Patent Application
20090263431
The invention relates to a process for producing polyurethane foams for wound management wherein a composition containing a polyurethane dispersion and specific coagulants is frothed and dried.
The use of wound contact materials made of foams for treating weeping wounds is prior art. Owing to their high absorbency and their good mechanical properties, polyurethane foams produced by reaction of mixtures of diisocyanates and polyols or NCO-functional polyurethane prepolymers with water in the presence of certain catalysts and also (foam) additives are generally used. Aromatic diisocyanates are generally employed, since they are best foamable. Numerous forms of these processes are known, for example described in U.S. Pat. No. 3,978,266, U.S. Pat. No. 3,975,567 and EP 0 059 048. However, the aforementioned processes have the disadvantage that they require the use of reactive mixtures, containing diisocyanates or corresponding NCO-functional prepolymers, whose handling is technically inconvenient and costly, since appropriate protective measures are necessary for example.
One alternative to the above-described process, in which diisocyanates or NCO-functional polyurethane prepolymers are utilized, is a process based on polyurethane dispersions (which are essentially free of isocyanate groups) into which air is incorporated by vigorous stirring in the presence of suitable (foam) additives. So-called mechanical polyurethane foams are obtained after drying and curing. In connection with wound contact materials, such foams are described in EP 0 235 949 and EP 0 246 723, the foam either having a self-adherent polymer added to it, or being applied to a film of a self-adherent polymer. In addition, the examples recited in EP 0 235 949 and EP 0 246 723 mandate the use as crosslinkers of polyaziridines which are no longer acceptable because of their toxicity. Moreover, crosslinking requires the use of high baking temperatures, reported to be in the range from 100° C. to 170° C. U.S. Pat. No. 4,655,210 describes the use of the aforementioned mechanical foams for wound dressings having a specific construction made up of backing, foam and skin contact layer. The foams produced according to the processes described in EP 0 235 949 and EP 0 246 723, moreover, have the immense disadvantage that the foams obtained are only minimally open-cell, reducing the absorbence of physiological saline and also the water or moisture vapour transmission rate.
The management of wounds having a complex topology or the coverage of particularly deep wounds is very difficult using ready-to-use, industrially manufactured sheetlike wound contact materials, since optimal covering of the wound surface is generally not accomplished, retarding the healing process. To achieve better covering of deep wounds, it has been proposed to use granules of microporous polyurethanes instead of compact wound dressings (EP-A-0 171 268). However, not even this achieves optimal covering of the wound.
The application of a (flowable) composition which optimally conforms to the wound shape would eliminate the disadvantages of sheetlike wound dressings. The two processes described above, which utilize either diisocyanates/NCO-functional polyurethane prepolymers or polyurethane dispersions in combination with polyaziridines to produce polyurethane foams, cannot be used for this, however: reactive compositions containing free isocyanate groups cannot be applied directly to the skin, even though this has been variously proposed (see WO 02/26848 for example). But even use of polyurethane dispersions with polyaziridines as crosslinkers is out of the question today because the crosslinker has properties which are not generally recognized as safe by toxicologists.
The present invention therefore has for its object to provide polyurethane foams for wound management by using a composition which is free of isocyanate groups. The production of the polyurethane foam shall in principle also be able to be carried out under ambient conditions, in which case the polyurethane foams, as well as good mechanical properties, formed shall have a high absorbence of physiological saline and a high water and moisture vapour transmission rate. This requires that the polyurethane foam have a certain open-cell content. Moreover, the composition shall be suitable for direct application to the skin, for example by spraying or pouring, in order that the wound may be optimally covered with the polyurethane foam; rapid drying is essential for this.
It has now been found that compositions containing polyurethane dispersions and specific cationic coagulants, both free of isocyanate groups, can be used to produce at ambient conditions polyurethane foams having good mechanical properties, a high absorbence of physiological saline and a high water and moisture vapour transmission rate. The polyurethane foams exhibit, at least to some extent, an open-cell pore structure. The flowable compositions, moreover, can be applied directly to the skin by spraying or pouring.
The present invention accordingly provides a process for producing wound contact materials made of polyurethane foams which comprises a composition containing an aqueous, anionically hydrophilicized polyurethane dispersion (I), a cationic coagulant (II) and additionally at least one active component selected from the group consisting of antiseptics, growth factors, protease inhibitors and non-steroidal anti-inflammatories/opiates being frothed and dried.
Polyurethane foam wound contact materials for the purposes of the present invention are porous materials, preferably having at least some open-cell content, which consist essentially of polyurethanes and protect wounds against germs and environmental influences like a sterile covering, have a fast and high absorbence of physiological saline or to be more precise wound fluid, have a suitable permeability for moisture to ensure a suitable wound climate, and have sufficient mechanical strength.
The aqueous, anionically hydrophilicized polyurethane dispersions (I) included in the compositions which are essential to the present invention are obtainable by
A) isocyanate-functional prepolymers being produced from
To achieve anionic hydrophilicization, A4) and/or B2) shall utilize hydrophilicizing agents that have at least one NCO-reactive group such as amino, hydroxyl or thiol groups and additionally have —COO− or —SO3− or —PO32− as anionic groups or their wholly or partly protonated acid forms as potentially anionic groups.
Preferred aqueous, anionic polyurethane dispersions (I) have a low degree of hydrophilic anionic groups, preferably from 0.1 to 15 milliequivalents per 100 g of solid resin.
To achieve good sedimentation stability, the number average particle size of the specific polyurethane dispersions is preferably less than 750 nm and more preferably less than 500 nm, determined by laser correlation spectroscopy.
The ratio of NCO groups of compounds of component A1) to NCO-reactive groups such as amino, hydroxyl or thiol groups of compounds of components A2) to A4) is in the range from 1.05 to 3.5, preferably in the range from 1.2 to 3.0 and more preferably in the range from 1.3 to 2.5 to prepare the NCO-functional prepolymer.
The amino-functional compounds in stage B) are used in such an amount that the equivalent ratio of isocyanate-reactive amino groups of these compounds to the free isocyanate groups of the prepolymer is in the range from 40 to 150%, preferably between 50 to 125% and more preferably between 60 to 120%.
Suitable polyisocyanates for component A1) include the well-known aromatic, araliphatic, aliphatic or cycloaliphatic polyisocyanates of an NCO functionality of ≧2.
Examples of such suitable polyisocyanates are 1,4-butylene diisocyanate, 1,6-hexamethylene diiso-cyanate (HDI), isophorone diisocyanate (IPDI), 2,2,4 and/or 2,4,4-trimethylhexamethylene diisocyanate, the isomeric bis(4,4′-isocyanatocyclohexyl)methanes or their mixtures of any desired isomer content, 1,4-cyclohexylene diisocyanate, 1,4-phenylene diisocyanate, 2,4- and/or 2,6-toluylene diisocyanate, 1,5-naphthalene diisocyanate, 2,2′- and/or 2,4′- and/or 4,4′-diphenyl-methane diisocyanate, 1,3- and/or 1,4-bis-(2-isocyanatoprop-2-yl)benzene (TMXDI), 1,3-bis-(isocyanatomethyl)benzene (XDI), and also alkyl 2,6-diisocyanatohexanoates (lysine diisocyanates) having C1-C8-alkyl groups.
As well as the aforementioned polyisocyanates, it is also possible to use, proportionally, modified diisocyanates of uretdione, isocyanurate, urethane, allophanate, biuret, iminooxadiazinedione and/or oxadiazinetrione structure and also non-modified polyisocyanate having more than 2 NCO groups per molecule, for example 4-isocyanatomethyl-1,8-octane diisocyanate (nonane triisocyanate) or triphenylmethane 4,4′,4″-triisocyanate.
Preferably, the polyisocyanates or polyisocyanate mixtures of the aforementioned kind have exclusively aliphatically and/or cycloaliphatically attached isocyanate groups and an average NCO functionality in the range from 2 to 4, preferably in the range from 2 to 2.6 and more preferably in the range from 2 to 2.4 for the mixture.
It is particularly preferable for A1) to utilize 1,6-hexamethylene diisocyanate, isophorone diisocyanate, the isomeric bis(4,4′-isocyanatocyclohexyl)methanes, and also mixtures thereof.
A2) utilizes polymeric polyols having a number average molecular weight Mn in the range from 400 to 8000 g/mol, preferably from 400 to 6000 g/mol and more preferably from 600 to 3000 g/mol. These preferably have an OH functionality in the range from 1.5 to 6, more preferably in the range from 1.8 to 3 and most preferably in the range from 1.9 to 2.1.
Such polymeric polyols are the well-known polyurethane coating technology polyester polyols, polyacrylate polyols, polyurethane polyols, polycarbonate polyols, polyether polyols, polyester polyacrylate polyols, polyurethane polyacrylate polyols, polyurethane polyester polyols, polyurethane polyether polyols, polyurethane polycarbonate polyols and polyester polycarbonate polyols. These can be used in A2) individually or in any desired mixtures with one another.
Such polyester polyols are the well-known polycondensates formed from di- and also optionally tri- and tetraols and di- and also optionally tri and tetracarboxylic acids or hydroxy carboxylic acids or lactones. Instead of the free polycarboxylic acids it is also possible to use the corresponding polycarboxylic anhydrides or corresponding polycarboxylic esters of lower alcohols for preparing the polyesters.
Examples of suitable diols are ethylene glycol, butylene glycol, diethylene glycol, triethylene glycol, polyalkylene glycols such as polyethylene glycol, also 1,2-propanediol, 1,3-propanediol, butanediol(1,3), butanediol(1,4), hexanediol(1,6) and isomers, neopentyl glycol or neopentyl glycol hydroxypivalate, of which hexanediol(1,6) and isomers, neopentyl glycol and neopentyl glycol hydroxypivalate are preferred. Besides these it is also possible to use polyols such as trimethylolpropane, glycerol, erythritol, pentaerythritol, trimethylolbenzene or trishydroxyethyl isocyanurate.
Useful dicarboxylic acids include phthalic acid, isophthalic acid, terephthalic acid, tetra-hydrophthalic acid, hexahydrophthalic acid, cyclohexanedicarboxylic acid, adipic acid, azelaic acid, sebacic acid, glutaric acid, tetrachlorophthalic acid, maleic acid, fumaric acid, itaconic acid, malonic acid, suberic acid, 2-methylsuccinic acid, 3,3-diethyl glutaric acid and/or 2,2-dimethylsuccinic acid. The corresponding anhydrides can also be used as a source of an acid.
When the average functionality of the polyol to be esterified is > than 2, monocarboxylic acids, such as benzoic acid and hexanecarboxylic acid can be used as well in addition.
Preferred acids are aliphatic or aromatic acids of the aforementioned kind. Adipic acid, isophthalic acid and optionally trimellitic acid are particularly preferred.
Hydroxy carboxylic acids useful as reaction participants in the preparation of a polyester polyol having terminal hydroxyl groups include for example hydroxycaproic acid, hydroxybutyric acid, hydroxydecanoic acid, hydroxystearic acid and the like. Suitable lactones include caprolactone, butyrolactone and homologues. Caprolactone is preferred.
A2) may likewise utilize hydroxyl-containing polycarbonates, preferably polycarbonate diols, having number average molecular weights Mn in the range from 400 to 8000 g/mol and preferably in the range from 600 to 3000 g/mol. These are obtainable by reaction of carbonic acid derivatives, such as diphenyl carbonate, dimethyl carbonate or phosgene, with polyols, preferably diols.
Examples of such diols are ethylene glycol, 1,2-propanediol, 1,3-propanediol, 1,3-butanediol, 1,4-butanediol, 1,6-hexanediol, 1,8-octanediol, neopentyl glycol, 1,4-bishydroxymethyl-cyclohexane, 2-methyl-1,3-propanediol, 2,2,4-trimethyl-1,3-pentanediol, dipropylene glycol, polypropylene glycols, dibutylene glycol, polybutylene glycols, bisphenol A and lactone-modified diols of the aforementioned kind.
The polycarbonate diol preferably contains 40% to 100% by weight of hexanediol, preference being given to 1,6-hexanediol and/or hexanediol derivatives. Such hexanediol derivatives are based on hexanediol and have ester or ether groups as well as terminal OH groups. Such derivatives are obtainable by reaction of hexanediol with excess caprolactone or by etherification of hexanediol with itself to form di- or trihexylene glycol.
In lieu of or in addition to pure polycarbonate diols, polyether-polycarbonate diols can also be used in A2).
Hydroxyl-containing polycarbonates preferably have a linear construction.
A2) may likewise utilize polyether polyols.
Useful polyether polyols include for example the well-known polyurethane chemistry polytetramethylene glycol polyethers as are obtainable by polymerization of tetrahydrofuran by means of cationic ring opening.
Useful polyether polyols likewise include the well-known addition products of styrene oxide, ethylene oxide, propylene oxide, butylene oxides and/or epichlorohydrin onto di- or polyfunctional starter molecules. Polyether polyols based on the at least proportional addition of ethylene oxide onto di- or polyfunctional starter molecules can also be used as component A4) (nonionic hydrophilicizing agents).
Useful starter molecules include all prior art compounds, for example water, butyl diglycol, glycerol, diethylene glycol, trimethylolpropane, propylene glycol, sorbitol, ethylenediamine, triethanolamine, 1,4-butanediol. Preferred starter molecules are water, ethylene glycol, propylene glycol, 1,4-butanediol, diethylene glycol and butyl diglycol.
Particularly preferred embodiments of the polyurethane dispersions (I) contain as component A2) a mixture of polycarbonate polyols and polytetramethylene glycol polyols, the proportion of polycarbonate polyols in this mixture being in the range from 20% to 80% by weight and the proportion of polytetramethylene glycol polyols in this mixture being in the range from 80% to 20% by weight. Preference is given to a proportion of 30% to 75% by weight for polytetramethylene glycol polyols and to a proportion of 25% to 70% by weight for polycarbonate polyols. Particular preference is given to a proportion of 35% to 70% by weight for polytetramethylene glycol polyols and to a proportion of 30% to 65% by weight for polycarbonate polyols, each subject to the proviso that the sum total of the weight percentages for the polycarbonate and polytetramethylene glycol polyols is 100% and the proportion of component A2) which is accounted for by the sum total of the polycarbonate and polytetramethylene glycol polyether polyols is at least 50% by weight preferably 60% by weight and more preferably at least 70% by weight.
The compounds of component A3) have molecular weights of 62 and 400 g/mol.
A3) may utilize polyols of the specified molecular weight range with up to 20 carbon atoms, such as ethylene glycol, diethylene glycol, triethylene glycol, 1,2-propanediol, 1,3-propanediol, 1,4-butanediol, 1,3-butylene glycol, cyclohexanediol, 1,4-cyclohexanedimethanol, 1,6-hexanediol, neopentyl glycol, hydroquinone dihydroxyethyl ether, bisphenol A (2,2-bis(4-hydroxy-phenyl)propane), hydrogenated bisphenol A, (2,2-bis(4-hydroxycyclohexyl)propane), trimethylol-propane, glycerol, pentaerythritol and also any desired mixtures thereof with one another.
Also suitable are ester diols of the specified molecular weight range such as α-hydroxybutyl-ε-hydroxycaproic acid ester, ω-hydroxyhexyl-γ-hydroxybutyric acid ester, β-hydroxyethyl adipate or bis(β-hydroxyethyl) terephthalate.
A3) may further utilize monofunctional isocyanate-reactive hydroxyl-containing compounds. Examples of such monofunctional compounds are ethanol, n-butanol, ethylene glycol monobutyl ether, diethylene glycol monomethyl ether, ethylene glycol monobutyl ether, diethylene glycol monobutyl ether, propylene glycol monomethyl ether, dipropylene glycol monomethyl ether, tripropylene glycol monomethyl ether, dipropylene glycol monopropyl ether, propylene glycol monobutyl ether, dipropylene glycol monobutyl ether, tripropylene glycol monobutyl ether, 2-ethylhexanol, 1-octanol, 1-dodecanol, 1-hexadecanol.
Preferred compounds for component A3) are 1,6-hexanediol, 1,4-butanediol, neopentyl glycol and trimethylolpropane.
An anionically or potentially anionically hydrophilicizing compound for component A4) is any compound which has at least one isocyanate-reactive group such as a hydroxyl group and also at least one functionality such as for example —COO−M+, —SO3−M+, —PO(O−M+)2 where M+ is for example a metal cation, H+, NH4+, NHR3+, where R in each occurrence may be C1-C12-alkyl, C5-C6-cycloalkyl and/or C2-C4-hydroxyalkyl, which functionality enters on interaction with aqueous media a pH-dependent dissociative equilibrium and thereby can have a negative or neutral charge. Useful anionically or potentially anionically hydrophilicizing compounds include mono- and dihydroxy carboxylic acids, mono- and dihydroxy sulphonic acids and also mono- and dihydroxy phosphonic acids and their salts. Examples of such anionic or potentially anionic hydrophilicizing agents are dimethylolpropionic acid, dimethylolbutyric acid, hydroxypivalic acid, malic acid, citric acid, glycolic acid, lactic acid and the propoxylated adduct formed from 2-butenediol and NaHSO3 and described in DE-A 2 446 440, page 5-9, formula I-III. Preferred anionic or potentially anionic hydrophilicizing agents for component A4) are those of the aforementioned kind that have carboxylate or carboxyl groups and/or sulphonate groups.
Particularly preferred anionic or potentially anionic hydrophilicizing agents are those that contain carboxylate or carboxyl groups as ionic or potentially ionic groups, such as dimethylolpropionic acid, dimethylolbutyric acid and hydroxypivalic acid and salts thereof.
Useful nonionically hydrophilicizing compounds for component A4) include for example polyoxyalkylene ethers which contain at least one hydroxyl or amino group, preferably at least one hydroxyl group.
Examples are the monohydroxyl-functional polyalkylene oxide polyether alcohols containing on average 5 to 70 and preferably 7 to 55 ethylene oxide units per molecule and obtainable in a conventional manner by alkoxylation of suitable starter molecules (for example in Ullmanns Encyclopädie der technischen Chemie, 4th edition, volume 19, Verlag Chemie, Weinheim pages 31-38).
These are either pure polyethylene oxide ethers or mixed polyalkylene oxide ethers, containing at least 30 mol % and preferably at least 40 mol % of ethylene oxide units, based on all alkylene oxide units present.
Preferred polyethylene oxide ethers of the aforementioned kind are monofunctional mixed polyalkylene oxide polyethers having 40 to 100 mol % of ethylene oxide units and 0 to 60 mol % of propylene oxide units.
Preferred nonionically hydrophilicizing compounds for component A4) include those of the aforementioned kind that are block (co)polymers prepared by blockwise addition of alkylene oxides onto suitable starters.
Useful starter molecules for such nonionic hydrophilicizing agents include saturated monoalcohols such as methanol, ethanol, n-propanol, isopropanol, n-butanol, isobutanol, sec-butanol, the isomers pentanols, hexanols, octanols and nonanols, n-decanol, n-dodecanol, n-tetradecanol, n-hexadecanol, n-octadecanol, cyclohexanol, the isomeric methylcyclohexanols or hydroxymethylcyclohexane, 3-ethyl-3-hydroxymethyloxetane or tetrahydrofurfuryl alcohol, diethylene glycol monoalkyl ethers, for example diethylene glycol monobutyl ether, unsaturated alcohols such as allyl alcohol, 1,1-dimethylallyl alcohol or oleic alcohol, aromatic alcohols such as phenol, the isomeric cresols or methoxyphenols, araliphatic alcohols such as benzyl alcohol, anis alcohol or cinnamyl alcohol, secondary monoamines such as dimethylamine, diethylamine, dipropylamine, diisopropylamine, dibutylamine, bis(2-ethylhexyl)amine, N-methylcyclo-hexylamine, N-ethylcyclohexylamine or dicyclohexylamine and also heterocyclic secondary amines such as morpholine, pyrrolidine, piperidine or 1H pyrazole. Preferred starter molecules are saturated monoalcohols of the aforementioned kind. Particular preference is given to using diethylene glycol monobutyl ether or n-butanol as starter molecules.
Useful alkylene oxides for the alkoxylation reaction are in particular ethylene oxide and propylene oxide, which can be used in any desired order or else in admixture in the alkoxylation reaction.
Component B1) may utilize di- or polyamines such as 1,2-ethylenediamine, 1,2-diaminopropane, 1,3-diaminopropane, 1,4-diaminobutane, 1,6-diaminohexane, isophoronediamine, isomeric mixture of 2,2,4- and 2,4,4-trimethylhexamethylenediamine, 2-methylpentamethylenediamine, diethylene-triamine, triaminononane, 1,3-xylylenediamine, 1,4-xylylenediamine, α,α,α′,α′-tetramethyl-1,3- and -1,4-xylylenediamine and 4,4-diaminodicyclohexylmethane and/or dimethylethylenediamine. It is also possible but less preferable to use hydrazine and also hydrazides such as adipohydrazide.
Component B1) can further utilize compounds which as well as a primary amino group also have secondary amino groups or which as well as an amino group (primary or secondary) also have OH groups. Examples thereof are primary/secondary amines, such as diethanolamine, 3-amino-1-methylaminopropane, 3-amino-1-ethylaminopropane, 3-amino-1-cyclohexylaminopropane, 3-amino-1-methylaminobutane, alkanolamines such as N-aminoethylethanolamine, ethanolamine, 3-aminopropanol, neopentanolamine.
Component B1) can further utilize monofunctional isocyanate-reactive amine compounds, for example methylamine, ethylamine, propylamine, butylamine, octylamine, laurylamine, stearylamine, isononyloxypropylamine, dimethylamine, diethylamine, dipropylamine, dibutylamine, N-methylaminopropylamine, diethyl(methyl)aminopropylamine, morpholine, piperidine, or suitable substituted derivatives thereof, amide-amines formed from diprimary amines and monocarboxylic acids, monoketimes of diprimary amines, primary/tertiary amines, such as N,N-dimethylaminopropylamine.
Preferred compounds for component B1) are 1,2-ethylenediamine, 1,4-diaminobutane and isophoronediamine.
An anionically or potentially anionically hydrophilicizing compound for component B2) is any compound which has at least one isocyanate-reactive group, preferably an amino group, and also at least one functionality such as for example —COO−M+, —SO3−M+, —PO(O−M+)2 where M+ is for example a metal cation, H+, NH4+, NHR3+, where R in each occurrence may be C1-C12-alkyl, C5-C6-cycloalkyl and/or C2-C4-hydroxyalkyl, which functionality enters on interaction with aqueous media a pH-dependent dissociative equilibrium and thereby can have a negative or neutral charge.
Useful anionically or potentially anionically hydrophilicizing compounds are mono- and diamino carboxylic acids, mono- and diamino sulphonic acids and also mono- and diamino phosphonic acids and their salts. Examples of such anionic or potentially anionic hydrophilicizing agents are N-(2-aminoethyl)-β-alanine, 2-(2-aminoethylamino)ethanesulphonic acid, ethylenediaminepropyl-sulphonic acid, ethylenediaminebutylsulphonic acid, 1,2- or 1,3-propylenediamine-β-ethyl-sulphonic acid, glycine, alanine, taurine, lysine, 3,5-diaminobenzoic acid and the addition product of IPDA and acrylic acid (EP-A 0 916 647, Example 1). It is further possible to use cyclohexyl-aminopropanesulphonic acid (CAPS) from WO-A 01/88006 as anionic or potentially anionic hydrophilicizing agent.
Preferred anionic or potentially anionic hydrophilicizing agents for component B2) are those of the aforementioned kind that have carboxylate or carboxyl groups and/or sulphonate groups, such as the salts of N-(2-aminoethyl)-β-alanine, of 2-(2-aminoethylamino)ethanesulphonic acid or of the addition product of IPDA and acrylic acid (EP-A 0 916 647, Example 1).
Mixtures of anionic or potentially anionic hydrophilicizing agents and nonionic hydrophilicizing agents can also be used.
A preferred embodiment for producing the specific polyurethane dispersions utilizes components A1) to A4) and B1) to B2) in the following amounts, the individual amounts always adding up to 100% by weight:
5% to 40% by weight of component A1),
55% to 90% by weight of A2),
0.5% to 20% by weight of the sum total of components A3) and B1)
0.1% to 25% by weight of the sum total of the components component A4) and B2), with 0.1% to 5% by weight of anionic or potentially anionic hydrophilicizing agents from A4) and/or B2) being used, based on the total amount of components A1) to A4) and B1) to B2).
A particularly preferred embodiment for producing the specific polyurethane dispersions utilizes components A1) to A4) and B1) to B2) in the following amounts, the individual amounts always adding up to 100% by weight:
5% to 35% by weight of component A1),
60% to 90% by weight of A2),
0.5% to 15% by weight of the sum total of components A3) and B1)
0.1% to 15% by weight of the sum total of the components component A4) and B2), with 0.2% to 4% by weight of anionic or potentially anionic hydrophilicizing agents from A4) and/or B2) being used, based on the total amount of components A1) to A4) and B1) to B2).
A very particularly preferred embodiment for producing the specific polyurethane dispersions utilizes components A1) to A4) and B1) to B2) in the following amounts, the individual amounts always adding up to 100% by weight:
10% to 30% by weight of component A1),
65% to 85% by weight of A2),
0.5% to 14% by weight of the sum total of components A3) and B1)
0.1% to 13.5% by weight of the sum total of the components A4) and B2), with 0.5% to 3.0% by weight of anionic or potentially anionic hydrophilicizing agents from A4) and/or B2) being used, based on the total amount of components A1) to A4) and B1) to B2).
The production of the anionically hydrophilicized polyurethane dispersions (I) can be carried out in one or more stages in homogeneous phase or, in the case of a multistage reaction, partly in disperse phase. After completely or partially conducted polyaddition from A1) to A4) a dispersing, emulsifying or dissolving step is carried out. This is followed if appropriate by a further polyaddition or modification in disperse phase.
Any prior art process can be used, examples being the prepolymer mixing process, the acetone process or the melt dispersing process. The acetone process is preferred.
Production by the acetone process typically involves the constituents A2) to A4) and the polyisocyanate component A1) being wholly or partly introduced as an initial charge to produce an isocyanate-functional polyurethane prepolymer and optionally diluted with a water-miscible but isocyanate-inert solvent and heated to temperatures in the range from 50 to 120° C. The isocyanate addition reaction can be speeded using the catalysts known in polyurethane chemistry.
Useful solvents include the customary aliphatic, keto-functional solvents such as acetone, 2-butanone, which can be added not just at the start of the production process but also later, optionally in portions. Acetone and 2-butanone are preferred.
Other solvents such as xylene, toluene, cyclohexane, butyl acetate, methoxypropyl acetate, N-methylpyrrolidone, N-ethylpyrrolidone, solvents having ether or ester units can additionally be used or wholly or partly distilled off or in the case of N-methylpyrrolidone, N-ethylpyrrolidone remain completely in the dispersion. But preference is given to not using any other solvents apart from the customary aliphatic, keto-functional solvents.
Subsequently, any constituents of A1) to A4) not added at the start of the reaction are added.
In the production of the polyurethane prepolymer from A1) to A4), the amount of substance ratio of isocyanate groups to with isocyanate-reactive groups is in the range from 1.05 to 3.5, preferably in the range from 1.2 to 3.0 and more preferably in the range from 1.3 to 2.5.
The reaction of components A1) to A4) to form the prepolymer is effected partially or completely, but preferably completely. Polyurethane prepolymers containing free isocyanate groups are obtained in this way, without a solvent or in solution.
The neutralizing step to effect partial or complete conversion of potentially anionic groups into anionic groups utilizes bases such as tertiary amines, for example trialkylamines having 1 to 12 and preferably 1 to 6 carbon atoms and more preferably 2 to 3 carbon atoms in every alkyl radical or alkali metal bases such as the corresponding hydroxides.
Examples thereof are trimethylamine, triethylamine, methyldiethylamine, tripropylamine, N-methylmorpholine, methyldiisopropylamine, ethyldiisopropylamine and diisopropylethylamine. The alkyl radicals may also bear for example hydroxyl groups, as in the case of the dialkylmonoalkanol-, alkyldialkanol- and trialkanolamines. Useful neutralizing agents further include if appropriate inorganic bases, such as aqueous ammonia solution, sodium hydroxide or potassium hydroxide.
Preference is given to ammonia, triethylamine, triethanolamine, dimethylethanolamine or diisopropylethylamine and also sodium hydroxide and potassium hydroxide, particular preference being given to sodium hydroxide and potassium hydroxide.
The bases are employed in an amount of substance which is between 50 and 125 mol % and preferably between 70 and 100 mol % of the amount of substance of the acid groups to be neutralized. Neutralization can also be effected at the same time as the dispersing step, by including the neutralizing agent in the water of dispersion.
Subsequently, in a further process step, if this has not already been done or only to some extent, the prepolymer obtained is dissolved with the aid of aliphatic ketones such as acetone or 2-butanone.
In the chain extension of stage B), NH2— and/or NH-functional components are reacted, partially or completely, with the still remaining isocyanate groups of the prepolymer. Preferably, the chain extension/termination is carried out before dispersion in water.
Chain termination is typically carried out using amines B1) having an isocyanate-reactive group such as methylamine, ethylamine, propylamine, butylamine, octylamine, laurylamine, stearylamine, isononyloxypropylamine, dimethylamine, diethylamine, dipropylamine, dibutylamine, N-methylaminopropylamine, diethyl(methyl)aminopropylamine, morpholine, piperidine or suitable substituted derivatives thereof, amide-amines formed from diprimary amines and monocarboxylic acids, monoketimes of diprimary amines, primary/tertiary amines, such as N,N-dimethylaminopropylamine.
When partial or complete chain extension is carried out using anionic or potentially anionic hydrophilicizing agents conforming to definition B2) with NH2 or NH groups, chain extension of the prepolymers is preferably carried out before dispersion.
The aminic components B1) and B2) can optionally be used in water- or solvent-diluted form in the process of the present invention, individually or in mixtures, any order of addition being possible in principle.
When water or organic solvent is used as a diluent, the diluent content of the chain-extending component used in B) is preferably in the range from 70% to 95% by weight.
Dispersion is preferably carried out following chain extension. For dispersion, the dissolved and chain-extended polyurethane polymer is either introduced into the dispersing water, if appropriate by substantial shearing, such as vigorous stirring for example, or conversely the dispersing water is stirred into the chain-extended polyurethane polymer solutions. It is preferable to add the water to the dissolved chain-extended polyurethane polymer.
The solvent still present in the dispersions after the dispersing step is then typically removed by distillation. Removal during the dispersing step is likewise possible.
The residual level of organic solvents in the polyurethane dispersions (I) is typically less than 1.0% by weight and preferably less than 0.5% by weight, based on the entire dispersion.
The pH of the polyurethane dispersions (I) which are essential to the present invention is typically less than 9.0, preferably less than 8.5, more preferably less than 8.0 and most preferably is in the range from 6.0 to 7.5.
The solids content of the polyurethane dispersions (I) is preferably in the range from 40% to 70%, more preferably in the range from 50% to 65%, even more preferably in the range from 55% to 65% by weight and in particular in the range from 60% to 65% by weight.
Coagulant (II) in the composition can be any organic compound containing at least 2 cationic groups, preferably any known cationic flocculating and precipitating agent of the prior art, such as a cationic homo- or copolymer of a salt of poly[2-(N,N,N-trimethylamino)ethyl acrylate], of polyethyleneimine, of poly[N-(dimethylaminomethyl)acrylamide], of a substituted acrylamide, of a substituted methacrylamide, of N-vinylformamide, of N-vinylacetamide, of N-vinylimidazole, of 2-vinylpyridine or of 4-vinylpyridine.
Preferred cationic coagulants (II) are acrylamide copolymers comprising structural units of the general formula (2) and more preferably of the general formula (1) and (2)
where
X− is a halide ion, preferably chloride.
The coagulants (II) preferably have number average molecular weights in the range from 500 000 to 50 000 000 g/mol.
Such coagulants (II), based on copolymers of acrylamide are marketed for example under the trade name of Praestol® (Degussa Stockhausen, Krefeld, Germany) as flocculants for activated sludges. Preferred coagulants of the Praestol® type are Praestol® K111L, K122L, K133L, BC 270L, K 144L, K 166L, BC 55L, 185K, 187K, 190K, K222L, K232L, K233L, K234L, K255L, K332L, K 333L, K 334L, E 125, E 150 and also mixtures thereof. Praestol® 185K, 187K and 190K and also mixtures thereof are very particularly preferred coagulating agents.
The residual levels of monomers, in particular acrylate and acrylamide monomers, in the coagulants are preferably less than 1% by weight, more preferably less than 0.5% by weight and most preferably less than 0.025% by weight.
The coagulants can be used in solid form or as aqueous solutions or dispersions. The use of aqueous dispersions or solutions is preferred.
As well as the polyurethane dispersions (I) and the coagulants (II), auxiliary and additive materials (III) can also be used.
Examples of such auxiliary and additive materials (III) are foam auxiliaries such as foam formers and stabilizers, thickeners or thixotroping agents, antioxidants, light stabilizers, emulsifiers, plasticizers, pigments, fillers and/or flow control agents.
Preferably, foam auxiliaries such as foam formers and stabilizers are included as auxiliary and additive materials (III). Useful foam auxiliaries include commercially available compounds such as fatty acid amides, sulphosuccinamides hydrocarbyl sulphates or sulphonates or fatty acid salts, in which case the lipophilic radical preferably contains 12 to 24 carbon atoms, and also alkylpolyglycosides obtainable in a conventional manner by reaction of comparatively long-chain monoalcohols (4 to 22 carbon atoms in the alkyl radical) with mono-, di- or polysaccharides (see for example Kirk-Othmer, Encyclopedia of Chemical Technology, John Wiley & Sons, Vol. 24, p. 29).
Preferred foam auxiliaries are sulphosuccinamides, alkanesulphonates or alkyl sulphates having 12 to 22 carbon atoms in the hydrocarbyl radical, alkylbenzenesulphonates or alkylbenzene sulphates having 14 to 24 carbon atoms in the hydrocarbyl radical or fatty acid amides or/and fatty acid salts having 12 to 24 carbon atoms in the hydrocarbyl radical.
Such fatty acid amides are preferably based on mono- or di-(C2-C3-alkanol)amines. The fatty acid salts may be for example alkali metal salts, amine salts or unsubstituted ammonium salts.
Such fatty acid derivatives are typically based on fatty acids such as lauric acid, myristic acid, palmitic acid, oleic acid, stearic acid, ricinoleic acid, behenic acid or arachidic acid, coco fatty acid, tallow fatty acid, soya fatty acid and their hydrogenation products.
Particularly preferred foam auxiliaries are mixtures of sulphosuccinamides and ammonium stearates, these preferably containing 20% to 60% by weight and more preferably 30% to 50% by weight of ammonium stearates and preferably 80% to 40% by weight and more preferably 70% to 50% by weight of sulphosuccinamides.
Commercially available thickeners can be used, such as derivatives of dextrin, of starch or of cellulose, examples being cellulose ethers or hydroxyethylcellulose, organic wholly synthetic thickeners based on polyacrylic acids, polyvinylpyrrolidones, polymethacrylic compounds or polyurethanes (associative thickeners) and also inorganic thickeners, such as bentonites or silicas.
In principle, although not preferably, the compositions which are essential to the present invention can also contain crosslinkers such as unblocked polyisocyanates, amide- and amine-formaldehyde resins, phenolic resins, aldehydic and ketonic resins, examples being phenol-formaldehyde resins, resols, furan resins, urea resins, carbamic ester resins, triazine resins, melamine resins, benzoguanamine resins, cyanamide resins or aniline resins.
The compositions which are essential to the present invention typically contain, based on dry substance, 80 to 99.5 parts by weight of dispersion (I), 0.5 to 5 parts by weight of cationic coagulant (II), 0 to 10 parts by weight of foam auxiliary, 0 to 10 parts by weight of crosslinker and 0 to 10 parts by weight of thickener.
Preferably, the compositions which are essential to the present invention contain, based on dry substance, 85 to 97 parts by weight of dispersion (I), 0.75 to 4 parts by weight of cationic coagulant (II), 0.5 to 6 parts by weight of foam auxiliary, 0 to 5 parts by weight of crosslinker and 0% to 5% by weight of thickener.
More preferably, the compositions which are essential to the present invention contain, based on dry substance, 89 to 97 parts by weight of dispersion (I), 0.75 to 3 parts by weight of cationic coagulant (II), 0.5 to 5 parts by weight of foam auxiliary, 0 to 4 parts by weight of crosslinker and 0% to 4% by weight of thickener.
As well as components (I), (II) and if appropriate (III), other aqueous binders can also be used in the compositions which are essential to the present invention. Such aqueous binders can be constructed for example of polyester, polyacrylate, polyepoxy or other polyurethane polymers. Similarly, the combination with radiation-curable binders as described for example in EP-A-0 753 531 is also possible. It is further possible to employ other anionic or nonionic dispersions, such as polyvinyl acetate, polyethylene, polystyrene, polybutadiene, polyvinyl chloride, polyacrylate and copolymer dispersions.
Frothing in the process of the present invention is accomplished by mechanical stirring of the composition at high speeds of rotation by shaking or by decompressing a blowing gas.
Mechanical frothing can be effected using any desired mechanical stirring, mixing and dispersing techniques. Air is generally introduced, but nitrogen and other gases can also be used for this purpose.
The foam thus obtained is, in the course of frothing or immediately thereafter, applied to a substrate or introduced into a mould and dried.
Application to a substrate can be for example by pouring or blade coating, but other conventional techniques are also possible. Multilayered application with intervening drying steps is also possible in principle.
A satisfactory drying rate for the foams is observed at a temperature as low as 20° C., so that drying on injured human or animal tissue presents no problem. However, temperatures above 30° C. are preferably used for more rapid drying and fixing of the foams. However, drying temperatures should not exceed 200° C., preferably 150° C. and more preferably 130° C., since undesirable yellowing of the foams can otherwise occur, inter alia. Drying in two or more stages is also possible.
Drying is generally effected using conventional heating and drying apparatus, such as (circulating air) drying cabinets, hot air or IR radiators. Drying by leading the coated substrate over heated surfaces, for example rolls, is also possible.
Application and drying can each be carried out batchwise or continuously, but the entirely continuous process is preferred.
Useful substrates include in particular papers or films which facilitate simple detachment of the wound contact material before it is used to cover an injured site. Human or animal tissue such as skin can similarly serve as a substrate, so that direct closure of an injured site is possible by a wound contact material produced in situ.
In a preferred embodiment of the present invention, the active component comprises an antiseptic biguanide. Biguanides are compounds derived from biguanide (C2H7N5), in particular its polymers. Antiseptic biguanides are biguanides that have an antimicrobial effect, i.e. act as bacteriostats or preferably as bactericides. The compounds in question preferably have a broad effect against many bacteria and can be characterized by a minimal microbicidal concentration (MMC, measured in the suspension test) of at least 0.5 μg/ml, preferably at least 12 or at least 25 μg/ml with regard to E. coli.
A preferred antiseptic biguanide according to this invention is poly(imino[imino-carbonyl]iminopolymethylene), the use of poly(hexamethylene)biguanide (PHMB), also known as polyhexanide, as antiseptic biguanide being particularly preferred. The term “antiseptic biguanides” according to this invention also comprehends metabolites and/or prodrugs of antiseptic biguanides. Antiseptic biguanides can be present as racemates or pure isoforms.
Particular preference is given to a process for producing wound contact materials from polyurethane foams or the compositions according to the present invention containing an aqueous, anionically hydrophilicized polyurethane dispersion (I), a cationic coagulan (II) and additionally at least polyhexamethylbiguanide (PHMB) and/or a salt, preferably the hydrochloride of PHMB.
Preferably the wound contact materials from polyurethane foams of the compositions of the present invention contain antiseptic biguanide in a concentration of 0.01% to 20% by weight, the concentration of 0.1% to 5% being particularly advantageous. The biguanide can have any desired molecular weight distribution.
The present invention further provides the wound contact materials obtainable by the process of the present invention.
Before drying, the foam densities of the polyurethane foams are typically in the range from 50 to 800 g/litre, preferably in the range from 100 to 500 g/litre and more preferably in the range from 100 to 250 g/litre (mass of all input materials [in g] based on the foam volume of one litre).
After drying, the polyurethane foams have a microporous, at least partial open-cell structure comprising intercommunicating cells. The density of the dried foams is typically below 0.4 g/cm3, preferably below 0.35 g/cm3, more preferably in the range from 0.01 to 0.3 g/cm3 and most preferably in the range from 0.1 to 0.3 g/cm3.
The DIN EN 13726-1 Part 3.2 physiological saline absorbency is typically in the range from 100 to 1500%, preferably in the range from 300 to 1500% and more preferably in the range from 300 to 800% for the polyurethane foams (mass of liquid taken up, based on the mass of dry foam). The DIN EN 13726-2 Part 3.2 water vapour transmission rate is typically in the range from 2000 to 8000 g/24 h*m2, preferably in the range from 3000 to 8000 g/24 h*m2 and more preferably in the range from 3000 to 5000 g/24 h*m2.
The polyurethane foams exhibit good mechanical strength and high elasticity. Typically, maximum stress is greater than 0.2 N/mm2 and maximum extension is greater than 250%. Preferably, maximum stress is greater than 0.4 N/mm2 and the extension is greater than 350% (determined according to DIN 53504).
After drying, the thickness of the polyurethane foams is typically in the range from 0.1 mm to 50 mm, preferably in the range from 0.5 mm to 20 mm, more preferably in the range from 1 to 10 mm and most preferably in the range from 1 to 5 mm.
The polyurethane foams can moreover be adhered, laminated or coated to or with further materials, for example materials based on hydrogels, (semi-) permeable films, coatings, hydrocolloids or other foams.
If appropriate, a sterilizing step can be included in the process of the present invention. It is similarly possible in principle for the wound contact materials obtainable by the process of the present invention to be sterilized after they have been produced. Conventional sterilizing processes are used where sterilization is effected by thermal treatment suitable chemicals such as ethylene oxide or irradiation with gamma rays for example.
Owing to the wide utility of the process of the present invention and of the wound contact materials obtainable thereby, it is possible in principle to use said process in the industrial production of wound contact materials. But it is similarly also possible to use it for producing sprayed plasters for example, in which case the wound contact material is formed by direct application of the composition to a wound and simultaneous frothing and subsequent drying.
For industrial production of wound contact materials, the polyurethane dispersion (I) is mixed with foam auxiliaries of the aforementioned kind and thereafter mechanically frothed by introduction of a gas such as air and finally coagulated by addition of the coagulant (II), to obtain a further processible, coagulated foam. This foam is applied to a substrate and dried. Owing to higher productivity, drying is typically carried out at elevated temperatures in the range from 30 to 200° C., preferably in the range from 50 to 150° C. and more preferably in the range from 60 to 130° C. Preference is further given to an at least two-stage drying beginning at temperatures of 40 to 80° C. and with subsequent further drying at elevated temperatures of 80 to 140° C. Drying is generally carried out using conventional heating and drying apparatus, for example (circulating air) drying cabinets. Application and drying can each be carried out batchwise or continuously, but preference is given to the wholly continuous process.
When the composition which is essential to the present invention is used to produce a sprayed plaster, the polyurethane dispersion (I) and the coagulant (II), which each may contain foam auxiliaries if appropriate, are separately provided and then mixed with each other immediately before or during application to the tissue to be covered. Frothing is here accomplished by simultaneous decompression of a blowing gas which was present in at least one of the components (I) and (II). To consolidate the foam formed, it is subsequently dried, for which temperatures of 20 to 40° C. are sufficient. When additional heat sources such as a hair dryer or an IR red light lamp are used, forced thermal drying up to a maximum temperature of 80° C. is also possible.
The blowing agents used are well known from polyurethane chemistry. n-Butane, i-butane and propane and also mixtures thereof are suitable for example, as is also dimethyl ether for example. Preference is given to using a mixture of n-butane, i-butane and propane, whereby the desired, fine-cell foams are obtained. The blowing agent or blowing agent mixture is typically used in an amount of 1% to 50% by weight, preferably 5% to 40% by weight and more preferably 5% to 20% by weight, the sum total of polyurethane dispersion (I) used, blowing agent (mixture) and also optional auxiliary and addition materials (II) being 100% by weight. Spray plasters are preferably provided in spray cans, the polyurethane dispersion (I) and the cationic coagulant (II) being included separately from each other and not being mixed with each other until immediately before application. The blowing agent can be included in either or both of the components. Either or both of the components (I) and (II) may additionally if appropriate also contain auxiliary and additive materials (III), preferably foam auxiliaries. Pouring of the composition is possible as well as spraying.
Unless indicated otherwise, all percentages are by weight.
Solids contents were determined in accordance with DIN-EN ISO 3251.
NCO contents were unless expressly mentioned otherwise determined volumetrically in accordance with DIN-EN ISO 11909.
The determination of the average particle sizes (the number average is reported) of the polyurethane dispersions (I) was carried out using laser correlation spectroscopy (instrument: Malvern Zetasizer 1000, Malver Inst. Limited).
987.0 g of PolyTHF® 2000, 375.4 g of PolyTHF® 1000, 761.3 g of Desmophen® C2200 and 44.3 g of LB 25 polyether were heated to 70° C. in a standard stirring apparatus. Then, a mixture of 237.0 g of hexamethylene diisocyanate and 313.2 g of isophorone diisocyanate was added at 70° C. in the course of 5 min and the mixture was stirred at 120° C. until the theoretical NCO value was reached or the actual NCO value was slightly below the theoretical NCO value. The ready-produced prepolymer was dissolved with 4830 g of acetone and, in the process, cooled down to 50° C. and subsequently admixed with a solution of 25.1 g of ethylenediamine, 116.5 g of isophoronediamine, 61.7 g of diaminosulphonate and 1030 g of water metered in over 10 min. The mixture was subsequently stirred for 10 min. Then, a dispersion was formed by addition of 1250 g of water. This was followed by removal of the solvent by distillation under reduced pressure.
The white dispersion obtained had the following properties:
223.7 g of PolyTHF® 2000, 85.1 g of PolyTHF® 1000, 172.6 g of Desmophen® C2200 and 10.0 g of LB 25 polyether were heated to 70° C. in a standard stirring apparatus. Then, a mixture of 53.7 g of hexamethylene diisocyanate and 71.0 g of isophorone diisocyanate was added at 70° C. in the course of 5 min and the mixture was stirred at 120° C. until the theoretical NCO value was reached or the actual NCO value was slightly below the theoretical NCO value. The ready-produced prepolymer was dissolved with 1005 g of acetone and, in the process, cooled down to 50° C. and subsequently admixed with a solution of 5.70 g of ethylenediamine, 26.4 g of isophoronediamine, 9.18 g of diaminosulphonate and 249.2 g of water metered in over 10 min. The mixture was subsequently stirred for 10 min. Then, a dispersion was formed by addition of 216 g of water. This was followed by removal of the solvent by distillation under reduced pressure.
The white dispersion obtained had the following properties:
987.0 g of PolyTHF® 2000, 375.4 g of PolyTHF® 1000, 761.3 g of Desmophen® C2200 and 44.3 g of LB 25 polyether were heated to 70° C. in a standard stirring apparatus. Then, a mixture of 237.0 g of hexamethylene diisocyanate and 313.2 g of isophorone diisocyanate was added at 70° C. in the course of 5 min and the mixture was stirred at 120° C. until the theoretical NCO value was reached or the actual NCO value was slightly below the theoretical NCO value. The ready-produced prepolymer was dissolved with 4830 g of acetone and, in the process, cooled down to 50° C. and subsequently admixed with a solution of 36.9 g of 1,4-diaminobutane, 116.5 g of isophoronediamine, 61.7 g of diaminosulphonate and 1076 g of water metered in over 10 min. The mixture was subsequently stirred for 10 min. Then, a dispersion was formed by addition of 1210 g of water. This was followed by removal of the solvent by distillation under reduced pressure.
The white dispersion obtained had the following properties:
201.3 g of PolyTHF® 2000, 76.6 g of PolyTHF® 1000, 155.3 g of Desmophen® C2200, 2.50 g of 1,4-butanediol and 10.0 g of LB 25 polyether were heated to 70° C. in a standard stirring apparatus. Then, a mixture of 53.7 g of hexamethylene diisocyanate and 71.0 g of isophorone diisocyanate was added at 70° C. in the course of 5 min and the mixture was stirred at 120° C. until the theoretical NCO value was reached or the actual NCO value was slightly below the theoretical NCO value. The ready-produced prepolymer was dissolved with 1010 g of acetone and, in the process, cooled down to 50° C. and subsequently admixed with a solution of 5.70 g of ethylenediamine, 26.4 g of isophoronediamine, 14.0 g of diaminosulphonate and 250 g of water metered in over 10 min. The mixture was subsequently stirred for 10 min. Then, a dispersion was formed by addition of 243 g of water. This was followed by removal of the solvent by distillation under reduced pressure.
The white dispersion obtained had the following properties:
201.3 g of PolyTHF® 2000, 76.6 g of PolyTHF® 1000, 155.3 g of Desmophen® C2200, 2.50 g of trimethylolpropane and 10.0 g of LB 25 polyether were heated to 70° C. in a standard stirring apparatus. Then, a mixture of 53.7 g of hexamethylene diisocyanate and 71.0 g of isophorone diisocyanate was added at 70° C. in the course of 5 min and the mixture was stirred at 120° C. until the theoretical NCO value was reached or the actual NCO value was slightly below the theoretical NCO value. The ready-produced prepolymer was dissolved with 1010 g of acetone and, in the process, cooled down to 50° C. and subsequently admixed with a solution of 5.70 g of ethylenediamine, 26.4 g of isophoronediamine, 14.0 g of diaminosulphonate and 250 g of water metered in over 10 min. The mixture was subsequently stirred for 10 min. Then, a dispersion was formed by addition of 293 g of water. This was followed by removal of the solvent by distillation under reduced pressure.
The white dispersion obtained had the following properties:
1072 g of PolyTHF® 2000, 407.6 g of PolyTHF® 1000, 827 g of Desmophen® C2200 and 48.1 g of LB 25 polyether were heated to 70° C. in a standard stirring apparatus. Then, a mixture of 257.4 g of hexamethylene diisocyanate and 340 g of isophorone diisocyanate was added at 70° C. in the course of 5 min and the mixture was stirred at 120° C. until the theoretical NCO value was reached or the actual NCO value was slightly below the theoretical NCO value. The ready-produced prepolymer was dissolved with 4820 g of acetone and, in the process, cooled down to 50° C. and subsequently admixed with a solution of 27.3 g of ethylenediamine, 126.5 g of isophoronediamine, 67.0 g of diaminosulphonate and 1090 g of water metered in over 10 min. The mixture was subsequently stirred for 10 min. Then, a dispersion was formed by addition of 1180 g of water. This was followed by removal of the solvent by distillation under reduced pressure.
The white dispersion obtained had the following properties:
The Table 1 amounts of the polyurethane dispersions produced as described in Examples 1-6 were mixed with the foam auxiliaries indicated in Table 1 and frothed by means of a commercially available hand stirrer (stirrer made of bent wire) to a 1 litre foam volume. While stirring was continued, the foams obtained were finally coagulated by addition of Praestol® 185 K; coagulation left foam volume unchanged (slight increase in viscosity). Thereafter, the foams were drawn down on silicone-coated paper by means of a blade coater set to the gap height reported in Table 1. Table 1 similarly recites the drying conditions for the foams produced as indicated. Clean white foams having good mechanical properties and a fine porous structure were obtained without exception.
1)blade coater gap height
As is discernible from Table 2, all the foams exhibited a very rapid imbibition of water, a high absorbence of physiological saline (“free swell absorbency”), a very high moisture vapour transmission rate (MVTR) and also good mechanical strength, in particular after moist storage.
1)time for complete penetration of a drop of distilled water into the foam (test on side facing the paper);
2)absorption of physiological saline determined according to DIN EN 13726-1 Part 3.2 (5 instead of 9 test samples);
3)moisture vapour transition rate determined according to DIN EN 13726-2 Part 3.2
54 g of a polyurethane dispersion prepared according to Example 2 were mixed with 1.37 g of Simulsol® SL 26. This mixture was introduced into a chamber of a suitable 2-component aerosol can; the other chamber was filled with 1.69 g of Praestol® 185 K. The components were finally admixed with 6 g of a blowing agent mixture of i-butane/propane/n-butane. After spraying (about 1 cm wet film thickness) and drying at ambient conditions, a clean white, fine-cell foam was obtained.
Example 14 describes the production of biomedical foam articles comprising antiseptic biguanide and particularly PHMB.
Free absorbency was determined by absorption of physiological saline to DIN EN 13726-1 Part 3.2. Moisture vapour transition rate (MVTR) was determined according to DIN EN 13726-2 Part 3.2.
1077.2 g of PolyTHF® 2000, 409.7 g of PolyTHF® 1000, 830.9 g of Desmophen® C2200 and 48.3 g of LB 25 polyether were heated to 70° C. in a standard stirring apparatus. Then, a mixture of 258.7 g of hexamethylene diisocyanate and 341.9 g of isophorone diisocyanate was added at 70° C. in the course of 5 min and the mixture was stirred at 120° C. until the theoretical NCO value was reached or the actual NCO value was slightly below the theoretical NCO value. The ready-produced prepolymer was dissolved with 4840 g of acetone and, in the process, cooled down to 50° C. and subsequently admixed with a solution of 27.4 g of ethylenediamine, 127.1 g of isophoronediamine, 67.3 g of diaminosulphonate and 1200 g of water metered in over 10 min. The mixture was subsequently stirred for 10 min. Then, a dispersion was formed by addition of 654 g of water. This was followed by removal of the solvent by distillation under reduced pressure.
The polyurethane dispersion obtained had the following properties:
120 g of a polyurethane dispersion produced according to Example 14.1 were mixed with 1.48 g of Plantacare® 1200 UP (previously adjusted to pH 7 with citric acid) and 0.24 g of Stokal® STA and also with 76 mg of polyhexamethylenebiguanide. After 20 minutes' beating and drying (20 min at 120° C.) a clean white, fine-cell, hydrophilic foam was obtained.
120 g of a polyurethane dispersion produced according to Example 14.1 were mixed with 1.48 g of Plantacare® 1200 UP (previously adjusted to pH 7 with citric acid) and 0.24 g of Stokal® STA and also with 151 mg of polyhexamethylenebiguanide. After 20 minutes' beating and drying (20 min at 120° C.) a clean white, fine-cell, hydrophilic foam was obtained.
120 g of a polyurethane dispersion produced according to Example 14.1 were mixed with 3.78 g of Pluronic® PE 6800 and also with 76 mg of polyhexamethylenebiguanide. After 20 minutes' beating and drying (20 min at 120° C.) a clean white, fine-cell, hydrophilic foam was obtained.
120 g of a polyurethane dispersion produced according to Example 14.1 were mixed with 13.40 g of Pluronic® PE 6800 and also with 400 mg of polyhexamethylenebiguanide. After 20 minutes' beating and drying (20 min at 120° C.) a clean white, fine-cell, hydrophilic foam was obtained.
| Number | Date | Country | Kind |
|---|---|---|---|
| 102007048078.6 | Oct 2007 | DE | national |
