JP7263495B2 - Method for manufacturing polyurethane foam - Google Patents

Description

TECHNICAL FIELD The present invention relates to a method for producing a polyurethane foam, and more particularly to a method capable of advantageously producing a polyurethane foam having excellent flame retardancy and a uniform density distribution.

Conventionally, polyurethane foam has been used mainly as a heat insulating material for building interior and exterior wall materials and panels, metal siding, electric refrigerators, etc. It is used for heat insulation, heat insulation and dew condensation prevention for building walls, ceilings, roofs, etc. of buildings, condominiums, cold storage warehouses, etc., heat insulation for infusion pipes, etc., and backfilling materials for filling voids generated in civil engineering work. It is also practically used as a reinforcing material etc. In addition, such polyurethane foam is generally a composition consisting of a polyol blended solution (premixed solution) in which a polyol is blended with a foaming agent and, if necessary, various auxiliary agents such as a catalyst, a foam stabilizer, and a flame retardant. A and a composition B containing polyisocyanate as a main component are mixed continuously or intermittently by a mixing device to obtain a foamable composition for polyurethane foam, which is subjected to a slab foaming method, an injection foaming method, It is produced by foaming and curing by methods such as spray foaming, lamination continuous foaming, lightweight embankment construction, injection backfilling, and the like.

By the way, the polyurethane foam formed as described above is required to have flame retardancy in view of its use. , it is known to impart flame retardancy to the obtained polyurethane foam by adding a flame retardant to a polyol component or the like. In particular, in recent years, polyurethane foams have been required to have better flame retardancy than ever before, and it has been proposed to use red phosphorus as a flame retardant to achieve even better flame retardancy in polyurethane foams. It is For example, in Patent Document 2 (Japanese Patent Application Laid-Open No. 2015-193839), a polyisocyanate compound, a polyol compound, an additive, etc. are included, and 100 parts by weight of a urethane resin composed of such a polyisocyanate compound and a polyol compound, the additive A flame-retardant urethane resin composition characterized by containing 3.5 to 20 parts by weight of red phosphorus as is proposed.

However, a composition containing red phosphorus as disclosed in Patent Document 2 is sprayed from a spray gun head of an on-site foaming machine onto a target adherend (structure) according to, for example, a spray foaming method, and foaming is performed.・When polyurethane foam is produced by curing, the following problems may occur. That is, 1) granular or powdered red phosphorus may inhibit the progress of the urethane reaction; Due to the low dispersibility of the phosphorus powder, etc., the red phosphorus powder and the like exist in an uneven state in the finally obtained polyurethane foam, resulting in an uneven density. Intrinsic is the problem of producing polyurethane foams with a distribution.

JP-A-2002-47325 JP 2015-193839 A

Here, the present invention has been made against the background of such circumstances, and the problem to be solved is that it is difficult to foam and cure according to any conventionally known foaming method. To provide a method for producing a polyurethane foam which can advantageously produce a polyurethane foam which is excellent in combustibility and has a uniform density distribution.

In order to solve the above-described problems, the present invention can be suitably implemented in various aspects as enumerated below. It should be understood that the aspects and technical features of the present invention are not limited to those described below, and can be recognized based on the inventive idea that can be grasped from the description of the specification. should.

(1) When producing a polyurethane foam by mixing and reacting a composition A containing a polyol as a main component and a composition B containing a polyisocyanate as a main component, followed by foaming and curing,
Coating red phosphorus is contained in the composition A and/or the composition B at a ratio of 10 to 70 parts by mass with respect to 100 parts by mass of the polyol in the composition A,
As a blowing agent, a blowing agent I consisting of critical, subcritical or liquid carbon dioxide and a blowing agent II consisting of at least one of water, hydrofluoroolefin and hydrochlorofluoroolefin are used in combination. Agent II is contained in at least one of said composition A, said composition B and said blowing agent I,
In the production site of the polyurethane foam, the foaming agent I is used in the composition A and / or the composition B at a ratio of 0.1 to 4 parts by mass with respect to 100 parts by mass of the polyol in the composition A. and the reaction is allowed to proceed immediately after such addition.
A method for producing a polyurethane foam, characterized by:
(2) The method for producing a polyurethane foam according to the aspect (1), wherein the red phosphorus component in the coating red phosphorus is 80% or more.
(3) The method for producing a polyurethane foam according to the aspect (1) or the aspect (2), wherein the coated red phosphorus has an average particle size of 1 to 50 μm.
(4) A flame retardant comprising at least one of phosphate esters, phosphate-containing flame retardants, stannate-containing flame retardants, bromine-containing flame retardants, boron-containing flame retardants and metal hydroxides, The method for producing the polyurethane foam according to any one of the aspects (1) to (3), which is contained in the composition A and/or the composition B.
(5) Any one of the above aspects (1) to (4), wherein the polyurethane foam is produced by a blow foaming method after the blowing agent I is added to the composition A and/or the composition B. 1. A method for producing a polyurethane foam according to claim 1.
(6) Production of the polyurethane foam according to any one of the above aspects (1) to (5), wherein the difference between the total density and the core density is 0.1 to 12 kg/m ³ . Method.
(7) Polyurethane foam with a total calorific value of 8 MJ/m ² or less after 10 minutes when heated at a radiant heat intensity of 50 kW/m ² in accordance with the test method specified in ISO-5660. A method for producing a polyurethane foam according to any one of the obtained aspects (1) to (6).
(8) Polyurethane foam with a total calorific value of 8 MJ/m ² or less after 20 minutes when heated at a radiant heat intensity of 50 kW/m ² in accordance with the test method specified in ISO-5660. A method for producing a polyurethane foam according to any one of the obtained aspects (1) to (7).

As described above, in the method for producing a polyurethane foam according to the present invention, the blowing agent used is a blowing agent I consisting of critical, subcritical or liquid carbon dioxide and a blowing agent II selected from predetermined substances such as water. Also, immediately after the blowing agent I is added to the composition A containing a polyol as a main component and/or the composition B containing a polyisocyanate as a main component, the composition A and the composition B react. It is something to be done. Therefore, in the production method of the present invention, the foaming agent I (critical, subcritical or liquid carbon dioxide) is mainly foamed in the early to middle stages of the reaction between the polyol and the polyisocyanate, and the foaming agent is foamed in the middle to late stages of the reaction. Due to the foaming of I and blowing agent II, red phosphorus exhibits good dispersibility in the mixture of composition A and composition B (in other words, it is uniformly present in the mixture without being unevenly distributed). Therefore, the resulting polyurethane foam exhibits excellent flame retardancy due to the red phosphorus and has a uniform density distribution. In addition, especially in winter when the environmental temperature is low, if the present invention is applied to perform two-layer spraying (two-stage spraying), the first layer foam (formed by the first spraying) and the second layer The density difference between the foam (the foam formed by the second blowing) is small, and therefore the occurrence of shrinkage differences between the layers is effectively suppressed. The foam as a whole is restrained from warping.

In the method for producing a polyurethane foam according to the present invention, a composition A containing a polyol as a main component and a composition B containing a polyisocyanate as a main component are mixed, foamed and cured to obtain the desired polyurethane foam. The polyol, which is the main component constituting the composition A used therein, contains various known polyol compounds that react with polyisocyanate to produce polyurethane, alone or as appropriate. is used in combination with Polyether polyols, polyester polyols, and the like are preferably used there. Needless to say, in addition to these polyols, various known polyol compounds such as polyolefin polyols, acrylic polyols, polymer polyols, etc. can be used alone or in appropriate combination. .

Specifically, among such polyols, polyether polyols contain at least one initiator such as polyhydric alcohols, sugars, aliphatic amines, aromatic amines, phenols, Mannich condensation products, and alkylene oxides. is obtained by reacting Examples of alkylene oxides include propylene oxide, 1,2-butylene oxide, 2,3-butylene oxide and ethylene oxide. Polyhydric alcohols as initiators include ethylene glycol, propylene glycol, diethylene glycol, dipropylene glycol, glycerin, trimethylolpropane, pentaerythritol and the like, and sugars include sucrose, dextrose, sorbitol and the like. Furthermore, aliphatic amines include alkanolamines such as diethanolamine and triethanolamine, and polyamines such as ethylenediamine, and aromatic amines include various methyl-substituted phenylenediamines collectively called tolylenediamine. In addition, derivatives obtained by introducing substituents such as methyl, ethyl, acetyl, and benzoyl into the amino group, 4,4'-diaminodiphenylmethane, p-phenylenediamine, o-phenylenediamine, naphthalenediamine, etc. Furthermore, examples of phenols include bisphenol A and novolac type phenol resins. Examples of Mannich condensation products include Mannich condensation products obtained by subjecting phenols, aldehydes and alkanolamines to a Mannich condensation reaction.

Examples of polyester polyols include polyols of polyhydric alcohol-polycarboxylic acid condensation system and polyols of cyclic ester ring-opening polymer system. Here, as the polyhydric alcohol, those mentioned above can be used, and dihydric alcohol is particularly preferably used. Examples of polyvalent carboxylic acids include succinic acid, glutaric acid, adipic acid, suberic acid, azelaic acid, sebacic acid, maleic acid, fumaric acid, phthalic acid, terephthalic acid, isophthalic acid, and anhydrides thereof. Furthermore, ε-caprolactone or the like is used as the cyclic ester.

Among them, as the polyester polyol, it is preferable to use an aromatic polyester polyol from the viewpoint of flame retardancy and compatibility. Specifically, it is preferable to use a phthalic acid-based polyester polyol. It is also effective to combine two or more types of polyols. The phthalic acid-based polyester polyol is a polyol consisting of a condensation product of phthalic acid, terephthalic acid, isophthalic acid, anhydrides thereof, and a dihydric alcohol such as ethylene glycol, propylene glycol, diethylene glycol, and dipropylene glycol. It means When such a phthalic acid-based polyester polyol is used, even when on-site foaming is performed at low temperatures (about -10°C to 5°C), the resulting foam is less likely to peel off from the building frame, etc. There is an advantage that it is possible to obtain a rigid polyurethane foam having such a degree of flexibility that processing of the foam ends after foaming is relatively easy. In particular, when a hydrofluoroolefin foaming agent or a hydrochlorofluoroolefin foaming agent is incorporated, the composition has excellent storage stability.

On the other hand, the polyisocyanate, which is the main component of composition B, is blended with composition A and reacts with the polyol in composition A to form polyurethane (resin). is an organic isocyanate compound having two or more isocyanate groups (NCO groups) in, for example, diphenylmethane diisocyanate, polymethylene polyphenylene polyisocyanate, tolylene diisocyanate, polytolylene triisocyanate, xylylene diisocyanate, naphthalene diisocyanate, phenylene diisocyanate, Aromatic polyisocyanates such as dimethyldiphenylmethane diisocyanate and triphenylmethane triisocyanate, aliphatic polyisocyanates such as methylene diisocyanate, ethylene diisocyanate, propylene diisocyanate, tetramethylene diisocyanate and hexamethylene diisocyanate, isophorone diisocyanate, cyclohexylene diisocyanate, methylcyclohexylene In addition to alicyclic polyisocyanates such as diisocyanate, dicyclohexylmethane diisocyanate and dimethyldicyclohexylmethane diisocyanate, urethane prepolymers having an isocyanate group at the molecular end, isocyanurate modified polyisocyanate, carbodiimide modified polyisocyanate and the like can be mentioned. These polyisocyanate compounds may be used alone or in combination of two or more. In general, polymethylene polyphenylene polyisocyanate (polymeric MDI) is preferably used from the viewpoint of reactivity, economy, handleability, and the like.

The ratio of polyisocyanate in composition B to polyol in composition A is appropriately determined according to the type of foam to be formed (e.g., polyurethane, polyisocyanurate). However, in general, the NCO/OH index (equivalence ratio), which indicates the ratio between the isocyanate group (NCO) of the polyisocyanate and the hydroxyl group (OH) of the polyol, is 0.9 to 4.5, preferably 1.5 to 4.0. It will be determined appropriately so as to be within the range of the degree.

In the present invention, the above composition A and composition B are mixed and allowed to react, foamed with a foaming agent, and cured to form a rigid polyurethane foam. However, in the reaction between composition A and composition B, a catalyst is generally used. In the present invention, the composition A preferably contains a trimerization catalyst, in other words, a catalyst (isocyanurate catalyst) that reacts the isocyanate groups of the polyisocyanate to trimerize and promote the formation of isocyanurate rings. It will be included. As the trimerization catalyst, various known catalysts can be appropriately selected and used, but preferred are quaternary ammonium salts, potassium octylate, potassium 2-ethylhexanoate, and sodium acetate. Carboxylic acid alkali metal salts such as; tris (dimethylaminomethyl) phenol, 2,4-bis (dimethylaminomethyl) phenol, tris (dimethylaminopropyl) hexahydrotriazine and other nitrogen-containing aromatic compounds; trimethylammonium salt, triethyl Examples include tertiary ammonium salts such as ammonium salts and triphenylammonium salts. Among these, it is preferable to use a quaternary ammonium salt from the viewpoint of improving flame retardancy, and among them, it is preferable to use a quaternary ammonium salt and a carboxylic acid alkali metal salt together. From the point of improvement, it is particularly preferable.

Quaternary ammonium salts advantageously used herein include tetramethylammonium, methyltriethylammonium, ethyltrimethylammonium, propyltrimethylammonium, butyltrimethylammonium, pentyltrimethylammonium, hexyltrimethylammonium, heptyltrimethylammonium, octyltrimethylammonium, Aliphatic ammonium such as nonyltrimethylammonium, decyltrimethylammonium, undecyltrimethylammonium, dodecyltrimethylammonium, tridecyltrimethylammonium, tetradecyltrimethylammonium, heptadecyltrimethylammonium, hexadecyltrimethylammonium, heptadecyltrimethylammonium and octadecyltrimethylammonium compounds, (2-hydroxypropyl)trimethylammonium, hydroxyethyltrimethylammonium, trimethylaminoethoxyethanol, hydroxyammonium compounds such as hydroxyethyl-2-hydroxypropyldimethylammonium, 1-methyl-1-azania-4-azabicyclo[2, Alicyclic ammonium compounds such as 2,2] octanium, 1,1-dimethyl-4-methylpiperidinium, 1-methylmorpholinium and 1-methylpiperidinium, and the like. Among these, tetramethylammonium, methyltriethylammonium, ethyltrimethylammonium, butyltrimethylammonium, hexyltrimethylammonium, octyltrimethylammonium, decyltrimethylammonium, dodecyltrimethylammonium, tetradecyltrimethylammonium, hexadecyltrimethylammonium, octadecyltrimethylammonium, (2-hydroxypropyl)trimethylammonium, hydroxyethyltrimethylammonium, hydroxyethyl-2-hydroxypropyldimethylammonium, 1-methyl-1-azania-4-azabicyclo [ 2,2,2]octanium and 1,1-dimethyl-4-methylpiperidinium will preferably be used.

Examples of the organic acid group or inorganic acid group constituting such a quaternary ammonium salt include formic acid group, acetic acid group, octylic acid group, oxalic acid group, malonic acid group, succinic acid group, glutaric acid group, organic acid groups such as adipic acid group, benzoic acid group, toluic acid group, ethylbenzoic acid group, methyl carbonate group, phenol group, alkylbenzenesulfonic acid group, toluenesulfonic acid group, benzenesulfonic acid group, phosphate ester group, Inorganic acid groups such as halogen groups, hydroxyl groups, hydrogen carbonate groups, and carbonate groups are included. Among these, a formic acid group, an acetic acid group, an octylic acid group, a methyl carbonate group, a halogen group, a hydroxyl group, a hydrogen carbonate group, and a carbonate group are preferable because of their excellent catalytic activity and industrial availability.

Furthermore, various types of catalysts comprising such quaternary ammonium salts are commercially available. 410, Kaorizer No. 420 (manufactured by Kao Corporation) and the like.

In this way, the amount of the trimerization catalyst used as one of the catalysts is 0 with respect to 100 parts by mass of the total polyol in the composition A in order to effectively exhibit its function as a catalyst. .1 to 10 parts by weight, preferably 0.5 to 8 parts by weight, more preferably 1 to 6 parts by weight. If the trimerization catalyst is used in an amount of less than 0.1 part by mass, the polyisocyanate cannot be sufficiently trimerized, making it difficult to sufficiently achieve the effect of improving flame retardancy. On the other hand, if the amount is more than 10 parts by mass, the reaction proceeds too much and the solidification is accelerated, making it difficult to spray.

In the present invention, it is also possible to use a urethanization catalyst, which is a resinification catalyst, together with such a trimerization catalyst. Examples of the urethanization catalyst include known catalysts such as dibutyltin dilaurate, bismuth octylate (bismuth 2-ethylhexylate), bismuth neodecanoate, bismuth neododecanoate, fatty acid bismuth salts such as bismuth naphthenate, and lead naphthenate. I can.

In addition, the amount of the resinification catalyst used is 0.1 to 10 parts by mass, preferably 0 parts by mass, based on 100 parts by mass of the total polyol in the composition A, in order to effectively exhibit its function as a catalyst. .5 to 8 parts by weight, more preferably 1 to 6 parts by weight. If the amount of the resinification catalyst used is less than 0.1 parts by mass, the resulting foam will be sticky, dust and the like will adhere, deteriorating the appearance of the foam. On the other hand, if the amount is more than 10 parts by mass, the heat generated during the resinification reaction will increase, and the foam will turn yellow, resulting in abnormal appearance. , and the catalyst containing the quaternary ammonium salt contained in the droplets generated during foaming may deteriorate the work environment at the work site where the spraying is performed.

On the other hand, in the present invention, for either the above-described composition A containing polyol as a main component or composition B containing polyisocyanate as a main component, or for both composition A and composition B, Red phosphorus is added. In the present invention, any conventionally known red phosphorus can be used, and usually, it is appropriately selected from commercially available products and used. The amount of red phosphorus used is 1 to 70 parts by mass, preferably 10 to 60 parts by mass, and more preferably 20 to 55 parts by mass with respect to 100 parts by mass of the polyol in composition A. determined in If the amount of red phosphorus added is too small, the resulting polyurethane foam may not exhibit sufficient flame retardancy. In addition to causing problems such as poor stirring due to an increase in viscosity, there is a risk of causing problems such as a decrease in workability and problems such as the polyurethane foam becoming more likely to burn.

In addition, in the present invention, coated red phosphorus is advantageously used among red phosphorus from the viewpoint of safety and ease of handling. Coated red phosphorus is red phosphorus that has been surface-treated with an inorganic substance and/or an organic substance. Excel (trade name, manufactured by Rin Kagaku Kogyo Co., Ltd.), Hishiguard (trade name, manufactured by Nippon Kagaku Kogyo Co., Ltd.), and the like can be exemplified. As the coated red phosphorus, a red phosphorus content ratio of 80% or more, preferably 80 to 99%, is more effective because it contributes more effectively to improving the flame retardancy of the polyurethane foam. A coated red phosphorus, preferably 90-98%, is advantageously used.

The red phosphorus used in the present invention is advantageously used in the form of granules or powder, like red phosphorus conventionally used in the production of polyurethane foams. In addition, red phosphorus particles or powder having an average particle size of 1 to 50 μm, preferably 5 to 45 μm, more preferably 10 to 40 μm are used so that the dispersion state in the finally obtained polyurethane foam is good. Advantageously the body is used.

On the other hand, in the method for producing a polyurethane foam according to the present invention, it is possible to use other conventionally known flame retardants together with the red phosphorus described above. By using other flame retardants together with red phosphorus, it is possible to further improve the flame retardancy of the final polyurethane foam. In addition, when red phosphorus is used in combination with other flame retardants, the amount of red phosphorus used can be kept to a small amount. is uniform (in other words, the difference between the overall density and the core density is small) can be advantageously obtained. In the present invention, examples of flame retardants that can be used with red phosphorus include phosphate esters, phosphate-containing flame retardants, stannate-containing flame retardants, bromine-containing flame retardants, boron-containing flame retardants, and metal hydroxides. can do One or more selected from various flame retardants described below are added to composition A and/or composition B together with red phosphorus or separately from red phosphorus.

-Phosphate ester-
Examples of the phosphate include monophosphate and condensed phosphate.

Monophosphates are not particularly limited, and examples include trimethyl phosphate, triethyl phosphate, tributyl phosphate, tri(2-ethylhexyl) phosphate, tributoxyethyl phosphate, triphenyl phosphate, tricresyl phosphate, trixylenyl Phosphate, tris(isopropylphenyl) phosphate, tris(phenylphenyl) phosphate, trinaphthyl phosphate, cresyl diphenyl phosphate, xylenyl diphenyl phosphate, diphenyl(2-ethylhexyl) phosphate, di(isopropylphenyl) phenyl phosphate, monoisodecyl Phosphate, 2-acryloyloxyethyl acid phosphate, 2-methacryloyloxyethyl acid phosphate, diphenyl-2-acryloyloxyethyl phosphate, diphenyl-2-methacryloyloxyethyl phosphate, melamine phosphate, dimelamine phosphate, melamine pyrophosphate, triphenylphosphine oxide, tricresylphosphine oxide, diphenyl methanephosphonate, diethyl phenylphosphonate, resircinol bis(diphenyl phosphate), bisphenol A bis(diphenyl phosphate), phosphaphenanthrene, tris(β-chloropropyl) phosphate, etc. , can be mentioned.

The condensed phosphate is not particularly limited, and examples thereof include trialkyl polyphosphate, resorcinol polyphenyl phosphate, resorcinol poly(di-2,6-xylyl) phosphate (manufactured by Daihachi Chemical Industry Co., Ltd., trade name : PX-200), hydroquinone poly(2,6-xylyl) phosphate, condensates thereof, and the like. Commercially available condensed phosphates other than those mentioned above include, for example, resorcinol polyphenyl phosphate (trade name: CR-733S), bisphenol A polycresyl phosphate (trade name: CR-741), and aromatic condensed phosphates. (trade name: CR747), resorcinol polyphenyl phosphate (manufactured by ADEKA, trade name: Adekastab PFR), bisphenol A polycresyl phosphate (trade name: FP-600, FP-700), and the like.

In the present invention, it is possible to appropriately select and use one or more of the conventionally known phosphate esters including the monophosphate esters and condensed phosphate esters described above. be. In addition, among the monophosphate esters and condensed phosphate esters described above, monophosphate esters can be used in that they are highly effective in reducing the viscosity of the composition before curing and in reducing the amount of heat generated in the initial stage. More preferably, tris(β-chloropropyl) phosphate is used.

-Phosphate containing flame retardant-
A phosphate-containing flame retardant contains a phosphate and has flame retardancy. Phosphoric acid used in the phosphate-containing flame retardant is not particularly limited, and various phosphoric acids such as monophosphoric acid, pyrophosphoric acid and polyphosphoric acid can be exemplified.

In addition, as the phosphate-containing flame retardant, for example, the various phosphoric acids described above and at least one metal selected from metals of Groups IA to IVB of the periodic table, ammonia, aliphatic amines, and aromatic amines, or compounds thereof Phosphates consisting of salts with can be mentioned. Examples of metals belonging to groups IA to IVB of the periodic table include lithium, sodium, calcium, barium, iron (II), iron (III) and aluminum. Examples of aliphatic amines include methylamine, ethylamine, diethylamine, triethylamine, ethylenediamine and piperazine, and examples of aromatic amines include pyridine, triazine, melamine and ammonium. The phosphate-containing flame retardant used in the present invention may be one to which a known water resistance improvement treatment such as silane coupling agent treatment or coating with melamine resin has been added, and melamine, pentaerythritol, etc. of known foaming aids may be added.

Specific examples of phosphates constituting the phosphate-containing flame retardant used in the present invention include monophosphates, pyrophosphates and polyphosphates.

The monophosphate is not particularly limited, and examples thereof include ammonium salts such as ammonium phosphate, ammonium dihydrogen phosphate, and diammonium hydrogen phosphate, monosodium phosphate, disodium phosphate, and trisodium phosphate. , sodium salts such as monosodium phosphite, disodium phosphite, sodium hypophosphite, monopotassium phosphate, dipotassium phosphate, tripotassium phosphate, monopotassium phosphite, dipotassium phosphite, Potassium salts such as potassium hypophosphite, lithium salts such as monolithium phosphate, dilithium phosphate, trilithium phosphate, monolithium phosphite, dilithium phosphite, lithium hypophosphite, diphosphate Barium salts such as barium hydrogen, barium hydrogen phosphate, tribarium phosphate, and barium hypophosphite; magnesium salts such as magnesium monohydrogen phosphate, magnesium hydrogen phosphate, trimagnesium phosphate, and magnesium hypophosphite; Calcium salts such as calcium dihydrogen phosphate, calcium hydrogen phosphate, tricalcium phosphate and calcium hypophosphite, and zinc salts such as zinc phosphate, zinc phosphite and zinc hypophosphite can be mentioned.

The polyphosphate is not particularly limited, and examples thereof include ammonium polyphosphate, piperazine polyphosphate, melamine polyphosphate, ammonium polyphosphate and aluminum polyphosphate.

In the present invention, it is possible to appropriately select and use one or more of the conventionally known phosphate-containing flame retardants, including those mentioned above. Among the phosphates described above, monophosphates are advantageously used, and ammonium dihydrogen phosphate is more advantageously used, in that they are excellent in self-extinguishing properties.

-Stanate-containing flame retardant-
A stannate-containing flame retardant is a flame retardant containing a metal stannate. Here, examples of the stannate metal salt contained in the stannate-containing flame retardant include zinc stannate, barium stannate, sodium stannate, potassium stannate, cobalt stannate, and magnesium stannate. Among them, zinc stannate is preferably used.

- Bromine-containing flame retardant -
The bromine-containing flame retardant used in the present invention is not particularly limited as long as it is a compound containing bromine in its molecular structure, and examples thereof include various aromatic brominated compounds. Specifically, hexabromobenzene, pentabromotoluene, hexabromobiphenyl, decabromobiphenyl, hexabromocyclodecane, decabromodiphenyl ether, octabromodiphenyl ether, hexabromodiphenyl ether, bis(pentabromphenoxy)ethane, ethylene-bis( tetrabromophthalimide), monomeric organic bromine compounds such as tetrabromobisphenol A; polycarbonate oligomers produced using brominated bisphenol A as a starting material, brominated polycarbonates such as copolymers of the above polycarbonate oligomers and bisphenol A; brominated bisphenol Brominated epoxy compounds such as diepoxy compounds prepared by reaction of A with epichlorohydrin, monoepoxy compounds obtained by reaction of brominated phenols with epichlorohydrin; poly(brominated benzyl acrylate); brominated polyphenylene ether; Condensates of bisphenol A, cyanuric chloride and brominated phenol; brominated polystyrene such as brominated (polystyrene), poly(brominated styrene), crosslinked brominated polystyrene; crosslinked or non-crosslinked brominated poly(-methylstyrene) Halogenated bromine compound polymers and the like can be mentioned.

In the present invention, it is possible to appropriately select and use one or more of the conventionally known bromine-containing flame retardants, including those mentioned above. Among the above-described bromine-containing flame retardants, brominated polystyrene, hexabromobenzene, etc. are advantageously used, and hexabromobenzene is more advantageously used, from the viewpoint of controlling the heat generation amount at the initial stage of combustion.

- Boron-containing flame retardant -
Examples of boron-containing flame retardants used in the present invention include borax, boron oxide, boric acid, borates, and the like. Specific examples of boron oxide include diboron trioxide, boron trioxide, diboron dioxide, tetraboron trioxide, and tetraboron pentoxide. Examples of borates include borates of alkali metals, alkaline earth metals, elements of Groups 4, 12 and 13 of the periodic table, and ammonium. More specifically, alkali metal borate salts such as lithium borate, sodium borate, potassium borate and cesium borate; alkaline earth metal borate salts such as magnesium borate, calcium borate and barium borate; Zirconium borate, zinc borate, aluminum borate, ammonium borate and the like can be exemplified.

In the present invention, it is possible to appropriately select and use one or more of the conventionally known boron-containing flame retardants including those mentioned above. Among the above boron-containing flame retardants, borates are preferably used, and zinc borate is more preferably used.

－Metal Hydroxide－
Metal hydroxides used as flame retardants in the present invention include, for example, magnesium hydroxide, calcium hydroxide, aluminum hydroxide, iron hydroxide, nickel hydroxide, zirconium hydroxide, titanium hydroxide, and zinc hydroxide. , copper hydroxide, vanadium hydroxide and tin hydroxide. One or two or more of these known substances are appropriately selected and used.

In the present invention, a flame retardant comprising at least one of the above-described phosphate ester, phosphate-containing flame retardant, stannate-containing flame retardant, bromine-containing flame retardant, boron-containing flame retardant and metal hydroxide. (hereinafter referred to as other flame retardants in this paragraph), when used with red phosphorus, the amount used (the total amount of other flame retardants used) is It is preferably in the range of 3 to 90 parts by mass, more preferably in the range of 10 to 80 parts by mass. If the amount of other flame retardants used is too small, there is a risk that the effect of using them in combination with red phosphorus cannot be enjoyed. Problems such as an increase in viscosity and a deterioration in workability are caused.

In the production method of the present invention, the blowing agent comprises a blowing agent I comprising critical, subcritical or liquid carbon dioxide and at least one of water, hydrocarbons, hydrofluorocarbons and halogenated olefins. A foaming agent II is used in combination.

Here, critical, subcritical or liquid carbon dioxide (hereinafter abbreviated as liquefied _CO2 ) means, as is well known, by pressurizing carbon dioxide gas at a predetermined temperature, supercritical state, subcritical state, or liquid state. Specifically, liquid carbon dioxide is liquefied under conditions of temperature and pressure above the triple point, and subcritical carbon dioxide means that the pressure is above the critical pressure and the temperature is below the critical temperature. Carbon dioxide in a liquid state where the pressure is less than the critical pressure and the temperature is equal to or higher than the critical temperature, or carbon dioxide in a state where the temperature and pressure are less than the critical point but close to it Furthermore, carbon dioxide in a supercritical state is carbon dioxide in a fluid state in which both the pressure and temperature exceed the critical points of the critical pressure and the critical temperature.

The liquefied CO ₂ described above exerts an effective foaming action immediately after being added to composition A, etc. It improves the dispersibility of red phosphorus in the foam, contributes to the thinning of the skin layer in the resulting polyurethane foam, and advantageously achieves the low density. In addition, by using liquefied _CO2 , for example, when the present invention is applied to a spray foaming method using a spray gun (spray foaming method), the sprayability of the mixture consisting of composition A and composition B is improved. In addition, the occurrence of clogging in the spray gun due to red phosphorus (flame retardant I) is advantageously suppressed. In the present invention, if the amount of liquefied CO ₂ used is too small, the effect of addition cannot be sufficiently exhibited, and in particular, foaming immediately after spraying by the blowing foaming method (spray foaming method) becomes insufficient. Since the difference in density between the core layer and the skin layer increases, problems such as a decrease in compressive strength and an increase in the rate of dimensional change occur. On the other hand, if the amount of liquefied CO ₂ used is too large, the gas (carbon dioxide) generated at the initial stage of the reaction becomes excessive, which adversely affects the foaming characteristics. In this case, problems such as difficulty in obtaining a good foam are caused. Therefore, in the present invention, the amount of liquefied CO ₂ used should be in the range of 0.1 to 4 parts by mass with respect to 100 parts by mass of the polyol in composition A, preferably It should be within the range of 0.2 to 3 parts by mass.

Then, such liquefied CO ₂ is supplied at a polyurethane foam manufacturing site by a carbon dioxide supply device as disclosed in JP-A-2011-247323, for example, to form a composition A containing a polyol as a main component. It is supplied to the channel or the channel of the composition B containing polyisocyanate as a main component and mixed therein, and contributes to the foaming of the polyurethane caused by the reaction between the polyol and the polyisocyanate. Of course, such supply of liquefied _CO2 is directly to the location where composition A and composition B are brought into contact and mixed, so that both are supplied with liquefied _CO2 . It is also possible to make

In the present invention, a blowing agent II comprising at least one of water, hydrocarbons, hydrofluorocarbons and halogenated olefins is used together with the liquefied _CO2 (foaming agent I) described above. Water reacts with polyisocyanate to produce carbon dioxide, which functions as a blowing agent. In addition, reaction heat is generated during the reaction between water and polyisocyanate, and the heat can effectively promote the urethanization reaction and the isocyanurate formation reaction, increasing the compressive strength of the obtained polyurethane foam. There is also the advantage that it can be further enhanced. However, if the amount of water used becomes too large, the strength will rather be reduced. This is because the urea bonds generated by the reaction between water and polyisocyanate increase in the resin, and the polyisocyanate used in the isocyanurate reaction is consumed by the reaction with water, resulting in less polyisocyanate in the reaction system. It's for. From the above, in the present invention, water as a foaming agent is preferably contained in the composition A containing polyol as a main component, and the content (used amount) is 100 parts by mass of the polyol in the composition A. On the other hand, it is desirably 5 parts by mass or less, preferably 4 parts by mass or less, more preferably 3 parts by mass or less, and in order to sufficiently exhibit the effect of the presence of water, 0.1 parts by mass or more, preferably It is desirable to make it 0.5 parts by mass or more, more preferably 1 part by mass or more. In addition, such water is added and blended separately as a blending component for forming composition A, and is added and blended as water contained in other blending components such as polyols. The water contained by moisture absorption during storage of the composition A is also taken into account, and the total amount thereof is adjusted so that the ratio is within the range specified above.

Due to the presence of water in composition A as described above, when composition A containing polyol as a main component and composition B containing polyisocyanate as a main component are mixed and reacted, the water and Carbon dioxide is generated by the reaction with polyisocyanate, and this carbon dioxide also contributes to polyurethane foaming. , with respect to 1 mol of the total amount of carbon dioxide used as the liquefied CO ₂ type, the organic blowing agent described later has a content of more than 1 mol and 20 mol or less. It is present in a mixture of composition A and composition B.

In the present invention, as the blowing agent II, instead of or together with the water described above, hydrocarbon (HC), hydrofluorocarbon (HFC), hydrofluoroolefin (HFO) and hydrochlorofluoroolefin (HFO), which are organic blowing agents, can be used. Halogenated olefins (halogenated alkenes) called HCFO) are used. HFC is classified as a fluorocarbon foaming agent, and HC, HFO and HCFO are classified as non-fluorocarbon foaming agents.

Examples of hydrocarbons (HC) that can be used in the present invention include propane, normal pentane, isopentane, cyclopentane, butane, isobutane, hexane, isohexane, neohexane, heptane, and isoheptane. Fluorocarbons (HFC) include, for example, difluoromethane (HFC32), 1,1,1,2,2-pentafluoroethane (HFC125), 1,1,1-trifluoroethane (HFC143a), 1,1,2 ,2-tetrafluoroethane (HFC134), 1,1,1,2-tetrafluoroethane (HFC134a), 1,1-difluoroethane (HFC152a), 1,1,1,2,3,3,3-heptafluoro propane (HFC227ea), 1,1,1,3,3-pentafluoropropane (HFC245fa), 1,1,1,3,3-pentafluorobutane (HFC365mfc), and 1,1,1,2,2, 3,4,5,5,5-decafluoropentane (HFC4310mee), dichloroethane, propyl chloride, isopropyl chloride, butyl chloride, isobutyl chloride, pentyl chloride, isopentyl chloride and the like can be mentioned.

Further, the halogenated olefins (halogenated alkenes) that can be used in the present invention include those called hydrofluoroolefins (HFO) and hydrochlorofluoroolefins (HCFO), and generally chlorine and fluorine as halogens It is an unsaturated hydrocarbon derivative having about 2 to 6 carbon atoms, which is bound to and contains. For example, propene, butene, pentene and hexene with 3 to 6 fluorine substituents, including tetrafluoropropene, pentafluoropropene and hexafluorobutene, as well as fluorochloropropene, trifluoromonochloropropene, fluorochlorobutene Unsaturated hydrocarbons having fluorine substituents and chlorine substituents such as and mixtures of two or more thereof can also be mentioned. Hydrofluoroolefins (HFO) include, for example, pentafluoropropenes such as 1,2,3,3,3-pentafluoropropene (HFO1225ye), 1,3,3,3-tetrafluoropropene (HFO1234ze), 2, Tetrafluoropropenes such as 3,3,3-tetrafluoropropene (HFO1234yf), 1,2,3,3-tetrafluoropropene (HFO1234ye), trifluoropropenes such as 3,3,3-trifluoropropene (HFO1243zf) , tetrafluorobutene isomers (HFO1354), pentafluorobutene isomers (HFO1345), 1,1,1,4,4,4-hexafluoro-2-butene (HFO1336mzz) and other hexafluorobutene isomers ( HFO1336), heptafluorobutene isomers (HFO1327), heptafluoropentene isomers (HFO1447), octafluoropentene isomers (HFO1438), nonafluoropentene isomers (HFO1429), and the like. Further, hydrochlorofluoroolefins (HCFO) include 1-chloro-3,3,3-trifluoropropene (HCFO-1233zd), 2-chloro-3,3,3-trifluoropropene (HCFO-1233xf), Dichlorotrifluoropropene (HCFO1223), 1-chloro-2,3,3-trifluoropropene (HCFO-1233yd), 1-chloro-1,3,3-trifluoropropene (HCFO-1233zb), 2-chloro- 1,3,3-trifluoropropene (HCFO-1233xe), 2-chloro-2,2,3-trifluoropropene (HCFO-1233xc), 3-chloro-1,2,3-trifluoropropene (HCFO- 1233ye), 3-chloro-1,1,2-trifluoropropene (HCFO-1233yc) and the like.

In particular, the hydrofluoroolefins (HFO) and hydrochlorofluoroolefins (HCFO) described above have a low global warming potential and are attracting attention as environmentally friendly blowing agents, and are thus advantageously used in the present invention.

The amount of the organic blowing agent (hydrocarbon, hydrofluorocarbon, halogenated olefin) used is preferably 5 to 50 parts by mass, more preferably 10 to 40 parts by mass, relative to 100 parts by mass of the polyol in composition A. It is preferable that it is a part. If the amount of the organic blowing agent used exceeds 50 parts by mass, the core density of the finally obtained polyurethane foam will be low, which may lead to a decrease in strength of the foam and, in turn, a deterioration in dimensional stability. There is In addition, there is also the problem of being disadvantageous in terms of cost. On the other hand, if the amount of the organic blowing agent used is less than 5 parts by mass, the function as a blowing agent cannot be sufficiently exhibited, and the resulting foam may have a high density. When it is added to A, if the amount added is too small, the viscosity of the composition A as a whole increases, and the miscibility with composition B deteriorates. , causing the problem of not being able to obtain a good spray pattern.

Further, in the present invention, the organic blowing agent (hydrocarbon, hydrofluorocarbon, halogenated olefin) serving as blowing agent II is composition A, composition B or blowing agent I (liquefied CO ₂ class: critical, subcritical or liquid If the organic blowing agent is added to the liquefied CO2 and used, the boiling point of the mixture of _the liquefied _CO2 and the organic blowing agent will be the boiling point of the liquefied _CO2 ( -78.5°C), there is an advantage that equipment and facilities for cooling liquefied CO ₂ are not required. As the organic blowing agent added to liquefied _CO2 , halogenated olefins are preferable from the viewpoint _of environmental _impact . Class: organic blowing agent = 1:9 to 9:1, preferably liquefied CO ₂ Class: organic blowing agent = 2:8 to 8:2.

Further, when an organic blowing agent (hydrocarbon, hydrofluorocarbon, halogenated olefin) and water are used in combination as the blowing agent II in the present invention, the organic blowing agent and water have a mass ratio of 60:40 to 99.5. It is desirable to use a ratio of 9:0.1, preferably 70:30 to 99:1, more preferably 80:20 to 98:2. If the ratio of water is out of this range and exceeds 40, brittleness develops as the reaction progresses, the adhesion to the building body surface decreases, and problems such as peeling may occur. In addition, carbon dioxide generated by the reaction with isocyanate may lower the thermal conductivity and form a foamed layer with insufficient thermal conductivity. When water is used as blowing agent II, water is preferably added to composition A or blowing agent I.

The composition used in producing the polyurethane foam according to the production method of the present invention has been described above in detail for each component. Anything that is used as an additive can be used as long as it does not hinder the object of the present invention. A foam stabilizer can be exemplified as such an additive. A foam stabilizer is used to uniformly arrange the cell structure of a polyurethane foam, and in the present invention, silicone-based surfactants and nonionic surfactants are preferably employed. Specific examples include polyoxyalkylene-modified dimethylpolysiloxanes, polysiloxane oxyalkylene copolymers, polyoxyethylene sorbitan fatty acid esters, castor oil ethylene oxide adducts, lauryl fatty acid ethylene oxide adducts, and the like. One type is used alone, or two or more types are used in combination. The amount of the foam stabilizer to be blended is appropriately determined according to the desired foam properties, the type of foam stabilizer to be used, and the like. On the other hand, it is selected in the range of 0.1 to 10 parts by mass, preferably 1 to 8 parts by mass.

Then, using the composition A, the composition B, and the blowing agent I (liquefied _CO2 : critical, subcritical, or liquid carbon dioxide) described above, a predetermined amount of the blowing agent I is added to the composition at a polyurethane foam manufacturing site. A and/or composition B are added, and immediately after such addition, the reaction between the polyol and the polyisocyanate is started, and foaming and curing are performed to produce the intended polyurethane foam.

Here, when the polyol and the polyisocyanate are reacted, foamed and cured, various known methods for producing polyurethane foams can be employed. For example, 1) composition A, composition B and foaming agent Laminated continuous foaming method in which the mixture of I is applied to the face material and foamed and cured into a plate shape, 2) The above mixture is applied to spaces such as electric refrigerators where heat insulation performance is required, and lightweight and high-strength boards. 3) The injection foaming method of injecting and filling the honeycomb structure of the above, and foaming and curing. The desired polyurethane foam is formed by foaming and curing according to the method). Incidentally, in the present invention, the expression that the blowing agent I is added to the composition A and/or the composition B, and the reaction between the polyol and the polyisocyanate is allowed to proceed immediately after such addition means that the composition to which the blowing agent I is added It merely excludes the intentional storage (leaving) of the substance A, etc., and the progress of the reaction after such storage (leaving). Therefore, at a polyurethane foam production site, a blowing agent I (liquefied CO ₂ ) is supplied to the flow path of composition A and the like by a conventionally known carbon dioxide supply device, and then composition A and composition B are supplied. In the case of mixing, reacting, foaming, and hardening, it is included in the term "immediately" as used in the present invention, although it takes time to flow through the channel.

In particular, the present invention is suitably applied to a blowing foaming method (spray foaming method) in which foaming is performed on site under ambient temperature (ambient temperature). By applying such an on-site blowing foaming method, it is possible to advantageously achieve a low density polyurethane foam and good dispersibility of red phosphorus, and the difference between the overall density and the core density of the foam is 1 to 12 kg/m ³ . When heated at a radiant heat intensity of 50 kW / m ² in accordance with the test method specified in ISO-5660, the total calorific value after 10 minutes is 8 MJ / m ² or less, preferably A polyurethane foam having excellent properties such as dimensional stability, which also has the property that the total calorific value after 20 minutes has passed is 8 MJ/m ² or less, can be advantageously obtained. In addition, when two-layer spraying (two-stage spraying) is performed especially in winter when the environmental temperature is low, in the conventional manufacturing method, the density of the foam of the first layer formed on the adherend surface is There was a problem that the resulting foam (foam) as a whole tends to warp because the density of the foam in the second layer formed on the . However, when the manufacturing method of the present invention is applied to the blow foaming method, the density of the foam in the first layer can be kept low, so warping of the finally obtained polyurethane foam can be suppressed. It becomes.

Some examples of the present invention are shown below to clarify the features of the present invention more specifically, but the present invention is not subject to any restrictions by the description of such examples. It goes without saying that it is not. In addition to the following examples, and furthermore, in addition to the above-described specific description, the present invention includes various modifications, It should be understood that modifications, improvements, etc., may be made. All % and parts shown below are based on mass.

First, each component is contained in the proportions shown in Tables 1 to 3 below (however, liquid CO ₂ , and liquid CO ₂ and HFO-1234ze indicated as “liquid CO ₂ +HFO-1234ze” in the table). ), a composition A containing polyol as the main component, and a composition B consisting of polyisocyanate (polymeric MDI, manufactured by Wanhua Chemical Japan Co., Ltd., product name: Wannate PM-130), Got ready. The raw materials used in the preparation of composition A are as follows.
・Polyol: terephthalic acid-based polyester polyol
(Kawasaki Kasei Co., Ltd., product name: RFK505)
・Foam stabilizer: Silicone foam stabilizer
(manufactured by Dow Corning Toray Co., Ltd., product name: SH-193)
・Red phosphorus: Nova Excel 140
(Product name, manufactured by Rin Kagaku Kogyo Co., Ltd., average particle size: 30 μm, with surface coating, red phosphorus content: 92% or more)
・Red phosphorus: Novaled 120
(Product name, manufactured by Rin Kagaku Kogyo Co., Ltd., average particle size: 25 µm, with surface coating, red phosphorus content: 85% or more)
・Flame retardant: Phosphate ester
[TMCPP: tris (1-chloro-2-propyl) phosphate, manufactured by Daihachi Chemical Industry Co., Ltd.]
・Flame retardant: Phosphate-containing flame retardant
(Ammonium dihydrogen phosphate, manufactured by FUJIFILM Wako Pure Chemical Industries, Ltd.)
・Flame retardant: stannate-containing flame retardant
(zinc stannate, manufactured by Nippon Light Metal Co., Ltd., product name: Flamtard S)
・Flame retardant: Bromine-containing flame retardant
(Hexabromobenzene, manufactured by FUJIFILM Wako Pure Chemical Industries, Ltd.)
・Flame retardant: Boron-containing flame retardant
(Zinc borate, manufactured by Mizusawa Chemical Industry Co., Ltd., product name: ALCANEX FR-100)
・Flame retardant: metal hydroxide
(Aluminum hydroxide, manufactured by Nippon Light Metal Co., Ltd., product name: B1403)
・Trimerization catalyst: quaternary ammonium salt
(manufactured by Kao Corporation, product name: Kaorizer No. 420)
- Resin catalyst: N,N-dicyclohexylmethylamine
(manufactured by Evonik Japan Co., Ltd., product name: Polycat 12)
・Blowing agent: HCFO-1233zd
(manufactured by Honeywell, 1-chloro-3,3,3-trifluoropropene)
・Blowing agent: HFO-1336mzz
(manufactured by Chemours, 1,1,1,4,4,4-hexafluoro-2-butene)
・Blowing agent: HFC245fa
(Central Glass Co., Ltd., 1,1,1,3,3-pentafluoropropane)
・Blowing agent: HFC365mfc
(manufactured by SOLVAY Co., Ltd., 1,1,1,3,3-pentafluorobutane)
・Blowing agent: liquid CO ₂ +HFO-1234ze (mixture)
(Tokyo Koatsu Yamazaki Co., Ltd., liquid CO ₂ :HFO-1234ze=3:7 (weight ratio))

－Manufacture of Polyurethane Foam－
Using composition A and composition B (polymeric MDI) prepared above, with an on-site foaming spray device (manufactured by Asahi Organic Chemicals Co., Ltd., product name: AYK-1000 series) equipped with a liquefied carbon dioxide supply device, First, liquid carbon dioxide or a mixture of liquid carbon dioxide and HFO-1234ze in the proportions shown in Tables 1 to 4 was supplied to composition A, mixed, and then the resulting liquid carbon dioxide was added. Composition A containing (liquid CO ₂ ) and the like was contact-mixed with composition B at a volume ratio of 1:1. Continuously from this contact mixing, the surface of the flexible board (910 mm × 910 mm) that is the building body is sprayed once downward and twice upward, and reacted on the board to foam and harden. , a bottom blowing layer of 5 mm or less and two top blowing layers of 30 mm or less each, foamed layers (total thickness: about 60 mm ), respectively.

Using each polyurethane foam thus obtained as a sample, the overall density and core density were measured (calculated), and the dimensional stability (shrinkage), dimensional stability (warpage) and flame retardancy were evaluated. Measurements and evaluations were carried out according to the following procedures. The results obtained are shown in Tables 1 to 4 below. In addition, "cannot be sprayed" in Comparative Example 4 in Table 3 means that although an attempt was made to produce a polyurethane foam by spraying according to the above procedure, a sufficient polyurethane foam was not formed.

-Measurement (calculation) of overall density and core density-
The thickness of the polyurethane foam having a skin layer (surface layer) formed by spraying onto the flexible board was measured at 13 points positioned at approximately equal distances vertically and horizontally. While determining the volume of the foam, measure the mass of the flexible board on which the polyurethane foam is sprayed, and subtract the pre-measured mass of the flexible board to determine the mass of the polyurethane foam, thereby calculating the total density. . Also, the skin layer (surface layer) was removed from the foam layer formed on the flexible board to expose the core layer, and a 100 mm × 100 mm × 25 mm polyurethane foam was cut out, and its mass was determined to determine the core density. Calculate The "difference between overall density and core density" shown in Tables 1 to 4 below is obtained by subtracting the numerical value of core density from the numerical value of overall density.

- Evaluation of dimensional stability (shrinkage) -
A test piece having a size of 100 mm×100 mm×25 mm, including an internal skin layer (skin layer formed by the first top-blowing), is cut out from each polyurethane foam obtained. The cut test piece is allowed to stand for 48 hours in an environment of -30 ° C., then the dimensions of the test piece are measured with a vernier caliper, and the measurement results are used to calculate the dimensional change rate (shrinkage ) is calculated.
Dimensional change rate (%)
= ([Dimensions of test piece after test] - [Dimensions of test piece before test])
/ [Dimensions of test piece before test] x 100
The calculated dimensional change rate (shrinkage) is evaluated according to the following criteria. In addition, the evaluation of ⊚ and ◯ is regarded as a pass.
A: The dimensional change rate is less than 1%.
○: The dimensional change rate is 1% or more and less than 3%.
Δ: The dimensional change rate is 3% or more and less than 7%.
x: The dimensional change rate is 7% or more.

-Evaluation of dimensional stability (warp)-
A test piece having a size of 100 mm×100 mm×25 mm, including an internal skin layer (skin layer formed by the first top-blowing), is cut out from each polyurethane foam obtained. The cut test piece was allowed to stand in an environment of −30° C. for 48 hours, then the test piece was placed on a horizontal table, and the presence or absence of warpage in the test piece was visually confirmed. The presence or absence of sticking is confirmed and evaluated according to the following criteria.
◯: Neither warpage nor rattling is observed.
x: Either warpage or rattling is observed.

-Evaluation of flame retardancy-
A cone calorimeter test sample with a size of 100 mm × 100 mm × 50 mm was cut out from each of the obtained polyurethane foams, and was tested at a radiant heat intensity of 50 kW/m ² in accordance with the combustion test method specified in ISO-5660. The maximum heat release rate and total heat release after heating for 10 minutes, and the total heat release after heating for 20 minutes (the maximum heat release is the same value as for 10 minutes) are measured. The flame retardancy of these measurement results is evaluated according to the following criteria. In the following, the total calorific value when heating for 10 minutes is indicated as total calorific value (10 minutes), and the total calorific value when heating for 20 minutes is indicated as total calorific value (20 minutes).
A: The maximum heat release rate is 80 kW/m ² or less, and both the total calorific value (10 minutes) and the total calorific value (20 minutes) are 7 MJ/m ² or less.
○: The maximum heat release rate is 80 kW/m ² or less, and both the total calorific value (10 minutes) and the total calorific value (20 minutes) are 8 MJ/m ² or less.
Δ: The maximum heat release rate is 80 kW/m ² or less, the total calorific value (10 minutes) is 8 MJ/m ² or less, and the total calorific value (20 minutes) exceeds 8 MJ/m ² .
x: Maximum heat release rate exceeds 80 kW/m ² , or total heat release (10 minutes) and total heat release (20 minutes) both exceed 8 MJ/m ² .

As is clear from the results in Tables 1 to 3, the polyurethane foams (Examples 1 to 24) produced according to the production method of the present invention are all excellent in flame retardancy and have a low overall density. Since the difference between the core density and the core density is small, it is recognized that the density distribution is uniform and the dimensional stability is also excellent.

On the other hand, as is clear from the results in Table 4, the polyurethane foams according to Comparative Examples 1 and 5, in which only water was used as the blowing agent and no liquid CO ₂ was used, had an overall density and a core density of It is recognized that the density distribution is uneven, and the dimensional stability is also inferior. In addition, it goes without saying that a polyurethane foam in which no red phosphorus is used is inferior in flame retardancy (Comparative Example 3). ), the resulting polyurethane foam is found to be inferior in flame retardancy.

Claims (8)

When producing a polyurethane foam by mixing and reacting a composition A containing polyol as a main component and a composition B containing a polyisocyanate as a main component, followed by foaming and curing,
Coating red phosphorus is contained in the composition A and/or the composition B at a ratio of 10 to 70 parts by mass with respect to 100 parts by mass of the polyol in the composition A,
As a blowing agent, a blowing agent I consisting of critical, subcritical or liquid carbon dioxide and a blowing agent II consisting of at least one of water, hydrofluoroolefin and hydrochlorofluoroolefin are used in combination. Agent II is contained in at least one of said composition A, said composition B and said blowing agent I,
In the production site of the polyurethane foam, the foaming agent I is used in the composition A and / or the composition B at a ratio of 0.1 to 4 parts by mass with respect to 100 parts by mass of the polyol in the composition A. and the reaction is allowed to proceed immediately after such addition.
A method for producing a polyurethane foam, characterized by:
2. The method for producing a polyurethane foam according to claim 1, wherein the red phosphorus component in the coating red phosphorus is 80% or more. 3. The method for producing a polyurethane foam according to claim 1, wherein the coated red phosphorus has an average particle size of 1 to 50 μm. A flame retardant comprising at least one of a phosphate ester, a phosphate-containing flame retardant, a stannate-containing flame retardant, a bromine-containing flame retardant, a boron-containing flame retardant, and a metal hydroxide is added to the composition A. and/or contained in the composition B, the method for producing a polyurethane foam according to any one of claims 1 to 3. 5. The polyurethane foam according to any one of claims 1 to 4, wherein after adding the blowing agent I to the composition A and/or the composition B, the polyurethane foam is produced according to a blow foaming method. manufacturing method. 6. The method for producing a polyurethane foam according to any one of claims 1 to 5, wherein a polyurethane foam having a difference between the total density and the core density of 0.1 to 12 kg/m ³ is obtained. Claims to obtain a polyurethane foam with a total calorific value of 8 MJ/m ² or less after 10 minutes when heated at a radiant heat intensity of 50 kW/m ² in accordance with the test method specified in ISO-5660. A method for producing a polyurethane foam according to any one of claims 1 to 6. Claims to obtain a polyurethane foam with a total calorific value of 8 MJ/m ² or less after 20 minutes when heated at a radiant heat intensity of 50 kW/m ² in accordance with the test method specified in ISO-5660. A method for producing a polyurethane foam according to any one of claims 1 to 7.