Three dimensional deposition method to create layers of polymeric material onto an object

Abstract

A process for providing one or more thermoset polymeric materials onto an object is disclosed wherein said process comprises at least the following steps: Providing a polymeric composition having a viscosity >10 Pa.s at room temperature comprising at least one cross-linkable polymeric material; and then Optionally heating the polymeric composition to achieve a liquid cross-linkable polymeric composition having a viscosity below 4 Pa.s, and then Depositing the polymeric composition onto an object using a spray, swirl or extrusion nozzle and wherein the deposition is performed while the object and/or nozzle are moving to create an object at least partly coated with said polymeric composition; and then Optionally cooling down the at least partly coated object to room temperature, and then Optionally repeating one of foregoing steps, and then Applying a cross-linking treatment selected from radical curing, UV curing and/or heat treatment in order to convert the cross-linkable polymeric material(s) into thermoset polymeric material(s).

Claims

1. A process for producing a three dimensional object made of one or more thermoset polymeric materials having elastomeric properties, said process having at least the following steps: providing a thermoplastic polymeric composition having a viscosity >10 Pa.s at room temperature measured according to ASTM D445-11a and comprising at least one cross-linkable thermoplastic polyurethane material containing radically polymerizable unsaturated groups; and then heating the polymeric composition to achieve a liquid cross-linkable polymeric composition having a viscosity below 4 Pa.s measured according to ASTM D445-11a, and then depositing the polymeric composition onto a pre-shaped object using a spray, swirl, or extrusion nozzle and wherein the deposition is performed while the pre-shaped object or nozzle are moving to at least partly coat the pre-shaped object with said polymeric composition; and then optionally, cooling down the at least partly coated pre-shaped object to room temperature, and then optionally, repeating one of foregoing steps, and then applying a cross-linking treatment selected from radical curing, UV curing, or heat treatment in order to convert the cross-linkable thermoplastic polyurethane material(s) into a cross-linked thermoset polymeric material(s); and removing the pre-shaped object from the cross-linked thermoset polymeric material(s) after the cross-linking step, optionally with the aid of a release agent, and wherein the cross-linked thermoset polymeric material defines the three dimensional object made of the thermoset polymeric material.

2. The process according to claim 1, wherein the step of depositing the polymeric composition onto the pre-shaped object using a spray, swirl, or extrusion is performed while the pre-shaped object is moving and the nozzle is fixed.

3. The process according to claim 1, wherein the polymeric composition is heated up to temperatures in the range 60° C.-120° C. before deposition.

4. The process according to claim 1, wherein the step of depositing the polymeric composition onto the pre-shaped object is performed while the pre-shaped object has a temperature below the temperature of the resin having a viscosity below 4 Pa.s.

5. The process according to claim 1, wherein the at least one cross-linkable thermoplastic polyurethane material is having thermoplastic polyurethane chains containing radically polymerizable unsaturated groups at the end of the thermoplastic polyurethane chains and one or more ethylenically unsaturated compounds serving as co-cross linker.

6. The process according to claim 1, wherein the cross-linkable polymeric material comprises a cross-linkable thermoplastic polyurethane having radically polymerizable unsaturated groups selected from the group consisting of polyalkylene glycol mono methacrylates and/or polyalkylene glycol mono acrylates and combinations thereof and wherein said thermoplastic polyurethane has a number average molecular weight in the range 5000-12000 g/mol.

7. The process according to claim 1, wherein the cross-linkable polymeric material comprises a cross-linkable thermoplastic polyurethane having radically polymerizable unsaturated groups at the end of the TPU chains and one or more ethylenically unsaturated compounds serving as co-cross linker wherein said ethylenically unsaturated compounds are selected from the group consisting of mono acrylates and/or mono methacrylates and combinations thereof.

8. The process according to claim 1, wherein the thickness of the deposited thermoset polymeric material(s) is in the range of 0.05 mm up to 5 mm.

9. The process according to claim 1, wherein the pre-shaped object is a shoe sock and the three dimensional object is at least part of a shoe upper.

10. The process according to claim 1, wherein the at least partly coated object comprises thermoset elastomeric polymeric materials with different mechanical properties and/or thermo stability properties and/or colours.

Description

DETAILED DESCRIPTION

(1) According to a first aspect of the invention, a process is disclosed for providing (at least partly) a polymeric material, said polymeric material preferably having elastomeric properties, onto an object thereby avoiding the use of glue and/or stitches. Said polymeric material being a thermoset polymeric material.

(2) The process for providing parts of a thermoset polymeric material onto an object is further characterized as an automated process wherein several layers or parts of different thermoset polymeric material(s) may be provided onto said object in order to build up an object having a variety of physical attributes, including grip, abrasion resistance and shock absorption very high tensile and tear strength, high flexibility at low temperatures, extremely good abrasion and scratch resistance and/or to create additional decoration.

(3) Therefore, the present invention provides a method which makes it possible to deposit a thermoset polymeric material onto an object, said method characterized as being time and cost efficient and thereby avoiding the use of glue and/or stitches.

(4) According to embodiments, the method according to the invention is able to convert a thermoplastic polymeric material after deposition (e.g. after spraying) into a thermoset polymeric material.

(5) The present invention therefore provides a novel deposition process which makes it possible to provide at least one thermoset polymeric material onto an object in order to form a 3 dimensional object which is at least partly coated with said thermoset polymeric material, said process having at least the following steps: Provide a thermoplastic polymeric composition comprising at least one cross-linkable polymeric material having a viscosity >10 Pa.s at room temperature; and then Optionally heat the polymeric composition to achieve a liquid polymeric composition having a viscosity below 4 Pa.s, and then Deposit the polymeric composition using a spray, swirl or extrusion nozzle onto an object to create an at least partly coated object wherein the object and/or nozzle is moving; and then Optionally cool down the at least partly coated object to room temperature, and then Optionally repeat foregoing steps, and then Apply a cross-linking treatment selected from radical curing, UV curing and/or heat treatment in order to convert the cross-linkable polymeric material(s) into thermoset polymeric material(s).

(6) According to embodiments, the object in the deposition process according to the invention may be an intermediate or temporary object which can be removed after the cross-linking step, optionally with the aid of a release agent, and the deposited cross-linked thermoset polymeric material defines a three dimensional object made of at least one thermoset polymeric material. The deposition method according to the invention thereby avoids or eliminates the use of moulds.

(7) According to embodiments, the step of depositing the thermoplastic polymeric composition onto the object using a spray, swirl or extrusion nozzle is performed while the object is having a temperature below the temperature of the thermoplastic polymeric composition (said polymeric composition being at a temperature at which the viscosity is below 4 Pa.s) such that dripping of the polymeric composition on/from the object is avoided. Using a thermoplastic polymeric composition having a viscosity at room temperatures>10 Pa.s and spraying of the polymeric composition at temperatures such that the polymeric composition has a viscosity<4 Pa.s onto the object being at temperatures below the temperature at which the polymeric composition has a viscosity<4 Pa.s makes sure that the polymeric material is not dripping from the object.

(8) According to embodiments, the nozzle in the deposition process according to the invention may be a swirl nozzle, more in particular a precision (pressure) swirl nozzle, preferably said spray nozzle is airless. These nozzles are known for their high-performance and creation of small droplet sizes. The stationary core induces a rotary fluid motion which causes the swirling of the fluid in the swirl chamber. A film is discharged from the perimeter of the outlet orifice producing a characteristic hollow cone spray pattern.

(9) According to embodiments, the deposition process is preferably performed using airless or gasless spray techniques in order to avoid inclusion of oxygen (O.sub.2) because O.sub.2 could hinder the UV polymerization. Alternatively, the deposition process may be performed using inert gases such as nitrogen (N.sub.2).

(10) According to embodiments, the thickness of the deposited thermoplastic polymeric composition in the deposition process according to the invention is depending on the type and deposition velocity of the nozzle and the (melt) viscosity of the thermoplastic polymeric composition at the deposition temperature.

(11) According to embodiments, the object, which may be a pre-shaped and/or intermediate object onto which thermoplastic polymeric material is provided using the spray process according to the invention is a shoe sock and the sprayed thermoplastic polymer creates at least part of a shoe upper.

(12) According to embodiments, the at least partly coated object (after depositing the polymeric composition(s)) according to the invention may comprise several (different) thermoset polymer materials with different mechanical properties and/or thermo stability properties and/or colours.

(13) According to embodiments, the at least one cross-linkable polymeric material may be selected from a thermoplastic polyurethane material.

(14) According to embodiments, the thermoplastic polymeric composition is having a viscosity above 10 Pa.s. at room temperature (temperature of about 20° C.), preferably the thermoplastic polymeric composition is having a viscosity above 20 Pa.s. at room temperature.

(15) According to embodiments, the at least one cross-linkable polymeric material suitable for use in the deposition process according to the invention may be cross-linkable thermoplastic polyurethane (TPU). TPU has the additional advantage that it is known to have intrinsic good adhesion with polyurethane (PU) which avoids the use of additional glue.

(16) According to embodiments, the at least one cross-linkable polymeric material suitable for use in the deposition process according to the invention may be selected from cross-linkable thermoplastic polyurethane (TPU) wherein the TPU chains contain radically polymerizable unsaturated groups at the end of the TPU chains and one or more ethylenically unsaturated compounds serving as co-cross linker. TPU's are also known for their superior dynamic properties, in particular, very high rebound figures, low compression set and hysteresis loss.

(17) According to embodiments, the at least one cross-linkable polymeric material suitable for use in the deposition process according to the invention may be selected from a cross-linkable thermoplastic polyurethane (TPU) having radically polymerizable unsaturated groups selected from the group of polyalkylene glycol mono methacrylates and/or polyalkylene glycol mono acrylates and combinations thereof at the end of the TPU chains and wherein said TPU has a number average molecular weight in the range 5000 g/mol to 12000 g/mol. Preferably said TPU has a number average molecular weight of 5000 g/mol to 12000 g/mol, more preferably between 5000 g/mol and 10000 g/mol, most preferably between 5000 g/mol and 8000 g/mol.

(18) According to embodiments, the at least one cross-linkable polymeric material suitable for use in the deposition process according to the invention may be selected from a cross-linkable thermoplastic polyurethane (TPU) having radically polymerizable unsaturated groups at the end of the TPU chains and one or more ethylenically unsaturated compounds serving as co-cross linker wherein said ethylenically unsaturated compounds are selected from mono acrylates and/or mono methacrylates and combinations thereof.

(19) According to embodiments, the at least one cross-linkable polymeric material suitable for use in the deposition process according to the invention may be selected from a cross-linkable thermoplastic polyurethane (TPU) and may be obtained according to the methods described in WO2012/004088 which is incorporated herein by reference.

(20) According to embodiments, the cross-linkable thermoplastic polyurethanes (TPU) suitable for use in the deposition process according to the invention may be obtained by mixing and reacting at least following ingredients: one or more polyfunctional isocyanates, one or more polyfunctional polyols, and one or more monols or monoamines comprising radically polymerizable unsaturation(s), and optionally one or more diol chain extenders
together with one or more ethylenically unsaturated compounds serving as reactive diluent (also called co-cross-linker) to create cross linking of the final thermoplastic polyurethane.

(21) According to embodiments, the cross-linking reaction of the cross-linkable thermoplastic TPU polymeric material(s) takes place after the process of depositing the cross-linkable mixture onto an object and during the step of applying a cross-linking treatment selected from radical curing, UV curing and/or heat treatment.

(22) The reactants for forming the cross-linkable thermoplastic polyurethane (TPU) suitable for use in the deposition process according to the invention are generally selected from: one or more polyfunctional isocyanates, preferably difunctional polyisocyanates, and one or more difunctional hydroxy compounds, and one or more mono functional hydroxy and/or amine compounds comprising radically polymerizable unsaturation(s) serving as chain stopper, and optionally one or more chain extenders (typically a low molecular weight diol)
in such amounts that the isocyanate index is generally between 80 and 110%, preferably between 96 and 102%. The polyfunctional, preferably difunctional isocyanates may comprise any aliphatic, cycloaliphatic or aromatic isocyanates.

(23) The one or more polyfunctional isocyanates used for forming the cross-linkable thermoplastic polyurethane (TPU) suitable for use in the deposition process according to the invention may consist essentially of pure 4,4′-diphenylmethane diisocyanate or mixtures of that diisocyanate with one or more other organic polyisocyanates, especially other diphenylmethane diisocyanates (MDI), for example the 2,4′-isomer optionally in conjunction with the 2,2′-isomer. The one or more polyfunctional isocyanates may also be an MDI variant derived from a polyisocyanate composition containing at least 95% by weight of 4,4′-diphenylmethane diisocyanate. Preferred polyfunctional isocyanates are those containing at least 90% by weight of 4,4′-diphenylmethane diisocyanate or its hydrogenated derivative. More preferably, the 4,4′-diphenylmethane diisocyanate content is at least 95% by weight, and most preferably at least 98% by weight.

(24) The one or more difunctional hydroxy compounds, preferably diols, used for forming the cross-linkable thermoplastic polyurethane (TPU) suitable for use in the deposition process according to the invention generally have a molecular weight of between 500 and 20000 and may be selected from polyesteramides, polythioethers, polycarbonates, polyacetals, polyolefins, polysiloxanes and, especially, polyesters and polyethers or mixtures thereof.

(25) Polyether diols used for forming the cross-linkable thermoplastic polyurethane (TPU) suitable for use in the deposition process according to the invention may include products obtained by the polymerization of a cyclic oxide, for example ethylene oxide, propylene oxide, butylene oxide or tetrahydrofuran in the presence, where necessary, of difunctional initiators. Suitable initiator compounds contain 2 active hydrogen atoms and include water, butanediol, ethylene glycol, propylene glycol, diethylene glycol, triethylene glycol, dipropylene glycol, 1,3-propane diol, neopentyl glycol, 1,4-butanediol, 1,5-pentanediol, 2-methyl-1,3-propanediol, 1,6-pentanediol and the like. Mixtures of initiators and/or cyclic oxides may be used.

(26) Polyester diols used for forming the cross-linkable thermoplastic polyurethane (TPU) suitable for use in the deposition process according to the invention may include hydroxyl-terminated reaction products of dihydric alcohols such as ethylene glycol, propylene glycol, diethylene glycol, 1,4-butanediol, neopentyl glycol, 2-methyl-1,3-propanediol, 1,6-hexanediol or cyclohexane dimethanol or mixtures of such dihydric alcohols, and dicarboxylic acids or their esterforming derivatives, for example succinic, glutaric and adipic acids or their dimethyl esters, sebacic acid, phthalic anhydride, tetrachlorophthalic anhydride or dimethyl terephthalate or mixtures thereof. Polycapro lactones and unsaturated polyesterpolyols should also be considered.

(27) Suitable low molecular weight (generally below 400) difunctional compounds that serve as chain extenders used for forming the cross-linkable thermoplastic polyurethane (TPU) according to the invention may include diols, such as aliphatic diols like ethylene glycol, 1,3-propanediol, 2-methyl-1,3-propanediol, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, 1,8-octanediol, 1,9-nonanediol, 1,10-decanediol, 1,12-dodecanediol, 1,2-propanediol, 1,3-butanediol, 2,3-butanediol, 1,3-pentanediol, 2-ethyl-butanediol, 1,2-hexanediol, 1,2-octanediol, 1,2-decanediol, 3-methylpentane-1,5-diol, 2-methyl-2,4-pentanediol, 3-methyl-1,5-pentanediol, 2,5-dimethyl-2,5-hexanediol, 3-chloro-propanediol, 1,4-cyclohexanediol, 2-ethyl-2-butyl-1,3-propanediol, diethylene glycol, dipropylene glycol and tripropylene glycol, 1,4′-butyl enediol, 3-hydroxy-2,2-dimethyl-propanoic acid, aminoalcohols such as ethanolamine, N-methyldiethanolamine and the like, diamines, hydrazines and hydrazides and mixtures thereof. Preferred are diols such as hexanediol, 1,4-butanediol or ethylene glycol. 1,4-Butanediol is most preferred. Di-esters of terephthalic acid with glycols having 2 to 4 carbon atoms, e.g. terephthalic acid bis(ethylene glycol) or bis-1,4-butanediol, and hydroxyalkylene ethers of hydroquinone, and polyoxytetramethylene glycols having molecular weights of from 162 to 378, are also suitable. Preferably the reaction mixture does not contain any low molecular weight triol.

(28) The amount of chain stopper used for forming the cross-linkable thermoplastic polyurethane (TPU) according to the invention may be such that the molecular weight (MW) of the final cross-linkable thermoplastic polyurethane (TPU) can be controlled and be comprised between 5,000 and 12,000 g/mol. The amount of chain stopper is typically from 0.08 mmole/g of cross-linkable mixture to 0.35 mmole/g of cross-linkable mixture, preferably from 0.12 mmole/g of cross-linkable mixture to 0.25 mmole/g of cross-linkable mixture.

(29) The co-cross-linkable ethylenically unsaturated compounds used for forming the cross-linkable thermoplastic polyurethane (TPU) suitable for use in the deposition process according to the invention which serve as a reactive diluent lie dormant during initial processing and polymerize if subjected to appropriate polymerization conditions. The co-cross-linker contains at least one polymerizable unsaturated group, preferably a radically polymerizable group. Examples of such ethylenically unsaturated compounds are dipentaerythritol penta acrylate, trimethylolpropane tri methacrylate, ditrimethylolpropane tri acrylate, pentaerythritol tetra acrylate, trimethylolpropane tri acrylate, butanediol di methacrylate, ethoxylated pentaerythritol tetra acrylate, hexanediol di methacrylate, hexanediol di acrylate, lauryl methacrylate, 2-phenoxyethyl methacrylate, 2-phenoxyethyl acrylate, polyethyleneglycol di acrylate, polypropyleneglycol di acrylate, polycaprolactone di acrylate. Most preferred are mono acrylates and mono methacrylates or combinations thereof.

(30) The viscosity of the cross-linkable thermoplastic polyurethane (TPU) used as polymeric material in the cross-linkable polymeric composition of the invention may be adjusted by altering the relative amounts of the TPU and the ethylenically unsaturated compounds, the latter serving as a reactive diluent and forming part of the final cross-linked material. Generally the amount of TPU is between about 45 wt % and 70 wt % and the amount of ethylenically unsaturated compounds is between about 55 wt % and 30 wt % based on the total cross-linkable mixture. Preferably the amount of TPU is between 45 wt % and 60 wt % and the amount of ethylenically unsaturated compounds is between 55 wt % and 40 wt %.

(31) The ratio of TPU and co-cross-linker, the hard block content of the TPU, the molecular weight of the TPU and the type of chain stopper used for forming the cross-linkable thermoplastic polyurethane (TPU) according to the invention may be chosen in such a way that the final viscosity of the thermoplastic polymeric composition of the invention has a viscosity value at 60° C. below 500 Pa.s, preferably below 300 Pa.s, more preferably in the range 5-120 Pa.s. The thermoplastic polymeric composition is having a viscosity above 10 Pa.s. at room temperature (temperature of about 20° C.), preferably the thermoplastic polymeric composition is having a viscosity above 20 Pa.s. at room temperature.

(32) The invention also allows further controlling the hard block content of the at least one cross-linkable thermoplastic polyurethane (TPU) that is used as cross-linkable polymeric material; especially one can control the processing and final use temperature of the final products in addition to the thermos-mechanical performance. The hardness of the materials of the invention can be varied by changing the amount of hard block level in the thermoplastic polyurethane. Typically, the hard block level is varied between 7 and 60 wt % with hard block level being defined as the weight percentage of chain extender, chain stopper and isocyanate in the TPU; preferred values are from 10 wt % to 50 wt %. Generally the number of urethane groups per kg of acrylate resin is between 0.5 and 2.5 and preferably between 0.5 and 1.5.

(33) Other conventional ingredients (additives and/or auxiliaries) may be used in making the at least one cross-linkable thermoplastic polyurethane (TPU) that is used in the invention. These include catalysts, surfactants, flame proofing agents, fillers, pigments (to provide different colors), stabilizers and the like. Catalysts which enhance the formation of urethane and urea bonds may be used, for example, tin compounds, such as a tin salt of a carboxylic acid, e.g. dibutyltin dilaurate, stannous acetate and stannous octoate; amines, e.g. dimethylcyclohexylamine and triethylene diamine.

(34) The reactants used to make the at least one cross-linkable thermoplastic polyurethane (TPU) according to the invention may be applied using the so-called one-shot, semi-prepolymer or prepolymer method known in the art by a batch or continuous process known to the person skilled in the art. The TPU's thus produced are dissolved into a reactive diluent, and can be processed according to known techniques. All reactants can be reacted at once, or can be reacted in a sequential manner into the reactive diluent. By prior mixing of all or part of the unsaturated chain stopper of the invention with all or part of the isocyanate-reactive compounds solutions or suspensions or dispersions are obtained, depending on the unsaturated chain stopper and isocyanate reactive compounds used. The various components used in the manufacture of the cross-linkable TPU mixture of the invention can in fact be added in any order.

(35) For example, one may use a prepolymer of polyisocyanate and polyol, then add the diol and the monol, or one may use a prepolymer of polyisocyanate and polyol and the monol, then add the diol in the process for making the cross-linkable thermoplastic polyurethane (TPU) used in the invention.

(36) Alternatively, the cross-linkable polymeric material may comprise or be selected from thixotropic polymers.

(37) Before providing the polymeric composition comprising at least one cross-linkable polymeric material, preferably the cross-linkable thermoplastic polyurethane (TPU) material(s) according to the invention in the spray nozzle, the polymeric composition may be heated to achieve a viscosity value suitable for spray and not too liquid to avoid sagging off the object after spraying. The viscosity after heating up to temperatures in the range 60° C. up to 120° C., preferably at temperatures of about 80° C. is maximum 4 Pa.s, preferably in the range 3-3.5 Pa.s.

(38) Upon cross-linking (during the step of applying a cross-linking treatment) there will be a chemical bond created between the polymeric material (e.g. TPU) and the (acrylic) polymer (at the interface with the interpenetrating polymer formed from the (mono) functionalized monomer). The covalent link formed during the cross-linking step is taking place substantially at the end of the polymeric molecules (e.g. at the end of the TPU chain) which means that the phase structure and chain mobility of the cross-linked material is not disadvantageously disturbed.

(39) According to embodiments, cross-linking of the at least one cross-linkable polymeric material (e.g. TPU) in the polymeric composition can be initiated either via the thermal route or via the actinic route, including UV and electron beam (EB) radiation.

(40) According to embodiments, thermal cross-linking initiators may be added to the cross-linkable polymeric composition beforehand. Said compounds suitable as thermal cross-linking initiators are organic peroxides such as dicumylperoxide, 2,5-dimethyl-2,5-di(tert.-butyl)peroxide, 2,5-Bis(tert.-butylperoxide)-2,5-dimethyl-3-hexyne, di-tert.-butylperoxide, 2,5-Bis(tert.-butylperoxide)-2,5-dimethyl-hexane, Bis(tert.-butylperoxyisopropyl)benzene, m-octadexylazoformate and tert.-butyl peroxycumene, tert.-butyl peroxy 2-ethylhexylcarbonate. A preferred cross-linker is tert.-butyl peroxy 2-ethylhexylcarbonate.

(41) Another method for cross-linking is exposure to actinic radiation such as ultraviolet light or electron beam for an appropriate period of time.

(42) According to embodiments, UV initiators may be added to the cross-linkable polymeric composition. Typical UV initiators comprise ketones such as 1 -hydroxy cyclohexylphenylketone, 2,2- dimethoxy- 1,2-diphenylethan- 1 -one, 1 - [4-(2-hydroxyethoxy)-phenyl]-2-methyl- 1 - propanone (HHPMP), and (bis)acylphosphineoxides such as bis(2,4,6-trimethylbenzoyl)- phenyl-phosphoneoxide (BTPPO).

(43) According to a second aspect of the invention a three dimensional (3D) object is disclosed comprising at least one thermoset (elastomeric) polymeric material obtained by using the above described deposition process.

(44) According to embodiments, the three dimensional (3D) object comprising at least one thermoset (elastomeric) polymeric material obtained by using the above described deposition process is a shoe containing a shoe upper wherein said shoe upper is at least partly created according to the deposition process of the invention.

(45) Using the deposition method according to the invention makes it possible to create a shoe with different parts made of different (thermoset) polymeric materials having different hardness, different stiffness and to realize this in precise and thin sections.

(46) Using the spray method according to the invention makes it possible to have an automatized 3D shoe upper production thereby avoiding the use of glue and/or stitches leading to a reduction in labour cost up to 90%. The deposition method further eliminates the use of expensive mould designs.

(47) Possible further applications in the shoe manufacturing include: Modification of existing shoes with local protection pads (e.g. safety shoe toe cap covers) Any type of coating to heavy duty consumer goods to protect them from impact Adding decorative elements to a shoe (upper), . . .

(48) The invention is illustrated with the following examples.

EXAMPLES

(49) Chemicals Used: Isocyanate Suprasec® 1306 (obtained from Huntsman) Polyol Daltorez® P765 (obtained from Huntsman) Irganox® 1010 Metal catalyst Metatin® S 26 t-Butylacetate 1,4 butanediol (BDO) Mono-functional aromatic acrylic monomer (50% SR®410 and 50% SR®7905 obtained from Arkema) Polypropyleneglycole monomethacrylate (Bisomer® PPM® 5LI, obtained from GEO Specialty Chemicals)

(50) Formulation (Ingredients Mentioned in wt %) to Obtain Cross-Linkable Polymeric Material (UV Curable Polyurethane (PU))

(51) TABLE-US-00001 14.91% Suprasec ® 1306 7.26% Bisomer ® PPM ® 5LI 43.13% Daltorez ® P 765 2.13% Irganox ® 1010 0.0041% catalyst solution (Metatie ® S26 and t-butylacetate 10/90 mixture) 2.55% BDO 15% SR ® 410 15% SR ® 7905

(52) Experimental Set Up: Preparation of Cross-Linkable Polymeric Material (UV Curable Polyurethane (PU))

(53) An oil bath is preheated to 80° C. and to a 1000 ml flask (preheated at 60° C.), 91.28 g of Suprasec® 1306 is added.

(54) The flask is then put under nitrogen and the Suprasec® 1306 is being stirred.

(55) The flask is then heated in the oil bath until 80° C.

(56) 44.37 g of Bisomer® PPM® 5LI is added (which has been dried beforehand using molecular sieves)

(57) Let the mixture react for about 90 minutes.

(58) Start adding 276.78 g polyol (dried Daltorez® P765 with 0.47% Irganox® 1010) slowly over 30 minutes.

(59) 0.0250 g of catalyst (0.3018 g Metatin® S 26 in 3.1010 g t-butylacetate) was added to the mixture and the mixture was left to react for about 90 minutes.

(60) Then a calculated amount of BDO was added (in this experiment it was 15.1663 g BDO) dropwise until a NCO value of 100 is obtained

(61) After approximately 5 minutes the acrylate (50% SR®410 and 50% SR®7905) was added to the mixture in a desired ratio (in this experiment 70% TPU=416.17 g and 30% acrylate=178.36 g)

(62) Experimental Set Up: Spray UV Curable Polyurethane (PU)

(63) The UV curable PU was heated to 110° C. before spray in order to obtain the desired viscosity<4 Pa.s (the measured viscosity was 3.4 Pa.s). A layer with final thickness ranging from 0.3 mm to 1.7 mm was sprayed using a precision swirl tool in a circular (swirl) motion. The nozzle was moving using a robot while the sample was fixed and the speed of the precision swirl can be changed to make coatings which are thicker (slower) or thinner (faster).

(64) The coated samples were then cured to fixate the deposited polyurethane using a F300 UV-light curing machine (Fusion LC6E equipped with a Fusion I300 & I6 UV lamp from DESMA). The photo initiator used for the UV curing was Irgacure® 500 (0.5% in the UV curable PU).