Carbon dioxide absorbent and method for separating and recovering carbon dioxide

The carbon dioxide adsorbent with a specific amine structure on a porous support addresses the challenges of high energy consumption and degradation by enhancing absorption and release efficiency at low temperatures, ensuring effective carbon dioxide separation and recovery.

WO2026127014A1PCT designated stage Publication Date: 2026-06-18TOYO INK MFG CO LTD +1

Patent Information

Authority / Receiving Office
WO · WO
Patent Type
Applications
Current Assignee / Owner
TOYO INK MFG CO LTD
Filing Date
2025-12-09
Publication Date
2026-06-18

AI Technical Summary

Technical Problem

Existing carbon dioxide adsorbents face challenges in achieving high carbon dioxide absorption and release capacity at low temperatures, while maintaining resistance to heat and oxygen, and minimizing degradation during the absorption and release process, leading to high energy consumption and reduced reusability.

Method used

A carbon dioxide adsorbent comprising an amine represented by specific formulas and supported on a porous material, with the amine positioned to enhance carbon dioxide contact efficiency and minimize degradation through intramolecular interactions, allowing efficient carbon dioxide absorption and release at low temperatures.

🎯Benefits of technology

The adsorbent achieves high carbon dioxide absorption and release capacity with low energy consumption, resistance to heat and oxygen, and reduced degradation, enabling efficient carbon dioxide separation and recovery.

✦ Generated by Eureka AI based on patent content.

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Abstract

The purpose of the present disclosure is to provide: an absorbent that is for separating and recovering carbon dioxide, that has high absorbing ability for carbon dioxide and high releasing ability for carbon dioxide at a low temperature, that has resistance against absorption and against heat and oxygen, and that exhibits less deterioration; and a method for separating and recovering carbon dioxide. This carbon dioxide absorbent contains: an amine (A) represented by formula (11); and a support. In the formula, R1 represents a hydrogen atom, an alkyl group optionally having a substituent, a heterocyclic group optionally having a substituent, or a cycloalkyl group optionally having a substituent, R2 represents a hydrogen atom or an alkyl group having 1-8 carbon atoms, A1 represents an organic residue that has a valence of n1 and that has, at a terminal, an oxygen atom or a nitrogen atom, and n1 represents an integer of 2-12.
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Description

Carbon dioxide adsorbent and method for separating and recovering carbon dioxide 【0001】 This disclosure relates to a carbon dioxide adsorbent and a method for separating and recovering carbon dioxide. 【0002】 In recent years, the rapid increase in greenhouse gas emissions such as carbon dioxide and methane associated with social activities has been cited as one of the causes of global warming. In particular, carbon dioxide is the most important greenhouse gas, and in accordance with the Paris Agreement which came into effect in 2016, measures to reduce carbon dioxide emissions have become an urgent necessity. 【0003】 As part of efforts to reduce carbon dioxide emissions, the separation and capture of carbon dioxide is attracting attention, and the development of carbon dioxide absorbent solutions is being actively pursued. Therefore, in recent years, the development of carbon dioxide separation and capture technologies using chemical absorption methods, primarily composed of aqueous solutions of amine compounds, has been vigorously promoted, targeting carbon dioxide-containing gases emitted from power plants and steel mills. 【0004】 On the other hand, as a method for separating acidic gases such as carbon dioxide, adsorption methods have also been developed, in which the acidic gas is adsorbed onto an adsorbent. In adsorption methods, porous materials filled with amine compounds are sometimes used. 【0005】 For example, Patent Document 1 discloses a polyethylene polyamine derivative with excellent carbon dioxide absorption and release properties, in which some or all of the primary amino groups of polyethylene polyamine having 4 or more nitrogen atoms are replaced with hydroxyalkyl groups having 1 to 4 carbon atoms, and an adsorbent comprising a porous support. 【0006】 Patent Document 2 discloses an adsorbent characterized by a reaction product of an amine and an epoxide that is excellent at adsorbing carbon dioxide at mild temperatures or room temperature. 【0007】 Patent documents 3 and 4 disclose adsorbents characterized by amines substituted with glycidyl ether groups. 【0008】Patent Document 5 discloses an acidic gas adsorbent comprising a porous body and a solid amine compound supported on the surface of the pores of the porous body. In this invention, an amine polymer containing constituent units derived from epoxy monomers is used as the amine compound. 【0009】 Patent documents 1 to 5 mentioned above all disclose the use of compounds as adsorbents in which part or all of the amine structure is modified by reacting polyethyleneimine or a polyamine structure containing two or more nitrogen atoms in the molecule with an epoxide compound. 【0010】 Japanese Patent Publication No. 2022-7403, International Publication No. 2016 / 114991, International Publication No. 2023 / 215873, International Publication No. 2024 / 124198, International Publication No. 2022 / 202848 【0011】 Carbon dioxide adsorbents absorb carbon dioxide from a gas containing carbon dioxide, for example, by coming into contact with the gas. After absorbing carbon dioxide, the adsorbent releases the carbon dioxide, for example, by pressurizing or heating, and it is desirable to reduce the energy used in these processes. Furthermore, it is desirable to reuse the adsorbent after releasing the carbon dioxide, but the amines in the adsorbent that have absorbed carbon dioxide sometimes degrade the adsorbent's performance when repeatedly subjected to heating under an oxygen stream. 【0012】 This disclosure aims to provide a carbon dioxide adsorbent and a carbon dioxide separation and recovery method that have high carbon dioxide absorption capacity and high carbon dioxide release capacity at low temperatures, high resistance to heat and oxygen, and less degradation during the absorption and release process. 【0013】 This disclosure provides a solid adsorbent and a method for separating and recovering carbon dioxide oxides from carbon dioxide, as follows: [1] A carbon dioxide adsorbent comprising an amine (A) represented by formula (11) and a support. 【0014】 In the formula, R 1 R is a hydrogen atom, an optionally substituted alkyl group, an optionally substituted heterocyclic group, or an optionally substituted cycloalkyl group. 2is a hydrogen atom or an alkyl group having 1 to 8 carbon atoms, and A 1 is an n1-valent organic residue having an oxygen atom or a nitrogen atom at the terminal, and n1 represents an integer of 2 to 12. [2] The above A 1 is the carbon dioxide adsorbent according to [1], represented by the following formula (12) or formula (13). [( * - ) n2 X 1 -] n A (12) 【0015】 In the formula, X 1 is an oxygen atom or a nitrogen atom, and n2 is 1 when X 1 is an oxygen atom, and n2 is 2 when X 1 is a nitrogen atom, A is an n-valent organic residue, n represents an integer of 2 to 6, and * indicates the bonding position. [3] The carbon dioxide adsorbent according to [1] or [2], wherein the amine (A) is represented by the following formula (1). 【0016】 In the formula, X is an oxygen atom or -NR 11 -, R 11 is a hydrogen atom, an alkyl group having 1 to 8 carbon atoms, or R 1 R 2 N-CH 2 CH(OH)CH 2 -, A is an n-valent organic residue, and n represents an integer of 2 to 6. [4] The carbon dioxide adsorbent according to [3], wherein X is an oxygen atom. [5] The alkyl group which may have a substituent of R 1 , the heterocyclic group which may have a substituent, and the cycloalkyl group which may have a substituent contain two or more nitrogen atoms, and is the carbon dioxide adsorbent according to any one of [1] to [4]. [6] The carbon dioxide adsorbent according to any one of [1] to [5], wherein R 1 is represented by the following formula (2) or (3). 【0017】 In the formula, 3 R is a hydrogen atom or a methyl group, p is an integer of 0 to 4, R 4 and R 6Each of these is independently a hydrogen atom, a C1-C8 alkyl group, or a hydroxyalkyl group, and R 5 This is a hydrogen atom, an alkyl group having 1 to 8 carbon atoms, a hydroxyalkyl group, or -(CH 2 ) s-R 7 And R 7 is a hydroxyl group, or -N(R 8 ) R 9 And R 8 and R 9 Each is independently a hydrogen atom, a methyl group, or a hydroxyalkyl group, q is 2 or 3, r is 2 to 4, s is 2 or 3, and m is 0 to 3. [7] The carbon dioxide adsorbent according to any one of [1] to [6], wherein the support is at least one selected from the group consisting of silica, silica alumina, alumina, zeolite, zeolite-related compounds, magnesia, titanium dioxide, calcium silicate, carbon nanotubes, activated carbon, polymethyl methacrylate, zirconia, natural minerals, waste solids, and carbon molecular sieves. [8] The carbon dioxide adsorbent according to any one of [1] to [7], wherein the organic residue in A is one of a linear or branched aliphatic hydrocarbon residue which may have a substituent, a linear or branched alkoxy residue which may have a substituent, a linear or branched polyoxyalkyl residue which may have a substituent, a (meth)acryloyl residue which may have a substituent, an alkyl ester residue which may have a substituent, an aromatic ester residue which may have a substituent, an alicyclic hydrocarbon residue which may have a substituent, an aromatic heterocyclic residue which may have a substituent, and an amino residue which may have a substituent. [9] The carbon dioxide adsorbent according to any one of [1] to [7], wherein R 2A carbon dioxide adsorbent according to any one of [1] to [8], wherein is a hydrogen atom.

[10] A carbon dioxide adsorbent according to any one of [1] to [9], wherein the content of the amine (A) is 5 to 70% by mass.

[11] A method for separating or recovering carbon dioxide, comprising: a first step of contacting a gas to be treated with a carbon dioxide adsorbent according to any one of [1] to

[10] to absorb carbon dioxide; and a second step of decarbonizing carbon dioxide from the carbon dioxide adsorbent that absorbed carbon dioxide in the first step, wherein the second step comprises one or more of the following steps: (a) placing the carbon dioxide adsorbent under reduced pressure conditions to decarbonize carbon dioxide; (b) contacting the carbon dioxide adsorbent with at least one of water vapor and an inert gas to decarbonize carbon dioxide; and (c) heating the carbon dioxide adsorbent to decarbonize carbon dioxide. 【0018】 According to this disclosure, it is possible to provide a carbon dioxide adsorbent and a carbon dioxide separation and recovery method that have high carbon dioxide absorption capacity and high carbon dioxide release capacity at low temperatures, high resistance to heat and oxygen and less degradation during the absorption and release process, enabling carbon dioxide separation and recovery with low energy consumption as a whole system. 【0019】 The carbon dioxide adsorbent and the method for separating and recovering carbon dioxide will be described below. In this disclosure, unless otherwise specified, the numerical range indicated by "~" includes the values ​​before and after it as the lower and upper limits. If there are multiple identical symbols in a chemical formula, unless otherwise specified, such identical symbols are not limited to representing the same substituent, but may represent different substituents within the range defined by the symbol. In this specification, "carbon dioxide adsorbent" may be referred to as "adsorbent". 【0020】 [Carbon Dioxide Adsorbent] The carbon dioxide adsorbent according to this embodiment includes an amine (A) represented by formula (11) described later, and a support. In this adsorbent, the amine (A) is supported on the surface of the support. The amine (A) has (-CHOHCH 2 ) n1 A 1The portion (more specifically, the -OH group) is more likely to be positioned on the surface side of the support, and as a result, the carbon dioxide adsorption portion NR 1 R 2 It is presumed that this adsorbent is more likely to be placed on the gas side to be treated. 2 ) n1 A 1 The adsorption of the portion onto the support surface makes it possible to suppress the desorption of amine (A) during heating. Furthermore, the (-CHOHCH 2 ) n1 A 1 A portion of the molecule exhibits intramolecular or intermolecular interactions with amino groups, which can suppress side reactions such as oxidation, and improves its resistance to heat and oxygen as a carbon dioxide adsorbent. 1 R 2 By placing it on the side of the gas to be treated, carbon dioxide and NR 1 R 2 The contact efficiency with the carbon dioxide is increased, improving the amount of carbon dioxide adsorbed, and carbon dioxide is efficiently desorbed by heating at a relatively low temperature of about 70°C. For these reasons, the carbon dioxide adsorbent of this embodiment has less degradation and excellent reusability. Furthermore, by using the carbon dioxide adsorbent of this embodiment, carbon dioxide separation and recovery can be achieved with low energy consumption for the entire system. The components of the carbon dioxide absorbent will be described below. 【0021】 <Amine (A)> Amine (A) is a compound represented by formula (11) above. 【0022】 In the formula, R 1 R is a hydrogen atom, an optionally substituted alkyl group, an optionally substituted heterocyclic group, or an optionally substituted cycloalkyl group. 2 A is a hydrogen atom or an alkyl group having 1 to 8 carbon atoms. 1 n1 is an n1-valent organic residue whose terminal is either an oxygen or nitrogen atom, where n1 represents an integer from 2 to 12. 【0023】 R 2The C1-C8 alkyl group in this context can be a linear or branched alkyl group. Specific examples of alkyl groups include methyl, ethyl, propyl, isopropyl, butyl, isobutyl, tert-butyl, neopentyl, n-hexyl, n-octyl, and 2-ethylhexyl groups. 2 Among these, hydrogen atoms or alkyl groups having 1 to 4 carbon atoms are preferred, hydrogen atoms, methyl groups, or ethyl groups are more preferred, and hydrogen atoms or methyl groups are even more preferred. 【0024】 R 1 Examples of substituents in "alkyl groups that may have substituents," "heterocyclic groups that may have substituents," and "cycloalkyl groups that may have substituents" include halogen atoms, linear or branched alkyl groups, alkylene groups, cycloalkyl groups, alkoxy groups, cyano groups, trifluoromethyl groups, nitro groups, hydroxyl groups, carbamoyl groups, N-substituted carbamoyl groups, sulfamoyl groups, N-substituted sulfamoyl groups, carboxyl groups, sulfo groups, amino groups, imino groups, nitrogen atoms, oxygen atoms, phenyl groups, sulfanyl groups, etc., and the substituents may have further substituents, and examples of substituents include the substituents listed above. 【0025】 Examples of alkyl groups that may have substituents include linear or branched alkyl groups such as methyl, ethyl, propyl, isopropyl, butyl, isobutyl, tert-butyl, neopentyl, n-hexyl, n-octyl, stearyl, and 2-ethylhexyl groups. 【0026】"Substitutable alkyl groups" include, for example, trichloromethyl group, trifluoromethyl group, 2,2,2-trifluoroethyl group, 2,2-dibromoethyl group, 2,2,3,3-tetrafluoropropyl group; 2-ethoxyethyl group, 2-butoxyethyl group; 2-nitropropyl group; benzyl group, 4-methylbenzyl group, 4-tert-butylbenzyl group, 4-methoxybenzyl group, 4-nitrobenzyl group, 2,4-dichlorobenzyl group; methylsulfanyl group, ethylsulfanyl group, propyl Sulfanyl group, butylsulfanyl group, pentylsulfanyl group, hexylsulfanyl group, octylsulfanyl group, decylsulfanyl group, dodecylsulfanyl group, octadecylsulfanyl group, methoxyethylsulfanyl group, aminoethylsulfanyl group, benzylaminoethylsulfanyl group, methylcarbonylaminoethylsulfanyl group, phenylcarbonylaminoethylsulfanyl group; sulfanylmethyl group, 2-sulfanylethyl group, 1-sulfanylethyl group;Aminomethyl group, aminoethyl group, N-methylaminoethyl group, N-ethylaminoethyl group, N-(aminoethyl)aminoethyl group, N-(hydroxyethyl)aminoethyl group, N-propylaminoethyl group, N-isopropylaminoethyl group, N-butylaminoethyl group, aminopropyl group, N-methylaminopropyl group, N-ethylaminopropyl group, N-propylaminopropyl group, N-(aminopropyl)aminopropyl group, N-isopropylaminopropyl group, N-butylaminopropyl group, aminobutyl group, aminopentyl group, aminohexyl group, aminooctyl group, aminodecyl group, aminododecyl group, aminooctadecyl group, aminoethoxymethyl group, aminoethylaminoethyl group, aminoethyl(methyl)aminoethyl group, aminopropylaminopropyl group, aminopropyl(methyl)aminopropyl group, dibutylaminopropyl group, di(aminoethyl)aminoethyl group, di(A Examples include the aminoethyl(aminoethylpropyl) group, aminopropylaminobutylaminopropyl group, aminopropylaminoethylaminopropyl group, aminoethylaminopropylaminoethyl group, aminoethylaminoethylaminoethyl group, aminopropylaminoethylaminoethyl group, aminoethylaminoethylaminoethylaminoethyl group, aminoethylaminoethylaminoethylaminoethylaminoethyl group, aminoethylaminomethylphenyl group, aminoethylaminocarbonylmethyl group, aminoethylaminocarbonylphenyl group; hydroxymethyl group, 2-hydroxyethyl group, 2-hydroxypropyl group, 3-hydroxypropyl group, 4-hydroxybutyl group; cyclopropylmethyl group, cyclobutylmethyl group, cyclopentylmethyl group, cyclohexylmethyl group, cyclopentylethyl group, cyclohexylethyl group, cyclopentylpropyl group, cyclohexylpropyl group, etc. 【0027】The "substituted alkyl group" is preferably aminoethyl group, N-methylaminoethyl group, N-ethylaminoethyl group, N-(aminoethyl)aminoethyl group, N-propylaminoethyl group, N-isopropylaminoethyl group, N-butylaminoethyl group, aminopropyl group, N-methylaminopropyl group, N-ethylaminopropyl group, N-propylaminopropyl group, N-(aminopropyl)aminopropyl group, N-isopropylaminopropyl group, N-butylaminopropyl group, or aminobutyl group. The aminoethyl(methyl)aminoethyl group, aminopropylaminopropyl group, aminopropyl(methyl)aminopropyl group, dibutylaminopropyl group, di(aminoethyl)aminoethyl group, di(aminoethyl)aminoethylpropyl group, aminopropylaminobutylaminopropyl group, aminopropylaminoethylaminopropyl group, aminoethylaminopropylaminoethyl group, aminoethylaminoethylaminoethyl group, aminoethylaminoethylaminoethyl group, aminopropylaminoethylaminoethylaminoethyl group, aminoethylaminoethylaminoethylaminoethyl group, and aminoethylaminoethylaminoethylaminoethylaminoethyl group are more preferred. 【0028】 Examples of heterocyclic groups that may have substituents include 2-pyridyl group, 3-pyridyl group, 4-pyridyl group, 2-pyrolyl group, 3-pyrolyl group, 2-furyl group, 3-furyl group, 2-thienyl group, 3-thienyl group, 2-imidazolyl group, 2-oxazolyl group, 2-thiazolyl group, piperidino group, 4-piperidyl group, morpholino group, 2-morpholinyl group, N-indolyl group, 2-indolyl group, 2-benzofuryl group, 2-benzothienyl group, 2-quinolino group, and N-carbazolyl group. 【0029】 Examples of cyclic alkyl groups that may have substituents include cyclopropyl group, methylcyclopropyl group, cyclobutyl group, cyclopentyl group, methylcyclopentyl group, ethylcyclopentyl group, cyclohexyl group, methylcyclohexyl group, ethylcyclohexyl group, and propylcyclohexyl group. 【0030】In terms of achieving both carbon dioxide adsorption and carbon dioxide release ability at low temperatures, R 1 It is preferable that it contains nitrogen atoms, more preferably two or more nitrogen atoms, and even more preferably three or more nitrogen atoms. 【0031】 Also, R 1 It is preferable that the group is represented by the following general formulas (2) and (3). In the formulas, * indicates the bond position with N in formula (1). 【0032】 【0033】 In formula (2), R 3 is a hydrogen atom or a methyl group, and p is an integer from 0 to 4. From the viewpoint of carbon dioxide adsorption and low-temperature release, R 3 Hydrogen atoms are preferred. Furthermore, from the viewpoint of carbon dioxide adsorption, low-temperature release, and ease of synthesis, p is preferably 1 to 4, and more preferably 2 to 3. 【0034】 In formula (3), R 4 and R 6 Each of these is independently a hydrogen atom, a C1-C8 alkyl group, or a hydroxyalkyl group, and R 5 This is a hydrogen atom, an alkyl group having 1 to 8 carbon atoms, a hydroxyalkyl group, or -(CH 2 ) s-R 7 And R 7 is a hydroxyl group, or -N(R 8 ) R 9 And R 8 and R 9 Each is independently a hydrogen atom, a methyl group, or a hydroxyalkyl group, q is 2 or 3, r is 2 to 4, s is 2 or 3, and m is 0 to 2. From the viewpoint of carbon dioxide adsorption and low-temperature release, R 4 and R 5 A hydrogen atom is preferred for q, and q is preferably 3. 【0035】 R 4 ~R 6Examples of C1-C8 alkyl groups in include methyl, ethyl, n-propyl, isopropyl, n-butyl, tert-butyl, hexyl, and octyl groups. From the viewpoint of carbon dioxide adsorption and low-temperature release, R 4 ~R 6 The alkyl group is preferably a C1-C4 alkyl group, and among these, a methyl group or an ethyl group is preferred. 【0036】 R 4 ~R 6 , R 8 and R 9 In the hydroxyalkyl group, the number of carbon atoms in the alkyl group is preferably 1 to 8, and more preferably 1 to 4, from the viewpoint of carbon dioxide adsorption and low-temperature release. Specific examples of hydroxyalkyl groups include hydroxymethyl group, hydroxyethyl group, hydroxypropyl group, and hydroxybutyl group. 【0037】 From the standpoint of carbon dioxide adsorption and low-temperature release, R 1 The group is preferably represented by general formula (3). 1 Specific examples will be shown later in the section on amine (A). 【0038】 A in formula (11) 1 This is an n1-valent organic residue whose terminal (i.e., the element at the binding site) is either an oxygen atom or a nitrogen atom. 【0039】 A 1 As such, a group represented by formula (12) or formula (13) below is preferred, due to the ease of synthesis of amine (A). [(*-) n2 X 1 -] n A (12) 【0040】 In the formula, X 1 is an oxygen atom or a nitrogen atom, and n2 is X 1 If it is an oxygen atom, it is 1, X 1 If it is a nitrogen atom, it is 2, A is an n-valent organic residue, n is an integer from 2 to 6, and * indicates the bond position. 【0041】 X in equation (12) 1 is A1 represents the end and is an oxygen atom or a nitrogen atom. n2 is the number of bonds of X 1 and indicates the number of bonds of X 1 is 1 when X is an oxygen atom, and X 1 is 2 when it is a nitrogen atom. In formula (12), the sum of multiple n2s becomes the valence n1 of A 1 and is the valence n1 of A 【0042】 A represents an n-valent organic residue. As the n-valent organic residue, it is preferable to have one or more carbon atoms. Preferred specific examples of the n-valent organic residue include a linear or branched hydrocarbon residue which may have an n-valent substituent, a linear or branched alkoxy residue which may have an n-valent substituent, a (meth)acryloyl residue which may have an n-valent substituent, a linear or branched polyoxyalkyl residue which may have an n-valent substituent, an alkyl ester residue which may have an n-valent substituent, an aromatic ester residue which may have an n-valent substituent, an alicyclic hydrocarbon residue which may have an n-valent substituent, an aromatic hydrocarbon residue which may have an n-valent substituent, an aromatic heterocyclic residue which may have an n-valent substituent, or an amino residue which may have an n-valent substituent, and oxygen atoms may be present between adjacent carbon atoms of these residues. Also, n represents an integer from 2 to 6. 【0043】 In the linear or branched hydrocarbon residue which may have an n-valent substituent, examples of the "linear or branched hydrocarbon" include an alkyl group, an alkenyl group, and an alkynyl group. 【0044】 Specific examples of the alkyl group include alkyls having 1 to 18 carbon atoms such as methyl group, ethyl group, propyl group, isopropyl group, butyl group, isobutyl group, sec-butyl group, tert-butyl group, pentyl group, isopentyl group, hexyl group, heptyl group, octyl group, 2-ethylhexyl group, nonyl group, decyl group, dodecyl group, tetradecyl group, pentadecyl group, octadecyl group, etc. 【0045】Furthermore, examples of alkenyl groups include C2 to C18 alkenyls such as vinyl group, 1-propenyl group, 2-propenyl group, isopropenyl group, 1-butenyl group, 2-butenyl group, 3-butenyl group, 1-octenyl group, 1-decenyl group, and 1-octadecenyl group. 【0046】 Furthermore, examples of alkynyl groups include ethylenyl groups, 1-propynyl groups, 2-propynyl groups, 1-butynyl groups, 2-butynyl groups, 3-butynyl groups, 1-octynyl groups, 1-decynyl groups, and 1-octadecynyl groups, which have 2 to 18 carbon atoms. 【0047】 Examples of alkoxy groups in linear or branched alkoxy residues that may have n-valent substituents include methoxy groups and ethoxy groups. 【0048】 Examples of the (meth)acryloyl group of the (meth)acryloyl residue, which may have an n-valent substituent, include the methacrylic group and the acryloyl group. 【0049】 Examples of polyoxyalkyl groups of linear or branched polyoxyalkyl residues that may have n-valent substituents include polyethylene oxide groups with 4 to 16 repeats and linear or branched polypropylene oxide groups with 4 to 16 repeats. Preferred substituents include alkyl groups, phenyl groups, and hydroxyl groups. 【0050】 Examples of alkyl ester groups of alkyl ester residues that may have n-valent substituents include methyl ester group, ethyl ester group, propyl ester group, butyl ester group, pentyl ester group, heptyl ester group, hexyl ester group, octyl ester group, hexadecyl ester group, cyclohexyl ester group, 1,2-cyclohexanediester group, and 1,2-cyclohexenediester group. 【0051】 Examples of aromatic ester groups in aromatic ester residues that may have n-valent substituents include phenyl ester groups and 4-tert-butylphenyl ester groups. 【0052】Examples of alicyclic hydrocarbon groups in alicyclic hydrocarbon residues that may have n-valent substituents include cycloalkyl groups, specifically cyclopropyl groups, cyclobutyl groups, cyclopentyl groups, cyclohexyl groups, cycloheptyl groups, cyclooctyl groups, cyclooctadecyl groups, and 2-indeno groups, which are cycloalkyl groups having 3 to 18 carbon atoms. In addition, alicyclic hydrocarbon groups also include groups in which multiple cycloalkyl groups are linked by alkylene groups or the like. 【0053】 Aromatic hydrocarbons of the aromatic hydrocarbon residue that may have n-valent substituents include aromatic hydrocarbons with condensation numbers 1 to 4, specifically benzene, biphenyl, naphthalene, anthracene, phenanthrene, tetracene, pyrene, 9,9-diphenylfluorene, bis(3-methylphenyl)fluorene, and binaphthyl. Preferably, the substituents are alkyl groups, alkylene groups, and halogen atoms, and particularly preferably methyl groups, methylene groups, tert-butylene groups, and bromine atoms. 【0054】 The aromatic heterocycle of the aromatic heterocycle residue, which may have an n-valent substituent, is an aromatic heterocycle with condensation numbers 1 to 4, and examples include pyrrole, imidazole, pyridine, triazine, indole, quinoline, carbazole, and phthalimide. 【0055】 An example of an amino group in an amino residue that may have an n-valent substituent is the aniline group. 【0056】 In an n-valent organic residue, examples of substituents include linear or branched alkyl groups, alkoxy groups, polyoxyalkyl groups, phenyl groups, 4-nitrophenyl groups, 2-methoxyphenyl groups, hydroxyl groups, halogen atoms, epoxy groups, etc., and these substituents may have further substituents. 【0057】 The specific alkyl group used as a substituent is synonymous with the alkyl group of a linear or branched hydrocarbon residue that may have an n-valent substituent, as mentioned above. 【0058】 Specific examples of alkoxy groups used as substituents include methoxy groups and ethoxy groups. 【0059】 Specific polyoxyalkyl groups as substituents include polyethylene oxide groups having a repeating number of 4 to 16, linear or branched polypropylene oxide groups having a repeating number of 4 to 16. 【0060】 Specific halogen atoms as substituents include a chlorine atom, a bromine atom, and an iodine atom. 【0061】 A is preferably a linear or branched hydrocarbon residue which may have an n-valent substituent, or an aromatic hydrocarbon residue which may have an n-valent substituent. More preferably, it is a linear or branched hydrocarbon residue which may have an n-valent substituent, and particularly preferably, it is an n-valent linear hydrocarbon residue. CO 2 From the viewpoint of the recovery amount, it is preferable that the partial molecular weight of the group A is small, and it may have -O- between carbon-carbon atoms and may have a hydroxyl group as a substituent. A linear or branched aliphatic hydrocarbon group having 1 to 12 carbon atoms is preferable, and a linear or branched aliphatic hydrocarbon group having 1 to 6 carbon atoms is preferable. Further, from the viewpoints such as heat resistance, it is preferable that the group A has a ring structure selected from an alicyclic ring and an aromatic ring. There may be one or more rings in the group A, and 1 to 3 rings are more preferable. A 1 Specific examples of A include groups represented by the following formulas. Here, * indicates the bonding position. 【0062】 【0063】 The amine (A) has a high ability to release carbon dioxide at low temperatures and high resistance to heat and oxygen. Among them, the compound represented by the following formula (1) is preferable. 【0064】 In the formula, X is an oxygen atom or -NR 11 -, and R 11 is a hydrogen atom, an alkyl group having 1 to 8 carbon atoms, or R 1 R 2 N-CH 2 CH(OH)CH 2 -, A is an n-valent organic residue, and n represents an integer of 2 to 6. 【0065】R in equation (1) 1 , R 2 A and n are as described above. Also, R 11 The alkyl group having 1 to 8 carbon atoms in the above R 2 Similar examples include the above. 【0066】 Table 1 shows representative examples of amines (A) in this embodiment, namely amines (A-1) to (A-208), but this embodiment is not limited to these representative examples. 【0067】 【0068】 【0069】 【0070】 【0071】 【0072】 【0073】 【0074】 【0075】 【0076】 【0077】 【0078】 【0079】 【0080】 【0081】 【0082】 【0083】 【0084】 Amine (A) can be obtained, for example, by reacting the following amine (B) with the following polyfunctional epoxy compound (C) in a suitable solvent. 【0085】 Examples of the aforementioned solvents include water, alkanols (e.g., methanol, ethanol, propanol, butanol, etc.), dimethylformamide (DMF), and dimethyl sulfoxide (DMSO). 【0086】 It is preferable to carry out the reaction when the total equivalent weight of the primary and secondary amino groups of amine (B) is in the range of 0.95 to 1.1 relative to the epoxy equivalent weight of the polyfunctional epoxy compound (C). Furthermore, amine (B) and polyfunctional epoxy compound (C) may be used individually or in combination of several different types. 【0087】 The polyfunctional epoxy compound (C) used in this embodiment will now be described. A polyfunctional epoxy compound is a compound having two or more epoxy groups in one molecule. 【0088】 The polyfunctional epoxy compound can be any compound commonly used in epoxy resin compositions, and its type is not particularly limited as long as it has two or more epoxy groups in one molecule. 【0089】 Polyfunctional epoxy compounds include polyfunctional aliphatic epoxy compounds and polyfunctional aromatic epoxy compounds. 【0090】 As the polyfunctional aliphatic epoxy compound, a cyclic structure may be used, and either synthesized or commercially available compounds may be used. 【0091】Examples of polyfunctional aliphatic epoxy compounds include difunctional aliphatic epoxy compounds having two epoxy groups in their molecule, such as alkylene glycol diglycidyl ether, alkenylene glycol diglycidyl ether, ethylene glycol diglycidyl ether, propylene glycol diglycidyl ether, neopentyl glycol diglycidyl ether, butanediol diglycidyl ether, hexanediol diglycidyl ether, cyclohexanedimethanol diglycidyl ether, polyethylene glycol diglycidyl ether, polypropylene glycol diglycidyl ether, trimethylolpropane diglycidyl ether, and 1,4-cyclohexanedimethanol diglycidyl ether; Examples include polyglycidyl ethers of trifunctional or more alcohols such as trimethylolpropane, pentaerythritol, and dipentaerythritol [trimethylolpropane polyglycidyl ether such as trimethylolpropane triglycidyl ether, trimethylolpropane triglycidyl ether, or a mixture of trimethylolpropane diglycidyl ether and trimethylolpropane triglycidyl ether (e.g., Denacol EX-321L: manufactured by Nagase Chemitex), pentaerythritol triglycidyl ether, pentaerythritol tetraglycidyl ether, sorbitol heptaglycidyl ether, sorbitol hexaglycidyl ether, resorcinol diglycidyl ether, pentaerythritol (tri, or tetra)glycidyl ether, dipentaerythritol (tri, tetra, penta, or hexa)glycidyl ether, etc.], which have three or more epoxy groups in their molecule. 【0092】 Commercially available polyfunctional aliphatic epoxy compounds can be used, such as "EP-4088S" (manufactured by ADEKA Corporation), "EHPE3150" (manufactured by Daicel Corporation), "EX-211L" and "EX-212L" (both manufactured by Nagase ChemteX Corporation), and "Showfree CDMDG" (manufactured by Resonac Corporation). 【0093】Examples of polyfunctional aromatic epoxy compounds include polyglycidyl ethers of polyhydric phenols having at least one aromatic ring, such as bisphenol A and bisphenol F, or alkylene oxide adducts thereof; epoxy novolac resins; polyglycidyl ethers of aromatic compounds having two or more phenolic hydroxyl groups, such as resorcinol, hydroquinone, and catechol; polyglycidyl ethers of aromatic compounds having two or more alcoholic hydroxyl groups, such as phenyldimethanol, phenyldiethanol, and phenyldibutanol; polyglycidyl esters of polybasic acid aromatic compounds having two or more carboxylic acids, such as phthalic acid, terephthalic acid, and trimellitic acid; and diepoxylated vinylbenzene. 【0094】 The polyfunctional aromatic epoxy compound may be synthesized or commercially available. 【0095】 The polyfunctional aromatic epoxy compounds can be commercially available, for example, "Denacol EX-201", "Denacol EX-711", and "Denacol EX-721" (all manufactured by Nagase ChemteX Corporation); "Ogusol EG-280" and "Ogusol CG-400" (both manufactured by Osaka Gas Chemical Co., Ltd.); "EXA-80CRP" and "HP4032D" (both manufactured by DIC Corporation); "jER828" and "jER828EL" (both manufactured by Mitsubishi Chemical Corporation); Examples include "Adeka Resin EP-4100", "Adeka Resin EP-4100G", "Adeka Resin EP-4100E", "Adeka Resin EP-4100L", "Adeka Resin EP-4100TX", "Adeka Resin EP-4000", "Adeka Resin EP-4005", "Adeka Resin EP-4901", and "Adeka Resin EP-4901E" (all manufactured by ADEKA Corporation). 【0096】 As specific examples of amine (B), the structures of amines (B-1) to (B-46) are shown in Tables 2-1 to 2-2. 【0097】 【0098】 【0099】 The structures of specific polyfunctional epoxy compounds (C-1) to (C-34) are shown in Tables 3-1 to 3-3. 【0100】 【0101】 【0102】 【0103】 <Support> The support is a solid material that supports compound (A) represented by general formula (1), and any material that can withstand the conditions for carbon dioxide separation and recovery may be used. For example, ceramics, porous materials, carbon materials, resin materials, etc. can be used. Specifically, examples include silica, silica-alumina, alumina, zeolite, zeolite-related compounds, magnesia, titanium dioxide, calcium silicate, carbon nanotubes, activated carbon, polymethyl methacrylate, zirconia, natural minerals, waste solids, carbon molecular sieves, etc. The support may be used alone or in combination of two or more types. Examples of the above-mentioned waste solids include waste containing ceramics, porous materials, carbon materials, resin materials, etc. The shape of the support can be appropriately selected according to the application of the carbon dioxide adsorbent, and may be particles, or it may be a structure with multiple through-holes such as a lattice or honeycomb. 【0104】 The support material may be a commercially available product as is, or a support material synthesized by a known method may be used. Examples of commercially available products include mesostructured silica MSU-F from Sigma-Aldrich, SIPERNAT® 50S from Evonik, CARiACT® Q10, Q30, Q50 from Fuji Silysia Chemical Co., Ltd., and cordierite support material Celcor® from Corning. 【0105】 The support material is preferably porous with a large specific surface area and pore volume in order to support a large amount of polyamine. The specific surface area (BET) is 50 m². 2 / g or more 2000m 2 Less than / g is preferable, 100m 2 / g or more 1000m2 A value of less than / g is preferable. The pore volume should be 0.1 cm³. 2 / g or more 2.3cm 2 A value of less than / g is preferable, and 0.7 cm. 2 / g or more 2.3cm 2 A value of less than / g is preferable. 【0106】 Specific surface area and pore volume can be measured, for example, using a specific surface area / pore diameter distribution analyzer (BELSORP: manufactured by Microtrac-Bell Co., Ltd.) with a constant volume method. A more specific method for measuring gas adsorption using a specific surface area / pore diameter distribution analyzer involves, for example, pre-treating the sample by heating and vacuum evacuation, and weighing approximately 0.1 g of the sample into a sample tube. Then, the sample is heated to 100°C, vacuum evacuation is performed for 4 hours, and the sample is cooled to room temperature before weighing the sample mass. For measurement, the liquid nitrogen temperature is set and the pressure range is specified. Specific surface area, pore volume, and pore diameter can be calculated by analyzing the obtained nitrogen adsorption isotherm. 【0107】 <Carbon Dioxide Adsorbent> A carbon dioxide adsorbent is a compound (A) represented by formula (1) supported on a support. The carbon dioxide adsorbent contains an amine (A) and a support on which it is supported. 【0108】 A carbon dioxide adsorbent can be manufactured by a manufacturing method comprising the steps of preparing compound (A) and obtaining the carbon dioxide adsorbent. In the step of obtaining the carbon dioxide adsorbent, compound (A) can be brought into contact with a support to produce a carbon dioxide adsorbent that supports amine (A). 【0109】 Amine (A) can be produced, for example, by mixing a support with a solution of amine (A), stirring at room temperature, and then distilling off the solvent (e.g., alcohol). Methods for distilling off the solvent include, for example, heating under reduced pressure using an evaporator. 【0110】The amine (B) and the polyfunctional epoxy compound (C) can be reacted separately to obtain amine (A) after the solvent has been removed. For example, the polyfunctional epoxy compound (C) and amine (B) can be added sequentially to a dispersion of the support while stirring to disperse the amino compound (A) on the support and form an adsorbent. Alternatively, the reaction product of amine (B) and polyfunctional epoxy compound (C) can be added directly to the support suspension while still in the reaction solution. 【0111】 Furthermore, if the polyfunctional epoxy compound is in liquid form, it can be used without dissolving it in a solvent. 【0112】 The present invention can be applied to pressure swing and temperature swing methods, which are not applicable to liquid carbon dioxide adsorbents, by supporting compound (A) on a support. The pressure swing method includes the step of placing the carbon dioxide adsorbent under reduced pressure conditions to desorb carbon dioxide. The temperature swing method includes the step of heating the carbon dioxide adsorbent to desorb carbon dioxide. 【0113】 The carbon dioxide adsorbent may further include a binder for granulating amine (A). That is, the carbon dioxide adsorbent may include amine (A) as a granule with a binder and a support. By granulating amine (A) with a binder, vibration resistance and abrasion resistance can be imparted, and stability in water can be further improved. 【0114】As the binder, at least one selected from the group consisting of silica, alumina, silica-alumina, clay minerals, fluororesins, cellulose derivatives, and epoxy resins may be used. Examples of fluororesins include polytetrafluoroethylene. Examples of cellulose derivatives include hydroxypropyl methylcellulose, methylcellulose, hydroxypropylcellulose, carboxymethylcellulose, hydroxyethylcellulose, and hydroxyethylated starch. Examples of epoxy resins include diglycerol polyglycidyl ether and sorbitol polyglycidyl ether, which may be used as a mixture with an epoxy resin curing agent (modified polyamide resin, etc.). Other polymers (polyvinyl alcohol, polyethylene oxide, sodium polyacrylate, polyacrylamide, etc.) may also be used. These compounds are commercially available or can be easily manufactured by known methods. The binder may be used alone or in combination of two or more types. 【0115】 As binders, commercially available products such as Snowtec 30 and AS-200 from Nissan Chemical Corporation, Polyflon PTFE D-210C from Daikin Industries, Ltd., NEOVISCO MC RM4000 from Sansho Co., Ltd., AQ Nylon P-70 from Toray Industries, Inc., and Denacol EX-421 from Nagase ChemteX Corporation can be used. 【0116】 The content of the carbon dioxide adsorbent in the binder is not particularly limited as long as it is in an amount that allows for granulation, but it is preferable that it be in a small amount in order to prevent a decrease in the content of amine compound (A). 【0117】 When granulation is performed using a binder, the average particle size of the granulated material is preferably 0.1 mm to 2.0 mm, from the viewpoint of reducing pressure loss when gas is supplied to the adsorbent-packed bed. 【0118】The content of amine (A) in the carbon dioxide adsorbent is not particularly limited, but from the viewpoint of efficiently separating and recovering carbon dioxide, the content of amine (A) is preferably, for example, 5% by mass or more and 70% by weight or less, based on the total mass of the carbon dioxide adsorbent, and is particularly preferably 20% by mass or more and 70% by weight or less. 【0119】 <Methods for Separating or Recovering Carbon Dioxide> The target of carbon dioxide separation (recovery) methods is gas containing carbon dioxide. Gas containing carbon dioxide may include, for example, exhaust gases emitted from thermal power plants that use coal, heavy oil, natural gas, etc. as fuel, blast furnaces in steel mills that reduce iron oxide with coke, converters in steel mills that burn carbon in pig iron to produce steel, boilers in various manufacturing plants, kilns in cement plants, etc., as well as exhaust gases emitted from transportation equipment such as automobiles, ships, and aircraft that use gasoline, heavy oil, light oil, etc. as fuel. Gas containing carbon dioxide may also include gases containing carbon dioxide emitted in enclosed spaces such as submersible research vessels, space stations, buildings, offices, etc., due to human respiration or energy conversion by equipment. It may also be carbon dioxide in the atmosphere. 【0120】 The method for separating or recovering carbon dioxide according to this disclosure is characterized by the use of a carbon dioxide adsorbent. 【0121】 The carbon dioxide separation (recovery) method includes a first step of bringing the gas to be treated into contact with a carbon dioxide adsorbent to absorb carbon dioxide, and a second step of decarbonizing the carbon dioxide from the carbon dioxide adsorbent that absorbed carbon dioxide in the first step. 【0122】 The carbon dioxide content and temperature of the gas to be treated in the first step are not particularly limited, as long as the carbon dioxide adsorbent can withstand the conditions. For example, the partial pressure of carbon dioxide may be 100 kPa or less, and the temperature may be 10°C to 60°C. Specifically, examples include operating conditions expected in thermal power plants, etc. (partial pressure of carbon dioxide: 7 to 100 kPa, temperature: 40 to 60°C) and operating conditions expected in space stations, etc. (partial pressure of carbon dioxide: 0 to 1 kPa, temperature: 20 to 25°C). The gas to be treated may be at atmospheric pressure or pressurized. 【0123】The gas to be processed in the first step may contain water vapor. Since the carbon dioxide adsorbent has excellent carbon dioxide adsorption properties even when the gas to be processed contains water vapor, the dehumidification operation can be omitted. 【0124】 Methods for removing carbon dioxide in the second step include (a) a step of removing carbon dioxide by placing the carbon dioxide adsorbent under reduced pressure conditions (pressure swing method), (b) a step of removing carbon dioxide by contacting the carbon dioxide adsorbent with at least one of water vapor and an inert gas (preferably a gas that does not contain carbon dioxide (or a gas with a low carbon dioxide content)), and (c) a step of removing carbon dioxide by heating the carbon dioxide adsorbent (temperature swing method). 【0125】 In the method including step (a), it is preferable to reduce the pressure to about 0.2 Pa in terms of the amount of carbon dioxide desorbed and the stability of the carbon dioxide adsorbent. The carbon dioxide adsorbent or the container containing it may be heated when the pressure is reduced. When heating, the temperature should preferably be up to about 60°C, and in this case, it is preferable to reduce the pressure to about 0.5 Pa. The method including step (A) is suitable when the gas to be treated has a temperature of 20 to 60°C and a carbon dioxide partial pressure of 100 kPa or less. 【0126】 In the method including step (B), for example, carbon dioxide partial pressure can be reduced and carbon dioxide can be desorbed by bringing an inert gas, water vapor, or a gas that does not contain carbon dioxide into contact with the carbon dioxide adsorbent. The gas to be brought into contact with the carbon dioxide adsorbent can be any gas in which the carbon dioxide adsorbent is stable, and inert gases such as argon, nitrogen, and water vapor are preferred, with depressurized water vapor being more preferred. 【0127】 In the method including step (C), carbon dioxide can be desorbed by raising the temperature above the temperature at which it was absorbed. In this case, the temperature at which carbon dioxide was absorbed may be, for example, 10 to 40°C, and the temperature at which carbon dioxide was desorbed may be, for example, around 60°C. 【0128】The carbon dioxide adsorbent in this embodiment, amine (A) represented by formula (1), and the support are also excellent at absorbing hydrogen sulfide in addition to carbon dioxide. 【0129】 The carbon dioxide adsorbent according to this embodiment will be described in more detail below with reference to examples. However, this disclosure is not limited to these examples. The carbon dioxide adsorbent according to the present invention can be easily prepared in two steps. 【0130】 Step 1: Preparation of amine (A) [Synthesis Example 1: Amine (A-1)] 【0131】 【0132】 Under a nitrogen atmosphere, 5.0 g (111.0 mmol) of ethylamine (B-1) mixed with 50 ml of methanol and 9.67 g (55.5 mmol) of ethylene glycol diglycidyl ether (C-1) were added, and the mixture was stirred. After addition, the mixture was stirred at room temperature for 24 hours, and the reaction was confirmed to have progressed by gas chromatography (GC) when ethylamine (B-1) was not detected. The solvent methanol was removed by reducing the pressure at a temperature below 40°C to obtain the target product, amine (A-1). 【0133】 [Synthesis Examples 2-102] Except that the starting materials amine (B) and polyfunctional epoxy compound (C) were appropriately changed to the amines listed in Tables 2-1 to 2-2 and the polyfunctional epoxy compounds listed in Tables 3-1 to 3-3 in the same manner as in Synthesis Example 1, amine (A) listed in Tables 4-1 to 4-3 was synthesized. The symbols of the amine compounds in Tables 4-1 to 4-3 correspond to those listed in Tables 1-1 to 1-17. 【0134】[Synthesis Example 103: Compound of Comparative Example 5] (Modified product of pentaethylenehexamine and monofunctional epoxy compound) 10 g of pentaethylenehexamine (0.043 mol) was dissolved in 40 ml of water. 5 g of propylene oxide (0.086 mol) was taken out and then added dropwise to the pentaethylenehexamine solution. The mixture was stirred at room temperature for 20 hours. Then the temperature was raised to 60°C and maintained at that temperature for 2 hours. The water was removed using a rotary evaporator, and then the target product was obtained by vacuum (<1 mmHg) overnight. 【0135】 [Synthesis Example 104: Compound of Comparative Example 6] (Modified product of polyethyleneimine and monofunctional epoxy compound) 10 g of polyethyleneimine (PEI: MW800, manufactured by Aldrich) (0.013 mol) was dissolved in 40 ml of water. 1.03 g (0.0065 mol) of hexaethyl glycidyl ether was taken out and then added dropwise to the polyethyleneimine solution. The mixture was stirred at room temperature for 20 hours. The temperature was then raised to 60°C and maintained at that temperature for 2 hours. The water was removed using a rotary evaporator, and then the mixture was subjected to vacuum (<1 mmHg) overnight to obtain the target product. 【0136】 [Synthesis Example 105: Compound of Comparative Example 7] (Modified product of triethylenetetramine and a bifunctional epoxy compound) 7.6 g (0.052 mol) of triethylenetetramine (TETA, manufactured by Sigma-Aldrich) was dissolved in 60 ml of methanol. Next, 0.60 g (0.0042 mol) of 1,7-octadiene diepoxide (ODE, manufactured by Tokyo Chemical Industry Co., Ltd.) and 0.15 g (0.0004 mol) of 1,3-bis(N,N-diglycidylaminomethyl)cyclohexane (TETRAD-C, manufactured by Mitsubishi Gas Chemical Co., Ltd.) were prepared as epoxy monomers and added dropwise to the triethylenetetramine solution. These mixtures were stirred at room temperature for 20 hours. Then, the temperature was raised to 50°C and maintained at that temperature for 2 hours. Methanol was removed using a rotary evaporator, and then the target product was obtained by vacuum (<1 mmHg) overnight. 【0137】Step 2: Preparation of carbon dioxide adsorbent [Example 1: Adsorbent (1)] Adsorbent (1), composed of 30% by mass of amine (A-1) and 70% by mass of silica gel as a support, was prepared as follows. 3.0 g of (A-1) obtained in Synthesis Example 1 was weighed and dissolved in 20.0 g of methanol solution weighed into a 200 ml flask. Then, 7.0 g of silica gel Q50 (CARiACT Q50 manufactured by Fuji Silicia Chemical Co., Ltd., with a specific surface area of ​​80 m²) was weighed and dissolved. 2 A solution containing (A-1) (1 / g, average pore size 30 nm, pore volume 1.0 ml / g) was placed in a round-bottom flask and stirred at room temperature for 2 hours. Then, the methanol solvent was removed by heating it to 40°C in a rotary evaporator while reducing the pressure in the system to 0.03 MPa. Subsequently, the mixture was vacuum-dried overnight at a vacuum degree of <1 mmHg and a temperature of 60°C to obtain an adsorbent (1) containing 30% by mass of (A-1). 【0138】 [Examples 2-113, Comparative Examples 1-7] Carbon dioxide adsorbents (2) to (120) were prepared in the same manner as in Example 1, except that the amine compound and support were changed to the combinations shown in Tables 4-1 to 4-3. 【0139】 【0140】 【0141】 【0142】 [Materials used for evaluation] To simplify notation, the following abbreviations were used: PEI: Polyethyleneimine (Mw = 600) Q10: Silica gel (CARiACT Q10 manufactured by Fuji Silicia Chemical Co., Ltd., specific surface area 300 m²) 2 ( / g, pore volume 1.0 ml / g) Q30: Silica gel (CARiACT Q30 manufactured by Fuji Silicia Chemical Co., Ltd., specific surface area 100 m²) 2 ( / g, pore volume 1.0 ml / g) Q50: Silica gel (CARiACT Q50 manufactured by Fuji Silicia Chemical Co., Ltd., specific surface area 80 m²) 2( / g, pore volume 1.0 ml / g) Celcor: Cordillerite carrier (Celcor manufactured by Corning, total volume: 0.0303 L (diameter 24 mm, length 67 mm, cylindrical), number of cells: 400 cells per square inch of cross-sectional area) 【0143】 [Method for measuring the absorption and release of carbon dioxide gas] 1.5 g of the adsorbent (1) prepared in Example 1 was filled into a temperature-controllable, gas-permeable glass cell, and the cell was evacuated at 100°C for 30 minutes using a vacuum pump at approximately 0.8 kPa to desorb carbon dioxide and water present in the adsorbent. After this pretreatment, the glass cell was placed in a water bath maintained at a constant temperature of 25°C, and adsorption measurements were performed. For absorption measurements, a carbon dioxide concentration meter equipped with an IR detector (consisting of a carbon dioxide concentration sensor (VAISALA, (GMP252)) and an indicator (VAISALA, (M-170))) was installed at the inlet and outlet of the glass cell, respectively. Compressed air (CO2: 400 ppm) was flow-controlled using a mass flow controller and the gas flow rate (6 L / min) was passed through the glass cell as a simulated gas. Immediately, the carbon dioxide concentration at the gas outlet decreased to less than 10 ppm, suggesting that carbon dioxide was essentially completely adsorbed from the air. Subsequently, a carbon dioxide concentration meter was used to record the carbon dioxide concentration as a function of time. Initially, the carbon dioxide concentration was close to 0 ppm, and then the carbon dioxide concentration at the outlet began to increase. Measurements were taken until the carbon dioxide concentration at the outlet reached a value close to the concentration reading on the carbon dioxide concentration meter at the inlet (until adsorption saturated). The total adsorption amount was calculated as the amount of carbon dioxide adsorbed per gram of carbon dioxide adsorbent (molecule·g) over the time until adsorption saturated. 【0144】Next, while operating a vacuum pump (100 kPa) installed outside the carbon dioxide concentration meter on the outlet side, the water bath containing the adsorbent was heated until the temperature of the glass cell reached 70°C, and carbon dioxide was desorbed from the adsorbent while flowing nitrogen gas at 10 ml / min. The carbon dioxide concentration was recorded as a function of time using the carbon dioxide concentration meter. Measurements were continued until the carbon dioxide concentration increased to a value exceeding 10,000 ppm due to heating, and then until the carbon dioxide concentrations at the cell outlet and inlet asymptotically approached each other. From the obtained results, the total release amount was calculated as the amount of carbon dioxide adsorbed per gram of carbon dioxide adsorbent (mol / g) during the time until asymptotic approaches were reached. 【0145】 [Measurement of Carbon Dioxide Absorption and Release] The amount of carbon dioxide absorption and release was measured using the method described above. For adsorbent (1) in Example 1, the amount of carbon dioxide absorbed per unit weight of adsorbent per hour was 1.23 mmol / g. On the other hand, the amount of carbon dioxide released per unit weight of adsorbent per hour was 1.22 mmol / g. The results of similar measurements for adsorbents (2) to (120) are shown in Tables 4-1 to 4-4. 【0146】 Based on the calculated carbon dioxide gas adsorption amount, the following criteria were established and evaluated, with S, A, and B being the usable ranges. S: Adsorption amount of 1.3 mmol / g or more A: Adsorption amount of 1.0 mmol / g or more and less than 1.3 mmol / g B: Adsorption amount of 0.7 mmol / g or more and less than 1.0 mmol / g C: Adsorption amount of less than 0.7 mmol / g 【0147】 Based on the calculated desorption amounts of carbon dioxide gas, the following criteria were established and evaluated, with S, A, and B being considered as usable ranges. S: Desorption amount of 1.3 mmol / g or more A: Desorption amount of 1.0 mmol / g or more and less than 1.3 mmol / g B: Desorption amount of 0.7 mmol / g or more and less than 1.0 mmol / g C: Desorption amount of less than 0.7 mmol / g 【0148】[Method for Evaluating the Adsorption Rate of Carbon Dioxide Gas] The adsorption rate was evaluated using the adsorbents described in Tables 4-1 to 4-3. Similar to the method for measuring the amount of carbon dioxide gas adsorbed described above, the adsorbents were filled into temperature-controllable, gas-permeable glass cells, and the cells were evacuated at 100°C for 30 minutes using a vacuum pump at approximately 0.8 kPa to desorb the carbon dioxide and water present in the adsorbent. After this pretreatment, the glass cells were placed in a water bath maintained at a constant temperature of 25°C, and compressed air (CO2: 400 ppm) was flown into the glass cells at a flow rate of 6 L / min using a mass flow controller, with the flow rate controlled by the mass flow controller. The amount of carbon dioxide gas adsorbed at this time (amount of carbon dioxide adsorbed in 10 minutes (mol / g)) was measured using a gas flow meter and a carbon dioxide concentration meter. The absorption rate (g / L / min) was defined as the value obtained by dividing this adsorption amount by 10. 【0149】 The evaluation criteria were as follows, with S, A, and B being the usable range. S: Adsorption rate of 0.10 mmol / g / min or higher A: Adsorption rate of 0.07 mmol / g / min or higher but less than 0.10 mmol / g / min B: Adsorption rate of 0.03 mmol / g / min or higher but less than 0.07 mmol / g / min C: Adsorption rate less than 0.03 mmol / g / min 【0150】 [Thermal Oxidation Resistance] For the samples in Examples 1 to 113 and Comparative Examples 1 to 7 in which the absorption and release of carbon dioxide gas was measured, the adsorbent was left in a hot air oven at 70°C for 24 hours in an air environment. Then, the same sample was used again, and an absorption and release test was performed in the same manner as the method for measuring the absorption and release of carbon dioxide gas described above, and the amount of CO2 absorbed after exposure in an air and heated environment was measured. From the results, the thermal oxidation resistance of the adsorbent was evaluated using the following formula: (Formula) Thermal oxidation resistance = Amount of CO2 absorbed by the adsorbent after exposure in an air and heated environment ÷ Amount of CO2 absorbed by the adsorbent before exposure in an air and heated environment The evaluation results are shown in Tables 4-1 to 4-3. 【0151】 Based on the above resistance results, the following criteria were established and evaluated, with S, AA, A, and B being considered as usable ranges. The evaluation results are shown in Tables 4-1 to 4-3. 【0152】S: Thermal oxidation resistance of 0.90 or higher AA: Thermal oxidation resistance of 0.80 or higher but less than 0.90 A: Thermal oxidation resistance of 0.70 or higher but less than 0.80 B: Thermal oxidation resistance of 0.50 or higher but less than 0.70 C: Thermal oxidation resistance less than 0.50 【0153】 As described in the above examples, the carbon dioxide adsorbent of the present invention exhibits superior carbon dioxide absorption and release rates, as well as excellent thermal oxidation resistance, compared to conventionally known carbon dioxide adsorbents. Furthermore, it was found to possess thermal oxidation resistance to the generally known PEI (polyethyleneimine). One possibility is that the amine compound (A) of the present invention, consisting of a polyfunctional epoxy and an amine, reacts to form a structure with multiple ether bonds and hydroxyl groups within the molecule, exhibiting high affinity for support materials such as silica, resulting in excellent supported adsorption, and also exhibiting excellent thermal oxidation resistance due to intramolecular / intermolecular interactions through hydrogen bonding with the amino group. As a result, it is presumed that the amine portion can react with carbon dioxide easily and rapidly, leading to high adsorption and desorption rates. 【0154】 This application claims priority based on Japanese Patent Application No. 2024-215070, filed on 10 December 2024, and incorporates all of its disclosures herein.

Claims

1. A carbon dioxide adsorbent comprising an amine (A) represented by formula (11) and a support. In the formula, R 1 R is a hydrogen atom, an optionally substituted alkyl group, an optionally substituted heterocyclic group, or an optionally substituted cycloalkyl group. 2 A is a hydrogen atom or an alkyl group having 1 to 8 carbon atoms. 1 n1 is an n1-valent organic residue whose terminal is either an oxygen or nitrogen atom, where n1 represents an integer from 2 to 12.

2. The above-mentioned A 1 is the carbon dioxide adsorbent according to claim 1, represented by the following formula (12) or formula (13). [(* -) n2 X 1 -] n A (12) In the formula, X 1 is an oxygen atom or a nitrogen atom, and n2 is 1 when X 1 is an oxygen atom, and n2 is 2 when X 1 is a nitrogen atom. A is an n-valent organic residue, n represents an integer of 2 to 6, and * indicates the bonding position.

3. The carbon dioxide adsorbent according to claim 1, wherein the amine (A) is represented by the following formula (1). In the formula, X is an oxygen atom or -NR 11 - and R 11 is a hydrogen atom, an alkyl group having 1 to 8 carbon atoms, or R 1 R 2 N-CH 2 CH(OH)CH 2 -, where A is an n-valent organic residue, and n represents an integer from 2 to 6.

4. The carbon dioxide adsorbent according to claim 3, wherein X is an oxygen atom.

5. The aforementioned R 1 The carbon dioxide adsorbent according to claim 1, wherein the alkyl group which may have substituents, the heterocyclic group which may have substituents, and the cycloalkyl group which may have substituents contain two or more nitrogen atoms.

6. The aforementioned R 1 The carbon dioxide adsorbent according to claim 1, wherein is represented by the following formula (2) or (3). In the formula, R 3 is a hydrogen atom or a methyl group, p is an integer from 0 to 4, and R 4 and R 6 Each of these is independently a hydrogen atom, a C1-C8 alkyl group, or a hydroxyalkyl group, and R 5 This is a hydrogen atom, an alkyl group having 1 to 8 carbon atoms, a hydroxyalkyl group, or -(CH 2 ) s-R 7 And R 7 is a hydroxyl group, or -N(R 8 ) R 9 And R 8 and R 9 Each of these is independently a hydrogen atom, a methyl group, or a hydroxyalkyl group, q is 2 or 3, r is 2 to 4, s is 2 or 3, and m is 0 to 3.

7. The carbon dioxide adsorbent according to claim 1, wherein the support is at least one selected from the group consisting of silica, silica alumina, alumina, zeolite, zeolite-related compounds, magnesia, titanium dioxide, calcium silicate, carbon nanotubes, activated carbon, polymethyl methacrylate, zirconia, natural minerals, waste solids, and carbon molecular sieves.

8. The carbon dioxide adsorbent according to claim 1, wherein the organic residue in A is one of the following: a linear or branched aliphatic hydrocarbon residue which may have a substituent, a linear or branched alkoxy residue which may have a substituent, a linear or branched polyoxyalkyl residue which may have a substituent, a (meth)acryloyl residue which may have a substituent, an alkyl ester residue which may have a substituent, an aromatic ester residue which may have a substituent, an alicyclic hydrocarbon residue which may have a substituent, an aromatic heterocyclic residue which may have a substituent, and an amino residue which may have a substituent.

9. The aforementioned R 2 The carbon dioxide adsorbent according to claim 1, wherein is a hydrogen atom.

10. The carbon dioxide adsorbent according to claim 1, wherein the content of the amine (A) is 5 to 70% by mass.

11. A method for separating or recovering carbon dioxide, comprising: a first step of contacting a gas to be treated with a carbon dioxide adsorbent described in any one of claims 1 to 10 to absorb carbon dioxide; and a second step of decarbonizing carbon dioxide from the carbon dioxide adsorbent that absorbed carbon dioxide in the first step, wherein the second step comprises one or more of the following steps: (a) placing the carbon dioxide adsorbent under reduced pressure conditions to decarbonize carbon dioxide; (b) contacting the carbon dioxide adsorbent with at least one of water vapor and an inert gas to decarbonize carbon dioxide; and (c) heating the carbon dioxide adsorbent to decarbonize carbon dioxide.