Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
  • C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
  • C08J9/12—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent
  • C08J9/122—Hydrogen, oxygen, CO2, nitrogen or noble gases
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/08—Processes
  • C08G18/10—Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/08—Processes
  • C08G18/14—Manufacture of cellular products
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
  • C08G18/30—Low-molecular-weight compounds
  • C08G18/32—Polyhydroxy compounds; Polyamines; Hydroxyamines
  • C08G18/3203—Polyhydroxy compounds
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
  • C08G18/30—Low-molecular-weight compounds
  • C08G18/32—Polyhydroxy compounds; Polyamines; Hydroxyamines
  • C08G18/3203—Polyhydroxy compounds
  • C08G18/3206—Polyhydroxy compounds aliphatic
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
  • C08G18/30—Low-molecular-weight compounds
  • C08G18/32—Polyhydroxy compounds; Polyamines; Hydroxyamines
  • C08G18/3225—Polyamines
  • C08G18/3234—Polyamines cycloaliphatic
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
  • C08G18/30—Low-molecular-weight compounds
  • C08G18/32—Polyhydroxy compounds; Polyamines; Hydroxyamines
  • C08G18/3225—Polyamines
  • C08G18/3237—Polyamines aromatic
  • C08G18/324—Polyamines aromatic containing only one aromatic ring
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
  • C08G18/30—Low-molecular-weight compounds
  • C08G18/32—Polyhydroxy compounds; Polyamines; Hydroxyamines
  • C08G18/3225—Polyamines
  • C08G18/3253—Polyamines being in latent form
  • C08G18/3259—Reaction products of polyamines with inorganic or organic acids or derivatives thereof other than metallic salts
  • C08G18/3265—Reaction products of polyamines with inorganic or organic acids or derivatives thereof other than metallic salts with carbondioxide or sulfurdioxide
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
  • C08G18/72—Polyisocyanates or polyisothiocyanates
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
  • C08G18/72—Polyisocyanates or polyisothiocyanates
  • C08G18/73—Polyisocyanates or polyisothiocyanates acyclic
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
  • C08G18/72—Polyisocyanates or polyisothiocyanates
  • C08G18/74—Polyisocyanates or polyisothiocyanates cyclic
  • C08G18/75—Polyisocyanates or polyisothiocyanates cyclic cycloaliphatic
  • C08G18/751—Polyisocyanates or polyisothiocyanates cyclic cycloaliphatic containing only one cycloaliphatic ring
  • C08G18/752—Polyisocyanates or polyisothiocyanates cyclic cycloaliphatic containing only one cycloaliphatic ring containing at least one isocyanate or isothiocyanate group linked to the cycloaliphatic ring by means of an aliphatic group
  • C08G18/753—Polyisocyanates or polyisothiocyanates cyclic cycloaliphatic containing only one cycloaliphatic ring containing at least one isocyanate or isothiocyanate group linked to the cycloaliphatic ring by means of an aliphatic group containing one isocyanate or isothiocyanate group linked to the cycloaliphatic ring by means of an aliphatic group having a primary carbon atom next to the isocyanate or isothiocyanate group
  • C08G18/755—Polyisocyanates or polyisothiocyanates cyclic cycloaliphatic containing only one cycloaliphatic ring containing at least one isocyanate or isothiocyanate group linked to the cycloaliphatic ring by means of an aliphatic group containing one isocyanate or isothiocyanate group linked to the cycloaliphatic ring by means of an aliphatic group having a primary carbon atom next to the isocyanate or isothiocyanate group and at least one isocyanate or isothiocyanate group linked to a secondary carbon atom of the cycloaliphatic ring, e.g. isophorone diisocyanate
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
  • C08G18/72—Polyisocyanates or polyisothiocyanates
  • C08G18/74—Polyisocyanates or polyisothiocyanates cyclic
  • C08G18/76—Polyisocyanates or polyisothiocyanates cyclic aromatic
  • C08G18/7657—Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings
  • C08G18/7664—Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings containing alkylene polyphenyl groups
  • C08G18/7671—Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings containing alkylene polyphenyl groups containing only one alkylene bisphenyl group
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
  • C08J9/02—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by the reacting monomers or modifying agents during the preparation or modification of macromolecules
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G2101/00—Manufacture of cellular products
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2203/00—Foams characterized by the expanding agent
  • C08J2203/06—CO2, N2 or noble gases
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2375/00—Characterised by the use of polyureas or polyurethanes; Derivatives of such polymers
  • C08J2375/02—Polyureas
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2375/00—Characterised by the use of polyureas or polyurethanes; Derivatives of such polymers
  • C08J2375/04—Polyurethanes

Definitions

• the present invention relates to a blowing agent, a foamable resin composition, a polyurethaneurea resin foam, and a method for producing a polyurethaneurea resin foam.
• Polyurethane resins have excellent mechanical strength, flexibility, abrasion resistance, oil resistance, etc., and are widely used in various industrial fields. Furthermore, in recent years, a polyurethane urea resin having both urethane bonds and urea bonds in its chemical structure has been developed as a new polyurethane resin, and its industrial application is expected.
• polyurethane resin with functions such as heat insulation, sound insulation, and lightness by foaming the polyurethane resin.
• Examples of techniques related to polyurethane resin foams include those described in Patent Documents 1 and 2.
• Patent Document 1 discloses that a polyhydroxy compound and an organic polyisocyanate are mixed in the presence of a blowing agent, a catalyst, and other foaming aids to produce a flexible or semi-rigid polyurethane foam by a one-shot method or a prepolymer method. , adding one or more aliphatic or alicyclic primary or secondary diamine carbonates, foaming the foam at a temperature below the decomposition of the carbonates, and then immediately or after a certain period of time.
• Polyurethane foam molding characterized by holding the foam in a desired shape, physically stretching and bending the foam at a temperature higher than the temperature at which the amine carbonate decomposes, and at the same time fixing the foam through a crosslinking reaction using dissociated amino groups.
• the manufacturing method of the product is described.
• Patent Document 2 describes that when producing flexible polyurethane foam from polyhydroxyl compounds, polyisocyanates, water and/or other blowing agents, catalysts, foam stabilizers, other additives, etc., aliphatic or aromatic A method for producing a polyurethane foam is described which is characterized by adding a carbonate of an aliphatic or alicyclic primary or secondary diamine having a ring.
• a blowing agent is required to obtain a foam, and in order to obtain higher foamability, a large amount of foam needs to be used and discarded.
• polyamines used as raw materials for polyurethane urea resins can absorb carbon dioxide, so they are useful as materials for absorbing waste carbon dioxide.
• the present invention provides a blowing agent and a foamable resin composition that can reduce environmental impact and obtain a polyurethane urea resin foam with improved foamability, as well as a polyurethane urea resin foam with improved foamability. This is what we provide.
• the present inventors have made extensive studies to solve the above problems. As a result, by using a reaction product of an amine compound with a specific structure and carbon dioxide as a blowing agent to obtain polyurethane urea resin foam, it is possible to reduce the amount of conventional blowing agents that have a large environmental impact.
• the present inventors have discovered that the foaming properties of the resulting polyurethane urea resin foam can be improved, and the present invention has been completed. Furthermore, since the reactant can be produced by absorbing carbon dioxide in the environment, it also contributes to reducing environmental load.
• a blowing agent a foamable resin composition, a polyurethaneurea resin foam, and a method for producing a polyurethaneurea resin foam are provided as shown below.
• a blowing agent for obtaining a polyurethaneurea resin foam which is an amine compound containing at least one selected from the group consisting of xylylene diamine and derivatives thereof, and bis(aminomethyl)cyclohexane and derivatives thereof.
• Mass increase rate of amine compound (a1) [mass%] 100 x mass increase of amine compound (a1) (g) / (mass of amine compound (a1) (g) + mass increase of amine compound (a1) (g)) [3]
• the amine compound (a1) is brought into contact with a gas having a carbon dioxide concentration of 0.01% by volume or more and 10% by volume or less to cause the amine compound (a1) and carbon dioxide to react. 1] to [3].
• a foamable resin composition for obtaining a polyurethane urea resin foam A foamable resin composition comprising a polyisocyanate compound (A), a polyol compound (B), and a blowing agent (C) according to any one of [1] to [4] above.
• a foamable resin composition for obtaining a polyurethane urea resin foam A foaming agent comprising an isocyanate group-terminated prepolymer obtained by reacting a polyisocyanate compound (A) and a polyol compound (B), and the foaming agent (C) according to any one of [1] to [4] above. Resin composition.
• the ratio of the number of amino groups in the blowing agent (C) to the total number of hydroxyl groups in the polyol compound (B) and the number of amino groups in the blowing agent (C) is 0.02 or more and 1.0 or less
• the ratio of the number of isocyanate groups in the polyisocyanate compound (A) to the total number of hydroxyl groups in the polyol compound (B) and the number of amino groups in the blowing agent (C) is 0.5 or more and 1.5 or more.
• the foamable resin composition according to any one of [5] to [9] above, which is as follows. [11] Any one of [5] to [10] above, wherein the polyisocyanate compound (A) is at least one selected from the group consisting of 4,4'-diphenylmethane diisocyanate (MDI) and isophorone diisocyanate (IPDI).
• MDI 4,4'-diphenylmethane diisocyanate
• IPDI isophorone diisocyanate
• a polyurethaneurea resin foam obtained by foam-molding the foamable resin composition according to any one of [5] to [11] above.
• a method for producing a polyurethaneurea resin foam comprising the step of foam-molding the foamable resin composition according to any one of [5] to [11] above.
• a blowing agent and a foamable resin composition capable of obtaining a polyurethaneurea resin foam with improved foamability, and a polyurethaneurea resin foam with improved foamability. can.
• this embodiment A mode for carrying out the present invention (hereinafter simply referred to as "this embodiment") will be described in detail.
• the present embodiment below is an illustration for explaining the present invention, and does not limit the content of the present invention.
• the present invention can be implemented with appropriate modifications within the scope of its gist.
• the preferred regulations can be arbitrarily adopted, and a combination of preferred regulations can be said to be more preferable.
• the description “XX to YY” means “XX or more and YY or less”.
• the blowing agent of the present invention (the blowing agent explained in this section is the same as the blowing agent (C) contained in the foamable resin composition described later) is a blowing agent for obtaining a polyurethaneurea resin foam. , comprising a reaction product (a2) of an amine compound (a1) containing at least one selected from the group consisting of xylylene diamine and its derivatives, and bis(aminomethyl)cyclohexane and its derivatives, and carbon dioxide, A foaming agent with a moisture content of 15% by mass or less.
• the foamability is improved by using the reaction product (a2) of the amine compound (a1) and carbon dioxide as a blowing agent for molding a polyurethaneurea resin foam.
• a polyurethaneurea resin foam can be obtained.
• polyurethane urea resin foaming with improved foaming properties is achieved by using a blowing agent that contains a reaction product (a2) of an amine compound (a1) and carbon dioxide and has a moisture content of 15% by mass or less. You can get a body. Although the reason is not certain, it is thought to be as follows. Since the amine compound (a1) has a relatively high ability to retain carbon dioxide and low water absorption, the amine compound and carbon dioxide are generated by heating when molding the resin. At this time, since a sufficient amount of carbon dioxide contributes to foaming, it is thought that a polyurethane urea resin foam with improved foaming properties can be obtained.
• the amine compound (a1) contains at least one member selected from the group consisting of xylylene diamine and derivatives thereof, and bis(aminomethyl)cyclohexane and derivatives thereof, from the viewpoint of further improving reactivity with carbon dioxide and foaming property. and preferably at least one selected from the group consisting of xylylene diamine and its derivatives, and bis(aminomethyl)cyclohexane and its derivatives.
• Examples of xylylene diamine and its derivatives include at least one selected from the group consisting of o-xylylene diamine and its derivatives, m-xylylene diamine and its derivatives, and p-xylylene diamine and its derivatives, and preferably is at least one selected from the group consisting of m-xylylene diamine and its derivatives, p-xylylene diamine and its derivatives, and more preferably m-xylylene diamine and its derivatives.
• bis(aminomethyl)cyclohexane and its derivatives examples include 1,3-bis(aminomethyl)cyclohexane and its derivatives, 1,4-bis(aminomethyl)cyclohexane and its derivatives, and trans-1,4-bis(aminomethyl)cyclohexane and its derivatives. At least one selected from the group consisting of methyl)cyclohexane and its derivatives is mentioned, and 1,3-bis(aminomethyl)cyclohexane and its derivatives are preferred.
• the amine compound (a1) is m-xylylenediamine and its derivatives, and 1,3-bis(aminomethyl)cyclohexane and its At least one selected from the group consisting of derivatives is more preferred, and m-xylylenediamine and its derivatives are even more preferred.
• At least one of the hydrogen atoms of the amino group has at least one substituent selected from the group consisting of an amino group, a cyano group, a phenyl group, a hydroxyl group, and a carboxy group.
• a hydrocarbon group having 1 to 10 carbon atoms which may have at least one hydrogen atom, preferably an amino group, is at least one hydrogen atom selected from the group consisting of an amino group, a cyano group, and a phenyl group.
• a hydrocarbon group having 1 to 10 carbon atoms that may have a substituent, more preferably at least one substituent selected from the group consisting of an amino group, a cyano group, and a phenyl group.
• An alkyl group having 1 to 4 carbon atoms more preferably an alkyl group having 1 to 4 carbon atoms, which may have at least one substituent selected from the group consisting of an amino group and a cyano group, even more preferably Examples include compounds substituted with an alkyl group having 2 or more and 4 or less carbon atoms, which may have at least one substituent selected from the group consisting of an amino group and a cyano group.
• the derivatives of the above-mentioned various amines for example, at least a part of the hydrogen atoms in the cyclic structure are hydrocarbon groups having 1 to 4 carbon atoms, preferably alkyl groups having 1 to 3 carbon atoms, and more preferably Examples include compounds substituted with a methyl group or an ethyl group, more preferably a methyl group.
• the amine compound (a1) amines (primary amines) are preferred. That is, the amine compound (a1) is preferably at least one selected from the group consisting of xylylene diamine and bis(aminomethyl)cyclohexane from the viewpoint of further improving reactivity with carbon dioxide and foaming properties.
• Examples of the xylylene diamine include at least one selected from the group consisting of o-xylylene diamine, m-xylylene diamine and p-xylylene diamine, preferably m-xylylene diamine and p-xylylene diamine. At least one selected from the group consisting of m-xylylenediamine, more preferably m-xylylenediamine.
• Bis(aminomethyl)cyclohexane is selected from the group consisting of 1,3-bis(aminomethyl)cyclohexane, 1,4-bis(aminomethyl)cyclohexane, and trans-1,4-bis(aminomethyl)cyclohexane. 1,3-bis(aminomethyl)cyclohexane is preferred.
• the amine compound (a1) is selected from the group consisting of m-xylylene diamine and 1,3-bis(aminomethyl)cyclohexane from the viewpoint of further improving the reactivity with carbon dioxide and foaming property.
• m-xylylene diamine is more preferred.
• amine compounds (a1) can be used alone or in combination of two or more.
• the maximum carbon dioxide dissociation temperature of the amine compound (a1) measured by the following method, is preferably 200°C or lower, more preferably 180°C or lower, from the viewpoint of improving the carbon dioxide dissociation property and foaming property. , more preferably 160°C or lower, still more preferably 150°C or lower, even more preferably 140°C or lower, even more preferably 135°C or lower, even more preferably 130°C or lower.
• the lower limit of the carbon dioxide maximum dissociation temperature is not particularly limited, but is, for example, 40°C or higher.
• the amine compound (a1) that has absorbed carbon dioxide is heated from 23°C to 250°C at a heating rate of 10°C/min, and the temperature at which the amount of heat absorbed due to the desorption of carbon dioxide is maximum is measured. Let be the maximum dissociation temperature of carbon dioxide.
• the amine compound (a1) that has absorbed carbon dioxide can be prepared by, for example, leaving 5 mmol of the amine compound (a1) in air at 23° C. and 50% RH for 24 hours.
• the acid dissociation constant (pKa) of the amine compound (a1) is preferably 8.0 or more, more preferably 8.5 or more, and still more preferably 9.0 or more, from the viewpoint of further improving carbon dioxide absorption and foaming properties. And from the viewpoint of improving the dissociation property of carbon dioxide and further improving the foamability, it is preferably 12.0 or less, more preferably 11.5 or less, and still more preferably 11.0 or less.
• the acid dissociation constant of the amine compound (a1) is a value determined by the following measuring method based on the acid-base suitability method. (1) Dissolve 0.2 g of amine compound (a1) in 30 mL of purified water.
• the maximum endothermic temperature of the amine compound (a1) measured by the following method is preferably 130°C or higher, more preferably 140°C or higher, and further The temperature is preferably 150°C or higher, and from the viewpoint of further improving carbon dioxide absorption and foamability, the temperature is preferably 260°C or lower, more preferably 230°C or lower, even more preferably 210°C or lower, and still more preferably 190°C or lower. . (Method)
• the amine compound (a1) is heated from 23°C to 350°C at a heating rate of 10°C/min, the temperature at which the amount of heat absorbed due to the volatilization of the amine compound (a1) is maximum is measured, and this temperature is a1) is the maximum endothermic temperature.
• the amine value of the amine compound (a1) is preferably 400 mgKOH/g or more, more preferably 500 mgKOH/g or more, still more preferably 600 mgKOH/g or more, and even more preferably from the viewpoint of further improving carbon dioxide absorption and foaming properties.
• the amine value indicates the amount of amine in the compound, and refers to the number of mg of potassium hydroxide (KOH) equivalent to the acid required to neutralize 1 g of the compound.
• KOH potassium hydroxide
• the amine value can be measured by the following method according to JIS K7237-1995. (1) Dissolve 0.1 g of amine compound (a1) in 20 mL of acetic acid. (2) By titrating the solution obtained in (1) above with a 0.1 N perchloric acid-acetic acid solution using an automatic potentiometric titrator (for example, AT-610, manufactured by Kyoto Electronics Co., Ltd.). Calculate the amine value.
• an automatic potentiometric titrator for example, AT-610, manufactured by Kyoto Electronics Co., Ltd.
• the mass increase rate of the amine compound (a1) calculated by the following formula when the amine compound (a1) is allowed to stand for one week in an air environment of 23 ° C. and 50% RH is calculated from the viewpoint of further improving foaming properties.
• more preferably 45% by mass or less still more preferably 40% by mass or less, still more preferably 30% by mass or less, still more preferably 28% by mass or less.
• Mass increase rate of amine compound (a1) [mass%] 100 x mass increase of amine compound (a1) (g) / (mass of amine compound (a1) (g) + mass increase of amine compound (a1) (g)) Specifically, the mass increase rate of the amine compound (a1) can be measured by the method described in Examples.
• the blowing agent of the present invention can be obtained, for example, by bringing the amine compound (a1) into contact with a gas containing carbon dioxide and reacting the amine compound (a1) with carbon dioxide. That is, in a preferred method for producing a blowing agent of the present invention, the amine compound (a1) is brought into contact with a gas containing carbon dioxide to cause the amine compound (a1) and carbon dioxide to react.
• the gas containing carbon dioxide may be carbon dioxide alone or a mixture of carbon dioxide and an inert gas. It is convenient and preferable to use air as the gas containing carbon dioxide.
• inert gas refers to a gas that does not affect the reaction when obtaining the polyurethane urea resin foam described below.
• the carbon dioxide concentration of the gas containing carbon dioxide is determined by the step of reacting the amine compound (a1) and carbon dioxide to obtain the reactant (a2) by contacting the gas with a carbon dioxide concentration of 0.01% by volume or more and 10% by volume or less. It is preferable to further include.
• the blowing agent of the present invention is produced by a method in which the amine compound (a1) is brought into contact with a gas having a carbon dioxide concentration of 0.01% by volume or more and 10% by volume or less to cause the amine compound (a1) and carbon dioxide to react.
• a gas having a carbon dioxide concentration of 0.01% by volume or more and 10% by volume or less to cause the amine compound (a1) and carbon dioxide to react.
• it is a manufactured blowing agent.
• the carbon dioxide concentration is preferably 0.01 volume% or more, more preferably 0.02 volume% or more, still more preferably 0.03 volume% or more, and preferably 10 volume% or less. It is more preferably 5% by volume or less, still more preferably 1% by volume or less, even more preferably 0.5% by volume or less, even more preferably 0.1% by volume or less.
• the gas having a carbon dioxide concentration of 0.01% by volume or more and 10% by volume or less is air.
• the method of bringing the amine compound (a1) into contact with a gas containing carbon dioxide there are no restrictions on the method of bringing the amine compound (a1) into contact with a gas containing carbon dioxide, but the method of contacting the amine compound (a1) with a gas containing carbon dioxide at 30° C. or lower with stirring or shaking, It is preferable to store it until the mass increase rate falls within the desired range.
• the pressure at which the amine compound (a1) is brought into contact with a gas containing carbon dioxide it is preferably stored under atmospheric pressure or under increased pressure, and more preferably stored under atmospheric pressure.
• the time of contact with the gas containing carbon dioxide may be adjusted according to the temperature, pressure, and amount of carbon dioxide contained in the gas as shown above, but air is used as the gas containing carbon dioxide and stored under atmospheric pressure.
• the time of contact with the gas containing carbon dioxide is preferably 1 hour or more, more preferably 1 day or more, still more preferably 5 days or more, even more preferably 10 days or more. , even more preferably 15 days or more, even more preferably 30 days or more. Although there is no upper limit, it is preferably 100 days or less.
• the reaction product (a2) of the amine compound (a1) and carbon dioxide preferably contains at least one selected from carbamic acid, carbamate, carbonate, and hydrogen carbonate.
• the blowing agent of the present invention is a reaction product (a2) of the amine compound (a1) and carbon dioxide, it forms a salt as described above.
• the molar ratio of the moiety and the carbon dioxide-derived moiety [amine compound (a1)/carbon dioxide] is preferably 70/30 to 30/70, more preferably 60/40 to 40/60, even more preferably 55/45 to 45/55.
• the foaming agent of the present invention has a moisture content of 15% by mass or less. When the moisture content is within the above range, foaming properties can be improved.
• the water content of the blowing agent of the present invention is 15% by mass or less, preferably 10% by mass or less, and more preferably 5% by mass or less.
• the blowing agent of the present invention can be obtained by contacting the amine compound (a1) with a gas containing carbon dioxide, but it is preferable not to add water at that time.
• the foamable resin composition of the present invention is a foamable resin composition for obtaining a polyurethaneurea resin foam, and comprises a polyisocyanate compound (A), a polyol compound (B), and the foaming agent (C).
• a foamable resin composition comprising: That is, the foamable resin composition of the present invention is a foamable resin composition for obtaining a polyurethaneurea resin foam, and comprises a polyisocyanate compound (A), a polyol compound (B), xylylenediamine, and It contains a derivative thereof, and a reaction product (a2) of an amine compound (a1) containing at least one selected from the group consisting of bis(aminomethyl)cyclohexane and its derivatives and carbon dioxide, and the water content is 15% by mass or less.
• This is a foamable resin composition containing a certain foaming agent (C).
• a polyurethane urea resin foam with improved foamability can be obtained.
• the foamable resin composition of the present invention is a foamable resin composition for obtaining a polyurethaneurea resin foam, and is an isocyanate formed by reacting a polyisocyanate compound (A) and a polyol compound (B).
• the foamable resin composition may include a group-terminated prepolymer and the foaming agent (C).
• the blowing agent (C) contained in the foamable resin composition of the present invention is the same as the blowing agent explained in the section of [Blowing agent (Blowing agent (C))] above.
• the foamable resin composition of the present invention may contain a blowing agent other than the blowing agent (C), but it is preferable that it is substantially not contained.
• the content of the blowing agent other than the blowing agent (C) in the foamable resin composition is preferably 5% by mass or less, more preferably 3% by mass or less, still more preferably 1% by mass or less, It is even more preferably 0.5% by mass or less, even more preferably 0.1% by mass or less, even more preferably 0% by mass, and even more preferably not contained.
• blowing agents other than the blowing agent (C) include fluorocarbon-based halogen-containing hydrocarbons such as chlorofluorocarbons and fluorocarbons; alicyclic hydrocarbons such as cyclopentane; dinitropentamethylenetetramine, azodicarbonamide, p , p'-oxybisbenzenesulfonyl hydrazide, and other organic blowing agents; and inorganic blowing agents such as sodium hydrogen carbonate.
• the content of the blowing agent (C) in the foamable resin composition is preferably determined by the ratio of the number of amino groups in the blowing agent (C) to the number of hydroxyl groups in the polyol compound (B) (the number of amino groups/the number of hydroxyl groups). is an amount of 0.01 or more and 0.7 or less.
• the ratio of the number of amino groups in the blowing agent (C) to the number of hydroxyl groups in the polyol compound (B) (the number of amino groups/the number of hydroxyl groups) is preferably 0.01 or more, and more It is preferably 0.05 or more, more preferably 0.10 or more, even more preferably 0.12 or more, even more preferably 0.15 or more, improving the heat resistance and mechanical strength of the foam. From the perspective of It is as follows.
• the polyisocyanate compound (A) is not particularly limited as long as it contains a compound having two or more isocyanate groups, and conventionally known compounds can be used.
• the polyisocyanate compound (A) is preferably a compound having two or more isocyanate groups.
• diisocyanate compounds having two isocyanate groups include 1,6-hexamethylene diisocyanate (HDI), 2,2,4-trimethylhexamethylene diisocyanate, methylene diisocyanate, isopropylene diisocyanate, lysine diisocyanate, lysine diisocyanate methyl ester, Aliphatic isocyanate compounds such as 1,5-octylene diisocyanate; 4,4'-dicyclohexylmethane diisocyanate, isophorone diisocyanate (IPDI), norbornene diisocyanate, hydrogenated tolylene diisocyanate, methylcyclohexane diisocyanate, isopropylidene bis(4-cyclohexyl isocyanate) ), alicyclic isocyanate compounds such as dimer acid diisocyanate; 2,4- or 2,6-tolylene diisocyanate (TDI), 4,4'-diphenyl
• polyisocyanate compounds having three or more isocyanate groups include triphenylmethane triisocyanate, triisocyanate phenylthiophosphate, polymethylene polyphenylene polyisocyanate (polymeric MDI), isocyanurate modified products that are trimers of HDI and TDI, and biuret. Examples include modified forms.
• the isocyanate compound (A) can be used alone or in combination of two or more.
• the polyisocyanate compound (A) is preferably a diisocyanate having two isocyanate groups, more preferably at least one selected from the group consisting of aromatic isocyanate compounds and alicyclic isocyanate compounds, and 4,4' At least one selected from the group consisting of -diphenylmethane diisocyanate (MDI) and isophorone diisocyanate (IPDI) is more preferred, and 4,4'-diphenylmethane diisocyanate (MDI) is even more preferred.
• MDI -diphenylmethane diisocyanate
• IPDI isophorone diisocyanate
• MDI 4,4'-diphenylmethane diisocyanate
• the polyol compound (B) is not particularly limited, and conventionally known compounds can be used.
• Examples of the polyol compound (B) include polyester polyols, polyether polyols, polycarbonate polyols, polylactone polyols, and the like.
• the polyester polyol is not particularly limited as long as it is a condensation product of a polycarboxylic acid or a reactive derivative thereof and a polyhydric alcohol, and for example, it can be obtained by condensation polymerization of a dicarboxylic acid and a glycol.
• dicarboxylic acids examples include aliphatic dicarboxylic acids such as succinic acid, glutaric acid, adipic acid, azelaic acid, sebacic acid, dodecanedicarboxylic acid, fumaric acid, and maleic acid; orthophthalic acid, terephthalic acid, isophthalic acid, 2,6 - Aromatic dicarboxylic acids such as naphthalene dicarboxylic acid; and reactive derivatives thereof; 1,3-cyclopentanedicarboxylic acid, 1,2-cyclohexanedicarboxylic acid, 1,3-cyclohexanedicarboxylic acid, 1,4-cyclohexanedicarboxylic acid Examples include alicyclic dicarboxylic acids such as.
• glycols include dimethylene glycol, ethylene glycol, diethylene glycol, triethylene glycol, tetraethylene glycol, propylene glycol, dipropylene glycol, tripropylene glycol, 1,3-propanediol, neopentyl glycol, 2,2- Diethyl-1,3-propanediol, butylethylpropanediol, 1,2-butanediol, butylene glycol, 1,4-butanediol, dimethylbutanediol, 1,5-pentanediol, 2,4-diethylpentanediol, 1,6-hexanediol, 3-methyl 1,5-pentanediol, 1,8-octanediol, 1,9-nonanediol, 1,10-decanediol, 1,12-d
• Aliphatic glycol such as 1,3-cyclopentanediol, 1,4-cyclohexanediol, 1,4-cyclohexanedimethanol, 2,2-bis(4-hydroxycyclohexyl)propane; m-xylylene Examples include aromatic glycols such as glycol, p-xylylene glycol, bisphenol A, bisphenol F, and bisphenol S. These glycols can be used alone or in combination of two or more.
• polyester polyol examples include condensed polyester polyols such as polyethylene adipate glycol, polybutylene adipate glycol, polyhexamethylene adipate glycol, and polyethylene butylene adipate glycol.
• polyether polyols examples include aliphatic polyether polyols such as polytetramethylene glycol, polyethylene glycol, and polypropylene glycol.
• polycarbonate polyols examples include low-molecular polyols such as ethylene glycol, propylene glycol, butanediol, pentanediol, hexanediol, octanediol, nonanediol, and 1,4-cyclohexanedimethanol, diethylene carbonate, dipropylene carbonate, Examples include polyols obtained by dealcoholization reaction with carbonate compounds such as diphenyl carbonate.
• polylactone-based polyols examples include lactone-based polyester diols such as polylactone diol, polycaprolactone diol, and polymethylvalerolactone diol, which are obtained by ring-opening polymerization of lactone using the above-mentioned low-molecular-weight polyol as an initiator.
• a polyol used in water-based polyurethane resins may be used.
• the polyol used in the water-based polyurethane resin is not particularly limited, but examples thereof include polyols having anionic groups, preferably carboxyl-based polyols such as dimethylolpropionic acid, dimethylolbutanoic acid, dimethylolbutyric acid, and dimethylolvaleric acid. Examples include polyols containing groups.
• the polyol compound (B) can be used alone or in combination of two or more.
• polyol compound (B) at least one selected from the group consisting of polyester polyols and polyether polyols is preferable, polyether polyols are more preferable, and cyclohexane glycol, polytetramethylene glycol, polyethylene glycol At least one type selected from the group consisting of and polypropylene glycol is more preferred, at least one type selected from the group consisting of cyclohexane glycol and polytetramethylene glycol is even more preferred, and cyclohexane glycol is even more preferred.
• the ratio of the number of amino groups in the blowing agent (C) to the total amount of the number of hydroxyl groups in the polyol compound (B) and the number of amino groups in the blowing agent (C) is preferably It is 0.02 or more, more preferably 0.04 or more, still more preferably 0.08 or more, even more preferably 0.12 or more, even more preferably 0.16 or more. Also, from the same viewpoint, it is preferably 1.0 or less, more preferably 0.8 or less, even more preferably 0.6 or less, even more preferably 0.4 or less, even more preferably is 0.3 or less.
• the ratio of the number of isocyanate groups in the polyisocyanate compound (A) to the total amount of the number of hydroxyl groups in the polyol compound (B) and the number of amino groups in the blowing agent (C) is preferably is 0.5 or more, more preferably 0.6 or more, still more preferably 0.7 or more, even more preferably 0.8 or more, even more preferably 0.9 or more. Also, from the same viewpoint, it is preferably 1.5 or less, more preferably 1.4 or less, even more preferably 1.3 or less, even more preferably 1.2 or less, even more preferably is 1.1 or less.
• the foamable resin composition further contains fillers, modifying components such as plasticizers, flow adjusting components such as thixotropic agents, pigments, leveling agents, tackifiers, elastomer fine particles, curing accelerators, foam stabilizers, Other components such as chemical blowing agents may be included depending on the application.
• modifying components such as plasticizers
• flow adjusting components such as thixotropic agents, pigments, leveling agents, tackifiers, elastomer fine particles, curing accelerators, foam stabilizers
• Other components such as chemical blowing agents may be included depending on the application.
• the foamable resin composition may contain a solvent, it is preferable that the foamable resin composition does not substantially contain the solvent. Since it does not contain a solvent, it is highly environmentally friendly and can be easily obtained as a foam.
• the total content of the isocyanate group-terminated prepolymer formed by reacting ) with the polyol compound (B) and the blowing agent (C) is 100% by mass of the total solid content contained in the foamable resin composition according to the present invention.
• it is preferably 50% by mass or more, more preferably 60% by mass or more, even more preferably 70% by mass or more, even more preferably 80% by mass or more, even more preferably 90% by mass. or more, still more preferably 95% by mass or more, even more preferably 98% by mass or more, even more preferably 99% by mass or more, and from the same viewpoint, preferably 100% by mass or less. .
• ⁇ Method for preparing foamable resin composition> There are no particular restrictions on the method for preparing the foamable resin composition, and the polyisocyanate compound (A), polyol compound (B), blowing agent (C), and other components as necessary are mixed using known methods and equipment. and can be manufactured. Note that a foamable resin composition containing an isocyanate group-terminated prepolymer formed by reacting a polyisocyanate compound (A) and a polyol compound (B) is prepared by reacting the polyisocyanate compound (A) and the polyol compound (B) in advance. The isocyanate group-terminated prepolymer is obtained, and the prepolymer, the blowing agent (C), and other components as necessary are mixed using known methods and equipment to produce the product.
• the polyurethaneurea resin foam of the present invention is formed by foam-molding the foamable resin composition according to the present invention described above.
• the method for producing the polyurethane urea resin foam of the present invention is not limited as long as it is formed by foam molding the foamable resin composition, but a preferred method for producing the polyurethane urea resin foam is as described above.
• the method includes a step of foam-molding the foamable resin composition.
• the amine compound (a1) and carbon dioxide are generated from the reactant (a2) (the foaming agent (C)), and the carbon dioxide is produced.
• the foamable resin composition is cured by the reaction of the generated amine compound (a1), polyisocyanate compound (A), and polyol compound (B).
• a polyurethane urea resin foam can be obtained by such a one-shot method.
• the foamable resin composition contains an isocyanate group-terminated prepolymer
• the amine compound (a1) and the dioxide are converted from the reactant (a2) (the blowing agent (C)). Carbon is generated, the foamable resin composition is foamed with carbon dioxide, and the foamable resin composition is cured by the reaction between the generated amine compound (a1) and the isocyanate group-terminated prepolymer.
• a polyurethane urea resin foam can also be obtained by such a prepolymer method.
• the heating temperature and heating time in the step of foaming the foamable resin composition can be selected as appropriate, but from the viewpoint of reaction rate, productivity, and prevention of decomposition of raw materials, etc., it is preferably 50 to 250 ° C., more preferably 100 ° C. ⁇ 200°C, more preferably 120 ⁇ 180°C.
• the reaction time is preferably 10 minutes to 12 hours, more preferably 15 minutes to 4 hours.
• foaming is preferably performed under atmospheric pressure.
• the amine compound (a1) is brought into contact with a gas containing carbon dioxide. ) and carbon dioxide to obtain a reactant (a2).
• the gas containing carbon dioxide may be carbon dioxide alone or a mixture of carbon dioxide and an inert gas. It is convenient and preferable to use air as the gas containing carbon dioxide.
• inert gas refers to a gas that does not affect the reaction when obtaining the polyurethane urea resin foam described below.
• the carbon dioxide concentration of the gas containing carbon dioxide is determined by the step of reacting the amine compound (a1) and carbon dioxide to obtain the reactant (a2) by contacting the gas with a carbon dioxide concentration of 0.01% by volume or more and 10% by volume or less. It is preferable to further include.
• the carbon dioxide concentration is preferably 0.01 volume% or more, more preferably 0.02 volume% or more, still more preferably 0.03 volume% or more, and preferably 10 volume% or less. It is more preferably 5% by volume or less, still more preferably 1% by volume or less, even more preferably 0.5% by volume or less, even more preferably 0.1% by volume or less. Moreover, it is more preferable that the gas having a carbon dioxide concentration of 0.01% by volume or more and 10% by volume or less is air.
• the mass of the amine compound (a1) is brought into contact with a gas containing carbon dioxide at 30°C or less while stirring or shaking. It is preferable to preserve it until the rate of increase falls within the desired range.
• the pressure at which the amine compound (a1) is brought into contact with a gas containing carbon dioxide it is preferably stored under atmospheric pressure or under increased pressure, and more preferably stored under atmospheric pressure.
• the reaction product (a2) of the amine compound (a1) and carbon dioxide preferably contains at least one selected from carbamic acid, carbamate, carbonate, and hydrogen carbonate.
• the ratio of the number of amino groups in the blowing agent (C) to the total amount of the number of hydroxyl groups in the polyol compound (B) and the number of amino groups in the blowing agent (C) is preferably is 0.02 or more, more preferably 0.04 or more, still more preferably 0.08 or more, even more preferably 0.12 or more, even more preferably 0.16 or more. Also, from the same viewpoint, it is preferably 1.0 or less, more preferably 0.8 or less, even more preferably 0.6 or less, even more preferably 0.4 or less, even more preferably is 0.3 or less.
• the ratio of the number of isocyanate groups in the polyisocyanate compound (A) to the total amount of the number of hydroxyl groups in the polyol compound (B) and the number of amino groups in the blowing agent (C) is: Preferably it is 0.5 or more, more preferably 0.6 or more, still more preferably 0.7 or more, even more preferably 0.8 or more, even more preferably 0.9 or more. . Also, from the same viewpoint, it is preferably 1.5 or less, more preferably 1.4 or less, even more preferably 1.3 or less, even more preferably 1.2 or less, even more preferably is 1.1 or less.
• the acid dissociation constant of the amine compound was determined by the following measurement method. (1) 0.2 g of an amine compound was dissolved in 30 mL of purified water. (2) The solution obtained in (1) above was titrated with a 0.1 N perchloric acid-acetic acid solution using an automatic potentiometric titrator (manufactured by Kyoto Electronics Industry Co., Ltd., AT-610). The dissociation constant (pKa) was calculated. Note that the temperature during measurement was 25 ⁇ 2°C.
• the amine value was measured by the following measuring method according to JIS K7237-1995. (1) 0.1 g of an amine compound was dissolved in 20 mL of acetic acid. (2) The solution obtained in (1) above was titrated with a 0.1 N perchloric acid-acetic acid solution using an automatic potentiometric titrator (manufactured by Kyoto Electronics Industry Co., Ltd., AT-610) to obtain amines. The value was calculated. Note that ethylenediamine cannot be measured under the above measurement conditions, so calculated values are shown in Table 1.
• the amine compound that had absorbed carbon dioxide was subjected to DSC measurement as follows, and the carbon dioxide maximum dissociation temperature of the amine compound was measured.
• an amine compound was measured using a differential thermal gravimeter (product name: DTG-60, manufactured by Shimadzu Corporation) under the conditions of a measurement temperature range of 23 to 250°C, a heating rate of 10°C/min, and a nitrogen atmosphere. Differential scanning calorimetry was performed using From the DSC curve thus obtained, the temperature at which the amount of heat absorbed due to the desorption of carbon dioxide was maximized was calculated, and this temperature was defined as the maximum carbon dioxide dissociation temperature of the amine compound.
• the amine compound that had absorbed carbon dioxide was subjected to DSC measurement as follows, and the carbon dioxide maximum dissociation temperature of the amine compound was measured.
• an amine compound was measured using a differential thermal gravimeter (product name: DTG-60, manufactured by Shimadzu Corporation) under the conditions of a measurement temperature range of 23 to 250°C, a heating rate of 10°C/min, and a nitrogen atmosphere. Differential scanning calorimetry was performed using From the DSC curve thus obtained, the temperature at which the amount of heat absorbed due to the desorption of carbon dioxide was maximized was calculated, and this temperature was defined as the maximum carbon dioxide dissociation temperature of the amine compound.
• the foamability of the foamable resin composition was evaluated based on the volume increase rate (fold, expansion ratio) of the polyurethane urea resin foam.
• the volume increase rate is the thickness after foaming divided by the thickness before foaming when foaming is performed in a rectangular parallelepiped container with a fixed bottom shape (bottom area). It means that the larger the volume increase rate is, the better the foamability is.
• Example 1 Production of blowing agent (absorption of carbon dioxide into amine compound) MXDA, which is an amine compound, was placed in a container and allowed to stand for one week in an air environment of 23° C. and 50% RH. Thereby, MXDA and carbon dioxide in the air were reacted to obtain a blowing agent (MXDA carbonate).
• MXDA molecular weight average
• the container containing the amine compound was shaken as appropriate to prevent unreacted MXDA from forming.
• the mass increase amount of MXDA was measured, and the mass increase rate of the amine compound was calculated from the following formula.
• Mass increase rate of amine compound [mass%] 100 x mass increase of amine compound (g) / (initial mass of amine compound (g) + mass increase of amine compound (g))
• Example 2 and Comparative Example 1 Polyurethane urea resin foams were obtained in the same manner as in Example 1, except that the type of amine compound was changed to the compound shown in Table 1. It was confirmed by visual inspection that a foamed structure was formed in the obtained polyurethane urea resin foam. Furthermore, the foamability of the obtained polyurethane urea resin foam was evaluated. The results obtained are shown in Table 1.
• Examples 3 to 6 and Comparative Examples 2 to 4 Polyurethane urea resin foams were obtained in the same manner as in Example 1, except that the types of the amine compound, polyol compound, and polyisocyanate compound were changed to those shown in Table 1. It was confirmed by visual inspection that a foamed structure was formed in the obtained polyurethane urea resin foam. Furthermore, the foamability of the obtained polyurethane urea resin foam was evaluated. The results obtained are shown in Table 1.
• Example 7 In Example 5 (amine compound: MXDA, polyol compound: CHG, polyisocyanate compound: MDI), the standing time for (1) blowing agent production (absorption of carbon dioxide into the amine compound) was from 1 week to 10 weeks. Polyurethane urea resin foams were obtained in the same manner as in Example 5 except that the following was changed. It was confirmed by visual inspection that a foamed structure was formed in the obtained polyurethane urea resin foam. Furthermore, the foamability of the obtained polyurethane urea resin foam was evaluated. The results obtained are shown in Table 1.
• Example 8 and Comparative Examples 5-6) Polyurethane urea resin foams were obtained in the same manner as in Example 7, except that the type of amine compound was changed to the compound shown in Table 1. It was confirmed by visual inspection that a foamed structure was formed in the obtained polyurethane urea resin foam. Furthermore, the foamability of the obtained polyurethane urea resin foam was evaluated. The results obtained are shown in Table 1. From the results of Examples 5 to 8, it can be seen that foaming properties are improved by allowing a sufficient amount of time for the amine compound to be brought into contact with air (carbon dioxide absorption time), especially in the production of the blowing agent of the present invention.
• air carbon dioxide absorption time
• Table 1 shows that according to the blowing agents and foamable resin compositions of Examples, polyurethane urea resin foams with improved foamability can be produced without using conventional blowing agents that have a large environmental impact. . Furthermore, the blowing agent and foamable resin composition of the Examples can be manufactured by absorbing carbon dioxide in the environment, which also contributes to reducing the environmental load.

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