate content of ≤ 8 weight %, preferably ≤ 6 weight %, determined by gas chromatography with an internal standard to DIN EN ISO 10283:2007-11, in pulp and paper applications. 3. Use of a polyurethane elastomer according to claim 1 or use of a kit-of-parts according to claim 2, wherein the at least one diphenylmethane diisocyanate, optionally modified by urethane- and/or carbodiimide-groups (A1), is selcted from the group consisting of diphenylmethane-4,4'- diisocyanate (4,4’-MDI), diphenylmethane-2,4'-diisocyanate (2,4’-MDI), diphenylmethane-2,2'- diisocyanate (2,2’-MDI), diphenylmethane-2,4'-diisocyanate (2,4’-MDI)/diphenylmethane-4,4'- diisocyanate (4,4’-MDI) mixtures, urethane-modified liquid diphenylmethane-4,4'-diisocyanates and diphenylmethane-2,4'-diisocyanates and carbodiimide-modified diphenylmethane-2,2'- diisocyanates, diphenylmethane-2,4'-diisocyanates and diphenylmethane-4,4'-diisocyanates. 4. Use of a polyurethane elastomer according to claim 1 or 3 or use of a kit-of-parts according to claim 2 or 3, wherein the at least one at least one polyadipate polyol (A2) is produced from adipic acid and/or at least one adipic acid derivative and from at least one polyhydric alcohol, wherein the at least one polyhydric alcohol is selected from the group consisting of ethylene glycol, diethylene 2022PF30241 – Foreign Countries 19 glycol, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, 1,10-decanediol, 1,12-dodecanediol, 2,2- dimethyl-1,3 propanediol (neopentyl glycol), propanediol, and dipropylene glycol. 5. Use of a polyurethane elastomer according to any of claims 1, 3 or 4 or use of a kit-of-parts according to any of claims 2, 3 or 4, wherein components (A1), (A2) and optionally (A3) are used in a molar ratio of isocyanate-groups of component (A1) to isocyanate-reactive groups of component (A2) and optionally (A3) of preferably 1.5 to 4 and more preferably 1.6 to 3. 6. Use of a polyurethane elastomer according to any of claims 1 or 3 to 5 or use of a kit-of-parts according to any of claims 2 to 5, wherein the at least one polyamine of chain extender component Bii) is selected from the group consisting of isophoronediamine, ethylenediamine, 1,2- propylenediamine, 1,3-propylenediamine, N-methylpropylene-1,3-diamine, N,N'- dimethylethylenediamine, and aromatic diamines, for example 4,4’-methylenebis (2-chloroaniline), 2,4-toluenediamine and 2,6-toluenediamine, 6-methyl-2,4-bis(methylthio)phenylene-1,3-diamine and 2-methyl-4,6-bis(methylthio)phenylene-1,3-diamine, 3,5-diethyl-2,4-toluenediamine, and 3,5- diethyl-2,6-toluenediamine, and primary mono-, di-, tri-, or tetraalkyl-substituted 4,4'- diaminodiphenylmethanes. 7. Use of a polyurethane elastomer according to any of claims 1 or 3 to 6 or use of a kit-of-parts according to any of claims 2 to 6, wherein the at least one polyol of chain extender component Bii) is used in an maximum amount of preferably 80 wt. %, more preferably 50 wt. %, most preferred 20 wt. % based on the total weight of Component (B). 8. Use of a polyurethane elastomer according to any of claims 1 or 3 to 6 or use of a kit-of-parts according to any of claims 2 to 6, wherein component B) consists of polyamines exclusively (embodiment i). 9. Use of a polyurethane elastomer according to any of claims 1 or 3 to 8 or use of a kit-of-parts according to any of claims 2 to 8, wherein the pulp and paper application is the manufacture of die cutting pads, of anvil covers, rollers or zero crush wheels. 10. Die cutting pads, anvil covers, zero crush wheels or rollers comprising or consisting of a polyurethane elastomer as specified in any of claims 1 or 2 to 8 or a kit-of-parts as specified in any of claims 2 to 8.