A method for preparing and applying a sprayable, light stable polyurethane

Abstract: A method for preparing a light stable polyurethane, sprayable by means of a spray pistol, wherein use is made of an active hydrogen containing compound, wherein the functional groups consist for at least 50 % of an active CH₂OH, NH and/or NH₂ group, the functionali­ ty of which varies from 2 to 8 and the equivalent weight of which is comprised between 100 and 3500, together with 2 to 300 parts, per 100 parts of said compound, of a chain extender and/or a cross-linker, the functional groups of which are OH groups, at least 50 % of which are primary OH groups, the equivalent weight of which is less than 100 and the functionality of which varies from 2 to 6, and with a catalytic system which comprises at least an organic lead, bismuth and/or tin (IV) compound and at least an amine initiator, having a functionality of 2 to 6, an equivalent weight lower than or equal to 200, and at least one aliphatic NH₂ or NH group.

Description: The present invention relates to a method for making a light stable polyurethane film comprising the steps of : preparing a polyurethane reaction mixture containing an isocyanate compound having at least two NCO-groups which are not directly attached to an aromatic group, and a compound containing active hydrogen with respect to NCO groups, and wherein the latter compound is reacting with isocyanate compound in the presence of a chain extender and/or cross-linker and a catalyst ; and spraying said reaction mixture by means of a spray pistol onto a surface so as to form said polyurethane film by at least one pass of the spray pistol over said surface. In this method, the chain extenders and cross-linkers are also compounds which contain active hydrogen with respect to NCO groups, but these compounds have, however, a relatively low equivalent weight (EW). A method as defined hereinabove is already disclosed in US-A-4 695 618. In this US patent, the possibility of using aliphatic isocyanates is however only given amongst all kinds of other isocyanates while no example is given wherein use is made of an aliphatic isocyanate. On the contrary, all of the given examples involve the use of aromatic MDI as isocyanate. Further, in the method according to US-A-4 695 618 no separate film is manufactured but the sprayed film adheres, on the contrary, as a coating onto the surface. The main object of the present invention is to provide a method for making a light stable polyurethane film wherein use is made of a polyurethane reaction mixture based on an aliphatic or alicyclic isocyanate which can notwithstanding its lower reactivity be sprayed in one single passage or spray process in a sufficiently thick and homogeneous layer onto a surface of an open mould. This reaction mixture has therefore to be relatively viscous and has to gel quickly in order to avoid run-off problems of the material on the mould surface under the influence of the gravity force while its viscosity being still sufficiently low in the initial phase in order to obtain a homogeneous spreading over the mould surface and also to prevent clogging of the spray pistol. More particularly, it is important that a too quick gelation does not occur during the spraying so that a homogeneous thickness would be obtained by a sufficient flow of the reactive mixture in the initial reaction stage, somewhat in an analogous manner as it is the case with a paint. Further, the initial viscosity increase may not be too large a.o. in order to prevent deposits on the spray nozzle outlet, which would change the spray pattern. In this respect, the fibre forming time "FT" should be higher than 3 seconds, and preferably higher than 4 seconds. Finally, in order to guarantee a sufficient productivity as to production cycle time, the gelation ("curing") of the reacting mixture and hence the demoulding time has to be as short as possible. In order to permit the reaction mixture to be sprayed in a homogeneous thickness of 0,3 to 3 mm per pass of the spray pistol onto an open mould surface and in order to permit the so-obtained polyurethane film to be demoulded after a demoulding time ("DT') of less than 10 minutes, the features defined in the characterizing portion of claim 1 are applied in the method according to the present invention. In a particular embodiment of the invention, use is made of a catalytic system comprising at least an amine initiator together with a lead, tin or bismuth compound and (a) a zeolite type catalyst formed of an alkaline aluminium silicate with sodium and/or potassium ions, and/or (b) an alkaline catalyst having a pH higher than 10 and consisting of diazobicyclo-alkenes or salts of the latters with weak organic acids or consisting of potassium, sodium or lithium salt of weak organic acids. In a preferred embodiment of the invention, said reaction mixture is sprayed according to a two component system, wherein one component comprises the isocyanate and all of the additives which are stable with respect to this isocyanate during a sufficient time period and also compatible with the latter and wherein the other component comprises the compounds containing active hydrogen with respect to NCO groups, especially polyols, chain extenders and cross-linkers and additives which are stable with respect to these compounds during a sufficient time period and also compatible with the latter. Other particularities and advantages of the invention will become apparent from the following description of a series of polyurethane formulations which are obtained by applying the method according to the invention and also of some specific embodiments of the method according to which the thus prepared polyurethane is sprayed. Generally, the invention relates to a multiple component polyurethane system which can be sprayed on an open mould or on other surfaces by means of a multicomponent spray nozzle in order to form inherent light stable, flexible, semi-flexible, or rigid, microcellular or non cellular films or layers having a density of 500 to 1200 kg/m³. These multicomponents comprise the following substances : a) an isocyanate, the NCO groups of which are not directly attached to an aromatic group, such as aliphatic or alicyclic polyisocyanates or derivatives of these ; b) with respect to the NCO groups active hydrogen containing compounds, especially so-called "basic polyols" containing with respect to NCO groups reactive groups which consist mainly of CH₂OH and/or NH and/or NH₂ or mixtures thereof, having a functionality between 2 and 8 and an equivalent weight between 100 and 3500 (within the context of this description, there is arbitrarily meant by "basic polyols"all of the here defined compounds) ; c) 2 to 300 parts per 100 parts of the "basic polyols", of a chain extender and/or a cross-linker, dependent upon the hardness degree of the foils, having only functional OH groups, at least 50 % of which are primary OH groups, the equivalent weight of which is lower than 100 and the functionality of which varies from 2 to 6 ; d) a synergic catalytic system comprising at least one compound of each of the next two series : 1. an organic lead, bismuth or tin compound or mixtures thereof ; 2. one or more amine containing initiators, (functionality ≧ 2), which in fact also serve as chain extender and/or as cross-linker and which are either or not combined with an alkaline catalyst or zeolite type catalyst, as will be defined further hereinafter ; e) 0 to 0.4 % water, present in the active hydrogen containing compounds; f) possibly low boiling liquids serving as a physical blowing agent and the amount of which is comprised between 0 and 0.04 moles with respect to 100 gr of the active hydrogen containing compounds (b) and (c), the boiling point of these liquids being preferably comprised between 20 and 70°C. The cross-linkers have a functionality higher than 2, whilst the chain extenders have a functionality of 2. In both cases, the molecular weight is relatively low. The suitable isocyanates can be very different. According to a first embodiment of the invention, use can thus be made of an isocyanate consisting mainly of IPDI monomer and/or mixtures of IPDI monomer with IPDI derivatives, such as trimers, more particularly isocyanurates or biuret, prepolymers and/or carbodiimide/urethidion derivatives and this in such proportions that a NCO value of 15 to 37.8 in percent by weight is obtained. In a second embodiment, the isocyanate consists of TMXDI or derivatives (except from isocyanurate trimer) : prepolymers, biuret trimer and/or carbodiimide/urethidion derivatives, in such proportions that a NCO value of 15 to 34.4 in percent by weight is obtained. In a third embodiment, the isocyanate is formed of HDI whether or not in combination with derivatives, such as trimers, prepolymers and/or carbodiimide/urethidion derivatives, as in the first embodiment, taking care that the NCO value is anyway finally situated between 15 to 50. In a fourth embodiment, the isocyanate is formed of H6XDI and possibly of analogeous combinations as is the case in the first hereabove described embodiment in which the NCO value is comprised between 15 and 43. A fifth embodiment consists in using H12MDI, possibly in combination with derivatives or consisting of prepolymers and/or carbodiimide/urethidion derivatives, the NCO value being comprised between 15 and 31.8. Generally, also other aliphatic or alicyclic isocyanates or derivatives thereof can be used provided that the following conditions are simultaneously met : 1) functionality of basic monomer = 2 2) NCO groups not directly attached to aromatic ring. The types or mixtures defined in the following Table 1 are preferred. It should be remarked that all the above described polyamines can also be directly added in the formulation (through blending into the polyolcompound) i.e. "one-shot" method, instead of through prepolymerisation with the polyisocyanate in a separate step. In case of an equivalent weight ≦ 200, such molecules, when added by the "one-shot" method, also function as "amine- initiators" (see further), i.e. as a combination of co-catalyst and extender/cross-linker. In case of a functionality of 2, such polyamines will also increase mechanical strength properties, such as elongation and tear resistance. The NCO index of these different isocyanates comprised in Table 1, representing the stoechiometric ratio between the NCO groups and the active hydrogen containing components, is generally comprised between 80 and 130 and preferably between 85 and 110. The active hydrogen containing compounds, which are particularly appropriate to react with the isocyanate in order to form polyurethane, preferably consist of "basic polyols" and especially polyoxyalkylene compounds (polyetherpolyols), which are thus formed by polyaddition of propylene oxide and/or ethylene oxide on low molecular starters with OH, NH and/or NH₂ groups, which have a functionality of 2 to 8. These compounds present specifically terminal groups consisting of OH groups, at least 50 % of which are primary OH groups, of secondary NH groups and/or of primary NH₂ groups. Table 2 is grouping the polyetherpolyols which are most suitable for applying the invention. Other types of active hydrogen containing compounds are the polyesterpolyols forming ester condensation products of dicarboxylic acids with low molecular polyalcohols having a functionality of 2 to 4, preference being given to polyesterpolyols having a terminal hydroxyl number of 30 to 200 (100 % primary OH groups) and a functionality of 2 to 3. A further very suitable compound with active hydrogen containing groups are the polytetramethylene ether glycols (PTMG), which are polytetrahydrofuran with 100 % primary OH groups, a functionality of 2 and a hydroxyl number of 35 to 200. Finally, this active hydrogen containing compound can consist of polyols with a functionality of 2 to 3 and a hydroxyl number of 25 to 200, which are further modified with polymerized organic fillers, such as polyols grafted with styrene/acrylonitrile, "PHD" polyols and "PIPA" polyols, the filler content varying between 3 and 50 % by weight (see Belgian Patent Application No. 08701053). The polyols of this type which are preferred are the ones having a hydroxyl number of 25 to 35, a functionality of 2 to 3 and a filler content of 5 to 20 %. The used chain extenders and/or cross-linkers can be considered as a special group of the active hydrogen containing compounds and contain only functional OH groups. Moreover, these ones have an equivalent weight of about 30 à 300 and preferably lower than 100. Table 3, given hereafter, shows the concentration of the chain extenders and/or cross-linkers in function of the equivalent weight of the used polyol as active hydrogen containing compound, which allows to obtain optimal results. In this table, the amounts are expressed in parts by weight per 100 parts "basic polyol" (b). Equivalent weight Conc. (parts by weight) generally preferably < 500 2 - 30 4 - 25 > 500 2 - 300 4 - 150 Typical preferred compounds of cross-linkers and chain extenders with only active OH groups having a functionality of 2 to 4, a hydroxyl number higher than 250 and a primary OH group concentration higher than 50 % are the next ones : ethylene glycol, propanediol, butanediol, pentanediol, hexanediol, glycerin, trimethylpropane, triethanolamine, trimethylolethane, pentaerythrol, bisphenol A and cyclohexanedimethanol, and also possible addition products of all these examples with less than or equal to 5 moles ethylene oxide and/or propylene oxide per mole chain extender/cross-linker. The nature of the above mentioned catalysts is further illustrated and described hereafter. (1) "Pb cat" These are lead compounds which are already known per se as catalysts for preparing polyurethane with an integral skin. Such catalysts have been described among others in the Dutch Patent Application No. 77,02676. Thus, usually a compound from one of the following groups is used as organolead compound : a) organolead (II) salts of carboxylic acids, containing at least one carboxylic group, b) lead dithiocarbamates having formula : wherein Q' and Q'' are different or the same and represent an alkyl group with 1 - 20 carbon atoms, c) organolead (IV) compounds having the formula PbQ₄''', wherein Q''' represents an alkyl group with 1 - 6 carbon atoms, and d) lead (II) acetylacetonate. More particularly, there has been determined that amongst these organolead compounds, the following compounds are very suitable : a) organolead (II) salts of carboxylic acids such as lead acetate, adipate, citrate, 2-ethylhexoate, laurate, linoleate, naphthenate, octanoate, oleate, oxalate, palmitate, resinate, ricinoleate, salicylate, stearate, tallate and tartrate, b) a dithiocarbamate having the formula : wherein Q′ and Q″ represent methyl, ethyl, butyl or amyl, and c) the compounds having the formula PbQ₄‴, wherein Q‴ represents methyl or ethyl. The Pb(II) carboxylates, being lead salts of organic monocarboxylic acids, are particularly preferred. A typical carboxylic acid is a whether or not branched aliphatic monocarboxylic acid with formula R-COOH, wherein R is an alkyl having 7 to 12 carbon atoms, such as lead-2-ethylhexoate. Another carboxylic acid is naphthenic acid which forms lead naphthenate. (2) "Bi cat" Use is made of organic bismuth compounds which are known per se for preparing polyurethane with integral skin, described a.o. in Dutch Patent Application No. 80,01362. Preference is especially given to three-valency bismuth compounds belonging to the same category as the above described organolead compounds, such as Bi-2-ethylhexoate and Bi-naphthenate. (3) "Sn cat" a. Sn(IV) carboxylates These compounds correspond to following general formula : wherein R₁ is a (C₁-C₄) alkyl radical and R₂ forms a (C₁-C₁₂) alkyl radical or a naphthenic acid radical, the alkyl radicals being linear or branched. Preference being given to compounds wherein R₁ is a methyl group and R₂ a (C₇-C₁₁) alkyl radical or a naphthenic acid radical, or also wherein R₁ is a butyl group and R₂ is a (C₁-C₄) alkyl radical. b. Dialkyldistannoxane dicarboxylates Those compounds have following general formula : wherein R₁ is a (C₁-C₄) alkyl radical and R′ a (C₁-C₁₂) whether or not branched alkyl radical. c. Alkyltinhalides These compounds have the following general formula : (R₁) x Sn(Hal) y wherein R₁ is a (C₁-C₄) alkyl radical, "Hal" is a halogene, preferably chlorine or bromine, x + y = 4 and x or y varies from 1 to 3. (4) "Alkaline cat" These compounds are strong, alkaline catalysts having a pH larger than 10 and belonging to one or more of the following classes : a) diazobicyclo-alkenes and salts of these with weak organic acids (pK a > 4), having general formula : A typical preference is given to 1,8-diazobicyclo-(5,4,0)-undecene-7 as well as to the octoate or phenolate salt of this compound. b) K, Na or Li salts of weak organic acids (pK a > 4). A typical preference is given to the octoate, phenolate and oleate salts of K or Na. (5) "Amine initiators " Such initiators which are known per se and which can be used in the method according to this invention, are described a.o. in Dutch Patent Applications 77,02676 and 80,01362, provided that a minimum functionality of 2 is required. Aliphatic or alicyclic alkanolamines or polyamines, having amino group not directly attached to an aromatic ring are generally considered in this respect. The number of NH and/or NH₂ groups is at least 2, if no OH groups are present and, at least 1 if OH groups are present. The total number of reactive groups, formed by NH, NH₂ or OH, mostly varies between 2 and 5. Typical preferred compounds, notably aliphatic compounds having a functionality of 2 to 4, are the following ones : monoethanolamine, diethanolamine, diisopropanolamine, ethylenediamine, isophoronediamine, N,N′-dimethyl(diethyl)-ethylenediamine, 2-amino-2-methyl (or ethyl) -1-propanol, 2-amino-1-butanol, 3-amino-1,2-propanediol, 2-amino-2-methyl (ethyl)-1,3-propanediol. "Jeffamines" (Texaco) (propylene oxide addition products having mainly terminal primary NH₂ or secondary NH groups - functionality 2 à 3). Addition products of propylene oxide and/or ethylene oxide on ethylenediamine initiator (2 à 8 moles/mole ethylenediamine). As mentioned already above the sufficient low reactive polyamines, suitable for the prepolimerization of the polyisocyanates, function also as amine initiators provided their molecular weight is less than 200 and that they are added by "one shot" method, i.e. that they are blended into the polyol compound. (6) "Zeolite type cat " These catalysts are alkaline aluminium silicates with Na and/or K ions, wherein the diameter of the micro-cavities is preferably comprised between 2 and 10 Angström and typically between 3 and 4 Angstrom and which show the following general formula : (M₂O) a - (Al₂O₃) b - (SiO₂) c - (H₂O) d , wherein M represents potassium and/or sodium, beside sodium and/or potassium, also calcium ions can possibly be present. These silicates can be mixed, as fine powders or as pastes, in liquid dispersion media with the other reaction products for forming polyurethane. It is important to notice that these zeolites have thereupon an extra possible function, notably the in situ dehydration of the active hydrogen containing compounds, mostly thus the polyols compounds, for example if a maximum density of the obtained polyurethane film, without cellular structure, is desired. Very suitable catalytic systems, which are applicable according to the invention and which specifically promote the reactions of aliphatic and alicyclic NCO groups with active hydrogen containing compounds, such as OH, NH and NH₂ groups, are shown in the following Table 4. Combin. ref. "Pbcat" (1) "Bi cat" (2) "amine initiator" (5) "Sn cat" (3) "Zeolite type cat" (6) "Alkaline cat" (4) C1 X - X - - - C2 X - X X - - C3 X - X - X - C4 X - X - - X C5-C8 X - X (X) (X) (X) C9 - X X - - - C10 - X X X - - C11 - X X - X - C12 - X X - - X C13-C16 - X X (X) (X) (X) C17 - - X X X - C18 - - X X - X C19 - - X X X X (x) indicates that at least two of the three catalysts are present. [types (3), (4) and (6)]. An explicite preference is given to the following catalytic combinations : C4, C5, C6, C7, C8, C11, C12, C13, C14, C15, C16 and C18. Recommended concentration ranges of these catalysts are as follows : Pb catalyst : 0 à 2 % and preferably less than 0.5 % for reducing or avoiding a metallic lustre and a H₂S effect (darkening by contact with H₂S as a result of PbS formation) ; Bi catalyst : 0 to 2 % and preferably less than 1.5 % for the technologic processability and heat stability of the final products ; Sn catalyst : 0 to 4 % and preferably less than or equal to 2 ; "Alkaline catalyst" : 0 to 2, and preferably less than 1, a.o. for the technologic processability and physical properties of the final products, more in particular the mechanical strength ; "Zeolite type catalyst" : 0 à 5 and preferably 0 à 3 ; "Amine initiators" : 1 to 30 and preferably 2 to 10. It should be noted that the overall concentration of catalysts and amine initiators is dependent on the catalyst combination type, the nature of the used isocyanates and active hydrogen containing compound, the reactive mixture temperature, the mould temperature, etc... For a well defined situation, this concentration is however usually higher than for a "RIM" (reaction injection moulding) or "casting" technique, and this in order to guarantee an optimal curing and a limited flow or run off of sprayed thin reaction mixture films. The possibly used blowing agent may be as well of chemical as of physical nature. For use as a chemical blowing agent, preference is given to an amount of water between 0 and 0.4 % by weight with respect to the total used raw material amount, except for the polyisocyanates, i.e. with respect to said active hydrogen containing compound, cross-linker, chain extender and initiator, an amount lower than 0.1 % by weight being preferred. The amount of used physical blowing agent having a boiling point of 20 à 70°C, is generally comprised between 0 and 0.4 moles with respect to 100 grams of the total amount of active hydrogen containing compound, preference being given to the total omission of a physical blowing agent. The most typical compounds are trichlorofluoromethane and methylene chloride. These physical blowing agents are preferably added to the isocyanate containing component. In order to guarantee the colour stability of the sprayed polyurethane, the reaction mixture comprises preferably antioxidants and UV absorbers, the following synergic combination being preferred : a) primary, substituted phenol antioxidants at a concentration which is usually comprised between 0.1 and 1 % by weight with respect to the total polyurethane polymer amount ; b) substituted ("hindered") alicyclic amines ("HALS") at a concentration which is generally comprised between 0.1 and 1 % by weight of the total polyurethane polymer amount ; c) secondary antioxidants (peroxide decomposition products) consisting of organic phosphites or thioesters at a concentration which is usually comprised between 0 and 5 % by weight of the total polyurethane polymer amount ; d) UV absorbers being preferably of the benzotriazole type, generally at a concentration between 0.1 and 1 % by weight of the total polyurethane polymer amount. For colour pigments, use is preferably made of light stable, anorganic and/or organic, solid pigments which are added in the shape of a dispersion in a liquid medium, such as in polyol. The solid pigment concentration is usually comprised between 1 and 10 % by weight with respect to the total polyurethane polymer amount and preferably between 2 and 5 % by weight. In most cases, it is preferred to add an internal release agent to the reaction mixture, preference being given to the polydimethylsiloxane-polyether copolymer types at a concentration lower than 20 % by weight polyether with respect to the total molecule and lower than 50 % by weight ethylene oxide with respect to the total ethylene oxide and propylene oxide amount in the polyether chain. Such internal release agents do not only facilitate the demolding of the polyurethane films but mostly also reduce the amounts of gas micropores in the film outer surface. Generally, the release agent concentration comprises between 0 and 3 % by weight with respect to the total polyurethane polymer amount, and preferably between 0.5 and 2 % by weight. Another substance which is usually added to the reaction mixture is a neutral, physical, tixotropic thickening agent consisting preferably of fumed, coagulated silicon dioxide, the concentration of which is generally comprised between 0 and 3 % by weight of the total polyurethane polymer amount ; and preferably between 0.5 and 2 % by weight. For spraying the light stable polyurethane foam with the hereabove described formulation, use is preferably made of a two-components system, wherein one component comprises the isocyanate and all of the additives which are with respect to this isocyanate during a sufficient time period stable and compatible with the latter and wherein the other component comprises the with respect to NCO groups active hydrogen containing component, more in particular polyols and the chain extenders, cross-linkers and initiators, and additives which are with respect to these different compounds during a sufficient time period stable and compatible with the latter . The first mentioned component comprises thus, in addition to the isocyanate, for example certain antioxidants, UV absorbers, catalysts, internal release agents, plasticizers, fire retardants, physical blowing agents, fillers, tixotropic thickening agents and the like. The second component comprises preferably, in addition to the active hydrogen containing compound, such as polyol, chain extenders and/or cross-linkers, water, pigments and certain catalysts, anti-oxidants, UV absorbers, water, release agents, plasticizers, fire retardants, fillers, tixotropic thickening agents, etc. These components are preferably preheated, before the spraying, upto a temperature not higher than 120° and usually between 30 and 70°C, and this in order to speed up the reactivity of the reaction mixture which is sprayed on the mould surface. The viscosity of the reaction mixture which is sprayed on a mould surface is a very important parameter. According to the invention, there is aimed at a temperature adjustment of the reaction mixture at spraying in such a way that the viscosity is not higher than 1200 cps and preferably not higher than 700 cps, this in order to obtain an as homogeneous as possible flow of the reaction mixture, and not lower than 200 cps preferably not lower than 500 cps in order to avoid run-off. For the spraying of the reaction mixture, use is preferably made of a spray pistol working with or without air. Mostly, use is made of the so-called airless two-components system without solvent. The mould surface, the reaction mixture has to be sprayed against for the formation of a polyurethane film, can have very various geometric shapes. The different places of this surface do actually have to be within reach of the movable spray nozzle. Further, this surface can be of any structure and nature and can be made of metal, plastic, rubber, leather, wood, whether or not provided with a film of an external release agent as generally used in the polyurethane casting and moulding methods. In order to facilitate the curing of the reaction mixture at the moment it is sprayed on the mould surface, the latter is preferably heated up to a temperature between 30 and 100° and more specifically between 50 and 80°C. The composition of the reaction mixture and the spray conditions, are preferably selected in such a manner that the films or layers, formed by spraying the reaction mixture on the mould surface, can be removed from the latter within less than 10 minutes after the spraying and preferably even within less than 3 minutes, and no excessive run-off of the reaction mixture occurs on this surface. The most typical way for making finished pieces by applying the method according to the invention consists in that in a separate step and in a separate mould, a so-called back-foaming is done with a cellular, flexible to semi-rigid classic polyurethane foam, such as it is customary for the back-foaming of plastic foils. In a very specific embodiment of the invention, a conventional polyurethane foam (MDI or TDI basis) with a typical mould foamed density of 50 to 600 kg/m³ and a typical free rise density of 30 à 200 kg/m³ is injected, after the spraying of a polyurethane film on a substantially hollow mould surface and before demoulding the latter, by means of a separate injection in the same mould cavity. Preferably, there is sought to obtain in one single passage of the spray nozzle, a film thickness between 0.3 and 3 mm, thicker layers being however obtainable by spraying a number of different reaction mixture layers upon each other by successive spray nozzle passages. The density of the obtained polyurethane film, which is preferably micro-cellular, is adapted in an advantageous manner between 500 and 1200 kg/m³ by adjusting the amount of blowing agent, consisting of water and/or of low boiling solvents, and also the amount of air dispersed in the raw materials. For some applications, it is important to realize a polyurethane layer substantially totally free of pores. This is realized according to the invention by degassing the isocyanate containing component and by degassing and dehydrating the active hydrogen containing component. The hardness of the polyurethane film, formed on the mould surface, can be adjusted by the choice of the type and amount of the employed isocyanate, polyol, chain extender and/or cross-linker. Preference is given to a hardness between shore A 20 and shore D 80 depending on the applications/ requirements of the final PU films. Finally, reinforcements such as glass fibre mats, can be inbedded in certain parts or in the complete, on the mould surface formed polyurethane film or layer. This can be done before or during the reaction mixture spraying. Hereafter, a review is given of the abbreviations and codes used in this description and claims. 1. ISOCYANATES I1 = IPDI = isophorone diisocyanate (Hüls Chemie) = 3-isocyanatomethyl-3.5.5-trimethylcyclohexyl-isocyanate (37.8 % by weight NCO) I2 = TMXDI = meta- or paratetramethyl xylene diisocyanate (Am.CYANAMID) (34.4 % by weight NCO). I3 = HDI = 1,6-hexamethylene diisocyanate (50 % by weight NCO) I4 = H6XDI = hydrogenated XDI (43 % by weight NCO) (TAKEDA CHEM. IND.). I5 = H12MDI hydrogenated MDI = DESMODUR W (MOBAY/BAYER) = dicyclohexylmethane diisocyanate (31.8 % by weight NCO) Ix-Iy = mixture of isocyanate trimers and isocyanate monomers based on an isocyanate Ix(I1,I2...) having a terminal NCO content = y (percent by weight free NCO groups with respect to the total isocyanate mixture). Ix-Py/z = mixture of isocyanate quasi-prepolymer (with free monomer) based on an isocyanate Ix(I1,I2,...) having a terminal NCO content = y %. The prepolymer being based on the polyol type Z(1,2,3,4) z = 1 : dipropylene glycol z = 2 : trimethylolpropane z = 3 : glycerin/propylene oxide addition product MW600 z = 4 : polypropylene glycol MW 400 (molecular weight : MW) or on the polyamine type Z(5,6,7) z = 5 : a polyamine having the formula : having a molecular weight of 2000 z = 6 : a polyamine having the formula : wherein R is isohexyl and which has a molecular weight of 2000 z = 7 : a polyamine having the formula : wherein R' is and which has a molecular weight of 313 Ix-Ty : = isocyanurate-trimer (with isocyanate monomer) mixture based on an isocyanate Ix(I1,I2...) having a terminal NCO content = y %. 2. Active hydrogen containing compounds : P1 = addition product of glycerin, propylene oxide and ethylene oxide, having a hydroxyl number of 35, 80 % primary OH groups, a molecular weight of 4800 and an equivalent weight of 1600. P2 = addition product of glycerin, propylene oxide and ethylene oxide, having a hydroxyl number of 28, a primary OH group content of 85 %, a molecular weight of 6000 and an equivalent weight of 2000. P3 = addition product of diethylene glycol with propylene oxide and ethylene oxide, having a hydroxyl number of 28, a primary OH groups content of 90 %, a molecular weight of 4000 and an equivalent weight of 2000. P4 = addition product of pentaerythrol with propylene oxide and ethylene oxide, having a hydroxyl number of 28, a primary OH groups content of 80 %, a molecular weight of 8000 and an equivalent weight of 2000. P5 = polytetramethylene oxide glycol (PTMG) having a hydroxyl number of 56, a primary OH groups content of 100 %, a molecular weight of 3000 and an equivalent weight of 1500. P6 = an addition product of sorbitol with propylene oxide and ethylene oxide, having a hydroxyl number of 400, a primary OH groups content of 55 %, a molecular weight of 840 and an equivalent weight of 140. P7 = addition product of glycerin and propylene oxide and terminal NH₂ groups, having a molecular weight of 5000 (Jeffamine T5000-TEXACO). P8 = polycaprolacton ester not according to the invention having a hydroxyl number of 56, a molecular weight of 2000 and an equivalent weight of 1000. P9 = polycondensate ester between diethylene glycol and adipic acid, having a hydroxyl number of 56, a molecular weight of 2000 and an equivalent weight of 1000. P10 = DURACARB 124 (PPG Industries Inc.-USA) = polycarbonate diol having an I OH number of 60. 3. Chain extenders, cross-linkers and amine initiators MEG = monoethylene glycol DEG = diethylene glycol BD = 1,4-butanediol TMP = trimethylolpropane (or possibly a liquid addition product of TMP with 1 mole ethylene oxide) TEOA = triethanolamine DEOA = diethanolamine MEOA = monoethanolamine CD400 = Jeffamine CD400 (TEXACO) = addition product of a diol initiator, with propylene oxide and terminal secondary NH groups, having a molecular weight of 400 and an equivalent weight of 200. EDA = ethylenediamine Quadrol = addition product of ethylendiamine and 4 moles PO IPDA = isophorondiamine AEPD = 2-amino-2-ethyl-1,3-propanediol AMP = 2-amino-2-methyl-1-propanol a2 = a polyamine having the formula : wherein R is isohexyl and which has a molecular weight of 200 (equivalent weght=100) b4 = a polyamine having the formula : wherein R′ is and which has a molecular weight of 256 (equivalent weight = 128). 4. Catalysts (except for amine initiators) a) Organolead catalysts (LC) LC1 = lead-2-ethylhexoate LC2 = lead-naphthenate b) Organobismuth catalysts (BC) BC1 = bismuth-(III)-2-ethylhexoate BC2 = bismuth-(III)-naphthenate c) Organotin catalysts (TC) TC1 = dimethyltindineodecanoate TC2 = dibutyltindiacetate TC3 = tetrabutyltindistanoxane dilaurate TC4 = dibutyltin dichloride d) Alkaline catalysts (AC) AC1 = 1,8-diazabicyclo (5,4,0) undecene-7-phenolate AC2 = idem AC1, but octoate salt AC3 = potassium octoate AC4 = sodium phenolate e) Zeolite type catalysts (ZC) ZC1 = sodium aluminium silicate - 3 Angström (powder) ZC2 = potassium aluminium silicate - 4 Angström (50 % powder, spread as a paste in ricinus oil) 5. Various additives a) Antioxidizers/UV absorbers (AO/UV) A mixture of antioxid ants and UV absorbers consisting in percent by weight of : 40 % trisphenylphosphite 20 % 2-(2-hydroxy-3,5-di tert.amyl-phenyl)-2H-benzotriazole 20 % pentaerythrityl-tetrakis [3-(3,5-di tert.butyl-4-hydroxyphenol)-propionate] 20 % di-sebacate ester of 4-hydroxy-2,2,6,6,-tetramethylpiperidine b) Tixotropic agents A200 = Aerosil 200 (DEGUSSA - Germany) Coagulated, fumed silicon dioxide having an active surface of 200 m²/gr and a grain size of about 12 µ. c) Colour pigment (concentrated dispersion in a P1 type active hydrogen containing compound). A mixture(in the proportions 1:1:1) of : titanium dioxide (white) copper phthalocyanine (blue) di-azo condensate (red) The concentrations given in the formulations relate to the solid pigments. d) Internal release agent (IRA) This release agent is based on a silicon, more in particular of the type polydimethylsiloxane-polyether copolymer having 90 % by weight siloxane and 10 % by weight polyether groups, the polyether chain containing 20 % ethylene oxide and 80 % propylene oxide units and the terminal groups being OH groups. 6) Kinetic process parameters a) FT : fibre forming time "fibre time" (expressed in seconds), indicates the beginning of the gelling, i.e. the moment on which a fibre can be drawn of the reaction mixture for example by means of a glass rod. This constitutes a measure for the pot-life. b) TFT : "tac free time" (expressed in seconds) is the time at which the surface skin becomes substantially dry, i.e. not any more sticky. c) DT : "demoulding time" (expressed in seconds) indicates the time at which the obtained film can be removed from the mould surface without problems, i.e. without sticking, deformation, etc.. d) run off : is a measure for the tendency of the reaction mixture, sprayed on the mould surface, to run off (at a too low viscosity build up) from a higher mould surface level to a lower level. The visual codes thereof are as follows : Code 0 : no "run off" (= ideal situation) Code 1 : tendency to run off (still satisfying) Code 2 : a slight run off (acceptable limit) Code 3 and higher : more definite run off (not acceptable) resulting in too large thickness variations of the sprayed film. 7. Properties of the sprayed films : D : apparent density (gr/cm³) ER : elongation at rupture (%) - ASTM D412 RR : tensile strength at rupture (MPa) - ASTM D412 TR : tear resistance in N/cm - ASTM D624 Shore A (D) : surface hardness - ASTM D2240 WOM : weatherometer test (accelerated light/heat aging test) under the following test conditions (ATLAS ES25 apparatus) xenon radiation source black panel temperature 88°C cycle : 3.8 hours light/1 hour dark (no direct water spray on samples) test duration : 1000 hours. In each of the examined cases, substantially no discouloration (ΔE<1.5) or gloss variation (gloss retention > 70 % with respect to the original gloss degree before the WOM test) has been determined. Internal codes relating to the visual degradation of the examined polyurethane film surface (cracks, brittleness) : code 0 : completely satisfying code 1 : tendency to cracks in surface (only microscopically visible) code 2 : small cracks in surface code 3 and higher : moderate to strong cracks (not acceptable). The mention "OK" for the visual appearance indicates that no visual defects concerning the micro porous skin structure, excessive gas bubbles, colour streak formation or gloss differences in the surface of the sprayed film, have been observed. The following Table 5 shows some specific examples of specific embodiments of the method according to the invention, except for Example 8 wherein use is made of caprolactone polyol P8. In these tables, the hereabove defined abbreviations and codes are thus used. Further, the technology processing conditions are in these examples the following ones : high pressure, two components spray unit (with spray pistol) raw materials temperature : 60°C metal mould surface temperature : 60°C total output of components : 20 gr/sec. sprayed film thickness : about 2 mm From the examples 21 to 25 following hereinafter in Table 6, it can be deducted that if one or more catalysts or initiators are deleted or if their concentration is strongly reduced, the reactivity is reduced too fast thereby arising a too critical run off of the reaction mixture and a too slow curing of the spayed film. In the examples 21 to 25 of Table 6, the same formulations as in exemple 1 are repeated, however the catalysts and initiators amount being reduced as shown in the Table. Example n° concentration (pph) FT (sec) TFT (sec) DT (sec) RUN OFF (CODE) VISUAL APPEARANCE LC1 AC4 AMP 1 0,5 0,8 5 8 30 120 1 OK 21 0,5 0 5 30 120 360 1-2 OK 22 0,25 0,4 5 25 120 300 2 OK 23 0,25 0,4 2,5 35 180 420 3 OK limit 24 0 1,5 5 120 600 +/-1h »3 unacceptable 25 0,5 0,8 0 180 600 +/-1h »3 unacceptable

Claims: A method for making a light stable polyurethane film comprising the steps of : preparing a polyurethane reaction mixture containing an isocyanate compound having at least two NCO-groups which are not directly attached to an aromatic group, and a compound containing active hydrogen with respect to NCO groups, and wherein the latter compound is reacting with said isocyanate compound in the presence of a chain extender and/or a cross-linker and a catalyst ; and spraying said reaction mixture by means of a spray pistol onto a surface so as to form said polyurethane film by at least one pass of the spray pistol over said surface, characterized in that, in order to permit said reaction mixture to be sprayed in a homogeneous thickness of 0,3 to 3 mm per pass of said spray pistol onto an open mould surface and to permit the so obtained polyurethane film to be demoulded after a demoulding time ("DT") less than 10 minutes, (a) use is made of an active hydrogen containing compound, other than a caprolactone polyol, wherein the functional groups consist for at least 50 % of an active CH₂OH, NH and/or NH₂ group, the functionality of which varies from 2 to 8 and the equivalent weight of which is comprised between 100 and 3500, together with 2 to 300 parts, per 100 parts of said compound, of a chain extender and/or a cross-linker, the functional groups of which are OH groups, at least 50 % of which are primary OH groups, the equivalent weight of which is less than 100 and the functionality of which varies from 2 to 6, and with a catalytic system which comprises at least an organic lead, bismuth and/or tin (IV) compound and at least an amine initiator, having a functionality of 2 to 6, an equivalent weight lower than or equal to 200, and at least one aliphatic or alicyclic NH₂ or NH group; and (b) said reaction mixture is preheated upto a temperature not higher than 120°C so that its viscosity is situated between 500 and 1200 cps upon spraying, and said open mould surface is preheated to a temperature of between 30 and 100°C. A method according to claim 1, characterized in that at the most 0.4 % of water and at the most 0.04 moles of a physical blowing agent, having a boiling point of 20 to 70°C, is added with respect to 100 grams of said active hydrogen containing compound, cross-linker, chain extender and initiator. A method according to anyone of claims 1 or 2, characterized in that an isocyanate is used consisting mainly of IPDI monomer and/or a mixture of IPDI monomer and IPDI derivatives, such as trimers, especially isocyanurate or biuret trimers, prepolymers and/or carbodiimide/urethidion derivatives, in such ratio's which allow to obtain a NCO value of 15 to 37.8 in procent by weight. A method according to anyone of claims 1 to 3, characterized in that an isocyanate is used consisting mainly of TMXDI monomer, (with meta and/or para isomer), prepolymers, biuret trimer and/or carbodiimide/urethidion derivatives, in such ratio's which allow to obtain a NCO value of 15 to 34.4 in percent by weight. A method according to anyone of claims 1 to 4, characterized in that use is made of an isocyanate consisting mainly of HDI monomer possibly with HDI derivatives, such as trimers, especially isocyanurate or biuret trimers, prepolymers and/or carbodiimide/urethidion derivatives, in such ratio's which allow to obtain a NCO value of 15 to 50 in percent by weight. A method according to anyone of claims 1 to 5, characterized in that an isocyanate is used consisting mainly of H6XDI monomer possibly with H6XDI derivatives, such as trimers, especially isocyanurate or biuret trimers, prepolymers and/or carbodiimide/urethidion, derivatives, in such ratios which allow to obtain a NCO value of 15 to 43 in percent by weight. A method according to anyone of claims 1 to 6, characterized in that an isocyanate is used consisting mainly of H12MDI monomer possibly with H12MDI derivatives, such as trimers, especially isocyanurate or biuret trimers, prepolymers and/or carbodiimide/urethidion derivatives, in such ratio's which allow to obtain a NCO value of 15 to 31.8 in percentage by weight. A method according to anyone of claims 3 to 7, characterized in that prepolymers based on polyetherpolyols, chain extenders and/or cross-linkers having as functional groups only OH (primary and/or secondary) a functionality of 2 to 6 and a hydroxyl number of 15 to 1800, are used. A method according to anyone of claims 1 to 8, characterized in that use is made of an active hydrogen containing compound, consisting mainly of polyether alcohols which are formed by the polyaddition of propylene oxide and/or ethylene oxide on low molecular initiators. A method according to anyone of claims 1 to 9, characterized in that use is made of an active hydrogen containing compound which comprises polyester alcohols consisting of the ester condensation products of dicarboxylic acids with low molecular polyalcohols having a functionality of 2 to 4. A method according to anyone of claims 1 to 10, characterized in that use is made of an active hydrogen containing compound consisting mainly of polytetramethylene ether glycols (PTMG). A method according to anyone of claims 1 to 11, characterized in that use is made of an active hydrogen containing compound consisting mainly of polyetherpolyols having a functionality of 2 to 3, a hydroxyl number of 15 to 200, and which are possibly modified with polymerized organic fillers, such as polyols grafted with styrene/acrylonitrile, PHD polyols and PIPA polyols, the filler content varying from 0 to 50 % by weight. A method according to anyone of claims 1 to 12, characterized in that use is made of an active hydrogen containing compound consisting mainly of polyols having at least 70 % primary OH groups. A method according to anyone of claims 1 to 13, characterized in that use is made of a chain extender and/or cross-linker consisting mainly of at least one of the following substances : ethylene glycol, propanediol, triethanolamine, butanediol, pentanediol, hexanediol, glycerin, trimethylpropane, trimethylolethane, pentaerythrol, bisphenol A, cyclohexanedimethanol, and ethylene oxide addition products of these substances with less than 5 moles ethylene oxide per mole of said substances. A method according to anyone of claims 1 to 14, characterized in that use is made of a catalytic system consisting at least of two elements being said amine initiator and at least one of the following metal compounds : (a) organic lead and/or bismuth catalysts, especially salts of organic acids, such as octoate and naphthenate salts, or (b) Sn (IV) carboxylates having general formula (A) : wherein R₁ represents a methyl group and R₂ forms a (C₁-C₁₂) alkyl radical or a naphthenic acid radical, the alkyl radicals being linear or branched, or (c) dialkyldistannoxane dicarboxylates having general formula (B) : wherein R₁ represents a (C₁-C₄) alkyl radical and R' a (C₁-C₁₂) whether or not branched alkyl radical or (d) alkyltinhalides having general formula (R₁) x Sn(Hal) y , wherein R₁ represents a (C₁-C₄) alkyl radical and "(Hal)" a chlorine or bromine atom, x + y = 4 and x or y varies from 1 to 3. A method according to anyone of claims 1 to 15, characterized in that use is made of an amine initiator comprising at least one of the following compounds : monoethanolamine, diethanolamine, diisopropanolamine, ethylenediamine, isophoronediamine, N,N'-dimethyl(diethyl)-ethylenediamine, 2-amino-2-methyl(or ethyl)-1-propanol, 2-amino-1-butanol, 3-amino-1,2-propanediol, 2-amino-2-methyl(ethyl)-1,3-propanediol "Jeffamines" (Texaco) (propylene oxide addition products having mainly terminal primary NH₂ or secondary NH groups - functionality 2 à 3 - equivalent weight < 200). A method according to anyone of claims 1 to 16, characterized in that use is made of a catalytic system comprising at least an amine initiator together with an organic lead, tin or bismuth compound and (a) a zeolite type catalyst formed of an alkaline aluminium silicate with sodium and/or potassium ions, and/or (b) an alkaline catalyst having a pH higher than 10 and consisting of diazobicyclo-alkenes or salts of the latter with weak organic acids or consisting of potassium, sodium or lithium salts of weak organic acids. A method according to anyone of claims 1 to 17, characterized in that an internal release agent is added to the reaction mixture, consisting preferably of a polydimethylsiloxane-polyether copolymer having less than 20 % by weight of polyether with respect to the total molecule and less than 50 % by weight ethylene oxide with respect to the sum of ethylene oxide and propylene oxide in the polyether chain, the concentration of this release agent varying between 0 and 5 % by weight with respect to the total polyurethane polymer amount. A method according to anyone of claims 1 to 18, characterized in that use is made of a tixotropic thickening agent consisting preferably of fumed coagulated silicon dioxide at a concentration between 0 and 3 % by weight with respect to the total polyurethane amount. A method according to anyone of the previous claims, characterized in that said polyurethane reaction mixture is sprayed according to a two components system, wherein one component comprises the isocyanate and all of the additives which are with respect to this isocyanate during a sufficient time period stable and compatible with the latter and wherein the other component comprises the compounds containing active hydrogen with respect to NCO groups, especially polyols, chain extenders and cross-linkers, and additives which are with respect to these compounds during a sufficient time period stable and compatible with the latters. A method according to claim 20, characterized in that the components are preheated up to a temperature not higher than 120°C and preferably between 30 and 70°C, before the spraying. A method according to claim 20 or 21, characterized in that the temperature of the polyurethane reaction mixture is adjusted upon spraying in such a manner that the viscosity thereof is not higher than 700 cps. A method according to anyone of claims 20 to 22, characterized in that said open mould surface, the polyurethane is sprayed on, is kept at a temperature of 50 to 80°C. A method according to anyone of claims 20 to 23, characterized in that the density of the sprayed polyurethane film is adjusted between 500 and 1200 kg/m³ by adapting the amount of blowing agent and dispersed air in the raw materials. A method according to anyone of claims 20 to 24, characterized in that a polyurethane film, substantially free of pores and having a density of 900 to 1200 kg/m³ is formed by degassing and dehydrating before the spraying, at least the component comprising the active hydrogen containing compound. A method according to anyone of claims 20 to 25, characterized in that the hardness of the sprayed polyurethane film is adjusted between shore A 20 and shore D 80 by selecting the type and the amount of the isocyanate, the active hydrogen containing compound, the chain extender and/or the cross-linker.

Inventors: DU PREZ EDDIE, JOURQUIN LUCIEN, DU PREZ, EDDIE, JOURQUIN, LUCIEN
Applicants: RECTICEL
Application year: 1990
Main classification: C09D175
IPC codes: C08G18, B05D7, C08L75, C08G101