PROCESS FOR THE PREPARATION OF DENSE POLYURETHANIC FILMS AND THEIR USE

Abstract: Dense films to be used in the separation or enrichment of oxygen in the air, consisting either of a hydrodispersable poly­ urethane containing ionizable groups inside the macromole­ cule in amounts ranging between 10 and 60 meq/100 g of dry product, or of a hydrodispersable polymer of α-β-ethylenically unsaturated monomers, modified by at least 5% by weight of an oligourethane containing ionizable groups and functional α-β unsaturated end groups of acrylic and/or methacrylic na­ ture.

Description: The present invention relates to a process for the preparation of dense polyurethane films. More particularly the invention relates to dense polyurethane films, suited to be used for the enrichment of the air in oxygen. Membrane gaseous separations and in particular the enrichment of the air in oxygen are of always wider industrial interest, as they allow to obtain significant energy savings in the combustion, in the production of chemical substances by oxidative way, in the production of ammonia and methanol and so on. Although in the later decade a lot of polymeric materials have been studied, to be used in such field, no product has been yet obtained, capable to achieve high permeabilities towards the gases together with high separation factors O₂/N₂. Polysiloxane, one of the most studied and used elastomeric materials, for instance, presents a permeability towards O₂, that is among the highest ones, whereas the spearation factor O₂/N₂ is very low (∼2). That entails the impossibility to achieve oxygen enrichments over 30 %, and, for a fixed percentage of oxygen enrichment, the use of working pressure gradients higher in comparison with materials at high separation factors. In the class of the elastomeric polyurethanes there are some polymers having a high permeability towards gases and vapours. A few of these are described in Japanese patent application No. 74026702. According to what is described in the above application, films of elastomeric polyurethanes are obtained: a)by adding an aliphatic carboxylic acid having up to 4 carbon atoms, in amounts ranging between 6-40%, to a solution of an elastomer polyurethane, whose segments consist of polyester-glycol or of a mixture of polyester-glycol and polyether-glycol, and b) by coagulating the solution in a bath consisting of a solvent and of a non-solvent for the elastomer, such as dimethyl-formamide or dimethyl-acetamide and water. A part from the drawbacks of the process due to the use of an organic solvent, the obtained films present a separation factor, that is not yet completely satisfactory especially when they are employed for the enrichment of oxygen in the air. An object of the present invention is to obtain elastomeric films which, besides having permeabilities comparable with those of the polyxiloxane films, allow to obtain higher separation factors O₂/N₂, with respect to the latter. Another object of the present invention is to obtain films of polymeric materials which may be prepared easily and economically. A further object of the present invention is to obtain films of polymeric materials that may be coupled with polymeric films of different nature, without utilizing solvents and therefore without damaging and destroying the latter. Now it has been found that the said objects are attained by using a dense film either of a hydro-dispersable polyurethane containing ionizable groups inside the macromolecule in amounts ranging between 10 and 60 meq/100 g of dry product, or of a hydro-dispersable polymer of α-β-ethylenically unsaturated monomers, modified by at least 5% by weight of an oligourethane containing ionizable groups and functional α-β-unsaturated end groups of acrylic and/or methacrylic nature. The hydro-dispersable polyurethanes containing ionizable groups inside the macromolecule are already known and described in issued EP-A-98752. Said polyurethanes are obtained according to a process consisting in: a) preparing firstly a polyisocyanate prepolymer, by reacting, at a temperature not over 100°C, an organic diisocyanate and a mixture consisting of a diol containing ionizable groups and of a substantially linear macroglycol, having a molar weight ranging between 500 and 5000, in such amounts that the molar ratio between the isocyanate groups and the sum of the hydroxyl groups of macroglycol and of diol ranges between 1.2 and 2.O; b) preparing an oligourethane containing ethylenically unsaturated end groups by reacting the polyisocyanic prepolymer obtained hereinbefore with a hydroxy-alkyl-acrylate and/or a hydroxy-alkyl-methacrylate having formula: wherein R is hydrogen or-CH₃ and X is a hydroxyalkyl radical containing from 1 to 8 carbon atoms, at a temperature below 150°C and in such amounts that the ratio by equivalents between the free isocyanate NCO groups and the OH groups of hydroxy-alkyl-acrylate or methacrylate having formula (I), ranges between 0.2 and 1.1, and preferably between 0.4 and 0.6; c) salifying the free ionizable groups of oligourethane to hydrophilic cations or anions such as, respectively, quaternary ammonium and carboxylate, sulphonate, or phosphonate groups, and d) subjecting to a polymerization treatment the unsaturated end groups of oligourethane, containing hydrophilic cationic or anionic groups, in an aqueous dispersion, in the presence of radical catalysts and at a temperature not over 100°C, in order to obtain an aqueous dispersion of polyurethane having a pre-established reticulation degree. The reticulation degree can be regulated by addition of copolymers in polymerization phase. The formation of polyisocyanate prepolymer and the subsequent reaction with hydroxy-alkyl-acrylate and/or methacrylate having formula (I) may be carried out in complete absence of organic solvents and in the presence or not of known catalysts such as tin-organic compounds, tertiary amines. For the preparation of the polyisocyanic prepolymer use may be made of macroglycols having a molar weight ranging between 500 and 5000, preferably between 800 and 3000, selected among saturated polyesters, polyethers and polyesters-urethanes. Examples of utilizable macroglycols are: the polyesters obtained by polycondensation of bicarboxylic acids or anhydrides, preferably the aliphatic ones, having from 4 to 9 carbon atoms, with aliphatic diols having 2-8 carbon atoms, which can be used singly or mixed together; the polyesters obtained by polycondensation on diolic "starters" of ε-caprolactone; the polyaddition products of the above mentioned polyesters with organic diisocyanates in molar deficiency; polyethylene glycol; polypropylene glycol; the polymerization products of tetrahydrofuran, etc. These macroglycols may be use singly or in mixture with small amounts of a polyalcohol haying a low molecular weight, of bi or tri-functional type, such as 1,4-butanediol, 1,6-hexanediol, tri-methylolpropane, glycerol, 1,2,6-hexanetriol etc. The utilizable organic diisocyanates may be both of aliphatic and of cycloaliphatic type. Examples of utilizable diisocyanates are: 4-4'-dicyclohexil-methanediisocyanate; 1-isocyanate-3-isocyanate-methyl-3,5,5-trimethylcyclohexane (or isophoronediisocyanate); 2,2,4-trimethylhexanethylenediisocyanate in mixture with isomer 2,4,4-trimethylhexamethylenediisocyanate, etc. As ionizable diols, use may be made of the ones capable of bestowing on the polyurethane macromolecule a preferably anionic charge, such as for instance: diols containing at leapt a free carboxylic group, diols containing at least a phosphonic group; diols containing at least a sulphonic group. In practice one prefers to use diols containing at leapt a free carboxylic group bound to the same carbon atom holding the two hydroxyl groups, for instance dimethylolacetic, dimethylolpropionic and dimethylolbutyric acid. Furthermore use may be made of the compounds containing at least two hydroxyl groups and a carboxylic group, that is not bound to the same carbon atom, such as for instance the products of hemiesterification of triols with aliphatic bicarboxylic anhydrides. As ionizable diols use may be also made of alkyl-dialkanol-amines, such as methyl-di-ethanol-amine, butyl-di-ethanol-amine and methyl-di-isopropanol-amine. The free ionizable groups, distributed statistically on the oligourethane chain, are successively salified both by means of inorganic bases such as sodium, potassium or ammonium hydroxide, and,preferably, by means of amines or tertiary alkanolamines such as triethylamine, dimethyl-ethanol-amine and methyl-diethanol-amine. The teriary nitrogen atom of the tertiary alkyl-dialkanol amines is salified by means of organic or inorganic acids such as hydrochloric, phosphoric and acetic acid. The salification of the oligourethane may be carried out by simple addition of the salifying agent either as such or dissolved in water and/or solvents at a temperature of about 60°C. Should the oligourethane have a too high viscosity at such temperatures, a dilution of same is suitable, before the salification, by means of solvents which are preferably miscible in water and have a boiling temperature below that of water, so that they may be removed by distillation. The amount of solvent, that is usually used, is not over the fifth of the oligourethane weight. The preferred solvents are: acetone, methyl-ethylketone, tetrahydrofuran. When the salification is over, subject to an optional dilution in organic solvents as described hereinbefore, the oligourethane is diluted in any ratio with water. Therefore one starts the dispersion in water, in order to obtain oligourethane concentrations which are variable, according to the content in ionizable groups. Concentrations ranging between 20 and 60% by weight and preferably between 30 and 50% by weight, are preferred. The unsaturated oligourethane, dissolved or dispersed in water as described hereinbefore, may be then polymerized by known techniques of radicalic polymerization. As catalysts use may be made of organic peroxides or hydroperoxides, such as benzoyl peroxide, dicumyl peroxide, ter-butyl-hydroperoxide, cumene hydroperoxide, p-menthane hydroperoxide, or sodium, potassium, ammonium persulfate, used singly or in combination with reducers such as sodium metabisulphite and sodium-formaldehyde-sulfoxylate. The polymerization temperature is not over 100°C and preferably ranges between 10 and 100°C, depending on the type of initiator or of the couple initiator-reducer; the most preferred temperature range is between 50° and 70°C. The presence of oligourethanes containing at least 2 unsaturated end groups leads to the formation of reticulated tridimensional macromolecular structures and the reticulation degree can be regulated at will, by carrying out the polymerization in the presence of other mono or polyfunctional ethylenically unsaturated monomers such as methyl, ethyl, butyl acrylates or methacrylates, vinyl esters, styrene, trimethylol-propane-triacrylate and trimethacrylate, pentacrythritol triacrylate and trimethacrylate, 1,6-hexanediol diacrylate, neopentylglycol di-acrylate and di-methacrylate, di-ethylene glycol di-acrylate and tetraethylene glycol di-acrylate. The hydrodispersable polymers of α-β-ethylenically unsaturated monomers modified by at least 5% by weight of an oligourethane containing ionizable groups and functional α-β-unsaturated end groups of acrylic and/or methacrylic nature, are described in EP-A-183 119 and are obtained by polymerization of one or more α-β-ethylenically unsaturated monomers in the presence of an aqueous dispersion of the oligourethane obtained in above reported stage c) and containing salified ionizable groups and functional α-β-unsaturated end groups of acrylic and/or methacrylic nature. Oligourethanes having a molecular weight ranging between 2.000 and 50.000 and containing at leapt two ethylenically unsaturated end groups, are preferred. The presence of α-β-unsaturated groups in the oligourethanes ensures a good copolymerization with the ethylenically unsaturated monomers, thereby allowing the formation of homogeneous structures. These oligourethanes, containing unsaturated acrylic and/or methacrylic end groups, may be used in any ratio with respect to the α-β-unsaturated monomers to be polymerized. Usually, the higher the oligourethane amount, the higher the characteristics of chemical and physical resistance of the films, due to the increase of the reticulation degree of the finished polymer. The high reticulation of the polymer is due both to the ethylenic bifunctionality of oligourethane itself and to the well known tendency of the urethanic groups to form cross-linkings through formation of hydrogen bridges. Use may be made of oligourethane amounts up to 90% by weight referred to the finished copolymer. In practice, amounts ranging between 10 and 60% by weight are preferred. The unsaturated oligourethane, dissolved or dispersed in water, is copolymerized with α-β-ethylenically unsaturated monomers, according to known techniques of radical polymerization. The polymerization is carried out preferably by feeding the monomer or the mixture of α-β-ethylenically unsaturated monomers as such into the aqueous dispersion of the preformed oligourethane. With the term "α-β-ethylenically unsaturated monomers", as used in the present application and in the claims, any compound is meant, containing the bond: C = C which can be polymerized or copolymerized with another similar comonomer in the presence of the unsaturated oligourethane dissolved or dispersed in water of the type above reported, using radicalic catalysts. Examples of α-β-ethylenically unsaturated monomers are: esters of acrylic and methacrylic acids such as ethyl acrylate, butyl acrylate, 2-ethyl-hexyl arylate, cyclo-hexyl-chloro acrylate, isobutyl-chloroacrylate, methyl-chloro acrylate, methyl-methacrylate, butyl-methacrylate, stearyl-methacrylate, phenyl-methacrylate, isopropyl-methacrylate, cyclo-hexyl-methacrylate, 3,3-dimethyl-2-butyl methacrylate etc., acrylonitrile, methacrylonitrile; the corresponding amides such as, acrylamide and methacrylamide optionally in the methylolated form and/or in the form successively eterified with monovalent C₁-C₄ alcohols; vinyl esters and ethers such as vinyl acetate, vinyl propionate,vinyl chloride, vinylidene chloride, vinyl-ethyl-ether; allyl compounds such as allyl alcohol and allyl acetate. Use may be also made of monomers containing two or more ethylenically unsaturated groups, such as butandiol diacrylate and dimethacrylate, trimethylpropane triacrylate and trimethacrylate, pentaerythrytol triacrylate and trimethacrylate. The α-β-ethylenically unsaturated monomers are polymerized in the presence of an aqueous solution or dispersion of unsaturated oligourethanes and using the well known initiators of radical polymerization such as potassium and ammonium persulphate, hydrogen peroxide, alkyl hydroperoxides such as terbutylhydroperoxide, cumene hydroperoxide, p-menthane hydroperoxide, di-cumyl peroxide, benzoyl peroxide and azo-bis-isobutyronitrile. Preferably these initiators are used in the presence of reducing agents, known in the prior art, to lower the temperature of radicalic decomposition, such as sodium metabisulfite, sodium-formaldehyde sulfoxylate, formic acid and ascorbic acid. Examples of couples initiator/reducer, preferred in the present invention, are: terbutyl-hydroperoxide/sodium-formaldehyde sulfoxylate and hydrogen peroxide/ascorbic acid. The initiator amounts that are used, range between 0.01 and 1%, preferably between 0.05 and 0.2% by weight, calculated on the total weight of the monomers. The feed time, both of the monomers and of the initiator may be varied between 2 and 8 hours, preferably between 3 and 5 hours, taking care of feeding the initiator in a period of time 30-60 minutes higher than the one of the monomers. The polymerization temperatures depend both on the nature of the used monomers and on the used catalytic system; they usually range between 40 and 90°C, preferably between 40 and 70°C. At the end of the feed of the initiator and/or of the catalytic couple, the copolymerization is usually over. The final aqueous solutions, containing from 20 to 60% by weight of dry polymer, are characterized by a high stability during the storing, even if surfactants with a low molecular weight, are completely absent. The dense films, object of the present invention, are produced by turning into film the aqueous dispersions of polyurethanes containing ionizable groups inside the macromolecule and the polymers of ethylenically unsaturated monomers modified by an oligourethane containing ionizable groups and functional unsaturated acrylic and/or methacrylic groups. The transformation into film of these aqueous dispersions may be carried out according to any known technique, such as, for instance, by spreading on a polyethylene support or on asymmetric membranes made of polymeric materials, below their glass transition temperature (in order to obtain a composite membrane) or by deposition on a roller or by evaporation of the water content of the dispersion deposited on mercury as well. According to the "casting" technique, the aqueous dispersion, containing from 20 to 60% by weight of dry polymer, is spread on a plane coated with polyethylene, delimited by edges made of polyvinyl chloride of about 1 mm. The spread dispersion is kept at room temperature till complete evaporation of the water. The film thus obtained can be removed easily and can be heated at 40-60°C in an oven for 10-24 hours in order to obtain a further reticulation. Should the transformation into film be carried out by deposition on a roller, the content by weight of dry polymer in the aqueous dispersion is 5-20%. The dispersion is poured into a small basin, into which a roller coated with Teflon, is dipped. The roller is rotated at a speed ranging between 0.5 and 5 revolutions/minute and a laminar stream of air is blown tangentially to the roller surface. Successive layers of films of polymer deposit in a homogeneous and regular way on the roller surface. The roller rotation is stopped when the desired thickness of the film is reached. The thickness of the film ranges between 10 and 200 µm. The film is removed from the roller and, if necessary, subjected to a further reticulation by treatment in an oven at 40-60°C for 10-24 hours. The transformation into film by evaporation of the water on mercury is carried out by pouring slowly an aqueous dispersion of the polymer, containing from 5 to 40% by weight of dry product, onto mercury contained in a crystallization vessel. The crystallization vessel is laid on an antivibrating plane in order to avoid the film curliness. After complete evaporation of the water, the film is removed and optionally treated in an oven, for a further reticulation, at 40-60°C. The aqueous dispersions of the polymer to be turned into a film, may contain, besides the polymer, other sub stances such as thickening agents, film forming substances, surfactants, etc. The polyurethane films thus obtained present a permeability towards the oxygen ranging between 6x10⁻⁸ and 2x10⁻⁹ cm³ (STP)cm/cm² sec. cm Hg and a separation factor oxygen/nitrogen over 2 and up to 4. Permeability and separation factor are determined by the methods described in example 1. The present invention will be further explained by the following examples. EXAMPLE 1 PREPARATION OF THE AQUEOUS POLYURETHANE DISPERSION . 254.78 g of polyoxytetramethylene glycol having a molar weight of about 980 (a commercial product by Du Pont de Nemours with trade mark Terathane 1000); 16.08 g of dimethylolpropionic acid 0.008 g of benzoyl chloride were loaded, according to the order described hereinbefore, into a reactor equipped with stirrer, thermometer and reflux cooler, kept under atmosphere of dry nitrogen and dipped in a bath with a temperature regulator. 86.2 g of hexamethylenediisocyanate were added at once at about 40°C. The reaction exothermicity was first controlled, so not to exceed 60°C; and then the temperature was raised to 80°C, till a content in free isocyanate groups of about 3.8% by weight was reached. The nitrogen atmosphere was replaced by dry air, then 17.29 g of 2-hydroxypropyl acrylate were added drop by drop. The reaction was carried on till a content in free isocyanate groups of about 2.4% by weight was reached. A solution, prepared separately, containing 8.02 g of dimethylethanol amine in 120 ml of deionized water, was added, quick and under strong stirring, to the mass of the prepolymer, afterwards a further addition of 760 g more of deionized water followed immediately. Then the nitrogen atmosphere and the thermoregulation, by means of a thermostat, of the dispersion obtained at 65°C were restored. 12.9 g of an aqueous solution of ter-butylhydroperoxide at 12% by weight were dripped over 2 hours and, at the end, the dispersion was kept at 65°C for one more hour. The final dispersion had a milk-like, translucent aspect, a content of solids of 30% by weight and a content of anionic groups of about 24 meq/100 g of dry substance. PREPARATION OF THE DENSE FILM . From the above obtained polyurethanic aqueous dispersion a dense film was prepared, having a thickness of 10 microns, according to the technique relating to the deposition of successive layers on a roller. Use was made of: a dispersion having a content of solids of 15% by weight; a roller haying a diameter of 12 cm; a roller speed of 1/4 revolution/minute and an evaporation temperature of 60°C. The time used for the preparation was 6 hours. From the film thus obtained, a disk was drawn having a diameter of 7 cm, that was put into a cell for the permeability measurement and conditioned for 12 hours with a helium flow on both the surfaces. Successively a flow of air at a pressure of 100 cm Hg (7,50 Pa) was conveyed onto the lower surface of the membrane, whereas a flow of helium of 1.4 cm³/second at a pressure of 70 cm Hg (5,25 Pa) was conveyed onto the upper surface. The latter, diluting the permeated gag insures that the difference of partial pressures of 0₂ and N₂, to which the film is subjected, remains constant. The working temperature had been fixed at 30°C, whereas the temperature of the environment at 22°C. The conveyance helium had been sampled by means of a Carlo Erba valve and then analysed by means of a Carlo Erba gas chromatograph of Fractovap 4200 series with molecular sieves columns 5A having a diameter of 4 mm and a length of 2 m. The measurement was carried out at a temperature of the detector equal to 110°C. The resultant gas chromatogram was recorded and integrated by means of an integrating recorder Hewlett Packard 3390. By such process, for the film in question, a permeability was calculated towards O₂ (PO₂) = 1.5x10⁻⁸ cm³ (STP) cm/cm² sec cm Hg and a separation factor: F(O₂/N₂) = 2.6. EXAMPLE 2 PREPARATION OF THE POLYURETHANIC AQUEOUS DISPERSION . 260 g (0.26 moles) of polyoxytetramethylene glycol (produced by Du Pont de Nemours with trade mark Terathane 1000); 16.08 g (0.12 moles) of dimethylolpropionic acid; 0.076 g of benzoyl chloride (as stabilizing agent of the prepolymer) and 86.29 g (0.513 moles) of hexamethylenediisocyanate were loaded in the order described hereinbefore into a reactor equipped with stirrer, thermometer, reflux cooler, system for the regulation of the temperature and compensating tank containing dry nitrogen. The exothermicity of the reaction was controlled, keeping the temperature of the mass under stirring at about 60°C for 30 minutes; then the temperature was brought to 80°C and kept at this value till the content in free isocyanate groups was below 3.6-3.8% by weight. 17.29 g (0.133 moles) of 2-hydroxypropylacrylate were added to the prepolymer thus obtained, cooled down to about 60°C and diluted with 90 ml of anhydrous acetone, changing the atmosphere from nitrogen to dry air. The temperature was kept at about 60°C till a content in free isocyanate groups of 1.7-1.9% by weight was reached. An aqueous solution of 10.7 g of dimethylethanolamine in 250 cc of deionized water was added, under efficient stirring, over 5 minutes, afterwards immediately the addition followed of further 635 g of deionized water. Then the acetone present was distilled under a weak vacuum. The final dispersion had a content of dry product of 31% by weight, consisting of an unsaturated oligourethane with a content of 30.7 milliequivalents of salified carboxylic groups per 100 g of dry product and having a calculated molecular weight of about 5500. 145.2 g of the oligourethane dispersion thus obtained and 600 g of deionized water were loaded into a reactor equipped with stirrer, thermometer, cooler, dosing funnels, compensating tank containing nitrogen and dipped in a thermostatic bath. The dispersion was thermoregulated at 50°C by means of a thermostat. On the reactor 3 dropping funnels were arranged, containing respectively: 405 g of a mixture 1/1 by weight consisting of butyl acrylate and methylmethacrylate 3.75 g terbutylhydroperoxide in an aqueous solution at 12% by weight, diluted in 125 g of deionized water 0.225 g of sodium-formaldehyde sulfoxylate dissolved in 125 g of deionized water. From the dropping funnels one fed simultaneously about 20 g of the monomer mixture and about 12 g of the aqueous solutions of initiator and reducing agent. One waited for the reaction start to take place, showed by the spontaneous increase of the temperature of about 3-4°C, then one started the three feeds, in such a way as to use up the monomer mixture over 3 hours and the two solutions of the catalytic couple over 3.5 hours. During the feeds, the temperature was kept at about 54-55°C. About 60 minutes after the end of the couple feed, the gaschromatographic analysis showed a substantial absence of free monomers. The final dispersion was practically free from precoagulum, had a content in dry product of 30.8% by weight and a surface tension of 62 dynes/cm. PREPARATION OF THE DENSE FILM The film was prepared by evaporation of the water contained in a thin layer of such an aqueous dispersion at 35% of solid substance, deposited on mercury. After 48 hours, at a temperature of 20°C, a film was obtained having a thickness of 150 µm. The latter, characterized according to the conditions reported in example 1, gave a permeability towards O₂(PO₂) = = 7x10⁻⁹ cm³ (STP) cm/cm² sec cm Hg and a separation factor F(O₂/N₂) = 3.

Claims: A process for the preparation of dense polyurethane films selected from the group consisting of 1) films of a hydro-dispersable polyurethane containing ionizable groups inside the macromolecule in amounts ranging between 10 and 60 meq/100 g of dry product; or 2) films of a hydro-dispersable polymer of α,β-ethylenically unsaturated monomers modified by at least 5% by weight of an oligourethane containing ionizable groups and functional α,β-unsaturated end groups of acrylic and/or methacrylic nature which films have a thickness in the range from 10 to 200 µm and have a permeability towards oxygen ranging between 7.99 · 10⁻⁵ and 2.66 · 10⁻⁶ cm³ (STP) cm/cm² Pa.s (6 · 10⁻⁸ and 2 · 10⁻⁹ cm³ (STP) cm/cm² sec. cm Hg) and a separation factor oxygen/nitrogen over 2 and up to 4 , characterized in that aqueous dispersions are evaporated which are produced according to a process consisting in: a) preparing at first a polyisocyanate prepolymer, by reacting at a temperature not over 100°C, an organic diisocyanate and a mixture consisting of a diol containing ionizable groups and a substantially linear macroglycol, having a molecular weight ranging between 500 and 5000, in such amounts that the molar ratio between the isocyanate groups and the sum of the hydroxyl groups of macroglycol and of diol ranges between 1.2 and 2.0; b) preparing an oligourethane containing ethylenically unsaturated end groups by reacting the above obtained polyisocyanate prepolymer with a hydroxy-alkyl-acrylate and/or a hydroxy-alkyl-methacrylate having formula: wherein R is hydrogen or -CH₃ and X is a hydroxyalkyl radical containing from 1 to 8 carbon atoms, at a temperature below 150°C and in such amount that the ratio by equivalents between the free isocyanate NCO groups and the OH groups of hydroxy-alkyl-acrylate or methacrylate of formula (I) ranges between 0.2 and 1.1, and preferably between 0.4 and 0.6; c) salifying the free ionizable groups of oligourethane to hydrophilic cations or anions, respectively, quaternary ammonium and carboxylic, sulphonic or phosphonic groups, and d) subjecting to a polymerization treatment: 1) the unsaturated end groups of oligourethane, containing hydrophilic cationic or anionic groups, in an aqueous dispersion, in the presence of radical catalysts at a temperature not over 100°C, in order to obtain an aqueous dispersion of polyurethane having a pre-established reticulation degree; or 2) the unsaturated end groups of oligourethane, containing hydrophilic cationic or anionic groups, in an aqueous dispersion, in the presence of radical catalysts and of α-β-ethylenically unsaturated monomers at a temperature not over 100°C, in order to obtain an aqueous dispersion of polyurethane having a pre-established reticulation degree. A process for the preparation of dense polyurethane films according to claim 1 wherein the oligourethane has a molecular weight ranging between 2.000 and 50.000 and contains at least two ethylenically unsaturated end groups. A process for the preparation of dense polyurethane films according to anyone of the preceding claims, characterized in that an aqueous dispersion of the polyurethane or of the hydrodispersable polymer having a concentration ranging between 20 and 60% by weight is spread on a plane, and, after complete evaporation of the water, the obtained film is heated in an oven at 40-60°C for 10-24 hours. A process for the preparation of dense polyurethane films according to anyone of the preceding claims 1 to 3, characterized in that it consists in rotating, at a speed ranging between 0.5 and 5 revolutions/minute, a roller coated with polytetrafluoroethylene in an aqueous dispersion of polyurethane or of the hydrodispersable polymer having a concentration ranging between 5 and 20% by weight, and after having obtained a film thickness ranging between 10 and 200 µm, the film is removed and heated at 40-60°C for 10-24 hours. A process for the preparation of dense polyurethane films according to anyone of the preceding claims 1 to 3, characterized in that an aqueous dispersion of the polymer or of the hydrodispersable polyurethane haying a concentration ranging between 5 and 40% by weight, is poured onto mercury, and after complete evaporation of the water, the film is removed and treated thermically at 40-60°C. Use of the dense polyurethane films obtainable according to anyone of the preceding claims 1 to 5 for the enrichment of oxygen in the air.

Inventors: BASTIOLI, CATIA, DR., GIANOTTI, GIUSEPPE, TROVATI, ALDO, TURCO, PIETRO
Applicants: AUSCHEM S.P.A., ISTITUTO GUIDO DONEGANI S.P.A.
Application year: 1986
Main classification: C08G18
IPC codes: C08F299, C08J5, C08G18