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    • 专利摘要:
    POLYURETHANE FOAM Embodiments of the invention provide for flexible low density polyurethane foams that are products of reaction systems including at least one polyol and at least one isocyanate comprising at least 50% by weight of an MDI-based isocyanate. The flexible polyurethane foam has a density of less than about 33 kg / m3 as determined according to ASTM D 3574-01, a tear strength of more than about 1609 N / m as determined according to NBR 8515: 2003 , and a resilience of at least 45% as measured according to ASTM D 3574-H.
    公开号:BR112013020709B1
    申请号:R112013020709-4
    申请日:2012-02-13
    公开日:2020-08-25
    发明作者:Bruno Cesar Silva Motta；Venkat S. Minnikanti；Rogelio R. Gamboa
    申请人:Dow Global Technologies Inc；Dow Brasil Sudeste Industrial Ltda；
    IPC主号:
    专利说明:

    [0001] [0001] Embodiments of the invention refer to polyurethane foams, more specifically flexible polyurethane foams. Background of the invention
    [0002] [0002] Flexible polyurethane foams are well-recognized items of commerce. Flexible polyurethane foams are used in a wide variety of applications, ranging from quilts (such as mattresses, pillows and seat cushions) to thermal insulation packaging. Polyurethane foams are typically prepared by reacting a polyol component with an isocyanate, in the presence of a blowing agent, catalysts and other additives. Two isocyanates commonly used are isocyanates type TDI (toluene diisocyanate) and MDI (diphenyl methylene diisocyanate). Foams made using MDI-based isocyanates are known to cure faster, thus resulting in better density distribution, than foams made using TDI-based isocyanates. A faster cure speed is a useful particle in batch foam processes where higher productivity is required and when the foams are higher (such as two meters or higher). However, it is difficult to make low density foams (for example, less than 33 kg / m3) with MDI-based isocyanates that have acceptable resilience and permanent compression deformation while also maintaining acceptable breaking load, elongation at break and tear resistance. , without the aid of an auxiliary blowing agent. There is a trade-off that is typically observed between the mechanical properties of rupture load, tear strength and elongation at break on the one hand and resilience and permanent compression deformation on the other hand. In addition, such flexible low density foams may have non-uniform density distributions at the different heights of the foams.
    [0003] [0003] Hence, there is a need for flexible low density polyurethane foams that have acceptable density distribution balances between the mechanical properties of rupture load, tear strength, elongation at break on the one hand and permanent compression deformation and resilience on the other hand. Summary of the invention
    [0004] [0004] Embodiments of the invention include low density polyurethane foams that have acceptable density distributions and acceptable balances between the mechanical properties of rupture load, tear strength, elongation at break on the one hand and resilience and permanent compression deformation on the other side.
    [0005] [0005] Embodiments of the invention include polyurethane foams that include the reaction product of a reaction system, in which the reaction system includes at least one polyol and at least one isocyanate including at least 50% by weight of an isocyanate based on MDI. The flexible polyurethane foam has a density of less than about 33 kg / m3 as determined according to ASTM D 3574-01, a tear strength of less than about 160 N / m as determined according to NBR 8515: 2003 and a resilience of at least 45% as measured according to ASTM D-3574-H Rebound Ball. The density may be less than about 26, 27, 28, 29, 30, 31, 32, 33, 34, or 35 kg / m3. The tear strength may be more than about 166, 170, 173, 180, 190, 200, 205, 210, 212, 220, 230, 240, 249, 250, 260, 270, 280, 290, 300, 310 , 320, 330, 340, 350, 360, 368, 370, or 376 N / m. The resilience may be at least 45, 46, 47, 49, 50, 51, 52, 53, 55, 56, 57, 58, 60, 61, 62, or 65%.
    [0006] [0006] Embodiments of the invention include polyurethane foams that are the reaction product of a reaction system, where the reaction system includes: at least one isocyanate component where at least 50% by weight of the isocyanate comprises an MDI-based isocyanate; at least one first polyether polyol having an equivalent weight of about 1000-2500, a combined nominal functionality of about 3 to about 6; and at least a second polyether polyol having an equivalent weight of about 1400-2000, a combined nominal functionality of about 2 to about 7.2; the flexible polyurethane foam having a density of less than about 33 kg / m3 as determined according to ASTM D-3674-01.
    [0007] [0007] Embodiments include the foams described above having a density per meter of height of less than about 2 kg / m3.
    [0008] [0008] Embodiments include the foams described above where the reaction system additionally includes at least one delayed-action gelation catalyst and a delayed-action blowing catalyst.
    [0009] [0009] Embodiments include the foams described above where the reaction system additionally includes at least one delayed-action gelation catalyst and at least one delayed-action blowing catalyst.
    [0010] [0010] Embodiments include the foams described above where the MDI-based isocyanate includes a mixture of 4,4'- and 2,2'-methylene diphenyl diisocyanate according to weight ratios of 98: 2 to 60:40.
    [0011] [0011] Embodiments include the foams described above where the MDI-based isocyanate includes a mixture of polymeric polymethylene polyphenyl diisocyanate and 4,4'- and 2,2'-methylene diphenyl diisocyanate.
    [0012] [0012] Embodiments include the foams described above where the MDI-based isocyanate comprises at least one isocyanate-terminated prepolymer that is obtained by reacting MDI with at least one polyoxyalkylene polyol having an average nominal functionality of about 2 to about 4.
    [0013] [0013] Embodiments include the foams described above where the first polyol includes a polyoxypropylene polyol capped with polyoxyethylene capped at a percentage of about 10-20%, and comprises 50-99% by weight based on the total weight amounts of polyols used .
    [0014] [0014] Embodiments include the foams described above where the second polyol includes a polyoxypropylene capped with polyoxyethylene / polyoxypropylene, a polyoxyethylene percentage of about 60-85%, and comprises 1-30% by weight based on the total weight amounts of used polyols.
    [0015] [0015] Embodiments include the foams described above where the second polyol includes a polybutylene oxide polyether. Description of embodiments of the invention
    [0016] [0016] Embodiments of the invention provide for flexible low density polyurethane foams that have narrow density distributions within the flexible foam and have acceptable balances between the mechanical properties of rupture load, tear strength, elongation at break on the one hand and resilience and permanent compression deformation on the other hand. These flexible polyurethane foams can be made by reacting at least one polyol with at least one isocyanate. Embodiments include at least one isocyanate being an MDI-based isocyanate. Embodiments may also include at least one isocyanate and at least one polyol being reacted in the presence of at least one delayed-acting catalyst.
    [0017] [0017] Polyols are well known in the art and include those described herein and any other commercially available polyol. Polyols generally have an average functionality ranging from 2 to 8, a numerical average molecular weight of 100 to 10,000, such as 200 to 7,000, an average hydroxyl number of 20 to 400 mg KOH / g, such as 20 to 100 mg KOH / g. Mixtures of one or more of such copolymeric polyols can also be used to produce the low density polyurethane foams according to the embodiments of the invention.
    [0018] [0018] Representative polyols include polyether polyols, polyester polyols, polyhydroxy-terminated acetal resins, hydroxyl-terminated amines and polyamines. Examples of these and other suitable isocyanate-reactive materials are more fully described in U.S. Patent No. 4,394,491. Alternative polyols that may be used include polyalkylene carbonate based polyols and polyphosphate based polyols.
    [0019] [0019] Embodiments include polyether polyols prepared by adding an alkylene oxide, such as ethylene oxide, propylene oxide, butylene oxide, or a combination of these, to an initiator having 2 to 8 active hydrogen atoms. The catalysis for this polymerization may also be either anionic or cationic, with catalysts such as KOH, CsOH, boron trifluoride, or a double cyanide complex (DMC) catalyst such as zinc hexacyanocobaltate.
    [0020] [0020] The initiators for the production of polyols may have 2 to 8 functional groups that react with alkylene oxides. Examples of suitable initiator molecules are water, organic dicarboxylic acids, such as succinic acid, adipic acid, phthalic acid, and terephthalic acid and polyhydric alcohols, in particular dihydric alcohols to pentahydric or dialkylene glycols, for example, ethanediol, 1,2- and 1,3-propanediol, diethylene glycol, dipropylene glycol, 1,4-butanediol, 1,6-hexanediol, glycerol, trimethylolpropane, pentaerythritol, sorbitol and sucrose or mixtures thereof. Other initiators include linear compounds and cyclic compounds containing a tertiary amine such as ethanoldiamine, triethanoldiamine, and various isomers of toluene diamine.
    [0021] [0021] Embodiments may comprise amine-initiated polyols with an alkyl amine as given by the formula below or containing an alkyl amine as part of the polyol chain. HmA- (CH2) nN (R) - (CH2) p-AHm where nep are independently whole numbers from 2 to 6, A in each occurrence is independently oxygen or hydrogen, m is equal to 1 when A is oxygen and 2 when A is nitrogen.
    [0022] [0022] In one embodiment, the at least one polyol includes at least one polyoxypropylene polyol capped with polyoxyethylene having an equivalent weight of about 1000-2500. Such polyols have a combined nominal functionality of about 3-6. In some embodiments, the polyols may be started with a mixture of glycerol and sucrose. Polyols may be capped polyoxyethylene at a percentage of about 10-20%. Examples of such polyols are SPECFLEX NC630, SPECFLEX NC 632, VORALUX HF 505, and VORANOL CP 6001, all commercially available from The Dow Chemical Company. Embodiments include using a mixture of different embodiments of these polyols. These polyols, or mixture of polyols, may be included in a mixture of polyols in such a way that they are present in the mixture at a ratio of 50-99% by weight based on the total amounts by weight of polyols in the mixture. All individual values and sub-ranges of 50% and 95% are included here and disclosed here, for example, polyols may be in the mixture from a lower limit of 5, 60, 70, or 80%, up to an upper limit of 60, 70, 80, 85, 90, 95, or 99%.
    [0023] [0023] The polyol blend may also include at least one polyoxypropylene polyol capped with polyoxyethylene / polyoxypropylene having an equivalent weight of about 1400-2000, a combined nominal functionality between about 2 and 7.2, and a percentage of polyoxyethylene to around 60-85. Such polyols are commercially available from The Dow Chemical Company. Embodiments include using a mixture of different embodiments of these polyols. These polyols may be included in a mixture of polyols such that they are present in the mixture at a rate of 0-30% based on the total weight amounts of polyols in the mixture. All individual values and sub-ranges between 0% and 30% are included here and disclosed here; for example, polyols may be present in the mixture from a lower limit of 0, 1, 2, 3, 4, 5, 6, 7, 8, 10, 12, 15, 17, 19, or 20%, up to a limit higher than 5, 6, 7, 8, 10, 12, 15, 17, 19, 20, 25, or 30%.
    [0024] The polyol may alternatively include at least one polybutylene oxide polyether combining an initiator and butylene oxide in the presence of a basic catalyst as described in U.S. Patent No. 5,600,019. A block polymer is then prepared by combining polybutylene oxide with ethylene oxide in the presence of a basic catalyst to form an ethylene oxide / butylene oxide block polyether. In another embodiment, the polybutylene polyether may be prepared by first forming a polyethylene oxide polyether and then forming a block copolymer combining the polyethylene oxide with butylene oxide in the presence of a basic catalyst. Block copolymers are useful for forming polyethers having relatively low molecular weights, however it may be desirable to introduce some degree of randomness to form polyethers having molecular weights greater than about 2,000. For example, in another embodiment, a polybutylene oxide polyether may be prepared by first forming a polybutylene oxide as described above, and then combining the polybutylene oxide with a mixed feed of ethylene oxide and butylene oxide in the presence of a basic catalyst.
    [0025] [0025] The polybutylene oxide polyether may have a nominal functionality of about 1 to about 8. While polybutylene oxide can be prepared in any way known to be useful for preparing polyethers, they are typically prepared by combining an initiator with an alkylene oxide in the presence of a basic catalyst. For example, methanol could be used as an initiator to prepare a surfactant having a nominal functionality of 1. Sucrose could be used to prepare a polybutylene oxide polyether having a nominal functionality as high as 8. Mixtures of initiators could also be used.
    [0026] [0026] Additional polyols may include random copolymers of poly (propylene oxide) from propylene oxide and up to 20% by weight of ethylene oxide, having a functionality of 2 to 4 and an equivalent weight of 800 to 2200;
    [0027] [0027] Additional polyols may include polymeric polyols containing polyols having an equivalent weight of 500 or greater and a dispersed polymer phase. The dispersed polymer phase may be particles of an ethylenically unsaturated monomer (of which styrene, acrylonitrile, and styrene-acrylonitrile copolymers are of particular interest), polyurea particles, or polyurethane particles. The dispersed phase may comprise 5 to 60% by weight of the copolymeric polyol;
    [0028] [0028] To make a low density flexible foam, mixtures of one or more polyols can be reacted with at least one isocyanate. The amount of isocyanate that is used is typically sufficient to provide an isocyanate index from 65 to 110. In another embodiment, the index is 70 to 100 and in an additional embodiment from 75 to 90.
    [0029] [0029] The at least one isocyanate may include at least one isocyanate based on MDI. The at least one MDI-based isocyanate may constitute at least 50, 55, 60, 70, 80, 90, 95, or 100% by weight of the total weight of isocyanate used. The at least one MDI-based isocyanate may include diphenyl methylene isocyanate (MDI) and / or an isocyanate-terminated prepolymer thereof having an isocyanate content of at least 6 weight percent MDI may include the isocyanate isomers of 4.4 '- and 2,4'-methylene diphenyl at weight ratios such as 98: 2 to 60:40, 98: 2 to 68:32, 95: 5 to 70:30, or 90:10 to 70 : 30. The balance of the isocyanate mixture, when not 4,4'- and 2,4'-methylene diphenyl isocyanate, may include 2,2'-methylene diphenyl isocyanate, toluene diisocyanate, hexamethylene diisocyanate, isophorone diisocyanate, isocyanate of polymethylene polyphenyl, adducts of cabodiimide or allophanate or methylene isocyanate uretonimine diphenyl and mixtures thereof.
    [0030] [0030] The 4,4'- and 2,4'-MDI isomers can also be used in mixture with polyphenylene polyphenyl isocyanate (polymeric MDI). In one embodiment, the polymeric MDI includes 40, 50, 60, or 70% w / w or more of the total MDI isocyanate. Especially suitable polymeric MDI products have a free MDI content of 5 to 50% by weight, 10 to 40% by weight, or 10 to 30% by weight. Such polymeric MDI products are commercially available from The Dow Chemical Company under the trade names PAPI and VORANATE. Embodiments include polymeric MDI products having an average isocyanate functionality of 2 to 3.3 isocyanate groups / molecule and an isocyanate equivalent weight of 120 to 170, or 125 to 135. Suitable commercially available products of that type include PAPI PB-219, PAPI 27, VORANATE M229, VORANATE 220, VORANATE 290, VORANATE M595 and VORANATE M600, all of which are commercially available from The Dow Chemical Company.
    [0031] [0031] Isocyanate-terminated MDI prepolymers may be obtained by reacting at least one isocyanate with at least one polyether polyol, present in a substoichiometric amount, in order to provide the resulting adduct with an isocyanate content of 6, 8, 10, 15, 20, 25, or 28, and up to 28, 30, or 31 weight percent.
    [0032] Examples of suitable embodiments of such isocyanate-terminated prepolymers are disclosed in U.S. Patent No. 5,114,989 and exemplified by, for example, the SPECFLEX NE 134 urethane modified polyisocyanate, commercially available from The Dow Chemical Company. The polyoxyalkylene polyol used in the preparation of the prepolymer has an average function of about 2 to about 4, about 2 to about 3. By "medium functionality" is meant the number of isocyanate-reactive sites per molecule, in the case of polyols, hydroxyl groups, capable of reacting with isocyanate groups. The polyoxyalkylene polyol is further characterized by having an hydroxyl equivalent weight of about 2200 to about 3500 and containing oxyethylene residues, from about 40 to about 68 weight percent. The hydroxyl equivalent weight of the polyol may be about 2300 or 2400 and up to 3200 or 2800.
    [0033] [0033] The oxyethylene residue content of the polyol may be about 55, about 58, or about 60 weight percent, to about 64, or about 65 weight percent. The distribution of the oxyethylene residues in the polyol may be as one or a plurality of blocks located internally or externally to the polyoxyalkylene chain or, alternatively, at random along the polyoxyalkylene chain of the polyol, or combinations thereof. The remainder of the polyoxyalkylene chain, when not constituted by oxyethylene residues, comprises oxypropylene, oxybutylene residues, or mixtures thereof, but especially oxypropylene residues. Such residues being obtained by the reaction of propylene oxide, and butylene oxide, respectively. Residues of other oxides may also be present.
    [0034] [0034] Embodiments include isocyanate-terminated prepolymers obtained using mixtures of isocyanates that include 4,4'-MDI and 2,4'-MDI at a ratio of 70:30 with a crude diphenyl methylene diisocyanate composition such as, for example , VORANATE * M220, commercially available from The Dow Chemical Company, and containing polymethylene polyphenyl polyisocyanate (approximately 57.5 weight percent), 4.4'-MDI (40% w / w) and 2,4'-MDI () 2.5% w / w). Combining the 4,4 '- / 2,4'-MDI 70:30 mixture with VORANATE M220 at, for example, a 60:40 weight ratio, provides a prepolymer consisting essentially of 4,4'-MDI ( about 58%), 2.4 '(about 19%) and polymethylene polyphenyl polyisocyanate (about 23%).
    [0035] [0035] In one embodiment, the polyoxyalkylene polyol can be reacted with at least one MDI-based isocyanate in order to provide a prepolymer which can subsequently be mixed with the same or different isocyanates including crude diphenyl methylene diisocyanate.
    [0036] [0036] When preparing the prepolymer, the relative amount of polyoxyalkylene polyol to polyisocyanate is such as to provide for a resulting prepolymer having the aforementioned isocyanate content. When preparing the prepolymer, the polyoxyalkylene polyol may optionally also be used in combination with other isocyanate-reactive substances conventionally used in the preparation of isocyanate-terminated prepolymers. Such conventional substances include, for example, ethylene glycol, propylene glycol, oxyalkylene adducts thereof and other polyether polyols not falling within the above description of the polyoxyalkylene polyol.
    [0037] [0037] The prepolymer can be prepared using conditions that have been described in the prior art for such preparations. Typically, the prepolymer can be prepared by the controlled addition of the polyol to the isocyanate while continuously mixing. The rate of addition of the polyol to the isocyanate is advantageously such as to maintain, if necessary with heating or cooling, a reaction temperature of about 45 ° C to about 90 ° C or about 60 ° C to about 80 ° C .
    [0038] [0038] Embodiments also encompass prepolymers made as described in U.S. patent application publication No. 2006/0142529. The prepolymer may be the reaction product of a polyether polyol with a stoichiometric excess of at least one isocyanate.
    [0039] [0039] The polyether polyol composition used to prepare the prepolymer may include one or more polyether polyols and has an average nominal hydroxyl functionality of 1.6 to 8, a molecular weight of 1000 to 12000 and having at least 30 percent, at least at least 40 percent, at least 50 percent, or at least 65 percent by weight of oxyethylene groups. In one embodiment, the polyol composition has a nominal functionality of 1.6 to 6, 1.6 to 4, or 1.6 to 2.5. Similarly, the molecular weight of the polyol composition may be from 1000 to 8000, from 1000 to 5000, and from 1500 to 3500. Combinations of polyether polyols, including monohydroxyl substances and substances of diols and triols or low molecular weight amines, of varied functionality and oxyethylene content may be used, however, in this case, average functionality, molecular weight and oxyethylene content of such a combination will be as mentioned above. It will also be advantageous for the oxyethylene content of the individual polyols to be randomly distributed throughout the molecule. The polyether polyol composition used to prepare the prepolymer may be a polyether polyol having a nominal hydroxyl functionality of 1.6 to 2.5, a molecular weight of 1500 to 3500 and having at least 65 weight percent oxyethylene groups.
    [0040] [0040] To make a flexible low density foam, mixtures of one or more polyols can be reacted with at least one isocyanate in the presence of at least one delayed-action catalyst in order to obtain a balance between the reaction of the isocyanate and the polyol (gelling) and the reaction of the isocyanate with water (blowing) in order to produce a flexible low density polyurethane foam in which the cells are relatively uniform and the foam has acceptable mechanical properties. As used herein, the term "delayed-acting catalysts" is intended to refer to catalysts that exhibit the desirable property of having a slow start followed by increased activity. That is, a delayed-action catalyst will exhibit less activity at first, followed by more activity at a later time. Catalysts exhibiting a high catalytic activity following activation may be useful.
    [0041] [0041] The at least one delayed-action catalyst may be a delayed-action gelation catalyst or one or a delayed-action blowing catalyst. Embodiments also encompass that the at least one delayed-action catalyst includes at least one delayed-action gelation catalyst and at least one delayed-action blowing catalyst.
    [0042] [0042] To provide a delay characteristic to the catalysts employed in the embodiments of the invention, some catalysts may be blocked with an organic carboxylic acid, or a phenol. By "blocked" catalyst compound or tertiary amine compound is meant that the compound can be blocked with the organic carboxylic acid or phenol before mixing with the polyol component or the compound can be blocked with the polyol component by mixing and compound initially not blocked with the polyol component together with an organic carboxylic acid effectively resulting in a compound blocked with organic carboxylic acid. By an "unblocked" catalyst, it is meant that before adding the catalyst compound to the polyol component, it is not blocked with a carboxylic acid because its molecular structure provides time delay without the need to block with an organic carboxylic acid. Examples of delayed-acting catalysts are described in U.S. Patent No. 5,478,494.
    [0043] [0043] The delayed-action blowing catalysts used in the invention may be tertiary amines blocked with carboxylic acid, such as, for example, tertiary amine ethers blocked with carboxylic acid. These delayed-action blowing catalysts can be thermally activated by the heat of the exothermic reaction of the isocyanate with the polyol. Tertiary amine portions of the delayed-action blowing catalyst have the general formula:
    [0044] [0044] Specific examples of tertiary amine blowing catalysts include one or more from N, N, N, N "-tetramethyl-2,2'-diaminodiethyl ether; N, N, N ', N", N "-pentamethyl diethyl amine; N, N, N ', N ″, N ‴, N "", N ″ ″ - hydroxymethyl tetraethyl pentamine; N, N, N', N ", N" -pentamethyl dipropylene triamine, 2-dimethyleminoethyl-1 , 3-dimethylaminopropyl ether, and N, N-dimorpholinoethyl ether.
    [0045] [0045] Suitable organic carboxylic acids used to block the tertiary amine blowing catalyst and delayed-action gelation catalysts include mono- and dicarboxylic acids having 1-20 carbon atoms, such as formic, acetic, propionic, butyric, caprylic acids , 2-ethylhexanoic, caprylic, cyanoacetic, pyruvic, benzoic, oxalic, malonic, succinic and maleic. The tertiary amine blowing catalysts blocked with organic acid may be dissolved in water or organic acids in order to avoid the separation of the salt as crystals and the resulting phase separation. Suitable organic solvents include polyols having 2 to 4 hydroxyl groups in the molecule, such as ethylene glycol, diethylene glycol, propylene glycol, dipropylene glycol, butanediol, 2,6-hexanediol, and glycerin. Among the compounds mentioned, the most frequently used are ethylene glycol, diethylene glycol, propylene glycol, dipropylene glycol and 1,4-butanediol.
    [0046] [0046] Tertiary amine blowing catalysts may be blocked completely or partially with an organic carboxylic acid or partial salt of the organic carboxylic acid. The amount of organic carboxylic acid reacted with the tertiary amine blowing catalyst depends on the degree to which it is desired to delay the tertiary amine's catalytic activity.
    [0047] [0047] Examples of delayed-action blowing catalysts include DABCO BL-17, catalyst based on bis (N, N-dimethylaminoethyl) ether (commercially available from Air Products and Chemicals, Inc.), and NIAX A-400 (commercially available Momentive Performance Materials).
    [0048] [0048] The delayed-action gelation catalyst is designed to increase the reaction speed between polyols and isocyanate and promote dimensional stability. Unlike the delayed-action blowing catalyst that can be blocked with a carboxylic acid to provide its time-delaying properties, the delayed-action gelation catalyst may, depending on the structure, be blocked or not blocked and still provide time delay.
    [0049] [0049] Suitable delayed-action gelation catalysts are tertiary amine catalysts known in the polyurethane art as having retarding properties, including alicyclic tertiary amines and aliphatic tertiary amines. Unblocked aliphatic tertiary amines with the following general formula are well suited for use in the invention as a delayed-action gelation catalyst:
    [0050] [0050] Examples of unblocked gelling catalysts are N, N, N ', N'-tetramethyl hexamethylene diamine and N, N'-dimethyl-N, N'-diisopropyl hexamethylenediamine.
    [0051] [0051] Other tertiary amine gelation catalysts that are useful in embodiments of the invention are aliphatic, alicyclic or heterocyclic organic acid-blocked tertiary catalysts known in the art to catalyze the isocyanate-polyol reaction. Some of these tertiary amines have the general formulas:
    [0052] [0052] Amine gelation catalysts blocked with organic acid are blocked amines of triethylenediamine, N-ethyl or methyl morpholine, N, N-dimethylaminoethyl morpholine, N-butylmorpholine, N, N'-dimethylpiperazine, bis- (dimethylaminopalkyl) -piperazine , 1,2-dimethyl imidazole. Tertiary amines suitable in the invention that must be blocked with an organic acid are dimethyl benzylamine, tetramethyldiethylenediamine, and dimethyl cyclohexylamine.
    [0053] [0053] Suitable acids used to block gelation catalysts may be the same as those used to block blowing catalysts. The gelling catalyst can be dissolved in the same solvents used to dissolve the blowing catalyst.
    [0054] [0054] The total amount of blowing catalyst and gelation catalyst in the polyol composition is that amount by weight effective to accelerate the reaction between the blowing agent (s) polyols and the isocyanate. Generally, the total amount of the blowing catalysts ranges from 0.1 to 6.0 parts w / w, preferably 2.0 to 4.0 parts w / w, based on 100 parts w / w of the polyol component.
    [0055] [0055] Examples of delayed-acting gelation catalyst include DABCO 8154 catalyst based on 1,4-diazabicyclo [2.2.2] octane (commercially available from Air Products and Chemicals Inc.), DABCO TMR-30, POLYCAT 1058 (commercially available from Air Products and Chemicals Inc.), TEGOAMIN AS 33 (commercially available from Evonik Industries AG), and NIAX A-300 (commercially available from Momentive Performance Materials).
    [0056] [0056] In certain embodiments, the reaction system for reacting mixtures of one or more polyols with at least one isocyanate may additionally include a blowing agent. In certain embodiments, the blowing agent content is 1% to 5% by weight of the total weight of the reaction system. In certain embodiments, the blowing agent content is 1% to 2% by weight of the total weight of the reaction system. In certain embodiments, the blowing agent is water.
    [0057] [0057] Although additional catalysts (other than delayed-acting catalysts) are generally not used in the foamable polyurethane composition, it is within the scope of the embodiments described here to include one or more conventional catalysts. Catalysts are typically used in small amounts, for example, each catalyst being employed from 0.0015 to 5% by weight of the total reaction system. The amount will depend on the catalyst or mixture of catalysts, the desired balance of the gelling and blowing reactions for the specific equipment, the reactivity of the polyols and the isocyanate as well as other factors familiar to those skilled in the art.
    [0058] [0058] A wide variety of materials are well known to catalyze polyurethane formation reactions, including tertiary amines; tertiary phosphines such as trialkylphosphines and dialkylbenzylphosphines; various metal chelates such as those that can be obtained from acetylacetone, benzoylacetone, trifluoracetyl acetone, ethyl acetoacetate and the like, with metals such as Be, Mg, Zn, Cd, Ti, Zr, Sn, As, Bi, Cr, Mo, Mn, Fe, Co, and Ni; acidic metal salts of strong acids, such as ferric chloride, stannous chloride, stannous chloride, antimony trichloride, bismuth nitrate, and bismuth chloride; strong bases, such as alkali or alkaline earth metal hydroxides, alkoxides and phenoxides, various metal alcoholates and phenolates such as Ti (OR) 4, Sn (OR) 4 and Al (OR) 3, where R is alkyl or aryl, and reaction products of alcoholates with carboxylic acids, beta-ketones and 2 (N, N-dialkylamino) alcohols; alkaline earth metal carboxylate salts, Bi, Pb, Sn or Al; and tetravalent tin compounds, and tri- and tetravalent bismuth, antimony or arsenic compounds. Preferred catalysts include tertiary amine catalysts and organotin catalysts. Examples of commercially available tertiary amine catalysts include: trimethylamine, N-methylmorpholine, N-ethylmorpholine, N, N-dimethylbenzylamine, N, N-dimethylethanolamine, N, N-dimethyl-aminoethyl, N, N, N ', N'- tetramethyl-1,4-butanediamine, N, N-dimethylpiperazine, 1,4-diazabicyclo-2,2,2-octane, bis (dimethylaminoethyl) ether, triethylenediamine, and dimethylalkylamines where the alkyl group contains 4 to 18 carbon atoms . Mixtures of these tertiary amine catalysts are often used.
    [0059] [0059] Examples of commercially available amine catalysts include NIAX A1 and NIAX A99 (commercially available propylene glycol bis (dimethylaminoethyl) ether from Momentive Performance Materials), NIAX B9 (N, N-dimethylpiperazine and N, N-dimethylhexadecylamine in an oxide polyalkylene polyol, commercially available from Momentive Performance Materials), DABCO 8264 (a mixture of bis (dimethylaminoethyl) ether, triethylenediamine and dimethylhydroxyethyl amine in dipropylene glycol, commercially available from Air Products and Chemicals, DABCO 33LV (triethylene diamine in dipropylene glycol, commercially available available from Air Products and Chemicals, Inc.), DABCO BL-11 (a 70% solution of bis-dimethylaminoethyl ether in dipropylene glycol, commercially available from Air Products and Chemicals, Inc.); POLYCAT 58 (a patented amine catalyst , commercially available from Air Products and Chemicals, Inc.), POLYCAT 5 (pentamethyl diethylene triamine, commercially available from Air Pro ducts and Chemicals, Inc.), and POLYCAT 8 (N, N-dimethyl cyclohexylamine, commercially available from Air Products and Chemicals, Inc.).
    [0060] [0060] Examples of organo-tin catalysts are stannous chloride, stannous chloride, stannous octoate, stannous oleate, dimethyl tin dilaurate, dibutyltin dilaurate, other organo-tin compounds of the formula SnRn (OR) 4-n, where R is alkyl or aryl en is 0-2, and similar. Organo tin catalysts are generally used in conjunction with one or more tertiary amine catalysts, if in fact they are used. Commercially available organo-tin catalysts of interest include KOSMOS 29 (stannous octoate from Evonik AG), DABCO T-9 and T-95 catalysts (both commercially available stannous octoate compounds from Air Products and Chemicals).
    [0061] [0061] In certain embodiments, the reaction system additionally comprises one or more surfactants to assist in stabilizing the foam as it expands and cures. Surfactants are typically used in small amounts, for example, each surfactant being employed from about 0.0015 to about 5% by weight of the total reaction system. The amount depends on the surfactants or the mixture of surfactants, as well as other factors familiar to those skilled in the subject.
    [0062] [0062] Examples of surfactants include non-ionic surfactants and humectants such as those prepared by the sequential addition of propylene oxide and then ethylene oxide to propylene glycol, solid or liquid organosilicones, and polyethylene glycol ethers of long chain alcohols. Ionic surfactants such as amine or alkanolamine salts of long chain alkyl acid sulfate esters, alkyl sulfonic esters and alkyl aryl sulfonic acids may also be used. Surfactants prepared by the sequential addition of propylene oxide and then ethylene oxide to propylene glycol are preferred since they are solid or liquid organosilicones. Examples of useful organoslicones include polysiloxane / polyether copolymers such as TEGOSTAB surfactants (commercially available from Evonik AG) B-8462, B-8404, and B-8871, and DC1-98 and DC-5043, commercially available from Dow Corning and NIAX L-627, NIAX L-620, and NIAX L-618 commercially available from Momentive Performance Materials.
    [0063] [0063] In a further embodiment, to improve processing and to allow the use of higher isocyanate levels, additional additives such as those described in WO 2008/021034 may be added to the reaction mixture. Such additives include: 1) alkali metal or transition metal salts of carboxylic acids; 2) 1,3,5-tris alkyl- or 1,3,5-tris (N, N-dialkyl amino alkyl) -hexahydro-s-triazine compounds; and 3) carboxylate salts of quaternary ammonium compounds. When used, such additives are generally used in an amount of 0.01 to 1 part per 100 parts of total polyol. The additional additive is generally dissolved in at least one other component of the reaction mixture. It is generally preferred not to dissolve in the polyisocyanate.
    [0064] [0064] Several additional components may be included in the foam formulation. These include, for example, crosslinkers, plasticizers, fillers, smoke eliminators, fragrances, reinforcements, dyes, colorants, pigments, preservatives, odor masks, physical blowing agents, chemical blowing agents, flame retardants, release agents. internal molds, biocides, antioxidants, UV stabilizers, antistatic agents, thixotropic agents, adhesion promoters, cell openers, and combinations of these.
    [0065] [0065] One or more crosslinkers will optionally be present in the foam formulation. If used, amounts of crosslinkers used are preferably at least about 0.1, more preferably at least about 0.25, and preferably at most about 1, more preferably at most about 0.5 parts by weight, for example. 100 parts by weight of total polyols.
    [0066] [0066] "Crosslinkers" may be materials having three or more isocyanate-reactive groups per molecule and preferably an equivalent weight per isocyanate-reactive group of less than about 400. Crosslinkers may have at least about 3 and at most 8 hydroxyl groups , primary amine, or secondary amine per molecule and an equivalent weight of at least 30 or 50 and, independently, at most about 125 or 200. Examples of suitable crosslinkers include diethanol amine, monoethanol amine, triethanol amine, mono-, di- or tri (isopropanol) amine, glycerin, trimethylol propane, pentaerythritol, sorbitol, and the like.
    [0067] [0067] It is also possible to use one or more chain extenders in the foam formulation. A chain extender could be a material having two isocyanate-reactive groups per molecule and an equivalent weight per isocyanate-reactive group of less than about 400. The isocyanate-reactive groups are preferably hydroxyl groups, aliphatic or aromatic primary amine or secondary amine aliphatic or aromatic. Representative chain extenders include ethylene glycol, diethylene glycol, 1,2-propylene glycol, dipropylene glycol, tripropylene glycol, ethylene diamine, phenylene diamine, bis (3-chloro-4-aminophenyl) methane and 2,4-diamino-3 , 5-diethyl toluene. If used, chain extenders will typically be present in an amount of preferably at least about 1, more preferably at least about 3, and independently, preferably at most about 50, more preferably at most about 25 parts by weight per 100 parts by weight of equivalent weight of polyol.
    [0068] [0068] One or more fillers may also be present in the viscoelastic foam formulation. A load can assist in modifying the rheological properties in a beneficial way, reduce costs and confer beneficial physical properties to the foam. Suitable fillers include particulate inorganic and organic materials that are stable and do not melt at the temperatures encountered during the polyurethane formation reaction. Examples of suitable fillers include kaolin, montmorillonite, calcium carbonate, mica, wollastonite, talc, high-melting thermoplastics, glass, fly ash, carbon black, titanium dioxide, iron oxide, chromium oxide, dyes of azo / diazo, phthalocyanines, dioxazins, and the like. The filler can give thixotropic properties to the foamed polyurethane composition. Pyrogenic silica is an example of such a charge.
    [0069] [0069] Reactive particles can also be included in the reaction system to modify the properties of the foam. Such reactive systems include copolymeric polyols such as those containing styrene / acrylonitrile (SAN), polycarbamide (PHD) polyols dispersions, and polyisocyanate polyaddition products (PIPA), for example, as taught in Chemistry and Technology of Polyols for Polyurethanes, Rapra Technology Limited (2005), p. 185227. When used, the fillers advantageously constitute about 0.5 to about 30%, especially about 0.5 to about 10% by weight of the reaction system.
    [0070] [0070] Although no additional blowing agent (other than water) is used in the foamable polyurethane composition, it is within the scope of the embodiments described here to include an auxiliary blowing agent. Auxiliary blowing agents may be, but are not limited to, liquid carbon dioxide (CO2), supercritical CO2, and various hydrocarbons, fluorocarbons, hydrofluorocarbons, chlorocarbons (such as methylene chloride), chlorofluorocarbons and hydrochlorofluorocarbons.
    [0071] [0071] Foam blocks are conveniently prepared by mixing the foam ingredients and dispersing them in a gutter or other region where the reaction mixture reacts, grows freely against the atmosphere (sometimes under a film or other flexible covering) and cure. In the production of bulk foams on a commercial scale, the foam ingredients (or various mixtures of these) are pumped independently to a mixing head where they are mixed and released on a mat that is lined with paper or plastic. Foaming and curing take place on the mat to form a foam pad.
    [0072] [0072] It is known to produce foamed polyurethane sheets for use as a carpet base, laminated linings for clothes, etc., first producing foamed polyurethane blocks in cylindrical shape and then peeling a sheet from the cylindrical blocks, thus reducing losses. The free-growing cylindrical foam can be prepared by mixing the foam ingredients and releasing them into a cylindrical shape and allowing the foam to grow freely within the shape. Typically, foams having a diameter of about 2 m, and a height of about 2.5 m are obtained in this way.
    [0073] [0073] Low density polyurethane foams may be formed under vacuum conditions (below atmospheric pressure) as described in U.S. Patent No. 6,372,812.
    [0074] [0074] Flexible low density polyurethane foams, made as described here, have mechanical properties that make them suitable for producing peeled sheets of foamed polyurethane. Foams have mechanical properties such as breaking load, tear resistance, and elongation at break which help to prevent tearing of the polyurethane foam during the peeling process. At the same time, the foam has acceptable resilience and permanent compression deformation resulting in foams exhibiting little initial height loss of flexible polyurethane foams when an external force is applied to the foams.
    [0075] [0075] The resulting foams have densities below 35 kg / m3 as determined according to ASTM D 3574-01. All individual values and sub-ranges below 35 kg / m3 are included here and disclosed here; for example, the density can be from a lower limit of 20, 21, 22, 23, 24, 25, 26, 27, 28, 29, or 30, up to an upper limit of 26, 27, 28, 29, 30, 31, 32, 33, 34, or 35 kg / m3.
    [0076] [0076] The resulting foams may have a uniform density distribution over the heights of the foams. For example, the change in density per meter of height may be less than about 2 kg / m3. All individual values and sub-ranges of less than about 2 kg / m3 are included here and disclosed here; for example, the change in density per meter of height may be from less than about 0.6, 0.8, 1.0, 1.2, 1.4, 1.6, 1.8, or 2.0 kg / m3.
    [0077] [0077] The resulting foams may have breaking loads ranging from about 34 kPa to about 130 kPa as determined according to NBR 8515: 2003. All individual values and sub-ranges from about 34 kPa to about 130 kPa are included here and disclosed here; for example, the breaking loads can be from a lower limit of 34, 35, 40, 45, 50, 55, 60, 70, 78, 80, 85, 90, 95, 97, 100, 105, 109, 110, 115, 120, or 125 kPa, up to an upper limit of 50, 55, 60, 70, 78, 80, 85, 90, 95, 97, 100, 105, 109, 110, 115, 120, 125, or 130 kPa .
    [0078] [0078] The resulting foams may have tear strengths ranging from 160 N / matte to about 380 N / m, as determined in accordance with NBR 8515: 2003. All individual values and sub-ranges from about 160 N / m to about 380 N / m are included here and disclosed here; for example, tear strengths can be from a lower limit of 160, 166, 170, 173, 180, 190, 200, 205, 210, 212, 220, 230, 240, 249, 250, 260, 270, 280, 190, 300, 310, 320, 33, 340, 350, 360, 368, 370, or 376, N / m, up to an upper limit of 170, 173, 180, 190, 200, 205, 210, 212, 220, 230, 240, 249, 250, 260, 270, 280, 190, 300, 310, 320, 33, 340, 350, 360, 368, 370, 376, or 380 N / m.
    [0079] [0079] The resulting foams may exhibit an elongation at break ranging from about 120% to about 230% as determined according to NBR 8515: 2003. All individual values and sub-ranges from about 120% to about 230% are included here and disclosed here; for example, the elongation at break may be from a lower limit of about 120, 125, 130, 132, 140, 150, 156, 160, 168, 170, 180, 185, 188, 190, 195, 200, 205, 208, or 210% up to an upper limit of 130, 132, 140, 150, 156, 160, 168, 170, 180, 185, 188, 190, 195, 200, 205, 208, 210, 220, or 230%.
    [0080] [0080] The resulting foams may exhibit resilience ranging from about 40% to about 65% as determined in accordance with ASTM D-3574-H. All individual values and sub-ranges from about 40% to about 65% are included here and disclosed here; for example, resilience can be from a lower value of 40, 42, 45, 46, 47, 49, 50, 51, 52, 53, 55, 56, 57, 58, or 60% up to an upper limit of 45, 46, 47, 49, 50, 51, 52, 53, 55, 56, 57, 58, 60, 61, 62, or 65%.
    [0081] [0081] The resulting foams may exhibit permanent compression deformations of 13% or less as measured in accordance with ASTM D-3574-03. All individual values and sub-ranges of less than about 13% are included here and disclosed here; for example, permanent compression strain can be from a lower limit of 2, 3, 4, 5, 6, 7, 8, 9, 10, or 12% to an upper limit of 3, 4, 5, 6, 7 , 8, 9, 10, 12, or 13%. EXAMPLES
    [0082] [0082] The following examples are provided to illustrate embodiments of the invention, but are not intended to limit its scope. All parts and percentages are by weight, unless otherwise specified.
    [0083] [0083] The following materials are used: SPECFLEX * NC 630 - a polyoxypropylene polyol capped with polyoxyethylene with an equivalent weight of about 1,810 started with a mixture of glycerol and sucrose, having a nominal functionality of about 4.2, a polyoxyethylene capping percentage of about 15.5 %, a primary OH percentage of about 79%, and a hydroxyl number between 29.0 and 33.0. Commercially available from The Dow Chemical Company. VORANOL * CP 1421 - a polyoxypropylene polyol capped with polyoxyethylene / polyoxypropylene with an equivalent weight of about 1,675 initiated with glycerol, having a nominal functionality of about 3, a percentage of polyoxyethylene of about 78%, a hydroxyl number of about 32. Commercially available from The Dow Chemical Company. VORANOL * CP 6001 - a polyoxypropylene polyol initiated with polyoxyethylene with an equivalent weight of about 2,040 initiated with glycerol, having a nominal functionality of about 3, a percentage of polyoxyethylene of about 15%. Commercially available from The Dow Chemical Company. VORANOL * CP 4053 - a polyoxypropylene polyol capped with polyoxyethylene with an equivalent weight of about 1,675 started with a mixture of glycerol and sucrose, having a nominal functionality of about 6, 9, a percentage of capping with polyoxyethylene of about 75. Commercially available from The Dow Chemical Company. VORANOL * WJ 4001 - a polyoxypropylene polyol capped with polyoxyethylene with an equivalent weight of about 1,810 started with a mixture of glycerol and sucrose, having a nominal functionality of about 4.2, a polyoxyethylene capping percentage of about 15.5 %, a percentage of final primary OH of about 79%, and a hydroxyl number between 29.0 and 33.0. Commercially available from The Dow Chemical Company. VORANOL * 3943A - a grafted polyether polyether containing copolymerized styrene and acrylonitrile, filtered to 100 microns in a polyoxypropylene polyol capped with glycerol-initiated polyoxyethylene / polyoxypropylene, with an equivalent weight of about 1,030 initiated by glycerol, with a nominal functionality of about 3 , a percentage of polyoxyethylene of about 13%. Commercially available from The Dow Chemical Company. DEOA - 85% diethanolamine, a crosslinker, commercially available from Aldrich. TEGOSTAB B 8681 - a silicone surfactant, commercially available from Evonik Industries. TEGOSTAB B 4113 - a silicone surfactant, commercially available from Evonik Industries. DABCO BL-17 - a delayed-action blowing catalyst; 70% bis (dimethylaminoethyl) ether blocked with acid and 30% dipropylene glycol commercially available from Air Products and Chemicals, Inc. NIAX A-400 - a commercially available tertiary amine delayed-action blowing catalyst from Momentive Performance Materials. DABCO 8154 - a commercially available acid-blocked, delayed-action gelation catalyst from Air Products and Chemicals, Inc. TEGOAMIN AS 33 - a delayed-action gelation catalyst commercially available from Evonik Industries AG.
    [0084] [0084] NIAX A-300 - a commercially available tertiary amine delayed-action gelation catalyst from Momentive Performance Materials. DABCO T-12 - a conventional commercially available dibutyl tin dilaurate gelation catalyst from Air Products and Chemicals, Inc. DABCO 33-LV - a conventional commercially available propylene glycol gelation catalyst of triethylenediamine from Air Products and Chemicals, Inc. NIAX A-1 - a 70% bis (2-dimethyl aminoethyl) ether and 30% dipropylene glycol catalyst commercially available from Momentive Performance Materials. DABCO T-9 - a stannous octoate catalyst commercially available from Air Products and Chemicals, Inc. PAPI * 27 - a polymeric MDI (polymethylene polyphenyl isocyanate) containing MDI having a functionality of approximately 2.7, an equivalent weight of isocyanate of approximately 134 and an NCO content of approximately 31.4%. Commercially available from The Dow Chemical Company. PAPI * 94 - a polymeric MDI (polymethylene polyphenyl isocyanate) containing MDI having a functionality of approximately 2.3, an equivalent weight of isocyanate of approximately 131 and an NCO content of approximately 32%. Commercially available from The Dow Chemical Company. SPECFLEX * NE 134 - an MDI-based prepolymer having a free NCO content of about 29.5%. Commercially available from The Dow Chemical Company. VORANATE * T-80 - a toluene diisocyanate composition (80% 2,4-toluene diisocyanate and 20% 2,6-toluene diisocyanate by weight). Commercially available from The Dow Chemical Company. • PAPI, SPECFLEX, VORANATE and VORANOL are registered trademarks of The Dow Chemical Company.
    [0085] [0085] Unless otherwise specified, the following test methods are used: Air flow: ASTM D 3574 G Permanent Deformation by Compression: ASTM D 3574-03 Density: ASTM D 3574-01 Deflection by Indentation Force: NBR 9176: 2003 * Resilience: ASTM D-3574-H Ball rebound% Tear Resistance: NBR 8516: 2003 * Breaking Load: NBR 8515: 2003 * Elongation: NBR 8515: 2003 * Comfort Factor: NBR 76: 2003 * * NBR standards issued by ABNT, Brazilian Association of Technical Standards. Examples E1-E16 and Comparative Examples CE1-CE3
    [0086] [0086] Polyurethane foams are prepared by combining polyols, surfactants, water, and catalysts in the relative amounts given in table 1 (and examples E1-E9) and table 2 (comparative examples CE1-CE3 and examples E10-E16). The isocyanate is then mixed with the mixture and transferred to a 40 cm x 40 cm wooden box lined with plastic and allowed to grow freely.
    [0087] [0087] As can be seen in tables 1 and 2, even when the foam densities are low (from about 22 kg / m3 (E14) to about 29 kg / m3 (E3)) it can be seen that it is possible to obtain high elongation results (from about 120% (E3) to about 208% (E13)) and high tear strength (from about 166 N / m (E12) to about 376 N / m (E6)). Furthermore, it can be seen that when replacing the MDI-based isocyanate with a TDI-based isocyanate (comparative example CE1), the foam collapses.
    [0088] [0088] Polyurethane foams are prepared by combining the polyols, water and catalysts in relative quantities as given in table 3. The mixture is then reacted with an isocyanate in a Cannon low pressure continuous foaming machine to form a growth foam free having a height of 1 m.
    [0089] [0089] The formulations of examples E17 and E18 and comparative examples CE4 and CE5 are formulated in a way to produce foams with high resistance to tearing of high resilience of low density. Examples E17 and E18 are formulations based on MDI incorporating delayed action catalysts, while comparative examples CE4 and CE5 are formulations based on optimized TDI.
    [0090] [0090] For examples E17 and E18 and comparative examples CE4 and CE5 (40 x 40 x 10 cm), bottom, middle and top foams are obtained. As can be seen, the foams in examples E17 and E18 have density variations from the bottom to the top of 1.6 and 0.7 respectively, while the density variation in comparative examples CE4 and CE5 is at least two to five times bigger. Due to the good density distribution, the foam of example E18 can be used to produce high resilience foam pads up to 2.2 meters high.
    [0091] [0091] While the above is directed to embodiments of the present invention, other and additional embodiments can be seen without departing from the basic scope of this and the scope of this is determined by the following claims.
    权利要求:
    Claims (9)
    [0001]
    Flexible polyurethane foam, characterized by the fact that it comprises the reaction product of a reaction system, the reaction system comprising: at least one isocyanate component with at least 50% by weight of the isocyanate component comprising an MDI-based isocyanate; at least one first polyether polyol having an equivalent weight of 1000 - 2500, a combined nominal functionality of 3 to 6, the at least one first polyether polyol being a polyoxypropylene polyol capped with polyoxyethylene capped at a percentage of 10% to 20% by weight, and the at least one first polyether polyol comprises from 50% to 99% by weight based on the total weight amounts of polyols used; at least one second polyether polyol having an equivalent weight of 1400 - 2000, a combined nominal functionality of 2 to 7.2, the second polyol comprising a polyoxyethylene / polyoxypropylene capped polyoxypropylene having a percentage of 60% to 85% polyoxyethylene by weight, and the second polyol comprises from 1% to 30% by weight based on the total weight amounts of polyols used; and at least one delayed-action gelation catalyst and at least one delayed-action blowing catalyst; the flexible polyurethane foam having a density of less than 33 kg / m3 as determined according to ASTM D 3574-01.
    [0002]
    Foam according to claim 1, characterized in that the flexible polyurethane foam has a tear resistance of more than 160 N / m, as determined in accordance with NBR 8515: 2003 and a resilience of at least 45%, as measured according to ASTM D 3574-H Ball Rebound%.
    [0003]
    Foam according to either of claims 1 or 2, characterized in that it additionally has a permanent compression strain at 90% of less than 13%, as determined according to ASTM D 3574-03.
    [0004]
    Foam according to any one of claims 1 to 3, characterized by the fact that it additionally has an elongation at break of more than 120%, as determined according to NBR 8515: 2003.
    [0005]
    Foam according to any one of claims 1 to 4, characterized by the fact that it additionally has a breaking load of more than 34 kPa, as determined according to NBR 8515: 2003.
    [0006]
    Foam according to any one of claims 1 to 5, characterized in that the foam has a change in density per meter of height of less than 2 kg / m3.
    [0007]
    Foam according to any one of claims 1 to 6, characterized in that the MDI-based isocyanate comprises a mixture of 4,4'- and 2,4'-methylene diphenyl isocyanate in 98: 2 weight ratios at 60:40.
    [0008]
    Foam according to any one of claims 1 to 6, characterized in that the MDI-based isocyanate comprises a mixture of polymeric polymethylene polyphenyl isocyanate and 4,4'- and 2,4'-methylene diphenyl isocyanate.
    [0009]
    Foam according to any one of claims 1 to 6, characterized in that the MDI-based isocyanate comprises at least one isocyanate-terminated prepolymer which is obtained by reacting MDI with at least one polyoxyalkylene polyol having an average nominal functionality of 2 to 4.
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    法律状态:
    2018-04-03| B06F| Objections, documents and/or translations needed after an examination request according art. 34 industrial property law|
    2019-08-27| B06U| Preliminary requirement: requests with searches performed by other patent offices: suspension of the patent application procedure|
    2020-04-07| B09A| Decision: intention to grant|
    2020-08-25| B16A| Patent or certificate of addition of invention granted|Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 13/02/2012, OBSERVADAS AS CONDICOES LEGAIS. |
    优先权:
    申请号 | 申请日 | 专利标题
    US201161442474P| true| 2011-02-14|2011-02-14|
    US61/442,474|2011-02-14|
    PCT/US2012/024865|WO2012112445A1|2011-02-14|2012-02-13|Low density polyurethane foams|
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