JP2005225974A - Method for producing polyurethane foam with high air permeability and low resilience - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To prepare a viscoelastically flexible polyurethane foam having excellent viscoelastic performance useful as a vibration, sound or impact absorber or as a mattress, pillow, cushion, or the like, capable of more uniformly dispersing human body pressure than conventional flexible polyurethane foam, thus effective in reducing sense of fatigue and bedsore, therefore excellent in terms of human engineering. <P>SOLUTION: A method for producing the flexible polyurethane foam is provided, comprising carrying out a reaction between a polyisocyanate(A), a polyol(B), a foaming agent(C), a catalyst(D) and a foam stabilizer(E). In this method, the polyol(B) comprises (b1) a polyester polyol with an average functional group number of 2.5-4.5 and a hydroxy equivalent of 300-500 and (b2) a polyalkylene polyol with an average functional group number of 2.5 and a hydroxy equivalent of 500-3,000 in a specific proportion. The isocyanate index of this flexible polyurethane foam is 50-100. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

  The present invention relates to a method for producing a flexible polyurethane foam having low rebound resilience and high air permeability.

  Conventionally, low resilience flexible polyurethane foams are known which are used for various types of lamination as shock absorbing materials and vibration absorbing materials, or used for pillows, mattresses, cushions, cushions, clothing pads and the like. The polyurethane foam used for these products is formulated so as to obtain a polyurethane foam having a desired rebound resilience by appropriately selecting the resin composition of the urethane foam, that is, the types of the polyol component and the polyisocyanate compound.

  By the way, although the low-rebound resilience polyurethane foams proposed so far have a desired low-rebound resilience, they have almost no breathability. For example, when used for pillows, mattresses, cushions or cushions, heat from the human body. The water vapor was not sufficiently dissipated and stuffiness was likely to occur.

  In addition, the low resilience polyurethane foam is strongly temperature sensitive and inevitably hardens when the temperature is low. For example, pillows, cushions, mattresses, and the like have a problem that the feel of the foam changes due to a change in environmental temperature, and the feeling of use greatly changes.

  As means for solving such a problem, Patent Document 1 discloses that a polyol component is a mixed polyol composed of a high molecular weight polyol having a molecular weight of 500 or more and a low molecular polyhydric alcohol, and a low molecular weight dihydric alcohol has Examples using propylene and / or 1,3-butanediol and using glycerin and / or trimethylolpropane as a low molecular weight trihydric alcohol are described. However, even in the prescription described in this document, the increase in hardness of the foam at a low temperature is not sufficiently improved, and there is a problem that a flexible feeling of use cannot be obtained at a low temperature such as winter.

JP 2004-2591 A

  In view of the above-mentioned present situation, the present invention provides a polyurethane foam having excellent low rebound resilience, high foam permeability, low dependency of hardness on temperature, and high durability. It was an issue.

  In order to solve such a problem, the present inventors have conducted intensive studies, and as a result, of the polyol component and polyisocyanate compound that have been formulated and formulated as a resin component of a polyurethane foam having low resilience so far, a polyol component is selected. A mixture of a specific molecular weight polyester polyol and a high molecular weight polyoxyalkylene polyol having a specific mixing ratio and reacting the mixed polyol component and the polyisocyanate compound with an isocyanate index of 100 or less results in low rebound resilience and extremely good ventilation. The present invention has been completed by confirming that a flexible polyurethane foam having good properties, temperature dependency of low hardness, and very good compression residual strain can be obtained.

  That is, this invention is shown by the following (1)-(6).

(1) Density of 40-80 kg / m ³ for reactive foaming of polyisocyanate (A), polyol (B), foaming agent (C), catalyst (D), foam stabilizer (E) with an isocyanate index of 50-100, A method for producing a flexible polyurethane foam having a hardness of 8 to 450 N / 100 cm ² , comprising:
Polyoxyl whose polyol (B) has an average functional group number of 2.5 to 4.5 and a hydroxyl group equivalent of 300 to 500 and a polyester polyol (b1) having an average functional group number of 2.5 to 4.5 and a hydroxyl group equivalent of 300 to 5000 Highly breathable, characterized by using a polyol component which is a mixed polyol with an alkylene polyol (b2) and whose mixing ratio is (b1) :( b2) = 70-90: 30-10 (mass ratio)・ Production method of polyurethane foam with low rebound resilience.

(2) The polyoxyalkylene polyol (b2) is a polyol obtained by adding propylene oxide and ethylene oxide to a polyhydroxy compound having two or more hydroxyl groups per molecule, described in (1) Manufacturing method for polyurethane foam with high air permeability and low resilience.

(3) The method for producing a polyurethane foam having high air permeability and low resilience according to (1) or (2), wherein the catalyst (D) contains an imidazole compound.

(4) The method for producing a polyurethane foam having high air permeability and low resilience according to (1), (2) or (3), wherein the polyol (B) further contains a polyoxyalkylene monool. .

(5) The polyol (B) further contains a polyoxyalkylene polyol having an average functional group number of 2.5 to 4.5 and a hydroxyl group equivalent of 100 to 500. A process for producing breathable, low resilience polyurethane foam.

(6) The high breathability and low resilience according to (1) to (5), wherein the dry heat compression residual strain value measured according to JIS K6400 (1997) is 2.5% or less. Polyurethane foam manufacturing method.

  According to the present invention, it has become possible to produce a flexible polyurethane foam having a sufficiently low resilience and high air permeability, and having greatly improved hardness dependency on temperature. Moreover, this flexible polyurethane foam has a very good compression residual strain rate not found in conventional foams. Accordingly, it is possible to provide a shock-absorbing material, a vibration-absorbing material, a pillow, a mattress, a cushion, a cushion, a garment pad, or the like that has a small change in feeling of use due to a change in environmental temperature, is less likely to stuffy, and is highly durable It has become possible.

As described above, the basis of the present invention is the polyester polyol (b1) having an average functional group number of 2.5 to 4.5 and a hydroxyl group equivalent of 300 to 500, an average functional group number of 2.5 to 4.5, and a hydroxyl group equivalent of 500 to 3000. The polyoxyalkylene polyol (b2) is used as a polyol component with a mixing ratio of (b1) :( b2) = 70-90: 30-10 by mass ratio, and the polyol component and the polyisocyanate compound are combined with an isocyanate index. A method for producing a polyurethane foam having high air permeability and low resilience, characterized by producing a foam having a density of 40 to 80 kg / m ³ and a hardness of 8 to 150 N / 100 cm ² obtained by reacting at 50 to 100 is there.

From the viewpoint of manufacturing costs, in general, the density of flexible polyurethane foam is preferred to be low. However, extremely low density foam has low rebound resilience and high durability, which are the problems to be solved by the present invention. , Can not be satisfied. Moreover, since problems such as insufficient hardness due to low density and poor touch on the surface of the foam product also occur, setting a density lower than 40 kg / m ³ is not preferable. In addition, the upper limit of the density is 80 kg / m ³ from the viewpoint of cost and production efficiency. Foam hardness, required to be in the predetermined range from the applications described above, the hardness 8N / 100 cm ² expressed in 25% CLD lower, same 150 N / 100 cm ² is the upper limit. If it is softer than this, low resilience foam with a large stress relaxation rate will not exhibit the effects of hardness, shape sinking, sufficient pressure dispersion, and impact relaxation on the surface in contact with the bottom of the foam. When it is harder, there is a problem that the softness is impaired and the texture is deteriorated and the impact absorbing performance cannot be obtained.

  The greatest feature of the present invention is the polyester polyol (b1) having an average functional group number of 2.5 to 4.5 and a hydroxyl group equivalent of 300 to 500, and a polyoxy compound having an average functional group number of 2.5 to 4.5 and a hydroxyl group equivalent of 500 to 3000. The mixed polyol which uses the alkylene polyol (b2) at a mixing ratio of b1: b2 = 70 to 90:30 to 10 is used as a polyol component.

  In the present invention, the average number of functional groups of the polyol is calculated from the number of functional groups and the number of moles of the raw material used at the time of polyol production, and in the polyester polyol (b1), the number of functional groups and the number of moles of the carboxylic acid component, It is calculated from the number of functional groups and the number of moles of the alcohol component. Furthermore, the hydroxyl equivalent of the polyester polyol is a value calculated from the hydroxyl value and the average number of functional groups.

  The average functional group number of the polyoxyalkylene polyol referred to in the present invention refers to the average functional group number of the polymerization initiator. When an alkylene oxide is added to a polyfunctional initiator, the reaction at the addition terminal is stopped by side reaction, and the generation of alcohol having a lower functional group number than that of the polymerization initiator has been confirmed. A measuring method has not been established, and in the present invention, the average number of functional groups of a polymerization initiator generally used as the number of functional groups of the polyoxyalkylene polyol is defined as the number of functional groups of the polyol. The hydroxyl equivalent of the polyoxyalkylene polyol is a value calculated from the hydroxyl value and the average number of functional groups.

  The polyester polyol (b1) is obtained by polycondensation of one or more polycarboxylic acid components with one or more polyol components. The polycarboxylic acid component may be in the form of an acid anhydride or carboxylic acid ester which is a derivative thereof in addition to the polycarboxylic acid. Further, cyclic ester ring-opening polymers such as polycaprolactone, compounds having both a hydroxyl group and a carboxylic acid group such as lactic acid, and the like may be added.

  Examples of the polycarboxylic acid include aliphatic carboxylic acids and aromatic carboxylic acids. Specific examples include malonic acid, maleic acid, succinic acid, adipic acid, tartaric acid, sebacic acid, oxalic acid, phthalic acid, terephthalic acid, and trimellitic acid.

  Examples of the polyol component that is a raw material of (b1) include diol and triol. Specifically, ethylene glycol, diethylene glycol, propylene glycol, dipropylene glycol, triethylene glycol, 1,3- and 1,4-butanediol, tetramethylene glycol, neopentyl glycol, hexamethylene glycol, decamethylene glycol, glycerin , Trimethylolpropane, pentaerythritol, sorbit and the like. Since the obtained polyester polyol is preferably liquid at normal temperature, it preferably contains diethylene glycol as the glycol component, and preferably contains trimethylolpropane as the trifunctional polyol component.

  Although the average functional group number of (b1) is 2.5 to 4.5, it is more preferably 2.5 to 3.5 from the viewpoint of viscosity.

  The hydroxyl equivalent of (b1) is 300 to 500, and even if it is less than 300 or more than 500, the low resilience that is the effect of the present invention is not sufficiently exhibited. 300 to 400 is more preferable from the viewpoint of low resilience.

  Examples of the polyoxyalkylene polyol (b2) include polyhydric alcohols such as ethylene glycol, propylene glycol, diethylene glycol, triethylene glycol, dipropylene glycol, trimethylene glycol, glycerin, pentaerythritol, trimethylolpropane, sorbitol, and sucrose. An alkylene oxide adduct with an initiator as an initiator; an alkylene oxide adduct of a polyhydric phenol such as bisphenol A; a polyhydric hydroxy compound such as phosphoric acid or polyphosphoric acid (for example, tripolyphosphoric acid or tetrapolyphosphoric acid), or phenol-aniline -Formaldehyde condensation products, ethylenediamine, diethylenetriamine, triethylenetetramine, methylenebisorthochloroaniline, 4,4'- and 2,4'- Polyamines such as phenylmethanediamine, 2,4-tolylenediamine, 2,6-tolylenediamine, alkanolamines such as triethanolamine and diethanolamine, and ethylene oxide, propylene oxide, butylene oxide, tetrahydrofuran, styrene oxide, etc. The polyoxyalkylene polyol obtained by adding seed | species or 2 or more types can be illustrated.

  A vinyl copolymer-containing polyoxyalkylene polyol may be added to the polyol component (B). Examples of this include those obtained by polymerizing vinyl polymers such as acrylonitrile and styrene in the presence of radicals in the polyoxyalkylene polyols exemplified above and stably dispersing them. In addition, content of the vinyl polymer in polyoxyalkylene polyol is about 10-45 mass% normally.

  The average functional group number of (b2) of this invention is 2.5-4.5, and the hydroxyl equivalent of (b2) is 500-3000. If the hydroxyl equivalent is less than 500, the hardness is excessively increased and the tactile sensation is deteriorated. In order to obtain a sufficiently good tactile sensation, the hydroxyl equivalent is preferably 1000 to 3000.

  Furthermore, the mixing ratio (mass ratio) of the polyester polyol (b1) and the polyoxyalkylene polyol (b2) in the polyol component (B) is (b1) :( b2) = 70 to 90: 30-10, (b1 ) Exceeds 90% by mass, the dependence of the hardness on the temperature becomes remarkably high. If it is less than 70% by mass, a general silicone-based surfactant cannot maintain the shape of the foam. I can't get it.

  In the present invention, it is preferable to add a polyoxyalkylene monool (b3) to the polyol component (B) in addition to the polyester polyol (b1) and the polyoxyalkylene polyol (b2). By adding (b3), it is possible to further improve the foam air permeability. As the polyoxyalkylene monool, an initiator obtained by adding an alkylene oxide to a monoalcohol such as methanol, ethanol, propanol, butanol, or 2-ethylhexanol can be used.

  As the alkylene oxide to be added, ethylene oxide and propylene oxide are preferable, and those having 30 to 80 mol% of ethylene oxide are preferable.

  The hydroxyl equivalent (= molecular weight) is preferably 76 to 1000. More preferably, it is 76-500 from the balance of the addition amount and the addition effect. The addition amount is preferably 0.5 to 10 parts by weight with respect to 100 parts by weight of (b1) + (b2). Below the lower limit, the effect of improving the air permeability is less likely to appear, and when added above the upper limit, the stickiness on the foam surface becomes stronger, causing adhesion between products and adhesion of dust.

   In the present invention, in addition to the polyester polyol (b1) and the polyoxyalkylene polyol (b2), the polyoxyalkylene polyol having an average functional group number of 2.5 to 4.5 and a hydroxyl group equivalent of less than 300 is added to the polyol component (B). It is preferable to add (b4). By adding an amount corresponding to the foam hardness for which (b4) is desired, it is possible to freely adjust the hardness while maintaining the advantages of the present invention. As addition amount, 0.5-10 weight part is preferable with respect to 100 mass parts of (b1) + (b2). The amount of (b4) added depends on the foam hardness to be obtained. However, when the amount is 0.5 parts or less, no increase in hardness is observed, and when the amount is 10 parts by weight or more, there is a problem that the foam cell becomes large and the tactile sensation deteriorates.

  On the other hand, it does not specifically limit as a polyisocyanate compound, The well-known polyisocyanate compound normally used for manufacture of a polyurethane foam can be used. Specifically, one or more of aromatic, alicyclic and aliphatic polyisocyanates and modified polyisocyanates obtained by modifying them are appropriately selected and used.

  Aromatic polyisocyanates include 2,4-tolylene diisocyanate, 2,6-tolylene diisocyanate, a mixture of 2,4-tolylene diisocyanate and 2,6-tolylene diisocyanate, diphenylmethane diisocyanate, naphthalene diisocyanate, triphenyl Examples include methane triisocyanate, xylylene diisocyanate, and polymethylene polyphenyl diisocyanate.

  Examples of the alicyclic polyisocyanate include cyclohexylmethane diisocyanate, cyclohexane diisocyanate, and hydrogenated MDI. Examples of the aliphatic polyisocyanate include hexamethylene diisocyanate.

  Among these polyisocyanate compounds, in the present invention, 2,4-tolylene diisocyanate or 2,6-tolylene diisocyanate, which are aromatic polyisocyanates, and mixtures thereof (TDI-80, TDI-65) gave good results.

  Another major feature of the present invention is the use of specific amine catalysts. In the foaming of flexible foams mainly composed of water as the foaming agent, it is necessary to balance resinification and carbon dioxide generation. If this balance is lost, the foam will sink in the middle of foaming or cell connectivity will be insufficient. Thus, there is a problem in moldability such as shrinkage after foaming. In addition, since the amine-based catalyst has a little odor, it is preferable to select a catalyst having a low odor particularly for bedding use.

  As the amine catalyst for improving the foam moldability, a catalyst that strongly activates the reaction between the alcohol and the isocyanate as compared with the reaction between water and the isocyanate is preferable. Furthermore, as a result of studying a number of catalysts, it has been found that by using an imidazole catalyst as a part or all of the catalyst, it is possible to achieve a very low compressive residual strain, which is an object of the present invention. A preferred ratio of the imidazole catalyst to the total amount of catalyst used for foaming is 5% or more. In order to obtain a sufficient effect, addition of 15% or more is preferable.

  Examples of the imidazole catalyst include alkyl imidazoles, and specific examples include 1,2-dimethylimidazole, 1-ethyl-2-methylimidazole, 1-butyl-2-methylimidazole, and the like. Commercial products containing these include TOYOCAT DMI, TOYOCAT DM70, TOYOCAT F2, TOYOCAT F10, TOYOCAT F94, etc. from Tosoh Corporation, NC-IM, IMICURE EMI-24, etc. from Air Products, Inc. The company sells U-CAT 2026, U-CAT 2030, U-CAT 2034X, U-CAT 2503, and the like.

  As the catalyst used in the present invention, known catalysts can be used in combination with urethane foams such as amine catalysts other than the imidazole catalysts and organometallic catalysts. As such a catalyst, for example, as an amine catalyst, 1,8-diazabicyclo- (5,4,0) undecene-7, bis (2-dimethylaminoethyl) ether, N, N, N ′, N ′ -Tetramethylhexamethylenediamine, triethylenediamine, triethylamine, tripropylamine, triisopropylamine, tributylamine, trioctylamine, N-methylmorpholine, N-ethylmorpholine, dimethylpiperazine, N, N-dimethylaminoethanol, N, N-dimethylaminoethoxyethanol, N, N, N′-trimethylaminoethylethanolamine, N, N, N ′, N ″, N ″ -pentamethyldipropylenetriamine, etc. and diluted products with these solvents , A mixture of two or more of these catalysts, part by organic acid Neutralized products and the like can be mentioned. For the above reasons, 1,8-diazabicyclo- (5,4,0) undecene-7, triethylenediamine, N-ethylmorpholine, N- Methylmorpholine, dimethylpiperazine, dimethylaminoethanolamine, and organic acid salts thereof are preferable.

  Examples of the metal catalyst include tin octylate, tin laurate, and dibutyltin dilaurate.

  In the polyurethane foam of the present invention, a plasticizer can be added in addition to these polyol component and polyisocyanate compound. Examples of plasticizers include dioctyl phthalate (DOP), diisononyl phthalate (DINP), butyl benzyl phthalate (BBP), diisodecyl phthalate (DIDP), and diundecyl phthalate (DUP). General phthalate plasticizers, adipic acid dioctyl ester (DOA), sebacic acid dioctyl ester (DOS), general fatty acid ester plasticizer represented by azelaic acid dioctyl ester (DOZ), trioctyl trimellitic acid General sebacic acid plasticizers such as trimellitic acid ester plasticizers typified by esters (TOTM), polyester plasticizers typified by polypropylene adipate, etc., chlorinated paraffin, etc. Plasticizer Phosphate ester plasticizers such as zilphate (TCP), trixylyl phosphate (TXP), tris (isopropylphenyl) phosphate, tributyl phosphate, triethyl phosphate, triphenyl phosphate, triethylphenyl phosphate, epoxidized products of vegetable oil, epoxy resin Examples of epoxidized vegetable oils include epoxidized soybean oil, epoxidized linseed oil, etc., and epoxy resins include epoxidized polybutadiene, epoxy methyl stearate, epoxy butyl stearate, ethyl hexyl epoxy stearate, tris ( Epoxypropyl) isocyanurate, 3- (2-xenoxy) -1,2-epoxypropane, bisphenol A diglycidyl ether, vinyl dicyclohexene die Examples thereof include epoxy plasticizers such as polycondensates of poxide, 2,2-bis (4-hydroxyphenyl) propane and epichlorohydrin. These plasticizers can be used alone or in admixture of two or more.

  These plasticizers can be added in an amount of 2 to 15 parts by mass with respect to 100 parts by mass of the polyol component (B) described above. If the amount of the plasticizer is too large, the foam surface may have an excessively high tackiness.

  In addition, in the polyurethane foam of the present invention, various other additives such as flame retardants, antioxidants, ultraviolet absorbers, colorants, pigments, antibacterial agents, deodorants, deodorants, and fragrances. Etc. can be used.

  Flame retardants include phosphate esters such as tricresyl phosphate (TCP), tris (β-chloroethyl) phosphate, tris (dichloropropyl) phosphate, tris (dibromopropyl) phosphate, bromophosphate; chlorinated paraffin, tetrabromide Halogenated hydrocarbons such as ethylene; inorganic flame retardants such as zinc borate, magnesium hydroxide, aluminum hydroxide, antimony oxide, molybdenum oxide, zinc molybdate and the like can be used. These flame retardants can be used alone or in combination.

  Examples of the antioxidant include alkylphenols, alkylene bisphenols, alkylphenol thioethers, β, β'-thiopropionic acid esters, and organic phosphites. These antioxidants can be used alone or in admixture of two or more.

  Examples of ultraviolet absorbers include salicylic acid esters, benzotriazoles, hydroxybenzophenones, acrylonitrile substitution products, and the like. These ultraviolet absorbers can be used alone or in admixture of two or more. Specifically, 2,4-dihydroxybenzophenone, 2-hydroxy-4-methoxybenzophenone, 2-hydroxy-4-ethoxybenzophenone, 2-hydroxy-4-octoxybenzophenone, 5,5′-methylenebis (2-hydroxy 2-hydroxybenzophenones such as 4-methoxybenzophenone); 2- (2′-hydroxy-5′-methylphenyl) benzotriazole, 2- (2′-hydroxy-3 ′, 5′-di-tert-butyl) Phenyl) -5-chlorobenzotriazole, 2- (2'-hydroxy-3'-tert-butyl-5'-methylphenyl) -5-chlorobenzotriazole, 2- (2'-hydroxy-5'-tert- Octylphenyl) benzotriazole, 2- (2'-hydroxy-3 ' , 5′-Dicumylphenyl) benzotriazole, 2- (2′-hydroxyphenyl) benzotriazoles such as 2,2′-methylenebis (4-tert-octyl-6-benzotriazole) phenol; Resorcinol monobenzoate, 2,4-di-tert-butylphenyl-3 ′, 5′-di-tert-butyl-4′-hydroxybenzoate, hexadecyl-3,5-di-tert-butyl-4-hydroxybenzoate, etc. Benzoates; oxanilides such as 2-ethoxy-4'-dodecyl oxanilide; ethyl-α-cyano-β, β-diphenyl acrylate, methyl-2-cyano-3-methyl-3- (p-methoxyphenyl) ) Cyanoacrylates such as acrylate. These ultraviolet absorbers may be used alone or in combination of two or more.

  As organic pigments, those generally used can be used, and specifically, azo pigments such as poorly soluble azo lakes, soluble azo lakes, insoluble azo chelates, condensable azo chelates and other azo chelates, phthalocyanine blue, phthalocyanine green, etc. Phthalocyanine pigments, Anthraquinone, Perinone, Perylene, Thylene pigments such as thioindigo, Anti pigments, Nitro pigments, Isoindolinone pigments, Architectural dye pigments, Nitroso pigments, Acid dye lakes, Basic dye lakes Quinacridone pigments, dioxazine pigments, isoindolinone pigments and the like.

  Examples of inorganic pigments include titanium oxide, iron oxide (such as Bengala), chromic acid (such as chrome lead), molybdate, cadmium-based selenide, mercury-based selenide, ferrocyanide, and carbon black. . These pigments may be used alone or in combination of two or more.

  Antibacterial agents include metal powders such as silver, zinc and copper, these metal powders, organic antibacterial agents such as alcohol antibacterial agents and phenolic antibacterial agents, natural antibacterial agents such as natural extracts and natural ores, Quaternary ammonium, inorganic particle antibacterial agents in which these are supported on a supporting body such as zeolite, silica, and alumina can be used. These antibacterial agents may be used alone or in combination of two or more.

  As the deodorizing agent, carbon powder such as charcoal, bamboo charcoal, Bincho charcoal, white charcoal, black charcoal, activated carbon, silica, alumina, zeolite, or the like can be used. These carbon powders act not only as a deodorizing agent but also as a humidity control agent, a hygroscopic agent, and a far infrared radiation agent.

  As the deodorant, for example, a deodorant component that is extracted from various plants such as camellia plant, periaceae plant, camphoraceae plant, camphoraceae plant, asteraceae plant, mallow family plant, etc., and separated by other means is suitable. Used. In particular, it is preferable to dry-distill tea, mountain tea flowers, persimmons, sakaki, mokkok, etc. under reduced pressure, and then distill under reduced pressure. Moreover, what manufactured the component (Polyphenol, a flavonoid, a flavanol, catechin, etc.) equivalent to the deodorizing component from the above natural products by the synthesis method can also be used. Furthermore, what carried | supported said deodorizer on support bodies, such as a silica, an alumina, a zeolite, a pearlite, ceramics, can also be used.

  There are no particular restrictions on the fragrance, but natural fragrances include animal fragrances such as musk, cybet (rebyo fragrance), castor (kairi fragrance) and ambergris; lavender oil, peppermint oil, lemon And vegetable fragrances such as oil, orange oil, rose oil, camphor oil, sandalwood oil, and cypress oil. In addition, artificial fragrances include acetoeugenol, acetoisoeugenol, oliveanol, ferrandrin, aliphatic aldehyde, thymol, carvacrol, bornyl methoxycyclohexanol, eugenol, cinnamic aldehyde, benzaldehyde, cariophylene, coumarin, macrocyclic musk. Synthetic fragrances such as ethyl crocodile, evelic acid, cinnamic acid, crocodile, guayol, furfural, acetophenone, γ-undecalactone, γ-decalactone, etc .; Or / and a blended fragrance prepared by mixing an artificial fragrance. Specific products of artificial fragrances are: Kao Corporation: ALDEHYDE C-10, ALD EHYDE C-11, UNDECYL, ALDEHYDE C-111 LEN, A LDEHYDE C-12 LAURYL, ALDEHYDE C-12 MNA, A LDEHYDE C -6, ALDEHYDE C-8, ALDEHYDE C-9, AMBERCORE, AMYL CINNAMICALDEHYDE, FRUITATE, GAMMA DECALACTION, GAMMA NONALACTONE, GAMMA UNDECALACTONE, HEXYL CINAMICONON PEARLIDEB. B. , PEARLIDE DEP, PEARLIDE IPM, PEARLIDE PURE, POIRENATE, POLLENAL 2, SAGETONEV, SANDALMYSORE CORE and the like.

  Examples of the foaming agent for producing polyurethane foam include water as a main component, carbon dioxide gas, methylene chloride, HFC-245fa, HFC-365mfc, and the like, and mixtures of two or more thereof.

  As the foam stabilizer, conventionally known organosilicone surfactants are used. Examples of such organosilicone surfactants include L-520, L-532, L-540, L-544, L-3550, L-5740S, L-5740M, and L-6202 manufactured by Nihon Unicar. Etc .; SH-190, SH-192, SH-193, SH-194, SRX-290, SRX-294A, SRX-298, etc. manufactured by Toray Dow Corning Silicone; F-114, F manufactured by Shin-Etsu Silicone -121, F-122, F-230, F-258, F-260B, F-317, F-341, F-601, F-606 Goldschmidt's TEGOSTAB B8002, B4900, B8040, B8233, B8229, B8110 , B8300, B8317, B8324, and the like. These foam stabilizers may be used alone or in combination of two or more.

  In the polyurethane foam composition of the present invention containing the polyol component, polyisocyanate compound, plasticizer, catalyst, foaming agent, and the like as described above, the proportion of each component is determined by the foaming of the urethane foam composition. The ratio is not particularly limited as long as it has a high air permeability and a low resilience polyurethane foam intended by the present invention.

  For example, the catalyst is 0.01 to 5 parts by weight, preferably 0.2 to 3 parts by weight, and water is 0.5 to 5 parts by weight, preferably 0.8 to 100 parts by weight of the polyol component (B). When 3.5 parts by mass and a foam stabilizer are blended, 0.1 to 4 parts by mass, preferably 0.4 to 2.0 parts by mass. When a pigment is blended, 0.001 to The amount is about 2.0 parts by mass, preferably about 0.01 to 1.5 parts by mass.

  In the present invention, the ratio of the polyisocyanate compound is 50 to 100, preferably 60 to 100, as the isocyanate index. The isocyanate index here is a value obtained by multiplying 100 by the value obtained by dividing the number of moles of isocyanate groups by the total number of moles of isocyanate-reactive active hydrogen groups including water. If the isocyanate index is too low, the mechanical strength of the foam may decrease, and the compressive residual strain may increase. If the isocyanate index is too high, the foam tends to be hard, and there are problems such as deterioration of touch and impact absorption performance.

  The method for producing the polyurethane foam of the present invention can be performed based on a conventional method for producing an open-cell polyurethane foam, for example, by applying a prepolymer method, a one-shot method, a partial prepolymer method, or the like. Can do.

The polyurethane foam having high breathability, low rebound resilience, and low compression residual strain in the present invention has an air permeability of 50 cm ³ / cm ² / s or more, a rebound resilience of 20% or less, and a compression residual strain of 5% or less. Point to.

  In terms of compression residual strain (specifically, dry heat compression residual strain measured according to JIS K6400 (1997)), a polyurethane foam more suitable in terms of tactile sensation and impact absorption performance can be obtained. It is preferably 2.5% or less, and more preferably 1.5% or less. Especially, it is especially preferable that it is 1.0% or less from a viewpoint that it is very excellent in terms of tactile sensation and impact absorption performance.

The flexible polyurethane foam of the present invention has a rebound resilience of 10% or less, an excellent low rebound resilience of around 1% in a particularly excellent formulation, and a breathability of at least 80 cm ³ / cm ² / s,
It has a high air permeability of 200 cm ³ / cm ² / s or more depending on the formulation. In addition, particularly good materials with low compression residual strain exhibit high durability of 1% or less for both dry heat and wet heat compression residual strain. Therefore, for vibration absorbing materials, various laminates, pillows, mattresses, cushions, and cushions. It can be suitably used for clothes pads and the like.

  EXAMPLES The present invention will be specifically described below with reference to examples, reference examples, and comparative examples, but the present invention is not construed as being limited to these examples.

Examples 1-3, Reference Example 1, Comparative Example 1
Polyurethane foams were produced according to the formulations described in Table 1 below. That is, a flexible polyurethane foam was produced by stirring and mixing a polyol component, water, a catalyst, a plasticizer and a foaming agent, adding a polyisocyanate compound thereto, mixing and foaming. In Reference Example 1 using a piperazine-based catalyst as the amine catalyst, the odor was strong, and it was preferable to avoid it for bedding and the like.

Examples 4-6, Comparative Examples 2 and 3
Polyurethane foams were produced in the same manner as in the above examples, with the results of changing the mixing ratio of the polyester polyol and the polyether polyol, according to each formulation described in Table 2.
In Comparative Example 3 in which the polyether polyol was 40 parts by mass, a foam having a normal appearance was not obtained. As is apparent from this table, it can be seen that the specific mixing ratio must be.

Examples 7-9, Comparative Examples 4 and 5
The results of changing the isocyanate index are shown in Table 3. As can be seen from this table, a specific range of isocyanate index is required.

About the polyurethane foam obtained by each example, reference example, and comparative example, density (kg / m ³ ), hardness (25% CLD: N / 100 cm ² ), tensile strength (kPa), compression residual strain (%), Ball rebound (%), shape restoration time, air permeability (cm ³ / cm ² / s), and the resulting foam cell roughness and foam stickiness were also evaluated.
The results are also shown in the table.

The raw materials used are shown below.
As the polyisocyanate, “Coronate T-80 (a mixture of 2,4-tolylene diisocyanate and 2,6-tolylene diisocyanate in a mass ratio of 80:20)” manufactured by Nippon Polyurethane Industry Co., Ltd. was used. The following polyols were used as the polyol.
Polyol 1: Adipic acid-based polyester polyol
Nippon Polyurethane Industry Co., Ltd .; Nippon Run 131
Average functional group number 3, hydroxyl value: 150 (hydroxyl equivalent: 374)
Polyol 2: Poly (oxypropyleneoxyethylene) triol
Sanyo Chemical Industries, Ltd .; Sannix FA703
Glycerin, hydroxyl value: 33 (hydroxyl equivalent: 1700)
Polyol 3: Adipic acid-based polyester polyol
Nipponporan 2200 made by Nippon Polyurethane Industry
Average functional group number 3, hydroxyl value: 60 (hydroxyl equivalent: 933)
Polyol 4: Poly (oxyethyleneoxypropylene) monool
50HB55 manufactured by Sanyo Chemical Industries
Hydroxyl value: 234 (hydroxyl equivalent: 240)
Catalyst 1: Amine catalyst that is not imidazole HX63 manufactured by Tosoh Corporation
Catalyst 2: 1,2-dimethylimidazole catalyst TOYOCAT DMI manufactured by Tosoh Corporation
Catalyst 3: Piperazine catalyst EPS manufactured by Goldschmidt
Catalyst 4: Imidazole catalyst U-2030 manufactured by San Apro
Foam stabilizer: SH190 (Toray Dow Corning Silicone)

Measurement method for measurement of various physical properties (a) Density, compression residual strain, impact resilience: Measured according to JIS K6400 (1997).
(B) Hardness: A sample piece of 100 mm × 100 mm × 50 mm is compressed and pre-compressed with a compressor larger than the sample pressure-receiving area, restored to a sufficient height, and compressed again. The sample thickness is 75% of the sample original thickness. The stress value when compressed to a certain point was measured.
(C) Tensile strength: measured with a No. 1 dumbbell in accordance with JIS K6400 (1997). (D) Restoration time was measured by the following procedure.
1. Measurement environment: Temperature 23 ± 2 ° C, relative humidity 50 ± 5%
2. Sample size: The center of a foam of length 100 mm × width 100 mm × thickness 40 mm is pushed 20 mm with a pressurizer having a diameter of 30 mm.
3. Hold in this state for 10 seconds.
4). The time from the moment when the pressurizer is removed to the restoration to the original shape (no dents) is measured.
(E) Air permeability: Measured according to method A of JIS K6400 (1997).
(F) Cell roughness was evaluated based on whether or not there was variation in the cell size of the polyurethane foam.
For those with variations, the cells were assumed to be rough.
(G) For stickiness, the following evaluation criteria were followed.
○: There is almost no stickiness, and there is no problem in processing and storage.
X: When touched, the touch feels like the adhesive is on the finger.

The polyurethane foam having high air permeability and low rebound resilience obtained by the production method according to the present invention has low rebound resilience, extremely good air permeability, and low hardness temperature dependence, which cannot be achieved by a conventionally known polyurethane foam. Furthermore, it has a very good compression residual strain. Therefore, it is preferably used in fields and applications where such polyurethane foam is required, for example, for various types of laminate processing as shock absorbing materials and vibration absorbing materials, or for pillows, mattresses, cushions, cushions, clothing pads, etc. In particular, it can be particularly suitably used as a bedding for nursing care.

Claims (6)

Density of 40-80 kg / m ³ , hardness 8 for reacting and foaming polyisocyanate (A), polyol (B), foaming agent (C), catalyst (D) and foam stabilizer (E) with an isocyanate index of 50-100 A method for producing a flexible polyurethane foam of ˜150 N / 100 cm ² , comprising:
Polyoxyl whose polyol (B) has an average functional group number of 2.5 to 4.5 and a hydroxyl group equivalent of 300 to 500 and a polyester polyol (b1) having an average functional group number of 2.5 to 4.5 and a hydroxyl group equivalent of 300 to 5000 Highly breathable, characterized by using a polyol component which is a mixed polyol with an alkylene polyol (b2) and whose mixing ratio is (b1) :( b2) = 70-90: 30-10 (mass ratio)・ Production method of polyurethane foam with low rebound resilience.   The high air permeability according to claim 1, wherein the polyoxyalkylene polyol (b2) is a polyol obtained by adding propylene oxide and ethylene oxide to a polyhydroxy compound having two or more hydroxyl groups per molecule.・ Production method of polyurethane foam with low rebound resilience.   The method for producing a polyurethane foam having high air permeability and low resilience according to claim 1 or 2, wherein the catalyst (D) contains an imidazole compound.   4. The method for producing a highly foamable and low resilience polyurethane foam according to claim 1, wherein the polyol (B) further contains a polyoxyalkylene monool.   The polyol (B) further contains a polyoxyalkylene polyol having an average number of functional groups of 2.5 to 4.5 and a hydroxyl group equivalent of 100 to 500. 5. High air permeability and low resilience according to claims 1-4 Method for producing elastic polyurethane foam. 6. The production of a highly breathable and low resilience polyurethane foam according to claim 1, wherein the dry heat compression residual strain value measured according to JIS K6400 (1997) is 2.5% or less. Method.