WO2023063050A1 - 酸性ガス吸着材、酸性ガス吸着材を備えた構造体、酸性ガス吸着装置、酸性ガス回収装置、酸性ガス吸着材の製造方法、及びシート状構造体 - Google Patents

酸性ガス吸着材、酸性ガス吸着材を備えた構造体、酸性ガス吸着装置、酸性ガス回収装置、酸性ガス吸着材の製造方法、及びシート状構造体 Download PDF

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WO2023063050A1
WO2023063050A1 PCT/JP2022/035486 JP2022035486W WO2023063050A1 WO 2023063050 A1 WO2023063050 A1 WO 2023063050A1 JP 2022035486 W JP2022035486 W JP 2022035486W WO 2023063050 A1 WO2023063050 A1 WO 2023063050A1
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Prior art keywords
acidic gas
gas adsorbent
polymer
porous sheet
acidic
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PCT/JP2022/035486
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English (en)
French (fr)
Japanese (ja)
Inventor
康壮 松田
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Nitto Denko Corp
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Nitto Denko Corp
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Priority to US18/700,808 priority Critical patent/US20240416319A1/en
Priority to CN202280068560.3A priority patent/CN118159358A/zh
Priority to JP2023555070A priority patent/JP7698727B2/ja
Priority to EP22880746.7A priority patent/EP4417410A4/en
Publication of WO2023063050A1 publication Critical patent/WO2023063050A1/ja
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    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/26—Synthetic macromolecular compounds
    • B01J20/262—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon to carbon unsaturated bonds, e.g. obtained by polycondensation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
    • B—PERFORMING OPERATIONS; TRANSPORTING
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    • B01D—SEPARATION
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    • B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B—PERFORMING OPERATIONS; TRANSPORTING
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    • B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
    • B01D53/0407—Constructional details of adsorbing systems
    • B01D53/0438—Cooling or heating systems
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    • B01J20/30—Processes for preparing, regenerating, or reactivating
    • B01J20/305—Addition of material, later completely removed, e.g. as result of heat treatment, leaching or washing, e.g. for forming pores
    • B01J20/3064—Addition of pore forming agents, e.g. pore inducing or porogenic agents
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    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
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    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
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Definitions

  • the present invention relates to an acidic gas adsorbent, a structure provided with an acidic gas adsorbent, an acidic gas adsorbing device, an acidic gas recovery device, a method for producing an acidic gas adsorbing material, and a sheet-like structure.
  • CCS carbon capture and storage
  • CCU carbon capture and utilization
  • Adsorbents used in adsorption methods can adsorb acid gases, for example, by contact with the atmosphere.
  • Patent Document 1 discloses an adsorbent whose substrate is coated with an amine compound. Specifically, in Patent Document 1, alumina porous particles are supported on a substrate, and the pores of the porous particles are filled with an amine compound.
  • a new acidic gas adsorbent suitable for adsorbing acidic gases is in demand.
  • the present invention comprising a porous sheet containing a polymer,
  • the polymer has an amino group
  • the porous sheet provides an acidic gas adsorbent having a three-dimensional network skeleton composed of the polymer.
  • the present invention the acidic gas adsorbent; a ventilation path; provides a structure with
  • the present invention An adsorption unit having a gas inlet and a gas outlet, The adsorption part provides an acidic gas adsorption device containing the above acidic gas adsorbent.
  • the present invention the acidic gas adsorbent; a media path; with an acidic gas recovery device in which a heat medium for heating the acidic gas adsorbent passes through the medium path during a desorption operation in which the acidic gas adsorbed by the acidic gas adsorbent is desorbed from the acidic gas adsorbent; offer.
  • the present invention A method for producing an acidic gas adsorbent comprising a porous sheet, comprising: A step (I) of curing a mixed liquid containing a compound group containing an amine monomer and a porogen to obtain a cured product; a step (II) of removing the porogen from the sheet-like cured body to obtain the porous sheet; To provide a method for producing an acid gas adsorbent, comprising:
  • the present invention a porous sheet comprising a polymer; a support that supports the porous sheet; with The polymer has an amino group,
  • the porous sheet provides a sheet-like structure having a three-dimensional network skeleton composed of the polymer.
  • a new acidic gas adsorbent suitable for adsorbing acidic gases can be provided.
  • FIG. 4 is a diagram for explaining a method for measuring the amount of carbon dioxide adsorbed by an acidic gas adsorbent;
  • FIG. 4 is a cross-sectional view schematically showing a modified example of the acidic gas adsorbent.
  • 1 is a perspective view schematically showing an example of a structure provided with an acidic gas adsorbent;
  • FIG. 10 is a perspective view schematically showing a modified example of a structure provided with an acidic gas adsorbent
  • FIG. 11 is a perspective view schematically showing another modified example of the structure provided with an acidic gas adsorbent
  • It is a perspective view which shows an example of an acidic gas collection
  • It is a sectional view showing a schematic structure of a modification of an acidic gas collection device.
  • 1 is a scanning electron microscope (SEM) image of a cross section of a porous sheet produced in Example 1.
  • FIG. 4 is a graph showing the results of measuring the amount of carbon dioxide adsorbed by the acidic gas adsorbents of Example 1 and Comparative Examples 1 to 3.
  • FIG. 4 is a graph showing the results of measurement of the amount of carbon dioxide adsorbed by the acidic gas adsorbents of Example 2 and Comparative Examples 4 to 6.
  • SEM scanning electron microscope
  • the acidic gas adsorbent according to the first aspect of the present invention is comprising a porous sheet containing a polymer,
  • the polymer has an amino group
  • the porous sheet has a three-dimensional network skeleton composed of the polymer.
  • the porous sheet includes continuous pores formed continuously in a three-dimensional shape.
  • the porous sheet contains the polymer as a main component.
  • the amino group contains a secondary amino group.
  • the polymer is an epoxy polymer containing structural units derived from amine monomers.
  • the polymer has a glass transition temperature of 40°C or lower.
  • the porous sheet has a specific surface area of 1.0 m 2 /g or more.
  • the porosity of the porous sheet is 20% or more.
  • the acidic gas adsorbent according to any one of the first to eighth aspects further comprises a support that supports the porous sheet.
  • the acidic gas adsorbent according to any one of the first to ninth aspects is carbon dioxide, nitrogen, and water vapor when contacted for 15 hours with a mixed gas.
  • the carbon adsorption amount is 0.1 mmol/cm 3 or more.
  • the concentration of carbon dioxide in the mixed gas is 400 volppm
  • the mixed gas has a temperature of 20° C. and a humidity of 50% RH.
  • the acidic gas adsorbent according to any one of the first to tenth aspects has a flat plate shape or a corrugated shape.
  • the structure according to the twelfth aspect of the present invention comprises an acidic gas adsorbent according to any one of the first to eleventh aspects; a ventilation path; Prepare.
  • the acidic gas adsorption device comprises: An adsorption unit having a gas inlet and a gas outlet, The adsorption part accommodates an acidic gas adsorbent according to any one of the first to eleventh aspects.
  • the acidic gas recovery device comprises an acidic gas adsorbent according to any one of the first to eleventh aspects; a media path; with A heat medium for heating the acidic gas adsorbent passes through the medium path during a desorption operation for desorbing the acidic gas adsorbed by the acidic gas adsorbent from the acidic gas adsorbent.
  • the medium path penetrates the acidic gas adsorbent in the thickness direction of the acidic gas adsorbent.
  • the acidic gas recovery device comprises two acidic gas adsorbents, and the medium path is formed between the two acidic gas adsorbents.
  • the cooling medium for cooling the acidic gas adsorbent is in the medium path pass through.
  • the method for producing an acidic gas adsorbent according to the eighteenth aspect of the present invention comprises: A method for producing an acidic gas adsorbent comprising a porous sheet, comprising: A step (I) of curing a mixed liquid containing a compound group containing an amine monomer and a porogen to obtain a cured product; a step (II) of removing the porogen from the sheet-like cured body to obtain the porous sheet; including.
  • the mixed liquid is applied onto a support, and the resulting coating film is cured to form a sheet-like film.
  • the cured body is obtained.
  • the sheet-like structure according to the twentieth aspect of the present invention comprises a porous sheet comprising a polymer; a support that supports the porous sheet; with The polymer has an amino group, The porous sheet has a three-dimensional network skeleton composed of the polymer.
  • the acidic gas adsorbent according to the twenty-first aspect of the present invention is comprising a porous resin sheet containing a polymer,
  • the polymer has amino groups.
  • the sheet-like structure according to the 22nd aspect of the present invention comprises a porous resin sheet containing a polymer; a support for supporting the porous resin sheet; with The polymer has amino groups.
  • the acidic gas adsorbent 10 of this embodiment includes a porous sheet 1 containing a polymer P, and further includes a support 2, for example.
  • the porous sheet 1 is a porous resin sheet containing a polymer P.
  • the polymer P has an amino group, and has a function of adsorbing acid gas due to the amino group.
  • the porous sheet 1 has a three-dimensional mesh skeleton made of polymer P.
  • the porous sheet 1 has a porous structure, and the porous structure contains pores derived from a three-dimensional network skeleton.
  • the pores derived from the three-dimensional network skeleton have a size that can be observed when observed at a magnification of 5000 times using a scanning electron microscope (SEM), for example.
  • the pore diameter (average pore diameter) is preferably 0.1 ⁇ m or more and 5 ⁇ m or less, more preferably 3 ⁇ m or less.
  • the pore diameter is 0.1 ⁇ m or more, there is a tendency that sufficient gas diffusibility within the porous sheet 1 can be ensured.
  • the pore size is 5 ⁇ m or less, the three-dimensional network skeleton in the porous sheet 1 does not become too thick even with a moderate porosity, and the decrease in diffusion rate of acid gas into the polymer P is suppressed.
  • Cheap the three-dimensional network skeleton in the
  • the support 2 supports the porous sheet 1 and is in direct contact with the porous sheet 1.
  • the acidic gas adsorbent 10 provided with the support 2 is suitable for use as a part of an acidic gas recovery device, which will be described later.
  • the acidic gas adsorbent 10 may or may not further include fixing means for fixing the porous sheet 1 and the support 2 together.
  • a specific example of the fixing means is an adhesive, more specifically an adhesive sheet containing an adhesive.
  • the term "adhesive" is used herein to encompass pressure-sensitive adhesives.
  • the acidic gas adsorbent 10 may not include the support 2 and may consist of only the porous sheet 1 . That is, the acidic gas adsorbent 10 may be a self-supporting film (single-layer film) of the porous sheet 1 .
  • the acidic gas adsorbent 10 is typically a sheet-like structure.
  • the acidic gas adsorbent 10 as a sheet-like structure has, for example, a flat plate shape or a corrugated shape.
  • a porous sheet 1 containing a polymer P; a support 2 that supports the porous sheet 1; with Polymer P has an amino group
  • the porous sheet 1 provides a sheet-like structure having a three-dimensional mesh-like skeleton composed of the polymer P.
  • a porous sheet 1 having a porous structure containing pores derived from a three-dimensional network skeleton; a support 2 that supports the porous sheet 1; with The above three-dimensional network skeleton provides a sheet-like structure containing the polymer P having amino groups.
  • the polymer P contains, for example, at least one amino group selected from the group consisting of primary amino groups, secondary amino groups and tertiary amino groups.
  • the polymer P preferably contains at least one selected from the group consisting of a primary amino group and a secondary amino group, and particularly preferably contains a secondary amino group.
  • the amino groups possessed by the polymer P preferably contain secondary amino groups.
  • Polymer P having a secondary amino group also tends to easily desorb adsorbed acidic gases. That is, according to the polymer P having a secondary amino group, the regeneration treatment of the acidic gas adsorbent 10 can be performed under relatively mild conditions.
  • the polymer P may contain a tertiary amino group, but may not contain a tertiary amino group.
  • the weight ratio of the nitrogen element in the polymer P is, for example, 5 wt% or more, preferably 10 wt% or more. The higher the weight ratio, the more the acidic gas adsorbing property of the acidic gas adsorbent 10 tends to improve.
  • the upper limit of the weight ratio of the nitrogen element in the polymer P is not particularly limited, and is, for example, 30 wt%.
  • the weight ratio of the nitrogen elements can be regarded as the weight ratio of the amino groups in the polymer P.
  • the density of amino groups in the polymer P is, for example, 1 mmol/g or more, preferably 5 mmol/g or more, more preferably 10 mmol/g or more.
  • the upper limit of the density of amino groups is not particularly limited, and is, for example, 30 mmol/g.
  • the density of amino groups in the polymer P means the substance amount of amino groups contained in 1 g of the polymer P.
  • the polymer P may contain functional groups other than amino groups.
  • Other functional groups include, for example, hydroxyl groups, ether groups, ester groups, amide groups, and the like.
  • the polymer P is, for example, an epoxy polymer containing a structural unit U1 derived from an amine monomer.
  • This epoxy polymer is preferably at least one selected from the group consisting of, for example, a polymer P1 of a monomer group containing an amine monomer and an epoxy monomer, and a reactant P2 of a compound group containing an amine monomer and an epoxy prepolymer. is the polymer P1.
  • a specific example of the reactant P2 is a product obtained by cross-linking an epoxy prepolymer with an amine monomer (cross-linked product).
  • the group of monomers for forming the polymer P1 includes amine monomers and epoxy monomers, and is preferably composed only of these monomers. That is, polymer P1 is preferably a polymer of amine monomers and epoxy monomers.
  • An amine monomer is a monomer containing at least one amino group, for example, at least one primary amino group.
  • the number of primary amino groups contained in the amine monomer is preferably 2 or more, may be 3 or more, or may be 4 or more.
  • the upper limit of the number of primary amino groups is not particularly limited, and is, for example, 30, and may be 10.
  • the amine monomer may contain a secondary amino group or a tertiary amino group in addition to the primary amino group, but may contain no tertiary amino group.
  • the molecular weight of the amine monomer is not particularly limited.
  • amine monomers examples include ethylamine, ethylenediamine, 1,4-butylenediamine, 1,5-pentanediamine, 1,6-hexanediamine, 1,7-heptanediamine, 1,8-octanediamine, diethylenetriamine, and triethylene.
  • Amine monomers may optionally be aliphatic polyamidoamines, including polyamines and dimer acids.
  • the amine monomer is an aliphatic amine, especially triethylenetetramine (TETA).
  • TETA triethylenetetramine
  • An amine monomer can be used individually or in combination of 2 or more types.
  • An epoxy monomer is a monomer containing at least one epoxy group.
  • the number of epoxy groups contained in the epoxy monomer is preferably 2 or more, may be 3 or more, or may be 4 or more.
  • the upper limit of the number of epoxy groups contained in the epoxy monomer is not particularly limited, and is 10, for example.
  • the molecular weight of the epoxy monomer is not particularly limited, and is, for example, less than 1000, preferably 500 or less.
  • epoxy monomers examples include n-butyl glycidyl ether, higher alcohol glycidyl ether, allyl glycidyl ether, 2-ethylhexyl glycidyl ether, phenyl glycidyl ether, cresyl glycidyl ether, p-sec-butylphenyl glycidyl ether, t-butylphenyl monofunctional epoxy compounds such as glycidyl ether; diepoxyalkanes such as 1,5-hexadiene diepoxide, 1,7-octadiene diepoxide and 1,9-decadiene diepoxide; (poly)ethylene glycol diglycidyl ether, ( poly) Ethers such as propylene glycol diglycidyl ether, 1,4-butanediol diglycidyl ether, neopentyl glycol diglycidyl ether, 1,6-hex
  • Epoxy monomers are preferably ether group-containing polyfunctional epoxy compounds such as ethylene glycol diglycidyl ether (EDE) and pentaerythritol tetraglycidyl ether (PETG).
  • EEE ethylene glycol diglycidyl ether
  • PETG pentaerythritol tetraglycidyl ether
  • An epoxy monomer can be used individually or in combination of 2 or more types. When using a monofunctional epoxy compound, it is preferable to use it in combination with another epoxy monomer containing two or more epoxy groups.
  • a monofunctional epoxy compound can also be utilized as a reactive diluent to adjust the viscosity of the monomer group to form the polymer P1.
  • Amine monomers for forming reactant P2 include those described above for polymer P1.
  • the epoxy prepolymer contains, for example, at least one epoxy group.
  • the number of epoxy groups contained in the epoxy prepolymer is preferably 2 or more, may be 3 or more, or may be 4 or more.
  • the upper limit of the number of epoxy groups contained in the epoxy prepolymer is not particularly limited, and is 100, for example.
  • the weight average molecular weight of the epoxy prepolymer is not particularly limited, and is, for example, 1,000 to 50,000.
  • Epoxy prepolymers include, for example, aromatic epoxy resins and non-aromatic epoxy resins.
  • Aromatic epoxy resins include polyphenyl-based epoxy resins, epoxy resins containing fluorene rings, epoxy resins containing triglycidyl isocyanurate, and epoxy resins containing heteroaromatic rings (eg, triazine rings).
  • Polyphenyl-based epoxy resins include bisphenol A type epoxy resin, brominated bisphenol A type epoxy resin, bisphenol F type epoxy resin, bisphenol AD type epoxy resin, stilbene type epoxy resin, biphenyl type epoxy resin, bisphenol A novolak type epoxy resin.
  • Non-aromatic epoxy resins include aliphatic glycidyl ether type epoxy resins, aliphatic glycidyl ester type epoxy resins, alicyclic glycidyl ether type epoxy resins, alicyclic glycidyl amine type epoxy resins, and alicyclic glycidyl ester type epoxy resins. etc.
  • An epoxy prepolymer can be used individually or in combination of 2 or more types.
  • the polymer P as an epoxy polymer contains a structural unit U1 derived from an amine monomer.
  • the polymer P further contains a structural unit U2 derived from an epoxy monomer.
  • the content of the structural unit U1 in the polymer P, particularly the polymer P1 is, for example, 30 wt% or more, preferably 50 wt% or more.
  • the upper limit of the content of the structural unit U1 is not particularly limited, and is, for example, 80 wt%.
  • the content of the structural unit U2 in the polymer P, particularly the polymer P1, is, for example, 20 wt% to 70 wt%.
  • the blending ratio of the amine monomer and the epoxy monomer or epoxy prepolymer is the epoxy group contained in the epoxy monomer or epoxy prepolymer with respect to the active hydrogen equivalent of the primary amino group contained in the amine monomer. is preferably 1 or less, preferably 0.9 or less, and more preferably 0.5 or less.
  • the glass transition temperature Tg of the polymer P is not particularly limited, and is, for example, 40° C. or lower, preferably 30° C. or lower, more preferably 20° C. or lower, and still more preferably 15° C. or lower.
  • the acidic gas adsorbent 10 can be regenerated under relatively mild conditions, such as heat treatment at a low temperature.
  • the lower limit of the glass transition temperature Tg of the polymer P is, for example, ⁇ 100° C., preferably ⁇ 50° C., from the viewpoint of sufficiently securing the acid gas adsorbability of the acid gas adsorbent 10 and from the viewpoint of heat resistance. , more preferably -10°C.
  • the glass transition temperature Tg means a midpoint glass transition temperature (T mg ) determined according to JIS K7121:1987.
  • the polymer P usually corresponds to a thermosetting resin.
  • Polymer P is, for example, solid at 25°C, preferably in the range from 25°C to 80°C.
  • the weight average molecular weight of the polymer P is not particularly limited, and is, for example, 500 or more, preferably 1000 or more, more preferably 10000 or more, still more preferably 100000 or more.
  • the upper limit of the weight average molecular weight of polymer P is, for example, 10,000,000.
  • the porous sheet 1 contains, for example, polymer P as a main component.
  • the term “main component” means the component contained in the porous sheet 1 in the largest amount by weight.
  • the content of the polymer P in the porous sheet 1 is, for example, 50 wt% or more, preferably 70 wt% or more, more preferably 90 wt% or more, and may be 95 wt% or more, or 99 wt% or more.
  • the porous sheet 1 may be substantially composed of the polymer P only. There is a tendency that the higher the content of the polymer P, the more the acidic gas adsorbing property of the acidic gas adsorbent 10 improves.
  • the porous sheet 1 may be substantially composed only of the polymer P, but may further contain materials other than the polymer P. Other materials include, for example, reaction accelerators, plasticizers, fillers, pigments, dyes, antioxidants, conductive materials, antistatic agents, ultraviolet absorbers, flame retardants, antioxidants, and the like.
  • the porous sheet 1 preferably does not contain, for example, other materials such as porous particles such as alumina and a binder for binding the porous particles together.
  • reaction accelerator is used, for example, when synthesizing polymer P.
  • reaction accelerators include tertiary amines such as triethylamine and tributylamine; imidazoles such as 2-phenol-4-methylimidazole, 2-ethyl-4-methylimidazole, and 2-phenol-4,5-dihydroxyimidazole. is mentioned. These reaction accelerators can accelerate the reaction for synthesizing the polymer P1, for example.
  • fillers include fibers and fiber structures containing fibers.
  • Fibers include, for example, glass fibers; natural fibers such as wood pulp, cotton, and hemp (for example, Manila hemp); polyester fibers, rayon, vinylon, acetate fibers, polyvinyl alcohol (PVA) fibers, polyamide fibers, polyolefin fibers, polyurethane fibers, etc. of chemical fibers (synthetic fibers).
  • Textile structures include woven fabrics, non-woven fabrics, and paper.
  • a specific example of the fibrous structure is glass paper.
  • the porous sheet 1 contains a fibrous structure as a filler
  • the three-dimensional network skeleton containing the polymer P and the fibrous structure may exist independently in the porous sheet 1.
  • the porous structure of the porous sheet 1 further has pores derived from the fiber structure together with pores derived from the three-dimensional network skeleton containing the polymer P, for example.
  • the porous sheet 1 it can be considered that the three-dimensional network skeleton containing the polymer P and the fiber structure are combined.
  • the fibrous structure as a filler preferably has a high tensile strength from the viewpoint of suppressing the dimensional change of the porous sheet 1 .
  • the fiber structure preferably has a tensile strength STD of 1 MPa or more as measured in Test 1 below.
  • Test 1 A fiber structure is cut into a width of 10 mm and a length of 100 mm to obtain a test piece. At this time, the longitudinal direction of the test piece is aligned with the TD direction (transverse direction) of the fiber structure.
  • a test piece is set in a tensile tester, and a tensile test is performed under conditions of a distance between chucks of 20 mm and a tensile speed of 100 mm/min. Determine the tensile strength STD when the specimen is elongated by 3%.
  • the tensile strength STD of the fiber structure is more preferably 2 MPa or more, and may be 3 MPa or more, 4 MPa or more, 5 MPa or more, 6 MPa or more, 7 MPa or more, or even 8 MPa or more.
  • the upper limit of the tensile strength STD is not particularly limited, and is, for example, 30 MPa.
  • the fiber structure has a tensile strength SMD of 1 MPa or more, measured by the same method as in Test 1 above, except that the longitudinal direction of the test piece matches the MD direction (machine direction) of the fiber structure. is preferred.
  • the tensile strength SMD is more preferably 2 MPa or more, and may be 5 MPa or more, 8 MPa or more, 10 MPa or more, 11 MPa or more, or even 12 MPa or more.
  • the upper limit of the tensile strength SMD is not particularly limited, and is, for example, 30 MPa.
  • the density d of the nitrogen element in the porous sheet 1 is not particularly limited, and is, for example, 1 mmol/g or more, preferably 5 mmol/g or more, more preferably 10 mmol/g or more.
  • the upper limit of the density d of the nitrogen element is not particularly limited, and is, for example, 30 mmol/g.
  • the density d of the nitrogen elements can be regarded as the density of amino groups in the porous sheet 1 .
  • the amount of amino group substance per unit volume of the porous sheet 1 is, for example, 4.0 mmol/cm 3 or more, 4.3 mmol/cm 3 or more, 4.5 mmol/cm 3 or more, or 5.0 mmol/cm 3 or more. , 6.0 mmol/cm 3 or more, 7.0 mmol/cm 3 or more, or even 8.0 mmol/cm 3 or more.
  • the upper limit of the amount of this amino group substance is not particularly limited, and is, for example, 20 mmol/cm 3 .
  • the weight ratio of the nitrogen element in the porous sheet 1 is, for example, 5 wt% or more, preferably 10 wt% or more. The higher the weight ratio, the more the acidic gas adsorbing property of the acidic gas adsorbent 10 tends to improve.
  • the upper limit of the weight ratio of the nitrogen element in the porous sheet 1 is not particularly limited, and is, for example, 30 wt%.
  • the weight ratio of the nitrogen elements can be regarded as the weight ratio of the amino groups in the porous sheet 1 .
  • the porous sheet 1 has a three-dimensional mesh skeleton made of the polymer P.
  • the three-dimensional network skeleton may contain, for example, the polymer P as a main component and may substantially contain the polymer P only.
  • the three-dimensional network skeleton may further contain components other than the polymer P.
  • the above three-dimensional network skeleton extends continuously.
  • the pores included in the porous sheet 1 are, for example, continuous pores formed continuously in a three-dimensional shape.
  • the porous sheet 1 includes, for example, continuous pores that are continuously formed in a three-dimensional shape.
  • the porous sheet 1 may have independent pores, or may have through-holes penetrating the porous sheet 1 .
  • the porous sheet 1 preferably does not have, for example, fibers containing the polymer P, and is preferably not a nonwoven fabric containing the fibers. That is, in the present embodiment, the porous sheet 1 excludes, for example, a nonwoven fabric having fibers containing the polymer P.
  • the thickness of the porous sheet 1 is not particularly limited, and is, for example, 1000 ⁇ m or less, preferably 500 ⁇ m or less, more preferably 300 ⁇ m or less.
  • a structure with a large cross-sectional area of the ventilation path is suitable for reducing the pressure loss that occurs when it comes into contact with acid gas.
  • the porous sheet 1 tends to have a relatively large amount of amino group substance per unit volume. According to this porous sheet 1, even when the thickness of the sheet 1 is small, there is a tendency that the acid gas can be sufficiently adsorbed.
  • the lower limit of the thickness of the porous sheet 1 is not particularly limited, and is, for example, 10 ⁇ m.
  • the specific surface area of the porous sheet 1 is not particularly limited, and is, for example, 0.1 m 2 /g or more, preferably 1.0 m 2 /g or more, more preferably 2.0 m 2 /g or more.
  • the upper limit of the specific surface area of the porous sheet 1 is not particularly limited, and is, for example, 10 m 2 /g.
  • the specific surface area of the porous sheet 1 means the BET (Brunauer-Emmett-Teller) specific surface area by nitrogen gas adsorption.
  • the BET specific surface area can be measured by a method conforming to JIS Z8830:2013.
  • the porosity of the porous sheet 1 is, for example, 20% or more, preferably 30% or more, more preferably 40% or more.
  • the upper limit of the porosity of the porous sheet 1 is not particularly limited, and is, for example, 80%, and may be 60%.
  • the porosity of the porous sheet 1 can be calculated by the following formula based on the volume V (cm 3 ), weight W (g) and true density D (g/cm 3 ) of the porous sheet 1 . Note that the true density D means the specific gravity of the material forming the porous sheet 1 .
  • Porosity (%) 100 ⁇ (V-(W / D)) / V
  • the porous sheet 1 is suppressed in dimensional change when the acidic gas adsorbent 10 is used, especially when the acidic gas adsorbent 10 comes into contact with water.
  • the porous sheet 1 with suppressed dimensional change tends to be less likely to come off from the support 2 or the acidic gas recovery device when the acidic gas adsorbent 10 is used.
  • the porous sheet 1 is less likely to be deformed when the acidic gas adsorbent 10 is used, and there is also a tendency that gas passage is less likely to be hindered due to deformation.
  • the porous sheet 1 containing a fibrous structure as a filler tends to suppress changes in its dimensions when the acidic gas adsorbent 10 is used.
  • the porous sheet 1 preferably has a dimensional change rate RTD of 5% or less as measured in Test 2 below.
  • Test 2 The porous sheet 1 is cut into a size of 30 mm long and 20 mm wide to obtain a test piece. At this time, the longitudinal direction of the test piece is aligned with the MD direction of the porous sheet 1 (if the fiber structure is included, the MD direction of the fiber structure), and the lateral direction of the test piece is aligned with the TD direction of the porous sheet 1 ( If a fibrous structure is included, match the TD direction of the fibrous structure).
  • the test piece is dried in a vacuum atmosphere at 60° C. for 2 hours. Place the specimen in a dry room with a dew point of about -60°C.
  • the dimensional change rate R TD (%) is calculated from the lateral length L TD1 (mm) of the test piece in the dry state and the lateral length L TD2 (mm) of the test piece in the water-absorbed state.
  • the dimensional change rate RTD of the porous sheet 1 is more preferably 4% or less, and may be 3% or less, 2% or less, 1% or less, or even 0.5% or less.
  • the lower limit of the dimensional change rate RTD is not particularly limited, and is, for example, 0.01%.
  • the porous sheet 1 preferably has a dimensional change rate RMD of 5% or less as measured in Test 2 above.
  • the dimensional change rate R MD of the porous sheet 1 is more preferably 4% or less, and may be 3% or less, 2% or less, or even 1% or less.
  • the lower limit of the dimensional change rate R MD is not particularly limited, and is, for example, 0.01%.
  • the material of the support 2 is not particularly limited, and examples thereof include cordierite, alumina, cordierite- ⁇ alumina, silicon nitride, zircon mullite, spodumene, alumina-silica magnesia, zircon silicate, sillimanite, and magnesium silicate.
  • the material of the support 2 preferably has excellent thermal conductivity and durability, and does not easily deteriorate due to rust generation or hydrolysis when it comes into
  • the support 2 may or may not have a porous structure.
  • Examples of the support 2 having a porous structure include paper, nonwoven fabric, foam, and mesh.
  • Examples of the support 2 having no porous structure include non-porous sheets and foils.
  • the support 2 is preferably an aluminum sheet, paper, non-woven fabric, or the like, from the viewpoint of easily manufacturing the acidic gas adsorbent 10 having a corrugated shape.
  • the support 2 may function as a planar heater, and may be a planar thermoelectric heater or a Peltier element.
  • the thickness of the support 2 is not particularly limited, and is, for example, 1 ⁇ m to 100 ⁇ m.
  • the support 2 may be thinner than the porous sheet 1 .
  • the method for producing the acidic gas adsorbent 10 includes, for example, a step (I) of curing a mixed liquid L containing a compound group containing an amine monomer and a porogen to obtain a cured body B; is removed to obtain the porous sheet 1 (II).
  • the compound group is typically a monomer group containing amine monomers and epoxy monomers.
  • the compound group may contain an epoxy prepolymer instead of the epoxy monomer or together with the epoxy monomer.
  • a porogen is, for example, a solvent that can dissolve the monomers and prepolymers contained in the compound group, and that can cause reaction-induced phase separation after the compound group reacts.
  • porogens include cellosolves such as methyl cellosolve and ethyl cellosolve, esters such as ethylene glycol monomethyl ether acetate and propylene glycol monomethyl ether acetate, glycols such as polyethylene glycol, polypropylene glycol and polyoxyalkylene glycol, polyoxy Ethers such as ethylene monomethyl ether and polyoxyethylene dimethyl ether are included.
  • polyoxyalkylene glycols include poly(1,2-butanediol)-6 propylene glycol and polyoxypropylene diglyceryl ether.
  • the porogen may be a polar solvent such as ethyl acetate, N,N-dimethylformamide (DMF), acetonitrile, ethanol, isopropanol, a non-polar solvent such as toluene, or a mixed solvent thereof.
  • a porogen can be used individually or in combination of 2 or more types.
  • Components other than the compound group and the porogen may be further added to the mixed liquid L.
  • Other components include, for example, the reaction accelerators described above.
  • step (I) the polymer P is formed by reacting the compound groups.
  • the mixed liquid L is cured and a cured body B is obtained.
  • the compound group reaction is typically a polymerization reaction of an amine monomer and an epoxy monomer.
  • the reaction of the compound group may be a cross-linking reaction of an epoxy prepolymer with an amine monomer.
  • the amino group of the amine monomer reacts with the epoxy group of the epoxy monomer or epoxy prepolymer.
  • Reaction of the compound group can be performed by applying energy to the liquid mixture L.
  • the energy applied to the liquid mixture L is preferably thermal energy. As an example, by heating the mixed liquid L at a temperature of 40° C. to 100° C., the reaction of the compound group can proceed. However, the energy applied to the liquid mixture L may be light energy.
  • the cured body B contains polymer P and porogen. In the cured body B, a co-continuous structure is formed by phase separation between the polymer P and the porogen.
  • the shape of the cured product B obtained in step (I) is typically sheet-like.
  • the sheet-like cured body B is obtained, for example, by applying the mixed liquid L on a support 2 (typically, a support 2 having no porous structure) and curing the resulting coating film. can be made.
  • a method for applying the mixed liquid L is not particularly limited, and a roll coating method, a spin coating method, a dip coating method, or the like can be used.
  • the sheet-shaped cured body B can also be produced by bringing the mixed liquid L into contact with another sheet-shaped base material other than the support 2 and then curing the mixed liquid L.
  • a base material for example, a release liner or a fiber structure can be used.
  • the substrate may be a laminate comprising a release liner and a fibrous structure.
  • the liquid mixture L tends to penetrate into the interior of the fibrous structure by bringing the mixed liquid L into contact with the fibrous structure.
  • a cured body containing the fiber structure as a filler can be obtained.
  • the shape of the cured body B obtained in step (I) may not be sheet-like, and may be, for example, block-like, particularly cylindrical or columnar.
  • the block-shaped cured body B can be produced, for example, by curing the mixed liquid L filled in the mold in step (I).
  • the sheet-like cured body B to be used in step (II) can be obtained by cutting the vicinity of the surface of the block-shaped cured body B to a predetermined thickness.
  • the hardened body B is cylindrical or columnar, the hardened body B is cut near the surface of the hardened body B while rotating the hardened body B around the cylindrical axis or the cylindrical axis to obtain a sheet-like hardened body B can be made.
  • the method for removing the porogen from the sheet-like cured body B in step (II) is not particularly limited.
  • the porogen may be extracted from the cured body B and removed by immersing the cured body B in a solvent.
  • a solvent for extracting the porogen water, an aliphatic hydrocarbon solvent, an aromatic hydrocarbon solvent, an aliphatic alcohol solvent, an ether solvent, a halogen-containing organic solvent, an ester solvent, or the like can be used.
  • Aliphatic hydrocarbon solvents include n-hexane, cyclohexane, methylcyclohexane, n-heptane, n-octane, isooctane, petroleum ether, benzine and the like.
  • Aromatic hydrocarbon solvents include toluene, xylene, mesitylene, benzene and the like.
  • Aliphatic alcohol solvents include methanol, ethanol, isopropanol, butanol, cyclohexanol, ethylene glycol, propylene glycol, propylene glycol monomethyl ether, diethylene glycol and the like.
  • Ether solvents include diethyl ether, diisopropyl ether, dibutyl ether, ethylene glycol dimethyl ether, ethylene glycol diethyl ether, propylene glycol dimethyl ether, propylene glycol diethyl ether, diethylene glycol dimethyl ether, tetrahydrofuran, dioxane, anisole and the like.
  • Halogen-containing organic solvents include dichloromethane, chloroform, carbon tetrachloride, dichloroethane, chlorobenzene and the like.
  • Ester solvents include ethyl acetate and the like. These solvents can be used alone or in combination of two or more.
  • a porous sheet 1 having a flat plate shape By removing the porogen from the sheet-like cured body B in step (II), for example, a porous sheet 1 having a flat plate shape can be obtained.
  • the porous sheet 1 and the support 2 are provided by removing the porogen from the cured body B.
  • a sheet-like acidic gas adsorbent 10 is obtained.
  • a self-supporting film of the porous sheet 1 may be produced by a method using a base material other than the support 2, and the self-supporting film may be used as the acidic gas adsorbent 10.
  • a self-supporting film of the porous sheet 1 may be prepared, and the self-supporting film fixed to the support 2 using a fixing means such as an adhesive sheet may be used as the acidic gas adsorbent 10 .
  • the acidic gas adsorbent 10 produced by the above method usually has a flat plate shape.
  • the acidic gas adsorbent 10 having a flat plate shape may be further corrugated. Thereby, the acidic gas adsorbent 10 having a corrugated shape can be obtained.
  • the acidic gas adsorbent 10 can be manufactured using the manufacturing apparatus 100 shown in FIG. 2A.
  • FIG. 2A shows a schematic configuration of the manufacturing apparatus 100.
  • the manufacturing apparatus 100 includes a delivery roll 45 for delivering the support 2 , a winding roll 49 for winding the produced acidic gas adsorbent 10 , and a plurality of guide rolls 46 positioned between the delivery roll 45 and the winding roll 49 . , 47 and 48 .
  • the support 2 is transported from the delivery roll 45 to the take-up roll 49 .
  • the manufacturing apparatus 100 further includes a liquid mixture discharge section 20, a first heating section 30, an extraction section 40, and a second heating section 35, which are arranged in this order in the conveying direction of the support 2.
  • a base other than the support 2 may be used instead of the support 2.
  • the mixed liquid discharge section 20 includes a first supply section 21 , a second supply section 22 , a mixing section 23 and a discharge port 24 .
  • the first supply section 21 can send the first raw material 5 to the mixing section 23 .
  • the second supply section 22 can send the second raw material 6 to the mixing section 23 .
  • the first raw material 5 contains amine monomers and the second raw material 6 contains epoxy monomers and/or epoxy prepolymers. At least one selected from the group consisting of the first raw material 5 and the second raw material 6 contains a porogen.
  • the mixed liquid L is prepared by mixing the first raw material 5 and the second raw material 6 in the mixing section 23 .
  • the liquid mixture L prepared in the mixing section 23 is discharged to the outside of the liquid mixture discharge section 20 through the discharge port 24 .
  • the mixed liquid discharge section 20 is located near the guide roll 46 and can apply the mixed liquid L onto the support 2 transported from the delivery roll 45 to the guide roll 46 .
  • the coating film 7 can be formed on the support 2 .
  • the coating film 7 is sent to the first heating section 30 through the guide rolls 47 together with the support 2 .
  • the first heating unit 30 has a heater 31 for heating the coating film 7 .
  • the coating film 7 is heated by moving inside the first heating unit 30 .
  • the coating film 7 is cured to form a sheet-like cured body 8 .
  • the cured body 8 is sent to the extraction section 40 together with the support 2 .
  • the extractor 40 contains a solvent 41 for extracting the porogen from the cured body 8.
  • the hardened body 8 is immersed in the solvent 41 in the extractor 40 .
  • the porogen is removed from the cured body 8 and the porous sheet 1 is formed.
  • the porous sheet 1 is sent to the second heating section 35 together with the support 2 .
  • the second heating section 35 has a heater 36 for drying the porous sheet 1 sent from the extraction section 40 .
  • the porous sheet 1 is heated by moving in the second heating section 35 .
  • the porous sheet 1 is dried, and a sheet-like acidic gas adsorbent 10 comprising the porous sheet 1 and the support 2 is obtained.
  • This acidic gas adsorbent 10 passes through a guide roll 48 and is wound up by a winding roll 49 .
  • FIG. 2B shows a schematic configuration of a manufacturing apparatus 110 according to a modification. As shown in FIG. 2B, the manufacturing apparatus 110 does not include the extraction section 40 and the second heating section 35 .
  • the configuration of the manufacturing apparatus 110 is the same as the configuration of the manufacturing apparatus 100 except for the above. Therefore, elements common to these manufacturing apparatuses 100 and 110 are denoted by the same reference numerals, and description thereof may be omitted.
  • the description of each embodiment below can be applied to each other as long as there is no technical contradiction. Furthermore, each embodiment may be combined with each other unless it is technically inconsistent.
  • the cured body 8 formed by the first heating section 30 passes through the guide roll 48 together with the support 2 and is wound up by the winding roll 49 . Thereby, a wound body of the cured body 8 and the support 2 is obtained. By immersing this wound body in a solvent and extracting the porogen from the cured body 8, the sheet-like acidic gas adsorbent 10 can be obtained.
  • the acidic gas adsorbent 10 of the present embodiment tends to have high adsorption properties for acidic gases such as carbon dioxide.
  • the adsorption amount a of carbon dioxide when the acidic gas adsorbent 10 is brought into contact with a mixed gas G composed of carbon dioxide, nitrogen, and water vapor for 15 hours is, for example, 0.1 mmol/cm 3 or more, It is preferably 0.3 mmol/cm 3 or more, more preferably 0.5 mmol/cm 3 or more, still more preferably 0.7 mmol/cm 3 or more, and particularly preferably 0.8 mmol/cm 3 or more. , particularly preferably 1.0 mmol/cm 3 or more.
  • the upper limit of the adsorption amount a of carbon dioxide is not particularly limited, and is, for example, 10 mmol/cm 3 .
  • the adsorption amount a can be measured, for example, using a measuring device 200 shown in FIG.
  • the measuring device 200 has a first tank 230 and a second tank 231 .
  • the first tank 230 stores dry nitrogen
  • the second tank 231 stores a mixed gas of dry nitrogen and dry carbon dioxide.
  • the concentration of carbon dioxide in the mixed gas in the second tank 231 is, for example, 5 vol %.
  • the measuring device 200 further comprises a first container 240 containing water 270 and a first path 260 for sending nitrogen from the first tank 230 to the first container 240 .
  • the first path 260 has one end connected to the gas outlet of the first tank 230 and the other end located in the water 270 of the first container 240 .
  • Nitrogen sent from first tank 230 to first container 240 is humidified by contact with water 270 .
  • a mass flow controller 235 for adjusting the flow rate of nitrogen sent from the first tank 230 to the first container 240 is arranged in the first path 260 .
  • the measuring device 200 further includes a second container 241 , a second path 262 and a bypass path 261 .
  • a second path 262 connects the first container 240 and the second container 241 .
  • the nitrogen sent to the first container 240 and humidified is sent to the second container 241 through the second path 262 .
  • the bypass path 261 branches off from the first path 260 and connects to the second path 262 at a position between the first tank 230 and the mass flow controller 235 . Part of the nitrogen sent from the first tank 230 flows into the bypass path 261 and is sent to the second container 241 through the second path 262 .
  • a mass flow controller 236 for adjusting the flow rate of nitrogen sent from the first tank 230 to the bypass route 261 is arranged in the bypass route 261 .
  • the measuring device 200 further includes a third path 263 for sending the mixed gas from the second tank 231 to the second path 262 .
  • the third path 263 has one end connected to the gas outlet of the second tank 231 and the other end connected to the second path 262 .
  • a mass flow controller 237 for adjusting the flow rate of the mixed gas sent from the second tank 231 to the second path 262 is arranged on the third path 263 .
  • the mixed gas sent to the second path 262 is sent to the second container 241 through the second path 262 .
  • the measuring device 200 further comprises a third container 242 and a fourth path 264.
  • the third container 242 contains water 271 and the adsorption section 221 arranged in the water 271 .
  • the temperature of the water 271 is maintained at 20°C.
  • the adsorption section 221 has a gas inlet 222 and a gas outlet 223 .
  • the adsorption part 221 accommodates the acidic gas adsorbent 10 therein.
  • the adsorption part 221 is configured so that the water 271 does not permeate inside.
  • the adsorption part 221 is typically a tube made of a hydrophobic resin such as a fluororesin such as tetrafluoroethylene-perfluoroalkoxyethylene copolymer (PFA).
  • a fluororesin such as tetrafluoroethylene-perfluoroalkoxyethylene copolymer (PFA).
  • the tube as the adsorption part 221 has an inner diameter of 4 mm and an outer diameter of 6 mm.
  • the suction unit 221 is configured to be detachable from the measuring device 200 .
  • the measuring device 200 can also be used as an acidic gas adsorption device having the adsorption section 221 .
  • the present invention provides an acid gas adsorption device 200 comprising an adsorption section 221 having a gas inlet 222 and a gas outlet 223, the adsorption section 221 containing the acid gas adsorbent 10. do.
  • the adsorption part 221 of the acidic gas adsorption device 200 may accommodate a structure described later that includes the acidic gas adsorbent 10 .
  • a fourth path 264 connects the second container 241 and the third container 242 . Specifically, the fourth path 264 is connected to the gas inlet 222 of the adsorption section 221 in the third container 242 .
  • a first densitometer 250 for measuring the concentration of carbon dioxide in the gas supplied to the adsorption unit 221 is arranged on the fourth path 264 .
  • the first densitometer 250 for example, a CO 2 /H 2 O gas analyzer LI-850-3 manufactured by LI-COR can be used.
  • the measurement device 200 further includes a fifth path 265 connected to the gas outlet 223 of the adsorption section 221 for discharging gas from the adsorption section 221 to the outside of the measurement device 200 .
  • a back pressure valve 255 and a second densitometer 251 are arranged in the fifth path 265 .
  • the pressure in the adsorption section 221 can be adjusted to a constant value by the back pressure valve 255 .
  • the second densitometer 251 can measure the concentration of carbon dioxide in the gas discharged from the adsorption section 221 .
  • As the second concentration meter 251 for example, a CO 2 /H 2 O gas analyzer LI-850-3 manufactured by LI-COR can be used.
  • Each path of the measuring device 200 is composed of, for example, metal or resin piping.
  • the acidic gas adsorbent 10 is dried.
  • the drying treatment is performed, for example, by treating the acidic gas adsorbent 10 at 60° C. for 2 hours or more in a vacuum atmosphere.
  • the adsorption part 221 is filled with the acidic gas adsorbent 10 after drying.
  • the acidic gas adsorbent 10 is measured in advance to specify the volume of the acidic gas adsorbent 10 .
  • the weight of the acidic gas adsorbent 10 filled in the adsorption part 221 is, for example, 50 mg.
  • the fourth path 264 and the fifth path 265 are connected to both ends of the adsorption part 221 and the adsorption part 221 is immersed in the water 271 of the third container 242 .
  • the nitrogen from the first tank 230 and the mixed gas from the second tank 231 are introduced into the second container 241 through the first path 260, the second path 262, the bypass path 261 and the third path 263 of the measuring device 200. supply to These gases are mixed in the second container 241 to obtain a mixed gas G composed of carbon dioxide, nitrogen and water vapor. Inside the second container 241, the concentration of carbon dioxide in the mixed gas G is adjusted to 400 volppm.
  • the mixed gas G has a temperature of 20° C. and a humidity of 50% RH.
  • the mixed gas G is supplied to the adsorption unit 221 through the fourth route 264 at a flow rate sufficient for the weight of the acidic gas adsorbent 10, for example, at a flow rate of 300 mL/min for 50 mg of the acidic gas adsorbent 10. .
  • the pressure of the mixed gas G is adjusted to 107 kPa by the back pressure valve 255.
  • the adsorption part 221 is taken out from the third container 242, and the adsorption part 221 is immersed in a hot water bath (not shown) at 80°C for two hours or more.
  • the adsorption part 221 is immersed in the hot water bath until the concentration of carbon dioxide measured by the first densitometer 250 and the concentration of carbon dioxide measured by the second densitometer 251 become substantially the same value. .
  • the pretreatment of the acidic gas adsorbent 10 in the adsorption section 221 is completed.
  • the substance amount M of carbon dioxide adsorbed by the acidic gas adsorbent 10 is measured from the start to 15 hours.
  • the substance amount M of carbon dioxide adsorbed by the acidic gas adsorbent 10 is the difference between the concentration of carbon dioxide measured by the first densitometer 250 and the concentration of carbon dioxide measured by the second densitometer 251 over time. It can be calculated from the results measured in Based on the substance amount M, the substance amount of carbon dioxide adsorbed by the acidic gas adsorbent 10 of 1 cm 3 in 15 hours is calculated, and the obtained calculated value is specified as the adsorption amount a.
  • the pores of porous particles supported on a substrate are filled with an amine compound. Since such an adsorbent requires porous particles and a binder for binding the porous particles together, it is possible to greatly adjust the amount of amino group substance per unit volume of the adsorbent. difficult.
  • conventional adsorbents when the filling amount of the amine compound is increased in order to increase the amount of amino group substance per unit volume, the pores of the porous particles are clogged, and the adsorption performance for acidic gases is rather reduced. be.
  • the acidic gas adsorbent 10 of the present embodiment by using the porous sheet 1 having a three-dimensional network skeleton made of the polymer P, the pores of the porous sheet 1 are maintained while The amount of amino group substance per unit volume can be easily increased.
  • the acidic gas adsorbent 10 of the present embodiment tends to have high adsorption performance for acidic gases, and can be said to be suitable for adsorbing acidic gases.
  • the acidic gas adsorbent 10 of this embodiment can adsorb acidic gases.
  • Acid gases include carbon dioxide, hydrogen sulfide, carbonyl sulfide, sulfur oxides (SOx), hydrogen cyanide, nitrogen oxides (NOx), etc. Carbon dioxide is preferred.
  • the acidic gas adsorbent 10 can be used, for example, by the following method. First, a mixed gas containing acidic gases is brought into contact with the acidic gas adsorbent 10 .
  • Mixed gas contains other gas other than acidic gas, for example.
  • gases include, for example, hydrogen, non-polar gases such as nitrogen, and inert gases such as helium, preferably nitrogen.
  • the mixed gas is typically atmospheric air.
  • the mixed gas may be the off-gas of a chemical plant or a thermal power plant.
  • the temperature of the mixed gas is, for example, room temperature (23°C).
  • the concentration of the acid gas in the mixed gas is not particularly limited, and is, for example, 0.01 vol% (100 volppm) or more, preferably 0.04 vol% (400 volppm) or more under standard conditions (0°C, 101 kPa). It may be 0 vol % or more.
  • the upper limit of the concentration of carbon dioxide in the mixed gas is not particularly limited, and is, for example, 10 vol % under standard conditions.
  • the pressure of the mixed gas is typically equal to the atmospheric pressure in the environment in which the acid gas adsorbent 10 is used. However, the mixed gas to be brought into contact with the acidic gas adsorbent 10 may be pressurized.
  • the acidic gas adsorbent 10 in contact with the mixed gas adsorbs the acidic gas contained in the mixed gas.
  • the operation of bringing the mixed gas into contact with the acidic gas adsorbent 10 is performed, for example, until adsorption of the acidic gas by the acidic gas adsorbent 10 reaches equilibrium.
  • the acidic gas adsorbent 10 that has adsorbed the acidic gas is regenerated.
  • the regeneration treatment can be performed, for example, by heating the acidic gas adsorbent 10 .
  • the heating temperature of the acidic gas adsorbent 10 is, for example, 50 to 80.degree.
  • the acidic gas adsorbent 10 may be heated under a reduced pressure atmosphere or a vacuum atmosphere.
  • the acidic gas is desorbed from the acidic gas adsorbent 10 by heating the acidic gas adsorbent 10 . Thereby, the acidic gas adsorbent 10 is regenerated, and the acidic gas adsorbent 10 can be used repeatedly.
  • the acid gas desorbed from the acid gas adsorbent 10, particularly carbon dioxide, can be used as a raw material for synthesizing chemicals and dry ice.
  • the operation of adsorbing the acidic gas by the acidic gas adsorbent 10 and the regeneration process of the acidic gas adsorbent 10 are performed using the measuring device 200 (acid gas adsorbing device) described above or the acidic gas recovery device described later. is possible.
  • the acidic gas adsorbent 10 may have a plurality of porous sheets 1 .
  • the acidic gas adsorbent 11 shown in FIG. 4 has two porous sheets 1A and 1B. Except for this, the structure of the acidic gas adsorbent 11 is the same as the structure of the acidic gas adsorbent 10 .
  • the support 2 is located between the two porous sheets 1A and 1B and is in direct contact with each of the porous sheets 1A and 1B.
  • the composition and structure of the porous sheet 1A may be the same as or different from those of the porous sheet 1B.
  • the structure 15 of this embodiment includes the acidic gas adsorbent 10 described above and the ventilation path 14 .
  • the acidic gas adsorbent 11 shown in FIG. 4 can also be used.
  • the structure 15 is typically a honeycomb structure having a plurality of ventilation channels 14 extending in the same direction.
  • the acidic gas adsorbent 10 preferably has the support 2 together with the porous sheet 1 .
  • the porous sheet 1 may contain a fibrous structure as a filler.
  • the acidic gas adsorbent 10 included in the structure 15 may be a self-supporting film of the porous sheet 1 .
  • the structure 15 includes an adsorbent unit U in which, for example, an acidic gas adsorbent 10A having a corrugated shape and an acidic gas adsorbent 10B having a flat plate shape are laminated.
  • an acidic gas adsorbent 10A a plurality of peaks 12 and a plurality of valleys 13 are arranged alternately.
  • a ventilation path 14 is formed between the peaks 12 or valleys 13 of the acidic gas adsorbent 10A and the acidic gas adsorbent 10B.
  • the direction x is the direction (wave direction) in which the plurality of peaks 12 and the plurality of valleys 13 of the acidic gas adsorbent 10A are alternately arranged.
  • the direction y is the direction in which the acidic gas adsorbents 10A and 10B in the adsorbent unit U are laminated.
  • a direction z is a direction perpendicular to each of the directions x and y, and is the direction in which the ventilation path 14 extends.
  • the structure 15 includes a plurality of adsorbent units U, for example.
  • the number of adsorbent units U in the structure 15 is not particularly limited, and is, for example, 2-100.
  • the plurality of adsorbent units U are stacked in the direction y such that the plurality of acidic gas adsorbents 10A and the plurality of acidic gas adsorbents 10B are alternately arranged.
  • the structure 15 has a block shape by stacking a plurality of adsorbent units U. As shown in FIG.
  • the ventilation path 14 is a through hole that penetrates the structure 15 in the direction z.
  • the ventilation path 14 is surrounded by acid gas adsorbents 10A and 10B.
  • the acid gas is efficiently adsorbed by the acid gas adsorbents 10A and 10B while moving through the ventilation path 14 in the direction z.
  • the structure 15 with a large cross-sectional area of the ventilation path 14 is suitable for reducing the pressure loss that occurs when it comes into contact with acid gas.
  • a structure 15 with reduced pressure loss can, for example, reduce the power of a fan used to move acid gases. Since the acidic gas adsorbent 10 tends to have a relatively large amount of amino group substance per unit volume, it tends to be able to sufficiently adsorb acidic gases even when the thickness of the porous sheet 1 is small. be.
  • the shape of the structure 15 including the acidic gas adsorbent 10 is not limited to that shown in FIG. 5A.
  • the structure 16 shown in FIG. 5B has a shape in which one adsorbent unit U is wound around the central tube 50 . Except for this, the configuration of structure 16 is the same as that of structure 15 .
  • the structure 16 has a cylindrical shape.
  • the plurality of peaks 12 and the plurality of valleys 13 of the acidic gas adsorbent 10A are alternately arranged in the circumferential direction of the structure 16 .
  • the ventilation path 14 formed between the ridges 12 or valleys 13 of the acidic gas adsorbent 10A and the acidic gas adsorbent 10B penetrates the structure 16 in the direction in which the central pipe 50 extends.
  • the acid gas is efficiently adsorbed by the acid gas adsorbents 10A and 10B while moving through the ventilation path 14 in the direction in which the central tube 50 extends.
  • the structure may not include the corrugated acidic gas adsorbent 10A, and may not be a honeycomb structure like the structures 15 and 16.
  • the structure 17 shown in FIG. 5C includes, as the acidic gas adsorbent 10, only an acidic gas adsorbent 10B having a flat plate shape. Specifically, the structure 17 includes a plurality of acidic gas adsorbents 10B, and the plurality of acidic gas adsorbents 10B are arranged with gaps therebetween. A space between the two acidic gas adsorbents 10B functions as a ventilation path 14 .
  • the structure 17 may further include a fixing member 55 that fixes the plurality of acidic gas adsorbents 10B to secure the ventilation path 14 described above.
  • the fixed member 55 is, for example, a rod.
  • a through hole is formed through the acidic gas adsorbent 10B in the thickness direction, and the rod as the fixing member 55 is formed through the through hole of each acidic gas adsorbent 10B.
  • a plurality of acidic gas adsorbents 10B are fixed by being inserted into.
  • the rod as the fixing member 55 may be a bolt having a male threaded side surface. In this case, by screwing a nut onto the bolt at the position between the two acidic gas adsorbents 10B, the ventilation path 14 can be secured more reliably. In this example the nut acts as a spacer.
  • each of the plurality of acidic gas adsorbents 10B has a rectangular shape in plan view, and through holes are formed near the four corners thereof. Furthermore, the acidic gas adsorbent 10C has four fixing members 55, and the four fixing members 55 are inserted into four through holes formed at the four corners of the acidic gas adsorbent 10B.
  • the number and positions of through-holes formed in the acidic gas adsorbent 10B and the number of fixing members 55 are not limited to the example of FIG. 5C.
  • the acidic gas is efficiently adsorbed by the two acidic gas adsorbents 10B while moving through the ventilation path 14 between the two acidic gas adsorbents 10B.
  • an acidic gas recovery device 300 of this embodiment includes the acidic gas adsorbent 10 described above and a medium path 60 .
  • the acidic gas adsorbent 11 shown in FIG. 4 can also be used.
  • the heat medium 61 for heating the acidic gas adsorbent 10 passes through the medium path 60 during the desorption operation for desorbing the acidic gas adsorbed by the acidic gas adsorbent 10 from the acidic gas adsorbent 10 . pass.
  • the acidic gas adsorbent 10 preferably has a support 2 together with the porous sheet 1.
  • the porous sheet 1 may contain a fibrous structure as a filler.
  • the acidic gas adsorbent 10 included in the acidic gas recovery device 300 may be a self-supporting membrane of the porous sheet 1 .
  • the acid gas recovery device 300 includes, for example, a plurality of acid gas adsorbents 10.
  • a plurality of acidic gas adsorbents 10 may be arranged with a gap therebetween, and a gap between two acidic gas adsorbents 10 may function as a ventilation path 14 .
  • the configurations of the acidic gas adsorbent 10 and the ventilation path 14 may be the same as those described above for the structures 15-17.
  • the medium path 60 is composed of, for example, a pipe made of metal such as copper, more specifically, a heat transfer pipe.
  • the medium path 60 penetrates the acidic gas adsorbent 10 in the thickness direction of the acidic gas adsorbent 10, for example.
  • a through hole is formed through the acidic gas adsorbent 10 in the thickness direction, and the medium path 60 is inserted into the through hole of the acidic gas adsorbent 10 .
  • the acid gas recovery device 300 typically has a structure similar to a fin-tube heat exchanger including heat transfer fins and heat transfer tubes passing through the heat transfer fins.
  • the medium path 60 has a U-shape and may be inserted into two through-holes formed in the acidic gas adsorbent 10 .
  • the number of through-holes formed in the acidic gas adsorbent 10 and the number of medium paths 60 are not limited to those shown in FIG. 6A.
  • four or more through-holes may be formed in the acidic gas adsorbent 10
  • two or more U-shaped medium paths 60 may be inserted into the through-holes of the acidic gas adsorbent 10 .
  • the medium path 60 functions as a path for the heat medium 61 that heats the acidic gas adsorbent 10 during the desorption operation.
  • the medium path 60 can also be used as a path of a cooling medium for cooling the acidic gas adsorbent 10 after the desorption operation. That is, the medium path 60 may serve as both a path for the heat medium 61 and a path for the cooling medium.
  • the acid gas recovery device 300 further includes a casing (not shown) that houses the acid gas adsorbent 10 and the medium path 60.
  • the casing has, for example, a mixed gas inlet for sending a mixed gas containing acid gas to the interior of the casing.
  • the casing further has a desorption gas outlet for discharging the desorbed gas desorbed from the acidic gas adsorbent 10 to the outside of the casing during the desorption operation, and a purge gas inlet for sending the purge gas to the inside of the casing.
  • the mixed gas inlet may also serve as the purge gas inlet.
  • the casing may have a medium inlet for sending the heat medium 61 and the cooling medium to the medium path 60 and a medium outlet for discharging the heat medium 61 and the cooling medium from the medium path 60 .
  • the acidic gas recovery device 300 performs, for example, an adsorption operation in which the acidic gas adsorbent 10 adsorbs the acidic gas, and a desorption operation in which the acidic gas adsorbent 10 desorbs the acidic gas adsorbed from the acidic gas adsorbent 10. repeat.
  • acid gas can be recovered.
  • the adsorption operation of the acidic gas recovery device 300 is performed, for example, as follows. First, a mixed gas containing acid gas is sent into the casing through the mixed gas inlet. Mixed gases include those described above. The mixed gas contacts the acidic gas adsorbent 10 while moving through the ventilation path 14, for example. Thereby, the acidic gas adsorbent 10 adsorbs the acidic gas contained in the mixed gas. The adsorption operation is performed, for example, until adsorption of acidic gas by the acidic gas adsorbent 10 reaches equilibrium.
  • the desorption operation of the acidic gas recovery device 300 is performed, for example, as follows.
  • the purge gas is sent into the casing through the purge gas inlet and is discharged to the outside of the casing through the desorbed gas outlet.
  • the mixed gas remaining inside the casing can be discharged to the outside of the casing, and the inside of the casing can be filled with the purge gas.
  • the purge gas for example, a water vapor gas or a gas containing a high concentration of acid gas such as carbon dioxide can be used.
  • An operation of decompressing the inside of the casing may be performed in place of or together with the operation of sending the purge gas into the casing. This decompression operation can be performed, for example, by a decompression device connected to the desorbed gas outlet of the casing.
  • the heat medium 61 is sent to the medium path 60 while the purge gas is being supplied to the inside of the casing.
  • Hot water, high-temperature gas, or the like can be used as the heat medium 61 .
  • gas contained in high-temperature gas are Freon, carbon dioxide, air, water vapor, and the like.
  • the heat medium 61 can be prepared using, for example, waste heat, a heat pump, self-heat regeneration, or the like.
  • the heat medium 61 By sending the heat medium 61 to the medium path 60, heat exchange occurs between the heat medium 61 and the acid gas adsorbent 10 via the medium path 60, and the acid gas adsorbent 10 is heated.
  • the heating temperature of the acidic gas adsorbent 10 is, for example, 50 to 80.degree.
  • the acidic gas is desorbed from the acidic gas adsorbent 10 .
  • the desorbed gas desorbed from the acidic gas adsorbent 10 is discharged from the desorbed gas outlet together with the purge gas. Thereby, acid gas can be recovered.
  • the purge gas contains water vapor, the water vapor can be removed by cooling the purge gas discharged from the desorption gas outlet and condensing the water vapor.
  • the heat medium 61 may be used to heat the acidic gas adsorbent 10 .
  • the support 2 functions as a planar heater
  • the acidic gas adsorbent 10 may be heated by energizing the support 2 .
  • the acid gas recovery device 300 is configured so that the heat medium 61 does not come into direct contact with the desorbed gas during the desorption operation. According to this acidic gas recovery apparatus 300, acidic gas can be efficiently recovered.
  • the recovered acid gas particularly carbon dioxide, can be used as raw materials for chemical synthesis and dry ice.
  • the acid gas recovery device 300 may perform a preparatory operation for performing the adsorption operation.
  • a preparatory operation is performed, for example, as follows. First, the supply of purge gas to the inside of the casing is stopped, and the heat medium 61 is discharged from the medium path 60 . A cooling medium is then routed through medium path 60 . Antifreeze or the like can be used as the cooling medium. Via the medium path 60, heat exchange occurs between the cooling medium and the acidic gas adsorbent 10, and the acidic gas adsorbent 10 is cooled. The acidic gas adsorbent 10 is cooled to room temperature (25° C.), for example. After cooling the acidic gas adsorbent 10, the cooling medium is discharged from the medium path 60, thereby completing the preparation for the adsorption operation.
  • the acid gas recovery device is not limited to that shown in FIG. 6A.
  • a medium path 60 is formed between two acidic gas adsorbents 10.
  • the acid gas recovery device 310 among the plurality of gaps formed between the plurality of acid gas adsorbents 10, some of the gaps function as the medium passages 60, and the remaining gaps function as the ventilation passages 14. Function.
  • the medium paths 60 and the ventilation paths 14 are alternately arranged along the arrangement direction of the plurality of acidic gas adsorbents 10 .
  • the acid gas recovery device 310 typically has a structure similar to a plate heat exchanger in which a plurality of heat transfer plates are stacked.
  • the acidic gas adsorbent 10 preferably has the support 2 together with the porous sheet 1 .
  • the porous sheet 1 included in the acidic gas adsorbent 10 faces the ventilation path 14 and the support 2 faces the medium path 60 .
  • a spacer 65 is arranged in the ventilation path 14 and a spacer (not shown) is also arranged in the medium path 60 . These spacers are configured to secure the vent passages 14 and media passages 60, to introduce the appropriate fluid to each passage, and to prevent fluid leakage to the other passages.
  • the ventilation path 14 is connected to the outer space of the acidic gas recovery device 310 at the back and front of the paper, so that the mixed gas can be taken into the ventilation path 14 from the outer space.
  • a member may be arranged between the ventilation path 14 and the external space to cut off the connection therebetween.
  • the acidic gas recovery device 310 further includes a restraining member 70 that restrains the plurality of acidic gas adsorbents 10 .
  • the restraining member 70 has, for example, a pair of plate members 71a and 71b, a rod 72 and a fixing member 73. As shown in FIG.
  • the plate members 71 a and 71 b are arranged in the arrangement direction of the plurality of acidic gas adsorbents 10 and sandwich the plurality of acidic gas adsorbents 10 . According to the plate members 71a and 71b, pressure can be applied to the plurality of acidic gas adsorbents 10 in the arrangement direction.
  • the plate members 71a and 71b may be formed with the desorption gas outlet, the purge gas inlet, the medium inlet, the medium outlet, and the like, which are described above for the acid gas recovery device 310 .
  • a through hole is formed in each of the plate members 71a and 71b, and the rod 72 is inserted into the through hole of the plate members 71a and 71b.
  • the rod 72 may be a bolt having a male thread on its side surface.
  • the fixing member 73 fixes one of the plate members 71a and 71b and the rod 72 to each other, for example.
  • Fixing member 73 is typically a nut having an internal thread that can be screwed onto rod 72 .
  • the restraining member 70 has a fixing member 73a that fixes the plate member 71a and the rod 72 to each other, and a fixing member 73b that fixes the plate member 71b and the rod 72 to each other.
  • each of the two rods 72 is fixed by a fixing member 73.
  • the number of rods 72 and the like are not limited to the example in FIG. 6B.
  • the acid gas recovery device 310 can implement the same operating method as the operating method described above for the acid gas recovery device 300 .
  • a medium path 60 is formed between two acidic gas adsorbents 10 in the acidic gas recovery device 310 . According to this configuration, in the desorption operation, the entire acidic gas adsorbent 10 can be uniformly heated by passing the heat medium through the medium path 60 .
  • the acid gas recovery device 310 is configured so that the ventilation path 14 does not interfere with the medium path 60. Therefore, in the acid gas recovery device 310, the pressure loss caused by the passage of the mixed gas through the ventilation path 14 tends to be small during the adsorption operation.
  • the acidic gas recovery device 310 is easier to remove members such as the acidic gas adsorbent 10. By removing the acidic gas adsorbent 10 from the acidic gas recovery device 310, the replacement of the acidic gas adsorbent 10 is facilitated. Furthermore, by removing each member of the acid gas recovery device 310, it is easy to perform maintenance such as cleaning operation for each member.
  • Example 1 First, 5.22 g of poly(1,2-butanediol)-6 propylene glycol (manufactured by NOF Corporation, Uniol (registered trademark) PB-500) and poly 5.22 g of oxypropylene diglyceryl ether (manufactured by NOF Corporation, Unilube (registered trademark) DGP-700) was added. 2.55 g of ethylene glycol diglycidyl ether (manufactured by Nagase ChemteX Corporation, EX-810) and pentaerythritol tetraglycidyl ether (manufactured by Showa Denko KK, Showfree (registered trademark) PETG)3. A mixture of epoxy monomer and porogen was prepared by dissolving 83 g.
  • Example 1 the desktop shaker (Angel Vibrator Digital 60 Hz) was set to intensity 5, and the mixture was shaken for 2 minutes. Next, using an applicator with a gap of 350 ⁇ m, this mixture was applied onto an aluminum sheet with a thickness of 20 ⁇ m. The resulting coating film was cured by standing in a drier at 120° C. for 30 minutes. As a result, a sheet-like cured body containing the polymer P having amino groups was obtained. The operation of immersing the cured product in ethyl acetate at 60° C. for 30 minutes was repeated twice with liquid exchange. As a result, the porogen was removed from the cured body to form a porous sheet. Next, it was dried in a drier at 60° C. for 30 minutes, and the aluminum sheet was removed to obtain the acidic gas adsorbent of Example 1 (self-supporting film of porous sheet). In Example 1, the porous sheet had a three-dimensional network skeleton composed of polymer P.
  • the porous sheet had a thickness of 215 ⁇ m, a basis weight of 13.03 mg/cm 2 , and a porosity calculated from the true density of the polymer P and the like of 45%.
  • the density of amino groups in the polymer P calculated from the blending ratio of the monomers was 13.87 mmol/g.
  • the amount of amino group substance per unit volume of the porous sheet was 8.39 mmol/cm 3 .
  • Example 2 a mixed solution was prepared in the same manner as in Example 1, except that the blending amounts of the epoxy monomer, amine monomer and porogen were changed as shown in Table 1.
  • a desktop shaker (Angel Vibrator Digital 60 Hz) was set to intensity 5 to shake the mixture for 2 minutes.
  • this mixture was applied onto a glass paper (PHN-50GC, manufactured by Oji F-Tex Co., Ltd.) with a thickness of 250 ⁇ m. At this time, the liquid mixture soaked into the inside of the glass paper. The liquid mixture was hardened by leaving the glass paper soaked with the liquid mixture in a drier at 120° C. for 30 minutes.
  • Example 2 a sheet-like cured body containing polymer P having an amino group and glass paper as a filler was obtained.
  • the porogen was removed from the cured body to form a porous sheet.
  • it was dried in a drier at 60° C. for 30 minutes to obtain an acidic gas adsorbent (self-supporting film of porous sheet) of Example 2 containing glass paper as a filler.
  • the porous sheet had a three-dimensional network skeleton composed of polymer P.
  • Example 2 the basis weight of the acidic gas adsorbent (porous sheet) was 15.8 mg/cm 2 .
  • the value (10.8 mg/cm 2 ) obtained by subtracting the basis weight (5.0 mg/cm 2 ) of the glass paper from the basis weight (15.8 mg/cm 2 ) of the acidic gas adsorbent is composed of polymer P. It can be regarded as the basis weight of the three-dimensional network skeleton.
  • the theoretical thickness of the three-dimensional network skeleton calculated from the true density of the polymer P (1.1 g/cm 3 ) and the porosity of the three-dimensional network skeleton (45%) was 179 ⁇ m.
  • the density of amino groups in the polymer P calculated from the blending ratio of the monomers was 12.38 mmol/g.
  • the amount of amino group substance per unit volume of the three-dimensional network skeleton contained in the porous sheet was 7.49 mmol/cm 3 .
  • the amount of amino group substance per unit volume of the porous sheet was 5.27 mmol/cm 3 .
  • Examples 3-6 Acid gas adsorbents (self-supporting films of porous sheets) of Examples 3 to 6 were obtained in the same manner as in Example 2, except that the fiber structure shown in Table 1 was used instead of the glass paper.
  • the porous sheet had a three-dimensional network skeleton composed of polymer P.
  • porous silica AAC Essence
  • porous silica AAC Essence
  • a pore volume of 1.5 mL/g a specific surface area of 700 m 2 /g, a pore diameter of 10 nm, and a true density of 2.2 g/mL was used.
  • 3.00 g of SUNSPERA H-52 manufactured by ITEC Co., Ltd. was prepared and immersed in 60 g of methanol (manufactured by Fuji Film Wako Pure Chemical Industries, Ltd., special grade) overnight to prepare a dispersion liquid.
  • BET specific surface area For the acidic gas adsorbents produced in Examples 1-2 and Comparative Examples 1-6, the BET specific surface area was measured by nitrogen gas adsorption. The BET specific surface area was measured using a specific surface area measuring device (trade name “BELSORP-mini”, manufactured by Microtrac Bell) in accordance with JIS Z8830:2013.
  • Glass transition temperature Tg The glass transition temperature Tg of the polymer P contained in the acidic gas adsorbents produced in Examples and Comparative Examples was measured by the following method. First, a polymer having the same composition as the polymer P contained in the acidic gas adsorbent was synthesized. About 5 mg of this polymer was set in a differential scanning calorimeter (DSC2500 manufactured by TA Instruments). Using this apparatus, the temperature was raised from 30° C. to 200° C. at a temperature elevation rate of 10° C./min in a nitrogen atmosphere, and held at that temperature for 1 minute. Next, it was cooled to ⁇ 50° C.
  • DSC2500 differential scanning calorimeter
  • the true density of the polymer P contained in the acidic gas adsorbents produced in Examples and Comparative Examples was determined by the following method. First, a mixed liquid containing epoxy monomers and amine monomers was prepared in the same amounts as the mixed liquids used in Examples and Comparative Examples. Next, a desktop shaker (Angel Vibrator Digital 60 Hz) was set to intensity 5 to shake the mixture for 2 minutes. The mixed liquid was poured into a PFA petri dish having an inner diameter of 75 mm, and the mixed liquid was cured by allowing it to stand in a drier at 120° C. for 30 minutes. As a result, a cured product containing the polymer P having amino groups was obtained.
  • Angel Vibrator Digital 60 Hz Angel Vibrator Digital 60 Hz
  • the amount of amino group substance per unit volume was specified by the following method.
  • the acidic gas adsorbent was set in a simultaneous thermal analysis DSC/TGA device (DSC6500, manufactured by TA Instruments). Using this apparatus, the temperature was raised from 30° C. to 100° C. at a temperature elevation rate of 10° C./min in a nitrogen atmosphere, and the temperature was maintained for 40 minutes (operation 1). This removed the water contained in the acidic gas adsorbent.
  • the temperature was raised from 100° C. to 800° C. at a temperature elevation rate of 10° C./min, and held at that temperature for 5 minutes (operation 2). This removed the polymer P from the acidic gas adsorbent.
  • the ratio of the weight (g) of the acidic gas adsorbent after performing the above operation 1 to the weight (g) of the acidic gas adsorbent before setting in the device (weight retention rate W1 (%))
  • the ratio of the weight (g) of the acidic gas adsorbent after performing the above operation 2 to the weight (g) of the acidic gas adsorbent before being set in the device was specified.
  • the volume A (mL) of the porous material per 1 g, the weight B (g) of the polymer P with respect to 1 g of the porous material, and the density C (g /mL), and the density D of amino groups in the composite particles were calculated.
  • volume A (mL) pore volume of porous material per gram (mL) + weight of porous material (g) / true density of porous material (g/mL)
  • Weight B (g) ratio F/(1-ratio F) ⁇ weight of porous body (g)
  • Composite particle density C (g/mL) (porous body weight (g) + weight B (g))/volume A (mL)
  • Density of amino groups D (mmol/g) ratio F x density of amino groups in polymer P (mmol/g)
  • the amount E of the amino group substance per unit volume of the acidic gas adsorbent was calculated by the following formula.
  • the packing rate of the composite particles adopts a numerical value (0.74) assuming that the composite particles are densely packed in the acidic gas adsorbent.
  • Amount of substance E (mmol/cm 3 ) Density of composite particles C (g/mL) ⁇ Filling rate of composite particles ⁇ Density of amino groups in composite particles D (mmol/g)
  • EX-810 ethylene glycol diglycidyl ether (manufactured by Nagase ChemteX Corporation, EX-810) PETG: Pentaerythritol tetraglycidyl ether (Showfree (registered trademark) PETG manufactured by Showa Denko) TETA: triethylenetetramine (manufactured by Tosoh Corporation)
  • PB-500 Poly(1,2-butanediol)-6 propylene glycol (manufactured by NOF Corporation, Uniol (registered trademark) PB-500)
  • DGP-700 Polyoxypropylene diglyceryl ether (manufactured by NOF Corporation, Unilube (registered trademark) DGP-700)
  • PHN-50GC Glass paper (pulp-containing nonwoven fabric) (PHN-50GC manufactured by Oji F-Tex Co., Ltd.)
  • MP-22 Pulp-containing nonwoven fabric (manufactured by N
  • Example 1 For the acidic gas adsorbents of Example 1 and Comparative Examples 1 to 3, the amount of carbon dioxide adsorbed was measured by the method described above. At this time, in Example 1, the acidic gas adsorbent cut so that the area of the main surface was 4.72 cm 2 was used as the measurement sample. In Comparative Examples 1 to 3, measurement samples whose weights were adjusted so as to have approximately the same volume as the measurement samples used in Example 1 were used. The weights of the measurement samples of Comparative Examples 1 to 3 were 49 mg, 64 mg and 76 mg, respectively.
  • the weight of the measurement sample which has a volume similar to that of the measurement sample used in Example 1, is the density C (g/mL) of the composite particles composed of the porous body and the polymer P and the composite It was calculated by the following formula using the packing rate of particles. In the following formula, a numerical value (0.74) assuming that the composite particles are most densely packed in the acidic gas adsorbent was adopted as the packing rate of the composite particles.
  • Weight (mg) of measurement sample of Comparative Example volume (cm 3 ) of measurement sample of Example 1 x density C (g/mL) x filling rate of composite particles
  • FIG. 8 shows the measurement results of the amount of carbon dioxide adsorbed in Example 1 and Comparative Examples 1 to 3.
  • FIG. 8 is a graph showing the relationship between the time from the start of the adsorption test and the amount of carbon dioxide adsorbed by the acidic gas adsorbent. From FIG. 8, it was confirmed that the amount of carbon dioxide adsorbed was saturated and stabilized after a predetermined time.
  • the acidic gas adsorbent of Example 1 had a larger amount of carbon dioxide adsorbed per unit volume than Comparative Examples 1 to 3, and was suitable for adsorbing acidic gases.
  • the adsorption amount a of carbon dioxide when the acidic gas adsorbent of Example 1 was brought into contact with the mixed gas G described above for 15 hours was 1.45 mmol/cm 3 .
  • Example 2 the carbon dioxide adsorption amounts of the acidic gas adsorbents of Example 2 and Comparative Examples 4 to 6 were measured by the method described above. At this time, in Example 2, the acidic gas adsorbent was cut so that the main surface area was 5.76 cm 2 and used as the measurement sample. In Comparative Examples 4 to 6, measurement samples whose weights were adjusted so as to have approximately the same volume as the measurement samples used in Example 2 were used. The weights of the measurement samples of Comparative Examples 4 to 6 were 50 mg, 60 mg and 72 mg, respectively. For Comparative Examples 4 to 6, the weight of the measurement sample having approximately the same volume as the measurement sample used in Example 2 was calculated by the same method as described above for Comparative Examples 1 to 3.
  • FIG. 9 shows the measurement results of the amount of carbon dioxide adsorbed in Example 2 and Comparative Examples 4 to 6.
  • FIG. 9 is a graph showing the relationship between the time from the start of the adsorption test and the amount of carbon dioxide adsorbed by the acidic gas adsorbent. From FIG. 9, it was confirmed that the amount of carbon dioxide adsorbed was saturated and stabilized after a predetermined time.
  • the acidic gas adsorbent of Example 2 had a larger adsorption amount of carbon dioxide per unit volume than Comparative Examples 4 to 6, and was suitable for adsorbing acidic gases.
  • the adsorption amount a of carbon dioxide when the acidic gas adsorbent of Example 2 was brought into contact with the mixed gas G described above for 15 hours was 1.27 mmol/cm 3 .
  • the acidic gas adsorbents of Examples 1 and 2 which are equipped with a porous sheet having a three-dimensional network skeleton containing the polymer P, adsorb more carbon dioxide than the comparative example, and adsorb acidic gases. found to be suitable for The acidic gas adsorbents of Examples 3 to 6 have the same structure as that of Example 2, except for the type of fiber structure used as the filler. Therefore, it is presumed that the acidic gas adsorbents of Examples 3 to 6 have the same adsorption performance as that of Example 2 for acidic gases such as carbon dioxide.
  • the acid gas adsorbents of the examples have a relatively large amount of amino group substance per unit volume, they are suitable for adjusting the thickness of the porous sheet to be small while maintaining the acid gas adsorption performance.
  • a porous sheet with a small thickness for example, it is possible to adjust the cross-sectional area of the ventilation passages of a structure, particularly a honeycomb structure, produced using an acidic gas adsorbent to be large.
  • a structure with a large cross-sectional area of the ventilation path is suitable for reducing the pressure loss that occurs when it comes into contact with acid gas.
  • the acidic gas adsorbents of the examples are suitable for reducing the pressure loss that occurs in the structure provided with the acidic gas adsorbents.
  • the porous particles were assumed to have a pore volume of 1.25 mL/g, a specific surface area of 175 m 2 /g, a pore diameter of 20 nm, and a true density of 3.8 g/mL.
  • the ratio F of the weight of the polymer P to the weight of the acid gas adsorbent was assumed to be 0.39. .
  • volume A of the porous particles per 1 g was calculated as 1.51 mL by the following formula.
  • the weight B of polymer P per 1 g of porous particles was calculated to be 0.639 g by the following formula.
  • the density C of the composite particles composed of the porous particles and polymer P was calculated to be 1.08 g/mL by the following formula.
  • the density D of amino groups in the above composite particles was calculated to be 5.4 mmol/g by the following formula.
  • the substance amount E of amino groups per unit volume of the acidic gas adsorbent was calculated as 4.34 mmol/cm 3 by the following formula.
  • the packing rate of the composite particles adopts a numerical value (0.74) assuming that the composite particles are densely packed in the acidic gas adsorbent.
  • the maximum amount of carbon dioxide that the acidic gas adsorbent of Calculation Example 1 can adsorb was calculated to be 0.75 mmol/cm 3 . From these results, it can be seen that the acidic gas adsorbents of Examples 1 and 2 have higher adsorption performance for acidic gases such as carbon dioxide than the acidic gas adsorbent of Calculation Example 1.
  • the acidic gas adsorbent of this embodiment can adsorb carbon dioxide in the atmosphere, for example.

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CN202280068560.3A CN118159358A (zh) 2021-10-15 2022-09-22 酸性气体吸附材料、具备酸性气体吸附材料的结构体、酸性气体吸附装置、酸性气体回收装置、酸性气体吸附材料的制造方法及片状结构体
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EP22880746.7A EP4417410A4 (en) 2021-10-15 2022-09-22 ACID GAS ADSORBENT, STRUCTURE WITH AN ACID GAS ADSORBENT, ACID GAS ADSORPTION DEVICE, ACID GAS RECOVERY DEVICE, ACID GAS PRODUCTION METHOD, AND LEAF-TYPE STRUCTURE

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WO2025204190A1 (ja) * 2024-03-29 2025-10-02 日東電工株式会社 酸性ガス吸着材、酸性ガス吸着材を備えた構造体、酸性ガス吸着装置、及び、酸性ガス吸着材の製造方法

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