JP6489849B2 - Rigid polyurethane foam - Google Patents

Description

  The present invention relates to a rigid polyurethane foam having excellent heat insulation performance by reacting a specific polyisocyanate and a specific polyol in the presence of a foaming agent, a catalyst, etc., miniaturizing the cell size in the obtained rigid polyurethane foam.

  Non-Patent Document 1 considers the contribution of radiation to the thermal conductivity of rigid urethane foam, and describes that radiation decreases as the cell diameter decreases. That is, if the cell diameter can be reduced, radiation is also reduced, and as a result, the thermal conductivity can be lowered and a foam excellent in heat insulation can be obtained.

  In addition, in order to reduce the cell diameter, for example, as in Non-Patent Document 2, a large amount of air is entrained in the process of stirring the urethane raw material components to form the core of bubbles during foaming, and the number of cells of the rigid polyurethane foam obtained is There is a description of increasing the cell diameter, that is, reducing the cell diameter.

  In addition, in order to reduce the cell diameter, for example, as disclosed in Patent Document 1, a gas is introduced into the urethane raw material component so that the bubble particle size during foaming is 20 μm or less, preferably 10 μm or less. There is a description that the number of cells in the foam is increased, that is, the cell diameter is decreased. As a method for introducing gas, a gas loading device having a static mixer and a forced stirring blade is described.

JP 2007-269820 A

L. D. Booth, “Radiation Contribution as an Element of Thermal Conductivity”, Polyurethanes World Congress 1987, p. 85-90 B. Kanner and T.G.Decker, “Urethane Foam Formation-Role of the Silicone Surfactant”, J. Cell. Plast. 5, (1969), p. 32-39

  However, the thermal conductivity of the rigid polyurethane foam obtained by the method described in Patent Document 1 exceeded 0.020 W / (m · K).

  Therefore, the present invention has a minute cell by reacting a specific polyisocyanate and a specific polyol in the presence of a blowing agent and a catalyst without using a special device such as a gas loading device. An object of the present invention is to provide a rigid polyurethane foam capable of obtaining a rigid polyurethane foam and having a thermal conductivity of 0.020 W / (m · K) or less.

  In the rigid polyurethane foam in the present invention, when a rigid polyurethane foam is produced by reacting a polyisocyanate and a polyol in the presence of a foaming agent and a catalyst, the polyol is a polyester polyol having an aromatic concentration of 17 to 35 wt%, and a non-polyol. Amine-based polyether polyol and / or aromatic amine-based polyether polyol is included, and the polyisocyanate is mixed so that MDI (diphenylmethane diisocyanate) / TDI (tolylene diisocyanate) = 4/6 to 9/1 It is characterized by that.

  In the present invention, a rigid polyurethane foam having a thermal conductivity of 0.020 W / (m · K) or less can be obtained.

  When the rigid polyurethane foam of the present invention is produced by reacting a polyisocyanate and a polyol in the presence of a foaming agent and a catalyst, the polyol is a polyester polyol having an aromatic concentration of 17 to 35 wt%, and a non-polyol. Amine-based polyether polyol and / or aromatic amine-based polyether polyol is included, and the polyisocyanate is mixed so that MDI (diphenylmethane diisocyanate) / TDI (tolylene diisocyanate) = 4/6 to 9/1 It is characterized by that.

[Polyol]
The polyol of the present invention includes a polyester polyol having an aromatic concentration of 17 to 35 wt%, a non-amine polyether polyol and / or an aromatic amine polyether polyol. For example, in the case of only polyester polyol having an aromatic concentration of 17 to 35 wt%, the resin skeleton of the rigid polyurethane foam becomes weak and the resulting foam shrinks. Therefore, together with the polyester polyol having an aromatic concentration of 17 to 35 wt%, non-amine type A polyether polyol and / or an aromatic amine polyether polyol is used in combination.

  The mixing ratio of the polyester polyol having an aromatic concentration of 17 to 35 wt% and the non-amine polyether polyol and / or aromatic amine polyether polyol (hereinafter also referred to as “specific polyether polyol”) is aromatic. It is preferable to mix so that the mixing ratio of polyester polyol having a group concentration of 17 to 35 wt% / specific polyether polyol = 3/7 to 9/1. For example, if the ratio of a specific polyether polyol is too large, the cell size of the resulting foam is difficult to be reduced, and as a result, the heat insulation performance cannot be improved. . And when the ratio of a specific polyether polyol decreases too much, the foam obtained easily contracts.

[Polyester polyol]
The polyester polyol of the present invention may be a polyester polyol having an aromatic concentration of 17 to 35 wt%. The polyester polyol having an aromatic concentration of 17 to 35 wt% is used for the purpose of improving the heat insulation performance. Note that if the aromatic concentration is less than 17 wt%, the desired heat insulation performance cannot be obtained. When the aromatic concentration exceeds 35 wt%, the viscosity as a polyol increases, which is not practical for producing foam.

As the polyester polyol having an aromatic concentration of 17 to 35 wt% according to the present invention, an aromatic polyester polyol obtained from a polyvalent carboxylic acid and a polyhydric alcohol in a normal esterification reaction, a polyester resin, or the like is transesterified with a polyhydric alcohol. An aromatic polyester polyol obtained in the above manner. Examples of the polyvalent carboxylic acid include aromatic polybasic acids such as phthalic acid, isophthalic acid, terephthalic acid, naphthalenedicarboxylic acid, trimellitic acid, and anhydrides thereof. These may be used alone or in combination of two or more. Can be used in appropriate combination. On the other hand, examples of the polyhydric alcohol include ethylene glycol, propylene glycol, glycerin, trimethylolpropane, pentaerythritol, sorbitol, sucrose, and bisphenol A. These are used alone or in appropriate combination of two or more. can do.
The hydroxyl value of the polyester polyol is not particularly limited, but is preferably 200 to 500 mgKOH / g.

[Polyether polyol]
The polyether polyol of the present invention may be a non-amine polyether polyol and / or an aromatic amine polyether polyol. The non-amine polyether polyol and / or aromatic amine polyether polyol is used for the purpose of suppressing shrinkage of the resulting foam and promoting cell miniaturization. For example, when an aliphatic amine-based polyether polyol is used in combination with a polyester polyol having an aromatic concentration of 17 to 35 wt%, the cell size increases and the desired thermal conductivity cannot be obtained.

  Examples of the non-amine polyether polyol of the present invention include ethylene glycol, propylene glycol, glycerin, trimethylolpropane, pentaerythritol, sorbitol, sucrose, bisphenol A, and other polyhydric alcohols such as ethylene oxide, propylene oxide, and butylene oxide. Non-amine polyether polyols obtained by addition polymerization of one or more of these alkylene oxides can be mentioned. These non-amine polyether polyols can be used alone or in combination of two or more. be able to. The hydroxyl value of the non-amine polyether polyol is not particularly limited, but the hydroxyl value is preferably 300 to 700 mgKOH / g.

  As the aromatic amine polyether polyol of the present invention, one kind of alkylene oxide such as ethylene oxide, propylene oxide, butylene oxide, etc. is added to an amine having an aromatic ring such as phenylenediamine, tolylenediamine, diaminodiphenylmethane, and Mannich condensation product. Alternatively, aromatic amine polyether polyols obtained by ring-opening addition polymerization of two or more kinds may be mentioned. These aromatic amine polyether polyols may be used alone or in appropriate combination of two or more. it can. The hydroxyl value of the aromatic amine polyether polyol is not particularly limited, but the hydroxyl value is preferably 300 to 600 mgKOH / g.

[Polyisocyanate]
As the polyisocyanate of the present invention, a mixture of MDI (diphenylmethane diisocyanate) / TDI (tolylene diisocyanate) = 4/6 to 9/1 is used. For example, if MDI is too much in a predetermined mixing ratio with TDI, a desired thermal conductivity cannot be obtained. Further, if the MDI is too smaller than a predetermined mixing ratio with TDI, the MDI contracts.

  Further, as MDI (diphenylmethane diisocyanate) of the present invention, diphenylmethane diisocyanate, polymeric diphenylmethane diisocyanate, modified MDI (partial chemical reaction of MDI, for example, ester group, urea group, burette group, allophanate group, isocyanurate group, urethane group are MDI). These MDIs can be used singly or in appropriate combination of two or more.

  In addition, examples of TDI (tolylene diisocyanate) of the present invention include 2,4-tolylene diisocyanate, 2,6-tolylene diisocyanate, and the like. These TDIs may be used alone or in combination of two or more. Can be used.

  And the usage-amount of the polyisocyanate mixed so that it might become MDI (diphenylmethane diisocyanate) / TDI (tolylene diisocyanate) = 4 / 6-9 / 1 of this invention is an isocyanate index (NCO group / OH group [equivalent ratio]). X100) may be used so as to be 100 to 160.

[Foaming agent]
Examples of the blowing agent used in the present invention include hydrocarbons such as normal pentane, isopentane, cyclopentane, and isobutane, hydrofluorocarbons such as HFC-365mfc, HFC-245fa, and HFC-134a, 1-chloro-3, 3, 3, -Hydrofluoroolefins such as trifluoropropene and 1,1,1,4,4,4-hexafluoro-2-butene can be used, and these can be used singly or in appropriate combination of two or more. . Moreover, you may use water together with the said foaming agent.

[catalyst]
As the catalyst used in the present invention, an amine catalyst or a metal catalyst that has been generally used can be used. Examples of the amine catalyst include N, N, N ′, N′-tetramethylhexanediamine, N, N, N ′, N′-tetramethylpropanediamine, N, N, N ′, N ″, N ′. '-Pentamethyldiethylenetriamine, N, N, N', N'-tetramethylethylenediamine, N, N, -dimethylbenzylamine, N-methylmorpholine, N-ethylmorpholine, triethylenediamine, N, N ', N '-Trimethylaminoethylpiperazine, N, N-dimethylcyclohexylamine, N, N ′, N ″ -tris (3-dimethylaminopropyl) hexahydro-s-triazine, bis (dimethylaminoethyl) ether, N, N— Aminoethoxyethanol, N, N-dimethylaminohexanol, tetramethylhexanediamine, 1-methylimidazole, 1-iso Butyl-2-methylimidazole and the like can be used. Examples of the metal catalyst that can be used include stannous octoate; dibutyltin dilaurate; lead octylate; potassium salts such as potassium acetate and potassium octylate. In addition to these amine catalysts and metal catalysts, quaternary ammonium salts of fatty acids such as formic acid and acetic acid can also be used. Each of the above catalysts may be used alone or in combination of two or more. In the present invention, the amount of the catalyst used is preferably about 0.1 to 15 parts by weight per 100 parts by weight of polyol.

  In the production of the rigid polyurethane foam of the present invention, in addition to the polyol, polyisocyanate, catalyst, and foaming agent, a flame retardant, a foam stabilizer, a compatibilizing agent, a thickener, a colorant, Additives generally used in the production of rigid polyurethane foams such as an agent and a crosslinking agent can be used.

[Foam stabilizer]
Examples of the foam stabilizer include silicone compounds and fluorine compounds that have been conventionally used. The amount of the foam stabilizer is preferably 0.1 to 10 parts by weight.

[Flame retardants]
As the flame retardant, for example, phosphoric acid esters such as trimethyl phosphate, triethyl phosphate, trischloroethyl phosphate, trischloropropyl phosphate are suitable. The amount used is preferably 5 to 40 parts by weight with respect to 100 parts by weight of the total polyol. If it is less than 5 parts by weight, it may be difficult to pass the combustion test specified in JIS-A-9511. On the other hand, if it exceeds 40 parts by weight, the plastic action is too strong, and the shrinkage of the foam and the mechanical strength may be insufficient. A particularly preferred use amount is 10 to 30 parts by weight.

  The rigid polyurethane foam of the present invention is obtained by reacting at least a polyol and a polyisocyanate in the presence of a catalyst, a foaming agent and the like. A foaming method in which a rigid polyurethane foaming machine is used, for example, a polyisocyanate and a mixture of a polyol, a catalyst, a flame retardant, a foam stabilizer, a foaming agent and other auxiliary agents are continuously or discontinuously mixed at a constant ratio. Can be used.

  The rigid polyurethane foam of the present invention includes rigid polyurethane foams such as urethane-modified rigid polyisocyanurate foams, rigid polyisocyanurate foams, and other rigid foams in addition to so-called rigid polyurethane foams.

The rigid polyurethane foam obtained by the present invention has a density of 33 to 60 kg / m ³ , a cell size of 230 μm or less, and a thermal conductivity of 0.020 W / (m · K) or less.

  Hereinafter, the present invention will be described in detail with reference to examples.

Examples 1-10, Comparative Examples 1-4
The raw materials used in Examples and Comparative Examples are shown below.
[Raw materials]
(Polyol)
Polyol A: hydroxyl value 315 mg KOH / g with phthalic anhydride as an initiator,
Polyester polyol with a molecular weight of 360 (aromatic concentration 22%)
Polyol B: hydroxyl value 250 mgKOH / g with terephthalic acid as an initiator,
Polyester polyol with a molecular weight of 450 (aromatic concentration 17%)
Polyol C: hydroxyl value 250 mg KOH / g with terephthalic acid as an initiator,
Polyester polyol with a molecular weight of 450 (aromatic concentration 13%)
Polyol D: Polyether polyol having a hydroxyl value of 450 mgKOH / g and molecular weight of 750 using sorbitol (non-amine) as an initiator Polyol polyol having a molecular weight of 450 mgKOH / g and molecular weight of 600 using sucrose (non-amine) as an initiator Polyether polyol / polyol F: hydroxyl value 420 mgKOH / g using toluenediamine (aromatic amine) as an initiator, polyether polyol / polyol G having a molecular weight of 530: hydroxyl value 500 mgKOH / using ethylenediamine (aliphatic amine) as an initiator g, polyether polyol having a molecular weight of 450

(Foaming agent)
・ C-pentane (cyclopentane)
・ HFC-365mfc (1,1,1,3,3-pentafluorobutane)
・ HFO (1-chloro-3,3,3, -trifluoropropene)

(catalyst)
・ TEDA-L33 manufactured by Tosoh Corporation

(Foam stabilizer)
・ SH-193 manufactured by Toray Dow

(Flame retardants)
-TMCPP manufactured by Daihachi Chemical

(Polyisocyanate)
MDI: polymeric diphenylmethane diisocyanate (Millionate MR-200 manufactured by Tosoh Corporation: NCO content 31%)
TDI: Tolylene diisocyanate (Cosmonate T-80 manufactured by Mitsui Chemicals, NCO content 48%)

[Form production method]
The mixture having the composition shown in Table 1 was stirred at 4500 rpm for 4 seconds using a hand mixer, and then freely foamed in a wooden box of 250 mm × 150 mm × 300 mm to obtain a rigid polyurethane foam.
Further, a mixture having the same composition was stirred at 4500 rpm for 4 seconds using a hand mixer, and then freely foamed on a metal plate adjusted to 45 ° C. to obtain a rigid polyurethane foam.
The polyol and polyisocyanate were blended so that the liquid temperature was 25 ° C. and the isocyanate index (NCO INDEX) was 120.

  About the rigid polyurethane foam obtained by the said manufacturing method, the density, cell size, and thermal conductivity were evaluated with the following method. The results are shown in Table 1.

〔Evaluation method〕
Density (kg / m ³ ): A test piece of 100 mm × 100 mm × 100 mm was cut out from a rigid polyurethane foam obtained by free foaming in a wooden box, and the density of the test piece was measured according to JIS A9511.

  Cell size (μm): A test piece was cut out from a rigid polyurethane foam obtained by free foaming on a metal plate temperature-controlled at 45 ° C., using a scanning electron microscope (JSM-6700F manufactured by JEOL Ltd.). It was measured.

  Thermal conductivity (W / (m · K)): A 200 mm × 200 mm × 25 mm test piece was cut out from a rigid polyurethane foam obtained by free foaming on a metal plate adjusted to 45 ° C., and is shown in JIS A1412. The heat flow meter method was used to measure at an average temperature of 23 ° C. using an auto λHC-074 manufactured by Eiko Seiki Co., Ltd.

Claims (1)

A rigid polyurethane foam obtained by reacting a polyisocyanate and a polyol in the presence of a blowing agent and a catalyst,
The polyol contains a polyester polyol having an aromatic concentration of 17 to 35 wt%, a non-amine polyether polyol and / or an aromatic amine polyether polyol,
Polyisocyanate, MDI (diphenylmethane diisocyanate) / TDI (tolylene diisocyanate) = 4 / 6-9 / 1 and all SANYO were mixed so that,
The TDI 2,4-tolylene diisocyanate, 2,6-tolylene diisocyanate alone, or rigid polyurethane foams, characterized in der Rukoto a combination of two or more.