Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J11/00—Recovery or working-up of waste materials
  • C08J11/04—Recovery or working-up of waste materials of polymers
  • C08J11/10—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation
  • C08J11/18—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation by treatment with organic material
  • C08J11/28—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation by treatment with organic material by treatment with organic compounds containing nitrogen, sulfur or phosphorus
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C209/00—Preparation of compounds containing amino groups bound to a carbon skeleton
  • C07C209/62—Preparation of compounds containing amino groups bound to a carbon skeleton by cleaving carbon-to-nitrogen, sulfur-to-nitrogen, or phosphorus-to-nitrogen bonds, e.g. hydrolysis of amides, N-dealkylation of amines or quaternary ammonium compounds
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C211/00—Compounds containing amino groups bound to a carbon skeleton
  • C07C211/01—Compounds containing amino groups bound to a carbon skeleton having amino groups bound to acyclic carbon atoms
  • C07C211/26—Compounds containing amino groups bound to a carbon skeleton having amino groups bound to acyclic carbon atoms of an unsaturated carbon skeleton containing at least one six-membered aromatic ring
  • C07C211/27—Compounds containing amino groups bound to a carbon skeleton having amino groups bound to acyclic carbon atoms of an unsaturated carbon skeleton containing at least one six-membered aromatic ring having amino groups linked to the six-membered aromatic ring by saturated carbon chains
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C263/00—Preparation of derivatives of isocyanic acid
  • C07C263/10—Preparation of derivatives of isocyanic acid by reaction of amines with carbonyl halides, e.g. with phosgene
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C265/00—Derivatives of isocyanic acid
  • C07C265/14—Derivatives of isocyanic acid containing at least two isocyanate groups bound to the same carbon skeleton
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C319/00—Preparation of thiols, sulfides, hydropolysulfides or polysulfides
  • C07C319/14—Preparation of thiols, sulfides, hydropolysulfides or polysulfides of sulfides
  • C07C319/20—Preparation of thiols, sulfides, hydropolysulfides or polysulfides of sulfides by reactions not involving the formation of sulfide groups
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C321/00—Thiols, sulfides, hydropolysulfides or polysulfides
  • C07C321/12—Sulfides, hydropolysulfides, or polysulfides having thio groups bound to acyclic carbon atoms
  • C07C321/14—Sulfides, hydropolysulfides, or polysulfides having thio groups bound to acyclic carbon atoms of an acyclic saturated carbon skeleton
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/08—Processes
  • C08G18/16—Catalysts
  • C08G18/22—Catalysts containing metal compounds
  • C08G18/24—Catalysts containing metal compounds of tin
  • C08G18/242—Catalysts containing metal compounds of tin organometallic compounds containing tin-carbon bonds
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
  • C08G18/30—Low-molecular-weight compounds
  • C08G18/38—Low-molecular-weight compounds having heteroatoms other than oxygen
  • C08G18/3855—Low-molecular-weight compounds having heteroatoms other than oxygen having sulfur
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
  • C08G18/30—Low-molecular-weight compounds
  • C08G18/38—Low-molecular-weight compounds having heteroatoms other than oxygen
  • C08G18/3855—Low-molecular-weight compounds having heteroatoms other than oxygen having sulfur
  • C08G18/3876—Low-molecular-weight compounds having heteroatoms other than oxygen having sulfur containing mercapto groups
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
  • C08G18/72—Polyisocyanates or polyisothiocyanates
  • C08G18/74—Polyisocyanates or polyisothiocyanates cyclic
  • C08G18/76—Polyisocyanates or polyisothiocyanates cyclic aromatic
  • C08G18/7614—Polyisocyanates or polyisothiocyanates cyclic aromatic containing only one aromatic ring
  • C08G18/7628—Polyisocyanates or polyisothiocyanates cyclic aromatic containing only one aromatic ring containing at least one isocyanate or isothiocyanate group linked to the aromatic ring by means of an aliphatic group
  • C08G18/7642—Polyisocyanates or polyisothiocyanates cyclic aromatic containing only one aromatic ring containing at least one isocyanate or isothiocyanate group linked to the aromatic ring by means of an aliphatic group containing at least two isocyanate or isothiocyanate groups linked to the aromatic ring by means of an aliphatic group having a primary carbon atom next to the isocyanate or isothiocyanate groups, e.g. xylylene diisocyanate or homologues substituted on the aromatic ring
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J11/00—Recovery or working-up of waste materials
  • C08J11/04—Recovery or working-up of waste materials of polymers
  • C08J11/10—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation
  • C08J11/18—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation by treatment with organic material
  • C08J11/22—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation by treatment with organic material by treatment with organic oxygen-containing compounds
  • C08J11/24—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation by treatment with organic material by treatment with organic oxygen-containing compounds containing hydroxyl groups
• • G—PHYSICS
  • G02—OPTICS
  • G02B—OPTICAL ELEMENTS, SYSTEMS OR APPARATUS
  • G02B1/00—Optical elements characterised by the material of which they are made; Optical coatings for optical elements
  • G02B1/04—Optical elements characterised by the material of which they are made; Optical coatings for optical elements made of organic materials, e.g. plastics
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2375/00—Characterised by the use of polyureas or polyurethanes; Derivatives of such polymers
  • C08J2375/04—Polyurethanes
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
  • Y02P20/00—Technologies relating to chemical industry
  • Y02P20/141—Feedstock
  • Y02P20/143—Feedstock the feedstock being recycled material, e.g. plastics
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
  • Y02W30/00—Technologies for solid waste management
  • Y02W30/20—Waste processing or separation
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
  • Y02W30/00—Technologies for solid waste management
  • Y02W30/50—Reuse, recycling or recovery technologies
  • Y02W30/62—Plastics recycling; Rubber recycling

Definitions

• the present disclosure relates to a method for producing a polythiol composition, a method for producing a polyamine compound, and their applications.
• Plastic lenses which are lenses containing resin, are lighter than inorganic lenses, are less likely to break, and can be dyed, so they have rapidly become popular in recent years for use in eyeglass lenses, camera lenses, and the like.
• various studies have been made on lenses containing thiourethane resins (for example, see Patent Documents 1 to 3).
• Patent Document 4 discloses a method for producing a polythiol composition that includes a reaction step of reacting a thiourethane resin and an amine compound to produce a polythiol composition.
• Patent Document 5 describes a first step in which a thiourethane resin and an amine compound A are reacted to produce a polyurea compound, and a second step in which a polyurea compound and an amine compound B are reacted to produce a polyamine compound.
• a method for producing a polyamine compound is disclosed.
• Patent Document 5 describes a step X1 in which a thiourethane resin and an alcohol compound are reacted in the presence of an amine compound XA, which is a tertiary amine compound, to produce a polycarbamate compound, and a step X1 in which a polycarbamate compound and an amine are reacted.
• a method for producing a polyamine compound is also disclosed, which includes a step X2 of reacting with compound XB to produce a polyamine compound.
• Patent Document 1 JP-A-63-46213
• Patent Document 2 JP-A-2-270859
• Patent Document 3 JP-A-7-252207
• Patent Document 4 International Publication No. 2021/157701
• Patent Document 5 International Publication No. 2021/157702
• an amine compound or an alcohol compound is used as a decomposing agent to decompose the thiourethane resin, and by decomposing the thiourethane resin with the decomposing agent, the target product is A polythiol composition or polyamine compound is obtained.
• the removability of the decomposing agent i.e., an amine compound or an alcohol compound
• the decomposing agent is improved when the decomposing agent is removed from the reaction system after the decomposition reaction of decomposing the thiourethane resin. Improvements may be required.
• An object of one aspect of the present disclosure is to provide a method for producing a polythiol composition, a method for producing a polyamine compound, and a method for producing a polyamine compound, which have excellent removability of the decomposer from a reaction system after a decomposition reaction in which a thiourethane resin is decomposed by a decomposer. It is to provide applications.
• Means for solving the above problems include the following aspects. ⁇ 1> A method for producing a polythiol composition, comprising a step of decomposing a thiourethane resin with a decomposing agent represented by the following formula (1) or the following formula (2) to produce a polythiol composition.
• R 1 and R 2 each independently represent a hydrogen atom, an alkyl group having 1 to 3 carbon atoms, or an amino group (provided that when R 1 and R 2 are both amino groups, except).
• R 3 represents an alkyl group having 1 to 3 carbon atoms.
• ⁇ 2> The method for producing a polythiol composition according to ⁇ 1>, wherein the production step includes reacting the thiourethane resin and the decomposing agent under a pressure higher than atmospheric pressure.
• ⁇ 3> The method for producing a polythiol composition according to ⁇ 1> or ⁇ 2>, which is a method for producing a polythiol composition for producing an optical material.
• ⁇ 4> Any one of ⁇ 1> to ⁇ 3>, wherein the thiourethane resin is recovered in at least one of a spectacle lens manufacturing process, a spectacle manufacturing process, and a spectacle disposal process.
• the step of obtaining the polymerizable composition comprises mixing the polythiol composition and a polyisocyanate composition containing a polyisocyanate compound, thereby producing a polymerization containing the polythiol composition and the polyisocyanate composition.
• the polyisocyanate composition is xylylene diisocyanate, At least one selected from the group consisting of the following compound (N1), the following compound (N2), and the following compound (N3), including;
• the peak area of the compound (N1) in high performance liquid chromatography measurement is 0.20 ppm or more with respect to 100 peak areas of xylylene diisocyanate
• the peak area of the compound (N2) in high performance liquid chromatography measurement is 0.05 ppm or more with respect to 100 peak areas of xylylene diisocyanate
• the polyisocyanate composition contains the compound (N3)
• the peak area of the compound (N3) in high performance liquid chromatography measurement is 0.10 ppm or more with respect to 100 peak areas of xylylene diisocyanate.
• a method for producing a polyamine compound comprising:
• R 1 and R 2 each independently represent a hydrogen atom, an alkyl group having 1 to 3 carbon atoms, or an amino group (provided that when R 1 and R 2 are both amino groups, except).
• R 11 and R 12 each independently represent a hydroxy group, a mercapto group, an amino group, or a monomethylamino group.
• the decomposing agent represented by the formula (3) is ethylenediamine, N,N'-dimethylethylenediamine, 2-aminoethanol, or ethylene glycol
• the first step includes reacting the thiourethane resin and the decomposing agent represented by the formula (1) under a pressure higher than atmospheric pressure.
• the second step includes reacting the polyurea compound and the decomposing agent represented by the formula (3) under a pressure higher than atmospheric pressure.
• a method for producing a polyamine compound comprising:
• R 3 represents an alkyl group having 1 to 3 carbon atoms.
• R 11 and R 12 each independently represent a hydroxy group, a mercapto group, an amino group, or a monomethylamino group.
• the step X1 includes reacting the thiourethane resin and the decomposing agent represented by the formula (2) under a pressure higher than atmospheric pressure.
• ⁇ 16> The method for producing a polyamine compound according to any one of ⁇ 8> to ⁇ 15>, which is a method for producing a polyamine compound as a raw material for a polyisocyanate compound for producing an optical material.
• ⁇ 17> Any one of ⁇ 8> to ⁇ 15>, wherein the thiourethane resin is recovered in at least one of a spectacle lens manufacturing process, a spectacle manufacturing process, and a spectacle disposal process.
• a method for producing a polyisocyanate compound comprising: ⁇ 19>
• a method for producing a polymerizable composition comprising: ⁇ 20> A step of manufacturing a polymerizable composition by the method for manufacturing a polymerizable composition according to ⁇ 19>; obtaining a resin by curing the polymerizable composition; A method for producing a resin containing.
• a method for producing a polythiol composition a method for producing a polyamine compound, and a method for producing a polyamine compound, which have excellent removability of the decomposer from a reaction system after a decomposition reaction in which a thiourethane resin is decomposed by a decomposer.
• a numerical range expressed using " ⁇ ” means a range that includes the numerical values written before and after " ⁇ " as lower and upper limits.
• the term “step” is used not only to refer to an independent process, but also to include a process that is not clearly distinguishable from other processes as long as the intended purpose of the process is achieved. .
• the amount of each component contained in the composition refers to the total amount of the multiple substances present in the composition. means.
• the upper limit or lower limit described in one numerical range may be replaced with the upper limit or lower limit of another numerical range described step by step.
• the upper limit or lower limit of the numerical range may be replaced with the values shown in the Examples. There may be overlap between the embodiments of this disclosure. That is, the features of one embodiment may be included in other embodiments.
• the method for producing a polythiol composition according to the first embodiment of the present disclosure includes a method for producing a polythiol composition by decomposing a thiourethane resin with a decomposing agent represented by the following formula (1) or the following formula (2). Including process.
• R 1 and R 2 each independently represent a hydrogen atom, an alkyl group having 1 to 3 carbon atoms, or an amino group (provided that when R 1 and R 2 are both amino groups, except).
• R 3 represents an alkyl group having 1 to 3 carbon atoms.
• the thiourethane resin is expressed by formula (1).
• it is decomposed by a decomposing agent represented by formula (2) to produce a polythiol composition.
• the method for producing a polythiol composition according to the first embodiment has excellent removability of the decomposer from the reaction system after the decomposition reaction of the thiourethane resin.
• the decomposer can be easily removed from the reaction system after the decomposition reaction by volatilization, distillation, or the like. The reason why such an effect is obtained is thought to be that the decomposing agent is a compound with a low boiling point.
• a thiourethane resin is decomposed by a decomposing agent represented by the above formula (1) or the above formula (2) (i.e., the thiourethane resin and the decomposing agent are reacted) to generate a polythiol composition.
• the decomposer represented by the above formula (1) is an amine compound.
• a decomposition reaction in which a thiourethane resin is decomposed by a decomposing agent represented by formula (1) is an aminated decomposition reaction.
• the decomposing agent represented by the above formula (1) is an alcohol compound.
• the decomposition reaction in which the thiourethane resin is decomposed by the decomposing agent represented by formula (1) is an alcoholytic decomposition reaction.
• Thiourethane resin is the starting material in the production process. There are no particular restrictions on the thiourethane resin, and examples thereof include JP-A-63-46213, JP-A-2-270859, JP-A-7-252207, International Publication No. 2008/047626, International Publication No. 2021/ Examples include thiourethane resins described in known documents such as No. 157701 and International Publication No. 2021/157702.
• a thiourethane resin usually includes a polymer of an isocyanate compound and a polythiol composition. That is, thiourethane resin is usually manufactured using an isocyanate compound and a polythiol composition as raw materials.
• a polythiol composition refers to at least one type of polythiol composition.
• a composition containing a polythiol compound may be any compound containing two or more thiol groups (also known as mercapto groups), and is not particularly limited.
• the polythiol composition may contain components other than the polythiol compound as impurities.
• the polythiol composition preferably contains at least one polythiol compound as a main component.
• the polythiol composition contains at least one type of polythiol compound as a main component
• the total content of at least one type of polythiol compound with respect to the total amount of the polythiol composition is 50% or more. do.
• the total content of at least one polythiol compound based on the total amount of the polythiol composition is preferably 60% or more, more preferably 70% or more, and even more preferably 80% or more.
• a composition "contains a certain component (hereinafter referred to as "component X") as a main component” means the content of component means that the total content of two or more compounds is 50% or more based on the total amount of the composition.
• component X which is the main component, is preferably 60% or more, more preferably 70% or more, and even more preferably 80% or more, based on the total amount of the composition.
• % refers to component X (for example, at least one component of It means the ratio (area %) of the total area of all peaks of polythiol compound).
• the polythiol compound contained in the polythiol composition is also referred to as a "polythiol component.”
• the polythiol composition as a raw material for thiourethane resin is 4-mercaptomethyl-1,8-dimercapto-3,6-dithiaoctane, 4,8-dimercaptomethyl-1,11-dimercapto-3,6,9-trithiaundecane, 4,7-dimercaptomethyl-1,11-dimercapto-3,6,9-trithiaundecane, 5,7-dimercaptomethyl-1,11-dimercapto-3,6,9-trithiaundecane, Pentaerythritol tetrakis (2-mercaptoacetate), Pentaerythritol tetrakis (3-mercaptopropionate), 2,5-dimercaptomethyl-1,4-dithiane, Bis(2-mercaptoethyl) sulfide
• the polythiol composition contains polythiol component A as a main component.
• the polythiol composition may contain at least one component other than the polythiol component A (for example, another polythiol compound, a component other than the polythiol compound, etc.).
• polythiol compounds include, for example, methanedithiol, 1,2-ethanedithiol, 1,2,3-propane trithiol, tetrakis(mercaptomethylthiomethyl)methane, tetrakis(2-mercaptoethylthiomethyl)methane, tetrakis( 3-Mercaptopropylthiomethyl)methane, bis(2,3-dimercaptopropyl)sulfide, 2,5-dimercapto-1,4-dithiane, 2,5-dimercaptomethyl-2,5-dimethyl-1,4 -dithiane, 1,1,3,3-tetrakis(mercaptomethylthio)propane, 1,1,2,2-tetrakis(mercaptomethylthio)ethane, 4,6-bis(mercaptomethylthio)-1,3-dithiane, etc. can be mentioned.
• polythiol composition as a raw material for thiourethane resin include, for example; An embodiment containing 4-mercaptomethyl-1,8-dimercapto-3,6-dithiaoctane (hereinafter also referred to as "polythiol component A1") as a main component; 4,8-dimercaptomethyl-1,11-dimercapto-3,6,9-trithiaundecane, 4,7-dimercaptomethyl-1,11-dimercapto-3,6,9-trithiaundecane, and 5 , 7-dimercaptomethyl-1,11-dimercapto-3,6,9-trithiaundecane (hereinafter, these three compounds are also collectively referred to as "polythiol component A2") as a main component; An embodiment containing pentaerythritol tetrakis (3-mercaptopropionate) (hereinafter also referred to as "polythiol
• Isocyanate compounds as raw materials for thiourethane resin The number of isocyanate compounds as a raw material for the thiourethane resin may be one, or two or more.
• Examples of the isocyanate compound as a raw material for the thiourethane resin include the known isocyanate compounds described in the above-mentioned known literature.
• the isocyanate compound as a raw material for the thiourethane resin preferably includes a polyisocyanate compound containing two or more isocyanate groups.
• Isocyanate compounds as raw materials for thiourethane resins are It is more preferable to include a diisocyanate compound containing two isocyanate groups, Pentamethylene diisocyanate, hexamethylene diisocyanate, m-xylylene diisocyanate, p-xylylene diisocyanate, isophorone diisocyanate, bis(isocyanatomethyl)cyclohexane, bis(isocyanatocyclohexyl)methane, 2,5-bis(isocyanatomethyl)bicyclo -[2.2.1]-heptane, 2,6-bis(isocyanatomethyl)bicyclo-[2.2.1]-heptane, tolylene diisocyanate, 4,4'-diphenylmethane diisocyanate and phenylene diisocyanate It is more preferable to include at least one kind selected from (hereinafter also referred to as "isocyanate component N"), It
• the isocyanate compound as a raw material for the thiourethane resin is m-xylylene diisocyanate from the viewpoint of the performance of the thiourethane resin (for example, optical properties (e.g., refractive index and/or Abbe number), heat resistance, specific gravity d, etc.).
• isophorone diisocyanate bis( It is more preferable to contain at least one member selected from the group consisting of isocyanatomethyl)cyclohexane and bis(isocyanatocyclohexyl)methane (hereinafter also referred to as "isocyanate component N1"), and contain isocyanate component N1 as the main component. is even more preferable.
• the thiourethane resin may contain components other than the polymer of at least one isocyanate compound and the polythiol composition.
• components that may be contained in the thiourethane resin reference may be made to the components that may be contained in the polymerizable composition described later.
• the thiourethane resin is preferably recovered in at least one of the process of manufacturing eyeglass lenses, the process of manufacturing eyeglasses, and the process of disposing of eyeglasses. According to this aspect, recycling of thiourethane resin, which is a material for eyeglass lenses, is realized.
• the manufacturing process of eyeglass lenses refers to the process of manufacturing resin by blending monomers that are resin raw materials and performing cast polymerization, and/or the process of cutting a resin molded body to obtain eyeglass lenses.
• the eyeglass manufacturing process refers to the process of manufacturing eyeglasses by combining eyeglass lenses and other components such as eyeglass frames.
• the process of disposing of glasses refers to the process of disposing of manufactured glasses that are no longer needed, used glasses, and the like.
• thiourethane resin which is a material for eyeglass lenses, may be generated as waste.
• the thiourethane resin produced in at least one of these processes is used as a starting material, and the thiourethane resin is reacted with a decomposition agent to obtain a polythiol composition that is a decomposition product of the thiourethane resin. .
• the thiourethane resin in the processing waste may be reacted with the decomposition agent by bringing the processing waste containing the thiourethane resin into contact with the decomposition agent. Thereby, the reaction efficiency between the thiourethane resin and the decomposing agent can be further improved.
• the form of the processing waste containing the thiourethane resin there is no particular restriction on the form of the processing waste containing the thiourethane resin, and it may be in the form of a powder or a lump.
• the processing waste containing the thiourethane resin is preferably cutting processing waste (including the concept of polishing waste; the same applies hereinafter) of a molded article containing the thiourethane resin and/or the above-mentioned cutting processing waste passed through a sieve (i.e., This is the cutting waste that passed through the sieve.
• Cutting waste from a molded article containing a thiourethane resin is produced, for example, when an optical material (for example, a lens) is manufactured by cutting a molded article containing a thiourethane resin.
• the generation step is a step of bringing a resin mixture containing a thiourethane resin into contact with a decomposition agent to cause the thiourethane resin in the resin mixture to react with the decomposition agent to generate a polythiol composition. Good too.
• the resin mixture containing the thiourethane resin further contains components other than the thiourethane resin.
• Components other than the thiourethane resin include resins other than the thiourethane resin, inorganic materials for making lenses (for example, glass), and the like.
• the resin other than the thiourethane resin there are no particular limitations on the resin other than the thiourethane resin.
• a hybrid material of thiourethane resin and urethane resin which is produced by adding a polyol compound to the raw materials when producing thiourethane resin
• a hybrid material of thiourethane resin and urea resin produced by adding a polyamine compound to the raw materials when producing thiourethane resin and the like are also included within the scope of resin mixtures containing thiourethane resins and resins other than thiourethane resins.
• a polyolefin film that protects the surface of resin molded objects for making eyeglass lenses.
• a hard coat or primer coat that protects the surface of a resin molded body for making eyeglass lenses, an abrasive used when polishing a resin molded body for making eyeglass lenses,
• a resin material for fixing a resin molded body when cutting a resin molded body for making eyeglass lenses, Tape or tape glue used to fix glass molds used when creating resin moldings for making eyeglass lenses; etc. can also be mentioned.
• the resin mixture contains at least one resin selected from the group consisting of polycarbonate resin, polyallyl carbonate resin, acrylic resin, urethane resin, and episulfide resin as resin other than thiourethane resin.
• resins like thiourethane resins, can also be used as materials for eyeglass lenses.
• the resin mixture containing the thiourethane resin is preferably recovered in at least one of a spectacle lens manufacturing process, a spectacle manufacturing process, and a spectacle disposal process.
• the manufacturing process of spectacle lenses, the manufacturing process of glasses, and the process of disposing of glasses are as described above.
• the resin mixture containing thiourethane resin preferably contains cutting waste containing thiourethane resin.
• the decomposing agent used in this step is a decomposing agent represented by the above formula (1) or the above formula (2).
• the decomposing agent represented by the above formula (1) include ammonia, monomethylamine, monoethylamine, monopropylamine, dimethylamine, diethylamine, dipropylamine, hydrazine, and the like. Among these, ammonia, monomethylamine, and diethylamine are preferred.
• the decomposing agent represented by the above formula (2) include methanol, ethanol, and propanol. Among these, methanol or ethanol is preferred, and methanol is more preferred.
• the charged mass ratio of the decomposing agent to the thiourethane resin (that is, the charged mass ratio [decomposing agent/thiourethane resin]) can be adjusted as appropriate, but is preferably 0.10 or more and less than 2.0.
• the charging mass ratio [decomposer/thiourethane resin] is 0.10 or more, the production of the polythiol composition is further promoted.
• the charged mass ratio [decomposing agent/thiourethane resin] is less than 2.0, the residual of the decomposing agent in the reaction mixture can be further suppressed.
• the charging mass ratio [decomposer/thiourethane resin] is more preferably 0.10 or more and less than 1.0, still more preferably 0.15 to 0.95, and still more preferably 0.20 to 0.90. It is.
• the number of millimoles of the decomposer charged per 1 g of thiourethane resin is preferably 1.0 mmol/g to 50.0 mmol/g, more preferably 2.0 mmol/g to 30.0 mmol/g, even more preferably 3 .0 mmol/g to 20.0 mmol/g.
• the charged equivalent of the decomposing agent to the thiourethane resin is preferably 1.0 to 15.0, more preferably 1.0 to 10.0, and even more preferably is more than 1.0 and less than 10.0.
• the charging equivalent [decomposer/thiourethane resin] is 1.0 or more, the production of the polythiol composition is further promoted.
• the charging equivalent [decomposing agent/thiourethane resin] is 15.0 or less, the residual of the decomposing agent in the reaction mixture can be further suppressed.
• the thiourethane resin is converted into a thiourethane resin represented by the above formula (2) in the presence of a tertiary amine compound as a decomposition aid. It is preferable to decompose the polythiol composition using a decomposing agent.
• the tertiary amine compound used as a decomposition aid is not particularly limited except that it is a tertiary amine compound.
• the tertiary amine compound as a decomposition aid may be a chain amine compound or a cyclic amine compound.
• the molecular weight of the tertiary amine compound as a decomposition aid is preferably 1000 or less, more preferably 500 or less, still more preferably 300 or less, still more preferably 200 or less.
• the lower limit of the molecular weight of the tertiary amine compound as a decomposition aid is, for example, 59 or more, preferably 70 or more.
• the tertiary amine compound used as a decomposition aid is not particularly limited except that it is a tertiary amine compound.
• a tertiary amine compound as a decomposition aid Preferably, N,N-dimethylethanolamine, N,N-dimethylaminopropanol, N,N-diethyleaminoethanol, N-methyldiethanolamine, diisopropylethylamine, triethylamine, triisopropylamine, triisobutylamine, N,N- Dimethylcyclohexylamine, N-methylmorpholine, N-ethylmorpholine, dimethylpiperazine, 1-ethylpiperidine, 4-(2-hydroxyethyl)morpholine, 1,4-diazabicyclo[2,2,2]octane, diazabicyclo nonene or diazabicycloundecene, More preferably, N,N-dimethylethanolamine, N,
• the charging mass ratio of the tertiary amine compound as a decomposition aid to the decomposition agent represented by the above formula (2) as a decomposition agent can be adjusted as appropriate. However, it is preferably 0.001 to 2.00.
• the charging mass ratio [decomposition aid/decomposition agent] is more preferably 0.002 to 1.50, and still more preferably 0.004 to 1.20.
• the charging molar ratio of the tertiary amine compound as a decomposition aid to the decomposition agent represented by the above formula (2) as a decomposition agent can be adjusted as appropriate. However, it is preferably 0.001 to 3.00.
• the charging molar ratio [decomposition aid/decomposition agent] is more preferably 0.002 to 2.50, still more preferably 0.003 to 2.00, even more preferably 0.004 to 1.50. Yes, more preferably 0.004 to 1.00.
• reaction solvent In the production step, it is preferable that the thiourethane resin and the decomposing agent represented by formula (1) or formula (2) are reacted in the presence of a reaction solvent.
• the reaction solvent is preferably an organic solvent, and more preferably a hydrocarbon compound having 5 to 12 carbon atoms (preferably 6 to 10 carbon atoms, more preferably 7 to 9 carbon atoms).
• the hydrocarbon compound is preferably hexane, heptane, octane, nonane, decane, xylene, mesitylene, or toluene, more preferably heptane, octane, nonane, xylene, mesitylene, or toluene, and particularly preferably , xylene or toluene.
• the number of reaction solvents may be one, or two or more.
• reaction temperature The reaction temperature between the thiourethane resin and the decomposing agent represented by formula (1) or formula (2) in the production step can be adjusted as appropriate.
• the thiourethane resin and the decomposing agent represented by formula (1) or formula (2) are heated at 50°C to 200°C (more preferably 60°C to 180°C, still more preferably 70°C to 150°C).
• the contact is preferably carried out under a temperature condition of (ie, reaction temperature).
• reaction temperature is 50° C. to 200° C.
• the purity of the polythiol component as the main component in the target polythiol composition i.e., the content of the main component relative to the total amount of the polythiol composition
• reaction time The reaction time between the thiourethane resin and the decomposing agent represented by formula (1) or formula (2) in the production step can be adjusted as appropriate, but is preferably 0.1 to 20 hours, more preferably The time period is from 0.5 hours to 16 hours, more preferably from 1 hour to 10 hours.
• the generation step includes reacting the thiourethane resin and the decomposing agent represented by formula (1) or formula (2) under a pressure higher than atmospheric pressure.
• the volatilization of the decomposer represented by formula (1) or formula (2) is further suppressed.
• the thiourethane resin and the decomposing agent represented by formula (1) or formula (2) are heated at a pressure lower than atmospheric pressure, preferably 0.01 MPa or more (more preferably 0.01 MPa or more and 2.0 MPa or less, and more preferably 0.01 MPa or more and 2.0 MPa or less, and It includes reacting under high pressure (preferably 0.02 MPa or more and 1.0 MPa or less).
• Examples of the polythiol composition that is the object of the method for producing a polythiol composition according to the first embodiment include those similar to the aforementioned polythiol composition that is a raw material for the thiourethane resin, and preferred embodiments are also the same. .
• the polythiol composition that is the target product and the polythiol composition that is the raw material for the thiourethane resin that is the starting material do not need to be completely the same.
• the type of polythiol component as the main component in the target polythiol composition and the thiourethane resin as the starting material It is preferable that the type of the polythiol component as the main component in the raw material polythiol composition is the same.
• optical material B optical material containing thiourethane resin
• cutting waste thiourethane resin
• the polythiol composition that is the target product may have the same polythiol component as the main component and a reduced content of impurities as compared to the polythiol composition that is the raw material for the thiourethane resin that is the starting material. .
• the content of impurities in the target polythiol composition is reduced, thickening of the polythiol composition is suppressed and the pot life of the polythiol composition is extended.
• the target polythiol composition can be used, for example, in the production of thiourethane resin.
• Specific applications of the target polythiol composition include polythiol compositions for producing optical materials (for example, spectacle lenses).
• a polythiol composition is produced by decomposing the thiourethane resin with a decomposer, and a polyurea compound or a polycarbamate compound may also be produced.
• a polythiol composition and a polyurea compound can be generated by decomposing the thiourethane resin.
• the production step in the method for producing a polythiol composition in this case may also correspond to the first step in the method for producing a polyamine compound according to the second embodiment described below.
• a polythiol composition and a polycarbamate compound can be produced by decomposition of the thiourethane resin.
• the production step in the method for producing a polythiol composition in this case may also correspond to step X1 in the method for producing a polyamine compound according to the third embodiment described below.
• the generation step may be a step of decomposing the thiourethane resin with a decomposing agent to generate the polythiol composition, and obtaining a reaction mixture containing the polythiol composition as the target product.
• Other components other than the polythiol composition in the reaction mixture include the aforementioned reaction solvent, residues of the raw materials (thiourethane resin and/or decomposition agent), impurities contained in the raw materials, the aforementioned polyurea compound, and the aforementioned polyurea compound. Examples include polycarbamate compounds, etc.
• the method for producing a polythiol composition according to the first embodiment may include a separation step of separating the polythiol composition from the reaction mixture containing the polythiol composition produced in the production step.
• a separation step There are no particular limitations on the separation method in the separation step, and known methods can be applied. Separation methods in the separation step include filtration, decantation, extraction, distillation, drying (including vacuum drying), purification (for example, column chromatography), and the like.
• a plurality of methods may be used in combination.
• the separation step preferably includes obtaining a filtrate containing the polythiol composition by filtering the reaction mixture containing the polythiol composition obtained in the reaction step. According to this aspect, it is easier to remove solids contained in the reaction mixture (for example, solids containing by-products).
• the separation step comprises obtaining a filtrate containing the polythiol composition
• the separation process is obtaining a filtrate containing the polythiol composition by filtering the reaction mixture containing the polythiol composition; Acid washing the filtrate containing the polythiol composition; separating the polythiol composition from the filtrate after acid washing; (hereinafter referred to as separation mode A).
• separation mode A the alkaline component (for example, the residue of the amine compound) can be easily removed from the filtrate by acid washing, so that a polythiol composition with higher purity of the polythiol component as the main component can be obtained.
• water washing may be added after acid washing, and the polythiol composition may be separated from the filtrate after water washing.
• the acids used for acid washing include hydrochloric acid, carbonic acid, nitric acid, sulfuric acid, acetic acid, formic acid, oxalic acid, and the like.
• the separation step comprises obtaining a filtrate containing the polythiol composition
• the separation process is obtaining a filtrate containing the polythiol composition by filtering the reaction mixture containing the polythiol composition;
• Obtaining an extract containing a polythiol composition by performing extraction by adding a hydrocarbon compound having 5 to 12 carbon atoms as an extraction solvent to an aqueous liquid containing the polythiol composition;
• separation mode B is also included.
• separation mode B first, the polythiol composition in the filtrate containing the polythiol composition is converted to an alkali metal salt, and then extracted with water to obtain an aqueous extract containing the alkali metal salt of the polythiol composition.
• the alkali metal salt of the polythiol composition is then returned to the polythiol composition by adding acid.
• the polythiol composition is extracted from the obtained aqueous liquid containing the polythiol composition using the extraction solvent to obtain an extract containing the polythiol composition.
• the polythiol composition is separated from the obtained extract containing the polythiol composition. According to separation mode B, even when the filtrate containing the polythiol composition contains a large amount of other components other than the polythiol composition, a polythiol composition with a higher purity of the polythiol component as the main component can be obtained.
• the alkali metal in the base containing an alkali metal is preferably sodium, potassium or lithium, more preferably sodium or potassium.
• the base containing an alkali metal include sodium methoxide, sodium ethoxide, sodium propoxide, sodium hydroxide, potassium hydroxide, lithium hydroxide, and the like.
• a base containing an alkali metal can be added to the filtrate in the form of an alcohol solution (methanol solution, ethanol solution, etc.) if necessary.
• examples of the acid added to the aqueous extract containing the alkali metal salt of the polythiol composition include hydrochloric acid, carbonic acid, nitric acid, sulfuric acid, acetic acid, formic acid, and oxalic acid.
• the number of hydrocarbon compounds used as the extraction solvent may be only one, or two or more.
• the preferred embodiment of the hydrocarbon compound as the extraction solvent is the same as the preferred embodiment of the hydrocarbon compound as the reaction solvent described above.
• the reaction solvent and the extraction solvent may be the same or different.
• the separation step comprises obtaining a filtrate containing the polythiol composition
• the separation process is separating the reaction mixture containing the polythiol composition by decantation to obtain a residue containing the polythiol composition;
• Obtaining an extract containing a polythiol composition by performing extraction by adding a hydrocarbon compound having 5 to 12 carbon atoms as an extraction solvent to an aqueous liquid containing the polythiol composition;
• separation mode C Separation mode C
• the method for producing a polythiol composition according to the first embodiment may further include, before the reaction step, a classification step of classifying cutting waste containing thiourethane resin.
• the classified cutting waste is reacted with a decomposing agent represented by formula (1) or formula (2).
• the method for producing a polythiol composition according to the first embodiment includes a classification step, in the reaction step, cutting waste consisting of particles having a small particle size (i.e., average particle diameter) and the formula (1) or the formula Since the thiourethane resin is brought into contact with the decomposing agent represented by formula (2), the reaction efficiency between the thiourethane resin and the decomposing agent represented by formula (1) or formula (2) can be further improved.
• the average particle diameter in the present disclosure includes, for example, the number average particle diameter.
• the particle diameter for example, an equivalent circle diameter can be mentioned.
• classification methods include sieving, centrifugation, and the like. Regarding the mode of performing sieving as classification, the following sieving process can be referred to.
• the method for producing a polythiol composition according to the first embodiment may further include, before the production step, a sieving step in which cutting waste containing thiourethane resin is sieved.
• a sieving step in which cutting waste containing thiourethane resin is sieved.
• the cutting waste that has passed through the sieve is brought into contact with the decomposing agent represented by formula (1) or formula (2), so that the thiourethane resin in the cutting waste that has passed through the sieve is A decomposing agent represented by formula (1) or formula (2) is reacted.
• the method for producing a polythiol composition according to the first embodiment includes a sieving step, in the generation step, cutting waste consisting of particles having a small particle size and a compound represented by formula (1) or formula (2) Since the decomposing agent is brought into contact with the decomposing agent, the reaction efficiency between the thiourethane resin and the decomposing agent represented by formula (1) or formula (2) can be further improved.
• the nominal opening of the sieve as defined in JIS Z-8801-1:2019 is, for example, 0.1 mm to 20 mm, preferably 0.1 mm to 10 mm, more preferably 0.1 mm to 5 mm, and Preferably it is 0.1 mm to 2 mm, more preferably 0.3 mm to 2 mm, still more preferably 0.5 mm to 1.5 mm.
• the method for producing a polythiol composition according to the first embodiment may further include, before the production step, a washing step of washing the thiourethane resin with a hydrocarbon compound having 5 to 12 carbon atoms as a washing solvent.
• a washing step of washing the thiourethane resin with a hydrocarbon compound having 5 to 12 carbon atoms as a washing solvent.
• the reaction step the thiourethane resin washed in the washing step is reacted with the decomposing agent represented by formula (1) or formula (2).
• the cleaning process removes the residue from the cutting machine attached to the cutting waste. Since the oil can be effectively removed, a polythiol composition with higher purity of the polythiol component as the main component can be obtained.
• the number of hydrocarbon compounds used as a cleaning solvent may be one, or two or more.
• Preferred embodiments of the hydrocarbon compound as the cleaning solvent are the same as the preferred embodiments of the hydrocarbon compound as the reaction solvent described above.
• the reaction solvent and the washing solvent may be the same or different.
• the cleaning method in the cleaning step is not particularly limited, and any known method can be applied, such as a method of adding and mixing the above-mentioned cleaning solvent to cutting debris containing thiourethane resin (for example, thiourethane resin debris).
• the sieving step and the washing step are preferably performed in this order. In this case, it is not necessary to wash the cutting debris that did not pass through the sieve, so the amount of cleaning solvent used can be further reduced.
• the method for producing a polymerizable composition according to the first embodiment of the present disclosure includes: A step of manufacturing a polythiol composition by the method for manufacturing a polythiol composition according to the first embodiment described above; A step of obtaining a polymerizable composition containing the polythiol composition and the polyisocyanate compound by mixing at least the polythiol composition and the polyisocyanate compound; including.
• the method for producing a polymerizable composition according to the first embodiment may include other steps as necessary.
• a polythiol composition is produced using a thiourethane resin (for example, thiourethane resin in cutting waste of a molded body of thiourethane resin) as a starting material
• a thiourethane resin for example, thiourethane resin in cutting waste of a molded body of thiourethane resin
• a polymerizable composition containing the polythiol composition produced above and a polyisocyanate compound is produced.
• the obtained polymerizable composition can be used again for producing thiourethane resin.
• the main component is A polythiol composition having a high purity polythiol component can be obtained. Since the method for producing a polymerizable composition according to the first embodiment uses such a polythiol composition, the polymerizable composition obtained by the method for producing a polymerizable composition according to the first embodiment has various performance characteristics. [For example, a resin with excellent optical properties (for example, refractive index and/or Abbe number), heat resistance, specific gravity d, etc.] can be produced. Therefore, the polymerizable composition obtained by the method for producing a polymerizable composition according to the first embodiment is particularly suitable as a composition for producing a thiourethane resin for optical materials.
• Step of obtaining polymerizable composition In the step of obtaining a polymerizable composition, at least the polythiol composition and the polyisocyanate compound are mixed to obtain a polymerizable composition containing the polythiol composition and the polyisocyanate compound.
• the preferred embodiment of the polyisocyanate compound used in the step of obtaining the polymerizable composition is the same as the preferred embodiment of the "isocyanate compound as a raw material for thiourethane resin" explained in the section "Production method of polythiol composition”.
• the mixing ratio of the polythiol composition and the polyisocyanate compound is not particularly limited.
• the ratio of the charged mass of the polythiol composition to the charged mass of the polyisocyanate compound is preferably 0.10 to 10.0. It is more preferably 0.20 to 5.00, still more preferably 0.50 to 1.50, and even more preferably 0.70 to 1.30.
• the molar ratio (mercapto group/isocyanato group) between the mercapto group of the polythiol compound and the isocyanato group of the polyisocyanate compound contained in the polythiol composition is preferably 0.5 to 3.0, more preferably 0.6 to 2. It is more preferably 0, and even more preferably 0.8 to 1.3.
• the total mass of the polythiol composition and the polyisocyanate compound is not particularly limited, but is preferably 60% by mass or more based on the total amount of the polymerizable composition to be produced, More preferably it is 80% by mass or more, and still more preferably 90% by mass or more.
• the step of obtaining a polymerizable composition is a step of obtaining a polymerizable composition containing a polythiol composition and a polyisocyanate composition by mixing a polythiol composition and a polyisocyanate composition containing a polyisocyanate compound. There may be.
• the polyisocyanate composition means a composition containing at least one polyisocyanate compound.
• the polyisocyanate composition may contain components other than the polyisocyanate compound as impurities.
• the polyisocyanate composition preferably contains at least one polyisocyanate compound as a main component.
• the meaning of "contained as a main component" is as described above.
• the polyisocyanate composition preferably contains xylylene diisocyanate.
• a polyisocyanate composition containing xylylene diisocyanate will also be referred to as an XDI composition.
• the XDI composition preferably contains xylylene diisocyanate as a main component.
• the XDI composition preferably contains at least one selected from the group consisting of the following compound (N1), the following compound (N2), and the following compound (N3).
• the peak area of compound (N1) in gas chromatography measurement under GC conditions 1 below is 0.20 ppm or more with respect to peak area 1 of xylylene diisocyanate. It is preferable.
• -GC condition 1- Filler; DB-1 (film thickness) 1.5 ⁇ m Column; inner diameter 0.53 mm x length 60 m (manufactured by Agilent)
• Oven temperature Increase the temperature from 130°C to 220°C at a rate of 3°C/min, and after reaching 220°C, increase the temperature to 300°C at a rate of 10°C/min.
• the peak area of the compound (N1) is more preferably 5.0 ppm or more, still more preferably 50 ppm or more, even more preferably 100 ppm or more, based on the peak area 1 of xylylene diisocyanate.
• the peak area of the compound (N1) is preferably 4000 ppm or less, more preferably 3000 ppm or less, even more preferably 2000 ppm or less, still more preferably 1500 ppm or less, still more preferably 1000 ppm or less, based on the peak area 1 of xylylene diisocyanate. .
• the peak area of the compound (N1) can be measured according to the method described in paragraph 0377 of Japanese Patent No. 6373536.
• the peak area of compound (N2) in gas chromatography measurement under GC conditions 2 below is 0.05 ppm or more with respect to the peak area 1 of xylylene diisocyanate. It is preferable.
• -GC condition 2- Column: HP-50+, inner diameter 0.25 mm x length 30 m x film thickness 0.25 ⁇ m (manufactured by Hewlett-Packard) Oven temperature: Raise the temperature from 50°C to 280°C at a rate of 10°C/min, and hold for 6 min after reaching 280°C.
• the peak area of the compound (N2) is more preferably 0.1 ppm or more, still more preferably 0.3 ppm or more, even more preferably 0.6 ppm or more, based on the peak area 1 of xylylene diisocyanate.
• the peak area of the compound (N2) is preferably 200 ppm or less, more preferably 150 ppm or less, even more preferably 100 ppm or less, still more preferably 80 ppm or less, still more preferably 70 ppm or less, and Preferably it is 60 ppm or less.
• the peak area of the compound (N2) can be measured according to the method described in paragraphs 0375 and 0376 of Japanese Patent No. 6373536.
• the peak area of compound (N3) in gas chromatography measurement under GC conditions 1 described above is 0.10 ppm or more with respect to the peak area 1 of xylylene diisocyanate. It is preferable that there be.
• the peak area of the compound (N3) is more preferably 0.1 ppm or more, still more preferably 3.0 ppm or more, still more preferably 5.0 ppm or more, based on the peak area 1 of xylylene diisocyanate.
• the peak area of the compound (N3) is preferably 1000 ppm or less, more preferably 500 ppm or less, even more preferably 300 ppm or less, still more preferably 100 ppm or less, and still more preferably 75 ppm or less, based on the peak area 1 of xylylene diisocyanate. .
• the peak area of the compound (N3) can be measured according to the method described in paragraph 0377 of Japanese Patent No. 6373536.
• the acid content of the XDI composition is preferably 3000 ppm or less, more preferably 2000 ppm or less, still more preferably 1000 ppm or less, even more preferably 100 ppm or less, even more preferably 50 ppm or less, still more preferably 30 ppm or less, and still more preferably less than 15 ppm. .
• the lower limit of the acid content of the XDI composition is not particularly limited, the lower limit is, for example, 1 ppm.
• the acid content of the XDI composition can be measured according to the method described in paragraph 0091 of International Publication No. 2021/256417.
• the XDI composition may also include a stabilizer.
• the above polythiol composition and a polyisocyanate compound are mixed, but if necessary, the above polythiol composition and polyisocyanate compound are mixed with other components. Good too.
• other components include polymerization catalysts, internal mold release agents, resin modifiers, chain extenders, crosslinking agents, radical scavengers, light stabilizers, ultraviolet absorbers, antioxidants, oil-soluble dyes, and fillers. , adhesion improvers, antibacterial agents, antistatic agents, dyes, optical brighteners, fluorescent pigments, inorganic pigments, and the like.
• polymerization catalyst examples include tertiary amine compounds, inorganic or organic acid salts thereof, metal compounds, quaternary ammonium salts, organic sulfonic acids, and the like.
• acidic phosphate ester can be used as the internal mold release agent.
• acidic phosphoric acid esters include phosphoric acid monoesters and phosphoric acid diesters, each of which can be used alone or in combination of two or more types.
• the resin modifier examples include olefin compounds including episulfide compounds, alcohol compounds, amine compounds, epoxy compounds, organic acids, organic acid anhydrides, (meth)acrylate compounds, and the like.
• the (meth)acrylate compound means at least one of an acrylate compound and a methacrylate compound.
• the above-mentioned components can be mixed according to a conventional method, and the mixing method is not particularly limited.
• the resin manufacturing method according to the first embodiment of the present disclosure includes: A step of manufacturing a polymerizable composition by the method for manufacturing a polymerizable composition according to the first embodiment described above; Obtaining a resin by curing the polymerizable composition; including.
• the resin manufacturing method according to the first embodiment may include other steps as necessary.
• the resin manufactured by the resin manufacturing method according to the first embodiment and the resin according to the first embodiment described below are both thiourethane resins, and the thiourethane resin is one of the starting materials of the polythiol composition. In order to distinguish it from the above, in this disclosure, it is simply referred to as "resin".
• the resin is obtained by curing the polymerizable composition.
• Curing of the polymerizable composition can be performed by polymerizing monomers (specifically, a polythiol composition and a polyisocyanate compound; the same applies hereinafter) in the polymerizable composition.
• the polymerizable composition may be subjected to treatments such as filtration and deaeration.
• the polymerization conditions for example, polymerization temperature, polymerization time, etc.
• the polymerization conditions for polymerizing the monomers in the above polymerizable composition include the composition of the composition, the type and amount of monomers used in the composition, and the amount of polymerization catalyst in the composition.
• Examples of the polymerization temperature include -50°C to 150°C, 10°C to 150°C, and the like.
• Examples of the polymerization time include 1 hour to 200 hours, 1 hour to 80 hours, and the like.
• the resin may be obtained by subjecting the polymer obtained by polymerization of monomers to a treatment such as annealing.
• a treatment such as annealing.
• the temperature for annealing include 50°C to 150°C, 90°C to 140°C, and 100°C to 130°C.
• a method for manufacturing a molded body according to a first embodiment of the present disclosure is a method for manufacturing a molded body containing a resin, comprising: A step of manufacturing a polymerizable composition by the method for manufacturing a polymerizable composition according to the first embodiment described above; obtaining a molded article containing a resin by curing the polymerizable composition; including.
• the method for manufacturing a molded body according to the first embodiment may include other steps as necessary.
• the resin-containing molded article is obtained by curing the polymerizable composition.
• the section "Method for producing resin" can be referred to as appropriate.
• polymerization in this step is cast polymerization.
• cast polymerization first, the polymerizable composition is injected between molds held by a gasket, tape, or the like. At this time, defoaming treatment, filtration treatment, etc. may be performed as necessary.
• the composition is cured between the molds to obtain a cured product.
• the cured product is removed from the mold to obtain a resin-containing molded product.
• the monomer may be polymerized by heating the polymerizable composition. This heating can be performed, for example, using a heating device equipped with a mechanism for heating the object to be heated, such as in an oven or in water.
• a method for manufacturing an optical material (for example, a lens) according to a first embodiment of the present disclosure is a method for manufacturing an optical material (for example, a lens) containing a molded body containing a resin, the method comprising: A step of manufacturing a polymerizable composition by the method for manufacturing a polymerizable composition according to the first embodiment described above; obtaining a molded article containing a resin by curing the polymerizable composition; including.
• the method for manufacturing an optical material (for example, a lens; the same applies hereinafter) according to the first embodiment may include other steps as necessary.
• the method for manufacturing an optical material according to the first embodiment is an application of the method for manufacturing a molded body according to the first embodiment.
• a molded body that can be applied to optical materials for example, lenses
• optical materials include lenses (for example, eyeglass lenses, camera lenses, polarized lenses), light emitting diodes (LEDs), and the like.
• lenses for example, eyeglass lenses, camera lenses, polarized lenses
• LEDs light emitting diodes
• the method for manufacturing an optical material may include a step of forming a coating layer on one or both sides of a molded article containing a resin.
• the coating layer include a primer layer, a hard coat layer, an antireflection layer, an antifogging coat layer, an antifouling layer, a water repellent layer, and the like.
• Each of these coating layers may be formed individually, or a plurality of coating layers may be formed in a multilayer structure. When coating layers are formed on both sides, the same coating layer or different coating layers may be formed on each side.
• the components of the coating layer can be appropriately selected depending on the purpose.
• Components of the coating layer include, for example, resins (for example, urethane resins, epoxy resins, polyester resins, melamine resins, polyvinyl acetal resins, etc.), infrared absorbers, light stabilizers, antioxidants, photochrome compounds, dyes, Examples include pigments and antistatic agents.
• the polymerizable composition according to the first embodiment of the present disclosure contains the polythiol composition obtained by the method for producing a polythiol composition according to the first embodiment described above, and a polyisocyanate compound.
• the polymerizable composition according to the first embodiment can be manufactured by the method for manufacturing a polymerizable composition according to the first embodiment described above.
• the method for manufacturing the polymerizable composition according to the first embodiment described above can be appropriately referred to.
• the charged mass [polythiol composition/polyisocyanate compound] should be read as the content mass ratio [polythiol composition/polyisocyanate compound], and the total charged mass of the polythiol composition and polyisocyanate compound is the proportion of the polythiol composition and polyisocyanate compound. It is read as the total content mass including the compound.
• the resin according to the first embodiment of the present disclosure is a cured product of the polymerizable composition according to the first embodiment of the present disclosure described above.
• the molded article according to the first embodiment of the present disclosure is a molded article containing the resin according to the first embodiment described above.
• the optical material (for example, a lens) according to the first embodiment is an optical material (for example, a lens) containing the resin according to the first embodiment described above.
• the resin according to the first embodiment, the molded article according to the first embodiment, and the optical material (for example, a lens) according to the first embodiment are the resin manufacturing method according to the first embodiment and the first embodiment, respectively. It can be manufactured by the method for manufacturing a molded body according to the embodiment and the method for manufacturing an optical material (for example, a lens) according to the first embodiment.
• Preferred aspects of the resin according to the first embodiment, the molded article according to the first embodiment, and the optical material (for example, a lens) according to the first embodiment are the method for manufacturing the resin according to the first embodiment described above, Preferred aspects of the method for manufacturing a molded body according to the first embodiment and the method for manufacturing an optical material (for example, a lens) according to the first embodiment can be referred to.
• the glass transition temperature Tg of the resin (or molded body) according to the first embodiment is preferably 70°C or higher, more preferably 80°C or higher, and even more preferably 85°C or higher.
• the glass transition temperature Tg may be 130°C or lower, 120°C or lower, or 110°C or lower.
• the refractive index (ne) of the resin (or molded body) according to the first embodiment is preferably 1.500 or more, more preferably 1.540 or more, and even more preferably is 1.590 or more.
• the upper limit of the refractive index (ne) is not particularly limited, but is, for example, 1.750.
• the Abbe number of the resin (or molded body) according to the first embodiment is preferably 28 or more, more preferably 30 or more from the viewpoint of application to optical materials.
• the upper limit of the Abbe's number is not particularly limited, but is, for example, 50, preferably 45.
• the specific gravity d of the resin (or molded body) according to the first embodiment is preferably 1.10 or more, more preferably 1.20 or more from the viewpoint of application to optical materials.
• the upper limit of the specific gravity d is not particularly limited, but is, for example, 1.50, preferably 1.40.
• the method for producing a polyamine compound according to the second embodiment includes: A first step of decomposing the thiourethane resin with a decomposing agent represented by the following formula (1) to generate a polyurea compound; A second step of decomposing the polyurea compound with a decomposing agent represented by the following formula (3) to generate a polyamine compound; including.
• R 1 and R 2 each independently represent a hydrogen atom, an alkyl group having 1 to 3 carbon atoms, or an amino group (provided that when R 1 and R 2 are both amino groups, except).
• R 11 and R 12 each independently represent a hydroxy group, a mercapto group, an amino group, or a monomethylamino group.
• the method for producing a polyamine compound according to the second embodiment has excellent removability of the decomposing agent represented by formula (1) from the reaction system after the decomposition reaction in the first step.
• the decomposing agent represented by formula (1) can be easily removed from the reaction system after the decomposition reaction in the first step by volatilization, distillation, or the like.
• the reason why such an effect is obtained is thought to be that the decomposer represented by formula (1) is a compound with a low boiling point.
• the concept of "reaction system after the decomposition reaction in the first step” includes not only the reaction system after the first step but before the second step, but also the reaction system after the first step and during the second step. The reaction system after the second step is also included.
• the decomposing agent represented by formula (1) can be produced together with the target polyamine compound. Even in this case, the removability of the decomposer represented by formula (1) from the reaction system during and after the second step is excellent.
• the method for producing a polyamine compound according to the second embodiment also has excellent removability of the decomposing agent represented by formula (3) from the reaction system after the decomposition reaction in the second step.
• the decomposing agent represented by formula (3) can be easily removed from the reaction system after the decomposition reaction in the second step by volatilization, distillation, or the like. The reason why such an effect is obtained is thought to be that the decomposer represented by formula (3) is a compound with a low boiling point.
• the first step is a step in which a thiourethane resin is decomposed by a decomposing agent represented by the above formula (1) to generate a polyurea compound.
• the production step in the method for producing a polythiol composition according to the first embodiment can be referred to.
• a polyurea compound and the above-mentioned polythiol composition can be produced by decomposing the thiourethane resin with the decomposing agent represented by the above formula (1).
• Preferred embodiments of the thiourethane resin and the decomposing agent represented by formula (1) in the first step are the thiourethane resin and the decomposition agent represented by formula (1) in the method for producing a polythiol composition according to the first embodiment, respectively. This is the same as the preferred embodiment of the decomposing agent.
• the first step preferably includes reacting the thiourethane resin and the decomposing agent represented by formula (1) under a pressure higher than atmospheric pressure. Thereby, the volatilization of the decomposing agent represented by formula (1) can be further suppressed.
• the thiourethane resin and the decomposing agent represented by formula (1) are heated at a pressure higher than atmospheric pressure, preferably 0.01 MPa or more (more preferably 0.01 MPa or more and 2.0 MPa or less, even more preferably 0.02 MPa). 1.0 MPa or less)).
• the polyurea compound produced in the first step is an aminated decomposition product of the thiourethane resin, which is produced by the reaction between the thiourethane resin and the decomposing agent represented by formula (1) (i.e., aminated decomposition).
• Polyurea compounds are compounds that contain two or more urea bonds. In the polyurea compound, for example, all the isocyanato groups in the polyisocyanate compound, which is one of the raw materials for the thiourethane resin, and the amino group or monoalkylamino group of the amine compound A react to form a urea bond.
• a polyurea compound having such a structure is defined as a polyamine compound (for example, m-xylylene diisocyanate (XDA)) corresponding to a polyisocyanate compound (for example, m-xylylene diisocyanate (XDI)), which is one of the raw materials, and an amine. It is sometimes referred to as the urea form of Compound A (eg, monoethanolamine (MEA)).
• the polyamine compound corresponding to the polyisocyanate compound means a compound in which all isocyanate groups in the polyisocyanate compound are replaced with amino groups.
• the polyamine compound corresponding to the polyisocyanate compound is the object in the method for producing a polyamine compound according to the second embodiment.
• the first step is A reaction step of reacting a thiourethane resin with a decomposing agent represented by formula (1) to obtain a reaction mixture containing a polyurea-containing mixture containing a polyurea compound; a separation step of separating the polyurea-containing mixture from the reaction mixture; May contain.
• the polyurea-containing mixture separated in the first separation step and the decomposing agent represented by formula (3) are mixed to remove the polyurea in the polyurea-containing mixture.
• the compound and the decomposing agent represented by formula (3) are reacted.
• the polyurea-containing mixture means a mixture of two or more urea compounds including a polyurea compound.
• the reaction mixture, the reaction step, and the separation step are also referred to as a first reaction mixture, a first reaction step, and a first separation step, respectively.
• the preferred embodiment of the reaction in the first reaction step is as described above.
• the separation method in the first separation step is not particularly limited, and any known method can be applied.
• Examples of the separation method in the first separation step include filtration, decantation, extraction, distillation, drying (including vacuum drying), purification (for example, column chromatography), and the like.
• As a separation method a plurality of methods may be used in combination.
• the first separation step preferably includes filtering the first reaction mixture to obtain the polyurea-containing mixture as a filtrate.
• the obtained filtrate may be subjected to operations such as washing.
• the filtrate obtained by filtering the first reaction mixture contains by-products produced by the aminolysis reaction (specifically, by-products when the polyurea-containing mixture is the main product).
• Polythiol compositions may be included.
• the polythiol composition as a by-product the aforementioned preferred embodiments of the polythiol composition as a raw material for thiourethane resin can be referred to as appropriate.
• the polythiol composition as a by-product resulting from the aminolysis reaction can be used as a raw material for the production of new thiourethane resins. This allows effective use (ie, recycling) of materials.
• the first separation step preferably involves separating the supernatant liquid and extracting and washing as an extraction residue by a decantation method. , obtaining a polyurea-containing mixture.
• the obtained extraction residue may be subjected to operations such as washing.
• the supernatant liquid may contain a polythiol composition, which is a byproduct produced by the aminolysis reaction (specifically, a byproduct when the polyurea-containing mixture is the main product).
• the aforementioned preferred embodiments of the polythiol composition as a raw material for thiourethane resin can be referred to as appropriate.
• the polythiol composition as a by-product resulting from the aminolysis reaction can be used as a raw material for the production of new thiourethane resins. This allows effective use (ie, recycling) of materials.
• the first separation step preferably comprises: filtering the first reaction mixture to obtain a filtrate; removing the alkali metal salt of the polythiol composition as a by-product from the filtrate by adding a base containing an alkali metal to the filtrate and then performing extraction by adding water; separating a polyurea-containing mixture from the filtrate from which the alkali metal salt has been removed; including.
• the polyurea-containing mixture can be separated from the filtrate from which the alkali metal salt has been removed, for example, by methods such as concentration and drying.
• the second step is a step in which the polyurea compound produced in the first step is decomposed by a decomposing agent represented by formula (3) to produce a polyamine compound.
• a decomposing agent represented by formula (3) to produce a polyamine compound.
• the second step by mixing the polyurea-containing mixture separated in the first separation step and the decomposing agent represented by formula (3), the polyurea compound in the polyurea-containing mixture and the formula ( 3) may be reacted with the decomposing agent represented by 3).
• the reaction in the second step is superior in production efficiency of polyamine compounds compared to the known reaction of obtaining polyamine compounds by reacting a polyurea compound with sodium hydroxide.
• the amount of polyamine compound produced can be increased compared to the case where the above-mentioned known reaction is applied.
• Such an effect can be confirmed by analyzing the reaction mixture obtained in the second step by gas chromatography (GC).
• the second step preferably includes reacting the polyurea compound and the decomposing agent represented by formula (3) under a pressure higher than atmospheric pressure. Thereby, the volatilization of the decomposing agent represented by formula (3) can be further suppressed.
• the polyurea compound and the decomposing agent represented by formula (3) are heated at a pressure higher than atmospheric pressure, preferably 0.01 MPa or more (more preferably 0.01 MPa or more and 2.0 MPa or less, still more preferably 0.02 MPa or more). 1.0 MPa or less).
• the decomposing agent represented by formula (3) used in the second step is preferably ethylenediamine, N,N'-dimethylethylenediamine, 2-aminoethanol, or ethylene glycol.
• the charged equivalent of the decomposing agent represented by formula (3) to the polyurea compound is preferably 0.1 to 50. Yes, more preferably 0.15 to 45, still more preferably 0.2 to 40.
• the charging equivalent [decomposer represented by formula (3)/polyurea compound] is 0.1 or more, the production of the polyamine compound is further promoted.
• the charging equivalent [decomposing agent represented by formula (3)/polyurea compound] is 50 or less, it is advantageous in terms of reducing the amount of the decomposing agent represented by formula (3) used.
• the second step by mixing the polyurea-containing mixture separated in the first separation step and the decomposing agent represented by formula (3), the polyurea compound in the polyurea-containing mixture and the formula (3) are mixed. ), the total amount of the polyurea-containing mixture is considered to be a polyurea compound, and the charging equivalent [decomposition agent represented by formula (3)/polyurea compound] is determined. Good too.
• the polyurea compound and the decomposing agent represented by formula (3) can be reacted in the absence of a reaction solvent.
• a reaction solvent for example, by directly mixing a polyurea-containing mixture containing a polyurea compound and a decomposition agent represented by formula (3) in the absence of a reaction solvent, the polyurea compound and formula (3) can be combined in the absence of a reaction solvent. It is possible to react with a decomposing agent represented by: However, in the second step, the polyurea compound and the decomposing agent represented by formula (3) may be reacted in the presence of a reaction solvent.
• reaction temperature The reaction temperature between the polyurea compound and the decomposing agent represented by formula (3) in the second step (hereinafter also referred to as second reaction temperature) is adjusted as appropriate.
• the polyurea compound and the decomposing agent represented by formula (3) are heated at 80°C to 200°C (more preferably 90°C to 200°C, still more preferably 100°C to 200°C, even more preferably 110°C).
• the reaction is preferably carried out under a temperature condition (ie, the second reaction temperature) of 190°C to 190°C, more preferably 120°C to 180°C.
• the reaction may be carried out under pressurized conditions. When the reaction is carried out under pressurized conditions, the reaction time may be shortened.
• reaction time The reaction time between the polyurea compound and the decomposing agent represented by formula (3) in the second step can be adjusted as appropriate, but is preferably 0.1 to 40 hours, more preferably 0.5 to 40 hours.
• the time period is 20 hours, more preferably 1 hour to 10 hours.
• the second step is A reaction step of reacting a polyurea compound with a decomposing agent represented by formula (3) to obtain a reaction mixture containing a polyamine compound; a separation step of separating the polyamine compound from the reaction mixture; May contain.
• the reaction mixture, the reaction step, and the separation step are also referred to as a second reaction mixture, a second reaction step, and a second separation step, respectively.
• the preferred embodiment of the reaction in the second reaction step is as described above.
• the separation method in the second separation step is not particularly limited, and any known method can be applied.
• Examples of the separation method in the second separation step include filtration, decantation, washing, extraction, distillation, reduced pressure (e.g., vacuum), purification (e.g., column chromatography), and the like.
• As a separation method a plurality of methods may be used in combination.
• the second separation step Extracting the polyamine compound from the second reaction mixture with a second extraction solvent to obtain an extract; separating polyamine compounds from the extract; (also referred to as "second separation mode C").
• the polyamine compound is not directly separated from the second reaction mixture, but is separated from the extract obtained by extracting the polyamine compound from the second reaction mixture. This further improves the isolation yield of the polyamine compound finally obtained.
• a preferred embodiment of the second separation step includes an embodiment that includes separating the polyamine compound from the second reaction mixture by a distillation method.
• the insoluble components may be removed from the second reaction mixture by filtration, and the polyamine compound may be separated by distillation from the second reaction mixture from which the insoluble components have been removed. good.
• the second reaction mixture may be diluted before filtration, and the diluted second reaction mixture may be filtered.
• Examples of the second extraction solvent in the second separation mode C include hydrocarbon compounds.
• preferred embodiments of the hydrocarbon compound as the second extraction solvent include the preferred embodiments of the hydrocarbon compound as the first reaction solvent described above.
• the hydrocarbon compound as the second extraction solvent and the hydrocarbon compound as the first reaction solvent may be the same or different.
• the operation for separating the polyamine compound from the extract in the second separation mode C preferably includes distillation.
• the polyamine compound as a target object in the method for producing a polyamine compound according to the second embodiment is a decomposed product of a tipolyurea compound produced by a reaction between a polyurea compound and a decomposing agent represented by formula (3).
• the polyamine compound as the target product is preferably a polyamine compound corresponding to the polyisocyanate compound as a raw material for the thiourethane resin, which is the starting material in the first step (specifically, the isocyanate group in the polyisocyanate compound is converted into an amino group). The substituted compound).
• the target polyamine compound may be any compound containing two or more amino groups.
• the polyamine compound as a target object is It is preferable to include a diamine compound containing two amino groups, Pentamethylene diamine, hexamethylene diamine, m-xylylene diamine, p-xylylene diamine, isophorone diamine, bis(aminomethyl)cyclohexane, bis(aminocyclohexyl)methane, 2,5-bis(aminomethyl)bicyclo-[2 .2.1]-heptane, 2,6-bis(aminomethyl)bicyclo-[2.2.1]-heptane, tolylenediamine, 4,4'-diphenylmethanediamine and phenylenediamine. It is preferable to contain at least one type (hereinafter also referred to as "polyamine component A”), It is more preferable to contain polyamine component A as a main component.
• the target polyamine compounds include m-xylylene diamine, 2,5-bis(aminomethyl)bicyclo-[2.2.1]-heptane, isophorone diisocyanate, bis(isocyanatomethyl)cyclohexane, bis(isocyanatomethyl)cyclohexane, and bis(isocyanatomethyl)cyclohexane.
• cyclohexyl)methane and 2,6-bis(aminomethyl)bicyclo-[2.2.1]-heptane hereinafter also referred to as "polyamine component A1").
• polyamine component A1 2,6-bis(aminomethyl)bicyclo-[2.2.1]-heptane
• the polyamine compound as a target product can be used, for example, as a raw material for a polyisocyanate compound.
• the produced polyisocyanate compound can be used, for example, to produce thiourethane resin or urethane resin.
• polyisocyanate compounds for producing optical materials (for example, lenses).
• a specific example of the method for producing a polyamine compound according to the second embodiment is a method for producing a polyamine compound as a raw material for a polyisocyanate compound for producing an optical material.
• cutting waste containing thiourethane resin generated during the production of optical materials is used as the starting material, recycling of the materials (thiourethane resin, polyisocyanate compound) is effectively realized. be done.
• the method for producing a polyamine compound according to the second embodiment may include steps other than those described above. Other steps include a classification step (for example, a sieving step) and a washing step, which may also be included in the method for producing a polythiol composition according to the first embodiment.
• a classification step for example, a sieving step
• a washing step which may also be included in the method for producing a polythiol composition according to the first embodiment.
• the method for producing a polyisocyanate compound according to the second embodiment of the present disclosure includes: A step of manufacturing a polyamine compound by the method for manufacturing a polyamine compound according to the second embodiment described above; Reacting at least one of the polyamine compound and the hydrochloride of the polyamine compound with carbonyl dichloride to obtain a polyisocyanate compound; including.
• a thiourethane resin is used as a starting material and a polyisocyanate compound can be obtained as a target product, making it possible to recycle the materials (thiourethane resin and its raw material, the polyisocyanate compound). be done.
• polyisocyanate compound produced by the method for producing a polyisocyanate compound according to the second embodiment is not particularly limited, and can be applied to various uses.
• Polyisocyanate compounds can be used, for example, in the production of thiourethane resins or urethane resins.
• target polyisocyanate compound examples include the same compounds as the specific example of "Isocyanate compound as raw material for thiourethane resin" in the "Method for producing polythiol composition” section.
• the target polyisocyanate compound include polyisocyanate compounds for producing optical materials (for example, lenses).
• a specific example of the method for producing a polyisocyanate compound according to the second embodiment is a method for producing a polyisocyanate compound for producing optical materials.
• the material thiourethane resin, polyisocyanate compound
• the material can be effectively utilized (i.e., recycled). ) is effectively realized.
• phosgene carbonyl dichloride
• the method for producing a polymerizable composition according to the second embodiment of the present disclosure includes: A step of manufacturing a polyisocyanate compound by the method for manufacturing a polyisocyanate compound according to the second embodiment described above; A step of obtaining a polymerizable composition containing a polyisocyanate compound and an active hydrogen compound by mixing at least a polyisocyanate compound and an active hydrogen compound; including.
• the method for producing a polymerizable composition according to the second embodiment may include other steps as necessary.
• a polyisocyanate compound is produced using a thiourethane resin (for example, a thiourethane resin in cutting waste of a molded body of thiourethane resin) as a starting material
• a thiourethane resin for example, a thiourethane resin in cutting waste of a molded body of thiourethane resin
• a polymerizable composition containing the polyisocyanate compound produced above and an active hydrogen compound is produced.
• the obtained polymerizable composition can be used again for producing thiourethane resin.
• Step of obtaining polymerizable composition In the step of obtaining a polymerizable composition, at least the above polyisocyanate compound and an active hydrogen compound are mixed to obtain a polymerizable composition containing the above polyisocyanate compound and an active hydrogen compound.
• the active hydrogen compound examples include polythiol compounds, polyol compounds, polyamine compounds, and the like.
• the number of active hydrogen compounds may be one, or two or more.
• a polythiol composition is preferred.
• Preferred embodiments of the polythiol composition as an active hydrogen compound are the same as the preferred embodiments of the "polythiol composition as a raw material for a thiourethane resin" described in the section "Method for producing a polyamine compound.”
• the mixing ratio of the active hydrogen compound and the polyisocyanate compound is not particularly limited.
• the ratio of the charged mass of the active hydrogen compound to the charged mass of the polyisocyanate compound is preferably 0.10 to 10.0. It is more preferably 0.20 to 5.00, still more preferably 0.50 to 1.50, and still more preferably 0.70 to 1.30.
• the molar ratio of the mercapto group of the polythiol compound and the isocyanato group of the polyisocyanate compound contained in the polythiol composition is preferably 0.5 to 3.0, and preferably 0.6 to 2. It is more preferably .0, and even more preferably 0.8 to 1.3.
• the total mass of the active hydrogen compound and the polyisocyanate compound is not particularly limited, but is preferably 60% by mass or more based on the total amount of the polymerizable composition to be produced, More preferably it is 80% by mass or more, and still more preferably 90% by mass or more.
• the above polyisocyanate compound and an active hydrogen compound are mixed, but if necessary, the above polyisocyanate compound and active hydrogen compound and other components may be mixed. Further, in the step of obtaining the polymerizable composition, after mixing at least the polyisocyanate compound and the active hydrogen compound, other components may be added to the mixture. For other components, reference can be made to other components used in the method for producing a polymerizable composition according to the first embodiment.
• the above-mentioned components can be mixed according to a conventional method, and the mixing method is not particularly limited.
• the resin manufacturing method according to the second embodiment of the present disclosure includes: A step of manufacturing a polymerizable composition by the method for manufacturing a polymerizable composition according to the second embodiment described above; Obtaining a resin by curing the polymerizable composition; including.
• the method for manufacturing a resin according to the second embodiment includes manufacturing the polymerizable composition according to the second embodiment instead of manufacturing the polymerizable composition by the method for manufacturing a polymerizable composition according to the first embodiment.
• the method for producing the resin according to the first embodiment is the same except that the polymerizable composition is produced by the method, and the preferred embodiments are also the same.
• a method for manufacturing a molded body according to a second embodiment of the present disclosure is a method for manufacturing a molded body containing a resin, comprising: A step of manufacturing a polymerizable composition by the method for manufacturing a polymerizable composition according to the second embodiment described above; obtaining a molded article containing a resin by curing the polymerizable composition; including.
• the method for producing a molded article according to the second embodiment is a method for producing a polymerizable composition according to the second embodiment, instead of producing a polymerizable composition by the method for producing a polymerizable composition according to the first embodiment. Except for producing the polymerizable composition by the production method, the method is the same as the production method of the molded article according to the first embodiment, and the preferred embodiments are also the same.
• a method for manufacturing an optical material (for example, a lens) according to a second embodiment of the present disclosure is a method for manufacturing an optical material (for example, a lens) including a molded body containing a resin, the method comprising: A step of manufacturing a polymerizable composition by the method for manufacturing a polymerizable composition according to the second embodiment described above; obtaining a molded article containing a resin by curing the polymerizable composition; including.
• the method for manufacturing an optical material (for example, a lens; the same applies hereinafter) according to the second embodiment may include other steps as necessary.
• the method for producing an optical material (for example, a lens) according to the second embodiment instead of producing a polymerizable composition by the method for producing a polymerizable composition according to the first embodiment, the method for manufacturing an optical material (for example, a lens) according to the first embodiment is the same as the method for manufacturing an optical material (for example, a lens), except that the polymerizable composition is manufactured by the method for manufacturing a polymerizable composition, and the preferred embodiments are also the same.
• the resin according to the second embodiment of the present disclosure is a cured product of the polymerizable composition according to the second embodiment of the present disclosure described above.
• the molded article according to the second embodiment of the present disclosure is a molded article containing the resin according to the second embodiment described above.
• the optical material (for example, a lens) according to the second embodiment is an optical material (for example, a lens) containing the resin according to the second embodiment described above.
• the resin, the molded body, and the optical material (for example, a lens) according to the second embodiment are each manufactured using the method of manufacturing a polymerizable composition according to the method of manufacturing the polymerizable composition according to the first embodiment.
• the preferred embodiment is the same as the resin, molded body, and optical material (e.g., lens) according to the first embodiment, except that the polymerizable composition is manufactured by the method for manufacturing a polymerizable composition according to the second embodiment. The same is true.
• the method for producing a polyamine compound according to the third embodiment includes: Step X1 of decomposing a thiourethane resin with a decomposing agent represented by the following formula (2) in the presence of a tertiary amine compound as a decomposition aid to produce a polycarbamate compound; Step X2 of decomposing the polycarbamate compound with a decomposing agent represented by the following formula (3) to generate a polyamine compound; including.
• R 3 represents an alkyl group having 1 to 3 carbon atoms.
• R 11 and R 12 each independently represent a hydroxy group, a mercapto group, an amino group, or a monomethylamino group.
• the method for producing a polyamine compound according to the third embodiment has excellent removability of the decomposing agent represented by formula (2) from the reaction system after the decomposition reaction in step X1.
• the decomposing agent represented by formula (2) can be easily removed from the reaction system after the decomposition reaction in step X1 by volatilization, distillation, or the like. The reason why such an effect is obtained is thought to be that the decomposing agent is a compound with a low boiling point.
• the concept of "reaction system after the decomposition reaction in step X1" includes not only the reaction system after step X1 and before step X2, but also the reaction system after step X1 during and after step Also included are systems.
• the decomposing agent represented by formula (2) can be produced together with the target polyamine compound. Even in this case, the removability of the decomposer represented by formula (2) from the reaction system during and after step X2 is excellent.
• the method for producing a polyamine compound according to the third embodiment also has excellent removability of the decomposing agent represented by formula (3) from the reaction system after the decomposition reaction in step X2.
• the decomposing agent represented by formula (3) can be easily removed from the reaction system after the decomposition reaction in step X2 by volatilization, distillation, or the like. The reason why such an effect is obtained is thought to be that the decomposer represented by formula (3) is a compound with a low boiling point.
• Step X1 is a step in which a thiourethane resin is decomposed by a decomposing agent represented by the following formula (2) in the presence of a tertiary amine compound as a decomposition aid to produce a polycarbamate compound.
• step X1 the generation step in the method for producing a polythiol composition according to the first embodiment can be referred to.
• the thiourethane resin is decomposed with a decomposing agent represented by the following formula (2) in the presence of a tertiary amine compound as a decomposition aid, thereby converting the polycarbamate compound and the polythiol composition described above. can be generated.
• Preferred embodiments of the thiourethane resin, the decomposition agent represented by formula (2), and the tertiary amine compound as a decomposition aid in step X1 are the method for producing a polythiol composition according to the first embodiment, respectively.
• the preferred embodiments of the thiourethane resin, the decomposing agent represented by formula (2), and the tertiary amine compound as a decomposition aid are the same as in the above.
• Step X1 includes reacting the thiourethane resin and the decomposing agent represented by formula (2) under a pressure higher than atmospheric pressure in the presence of a tertiary amine compound as a decomposition aid. is preferred. Thereby, the volatilization of the decomposing agent represented by formula (2) can be further suppressed.
• the thiourethane resin and the decomposing agent represented by formula (2) are heated at a pressure higher than atmospheric pressure, preferably 0.01 MPa or more (more preferably 0.01 MPa or more and 2.0 MPa or less, even more preferably 0.02 MPa). 1.0 MPa or less)).
• the polycarbamate compound produced in step X1 is an alcoholylated product of the thiourethane resin produced by the reaction (i.e., alcoholysis) of the thiourethane resin with the decomposing agent represented by formula (2).
• a polycarbamate compound is a compound (ie, a polyurethane compound) that includes two or more carbamate bonds (ie, urethane bonds).
• carbamate bonds ie., urethane bonds
• a polycarbamate compound having such a structure is defined as a carbamate of a polyamine compound (e.g., XDA) corresponding to a polyisocyanate compound (e.g., XDI), which is one of the raw materials, and an alcohol compound (e.g., 1-octanol).
• a polyamine compound corresponding to the polyisocyanate compound means a compound in which all isocyanate groups in the polyisocyanate compound are replaced with amino groups.
• the polyamine compound corresponding to the polyisocyanate compound is the object in the method for producing a polyamine compound according to the third embodiment.
• Process X1 is A reaction step of reacting a thiourethane resin with a decomposing agent represented by formula (2) to obtain a reaction mixture containing a polycarbamate-containing mixture containing a polycarbamate compound; a separation step of separating the polycarbamate-containing mixture from the reaction mixture; May contain.
• the compound and the decomposing agent represented by formula (3) are reacted.
• the polycarbamate-containing mixture means a mixture of two or more carbamate compounds including a polycarbamate compound.
• the reaction mixture, the reaction step, and the separation step are also referred to as reaction mixture X1, reaction step X1, and separation step X2, respectively.
• reaction step X1 The preferred conditions for the reaction step X1 are as described above.
• the reaction mixture produced in the reaction step X1 may contain a polycarbamate-containing mixture as a main product produced by alcoholysis and other components other than the polycarbamate-containing mixture.
• Other components include by-products produced by alcoholysis (for example, polythiol composition), the aforementioned reaction solvent, residues of raw materials (thiourethane resin and/or alcohol compound), and impurities contained in raw materials. etc.
• the polythiol composition as a by-product the aforementioned preferred embodiments of the polythiol composition as a raw material for thiourethane resin can be referred to as appropriate.
• the polythiol composition as a by-product resulting from the alcoholysis reaction can be used as a raw material for the production of new thiourethane resins. This achieves material recycling.
• separation method in the separation step X2 There is no particular restriction on the separation method in the separation step X2, and known methods can be applied. Examples of the separation method in the separation step X2 include filtration, decantation, extraction, distillation, drying (including vacuum drying), purification (for example, column chromatography), and the like. As a separation method, a plurality of methods may be used in combination.
• separation step X2 filtering the reaction mixture X1 to obtain a filtrate; washing the filtrate with acid and then with water; Adding a base containing an alkali metal to the filtrate washed with water, and then washing with water to remove salts (for example, an alkali metal salt of the polythiol composition that is a reaction by-product); separating a polycarbamate-containing mixture from the filtrate from which salts have been removed; (hereinafter referred to as separation mode X1).
• salts for example, an alkali metal salt of the polythiol composition that is a reaction by-product
• the filtrate is washed with an acid (hereinafter also referred to as acid washing), thereby removing amines (eg, tertiary amine compounds) from the filtrate.
• acids used for acid cleaning include hydrochloric acid, carbonic acid, nitric acid, sulfuric acid, acetic acid, formic acid, and oxalic acid.
• the acid is removed from the filtrate by washing the filtrate after acid washing with water.
• the filtrate contains the target polycarbamate-containing mixture, but it is thought that it may also contain a polythiol composition, which is a by-product.
• separation mode X1 a base containing an alkali metal is added to the filtrate washed with water. This converts the polythiol composition in the filtrate into an alkali metal salt. The alkali metal salt of the polythiol composition is then removed from the filtrate by washing the filtrate with water. In separation mode X1, the polycarbamate-containing mixture is separated from the filtrate from which the alkali metal salt of the polythiol composition has been removed by a known method.
• the alkali metal in the base containing an alkali metal is preferably sodium, potassium or lithium, more preferably sodium or potassium.
• the base containing an alkali metal include sodium methoxide, sodium ethoxide, sodium propoxide, sodium hydroxide, potassium hydroxide, lithium hydroxide, and the like.
• a base containing an alkali metal can be added to the filtrate in the form of an alcohol solution (methanol solution, ethanol solution, etc.) if necessary.
• separation solvent X1 a solvent (hereinafter also referred to as separation solvent X1) is added to the filtrate, and separation solvent X1 is added to the filtrate.
• the filtrate may be sequentially subjected to acid washing and water washing.
• the separation solvent X1 the same solvent as the reaction solvent may be used, or an alcohol solvent may be used.
• the addition of the separation solvent X1 to the filtrate may be omitted.
• Step X2 is a step in which the polycarbamate compound produced in Step X1 is decomposed by a decomposing agent represented by formula (3) to produce a polyamine compound.
• the polycarbamate compound in the polycarbamate-containing mixture and the formula (3) are mixed together with the polycarbamate-containing mixture separated in the separation step You may react with the decomposition agent represented by (3).
• the reaction in step X2 is superior in production efficiency of a polyamine compound compared to the known reaction of obtaining a polyamine compound by reacting a polycarbamate compound with sodium hydroxide.
• the amount of polyamine compound produced can be increased compared to the case where the above-mentioned known reaction is applied.
• Such an effect can be confirmed by analyzing the reaction mixture obtained in step X2 by gas chromatogram (GC).
• step X2 in the method for producing a polyamine compound according to the third embodiment the object to be decomposed by the decomposing agent represented by formula (3) is not the polyurea compound produced in the first step in the second embodiment, Except for the polycarbamate compound produced in step X1 in the third embodiment, this step is the same as the second step in the method for producing a polyamine compound according to the third embodiment, and the preferred embodiments are also the same.
• Step X2 includes reacting the polycarbamate compound and the decomposing agent represented by formula (3) under a pressure higher than atmospheric pressure. Thereby, the volatilization of the decomposing agent represented by formula (3) can be further suppressed.
• the polycarbamate compound and the decomposing agent represented by formula (3) are heated at a pressure higher than atmospheric pressure, preferably 0.01 MPa or more (more preferably 0.01 MPa or more and 2.0 MPa or less, still more preferably 0.02 MPa). 1.0 MPa or less)).
• the polyamine compound as a target object in the method for producing a polyamine compound according to the third embodiment is a decomposed product of a thiourethane resin produced by a reaction between a polycarbamate compound and a decomposing agent represented by formula (3).
• the polyamine compound as the target product is preferably a polyamine compound corresponding to the polyisocyanate compound as a raw material for the thiourethane resin that is the starting material in step X1 (specifically, the isocyanate group in the polyisocyanate compound is replaced with an amino group). compound).
• Preferred aspects and preferred uses of the polyamine compound as the target object in the third embodiment are the same as those of the polyamine compound as the target object in the third embodiment, respectively.
• the method for producing a polyamine compound according to the third embodiment may include steps other than those described above. Other steps include a classification step (for example, a sieving step) and a washing step, which may also be included in the method for producing a polythiol composition according to the first embodiment.
• a classification step for example, a sieving step
• a washing step which may also be included in the method for producing a polythiol composition according to the first embodiment.
• the method for producing a polyisocyanate compound according to the third embodiment of the present disclosure includes: A step of manufacturing a polyamine compound by the method for manufacturing a polyamine compound according to the third embodiment described above; Reacting at least one of the polyamine compound and the hydrochloride of the polyamine compound with carbonyl dichloride to obtain a polyisocyanate compound; including.
• the method for producing a polyisocyanate compound according to the third embodiment is to produce a polyamine compound by the method for producing a polyamine compound according to the third embodiment instead of producing the polyamine compound by the method for producing a polyamine compound according to the second embodiment.
• the method for producing a polyisocyanate compound according to the second embodiment is the same except for producing the following, and the preferred embodiments are also the same.
• the method for producing a polymerizable composition according to the third embodiment of the present disclosure includes: A step of manufacturing a polyisocyanate compound by the method for manufacturing a polyisocyanate compound according to the third embodiment described above; A step of obtaining a polymerizable composition containing a polyisocyanate compound and an active hydrogen compound by mixing at least a polyisocyanate compound and an active hydrogen compound; including.
• the method for manufacturing a polymerizable composition according to the third embodiment includes manufacturing a polyisocyanate compound according to the third embodiment, instead of manufacturing a polyisocyanate compound by the method for manufacturing a polyisocyanate compound according to the second embodiment.
• the method for producing the polymerizable composition according to the second embodiment is the same except that the polyisocyanate compound is produced by the method, and the preferred embodiments are also the same.
• the resin manufacturing method according to the third embodiment of the present disclosure includes: A step of manufacturing a polymerizable composition by the method for manufacturing a polymerizable composition according to the third embodiment described above; Obtaining a resin by curing the polymerizable composition; including.
• the method for manufacturing a resin according to the third embodiment includes manufacturing the polymerizable composition according to the third embodiment instead of manufacturing the polymerizable composition by the method for manufacturing a polymerizable composition according to the second embodiment.
• the method is the same as the resin manufacturing method according to the second embodiment except that the polymerizable composition is manufactured by the method, and the preferred embodiments are also the same.
• a method for manufacturing a molded body according to a second embodiment of the present disclosure is a method for manufacturing a molded body containing a resin, comprising: A step of manufacturing a polymerizable composition by the method for manufacturing a polymerizable composition according to the second embodiment described above; obtaining a molded article containing a resin by curing the polymerizable composition; including.
• the method for producing a molded article according to the second embodiment is a method for producing a polymerizable composition according to the second embodiment, instead of producing a polymerizable composition by the method for producing a polymerizable composition according to the first embodiment. Except for producing the polymerizable composition by the production method, the method is the same as the production method of the molded article according to the first embodiment, and the preferred embodiments are also the same.
• a method for manufacturing an optical material (for example, a lens) according to a third embodiment of the present disclosure is a method for manufacturing an optical material (for example, a lens) containing a molded article containing a resin, the method comprising: A step of manufacturing a polymerizable composition by the method for manufacturing a polymerizable composition according to the third embodiment described above; obtaining a molded article containing a resin by curing the polymerizable composition; including.
• the method for producing an optical material for example, a lens
• the method for manufacturing an optical material is the same as the method for manufacturing an optical material (for example, a lens), except that the polymerizable composition is manufactured by the method for manufacturing a polymerizable composition, and the preferred embodiments are also the same.
• the resin according to the third embodiment of the present disclosure is a cured product of the polymerizable composition according to the third embodiment of the present disclosure described above.
• a molded article according to a third embodiment of the present disclosure is a molded article containing the resin according to the third embodiment described above.
• the optical material (for example, a lens) according to the third embodiment is an optical material (for example, a lens) containing the resin according to the third embodiment described above.
• the resin, the molded body, and the optical material (for example, a lens) according to the third embodiment are each manufactured using the method of manufacturing a polymerizable composition according to the method of manufacturing a polymerizable composition according to the second embodiment.
• the preferred embodiment is the same as the resin, molded body, and optical material (e.g., lens) according to the second embodiment, except that the polymerizable composition is manufactured by the method for manufacturing a polymerizable composition according to the third embodiment. The same is true.
• ⁇ Resin performance test> As a performance test of the resin, a performance test was conducted on a flat molded body having a thickness of 2.5 mm. The items of the performance test are as follows. ⁇ Yellow Index (YI) Yellowness was measured using a spectrophotometer CM-5 manufactured by Konica Minolta, Inc. ⁇ L*, a*, and b* Using a spectrophotometer CM-5 manufactured by Konica Minolta, Inc., L*, a*, and b* in the CIE1976 (L*, a*, b*) color system were measured.
• YI Yellowness was measured using a spectrophotometer CM-5 manufactured by Konica Minolta, Inc.
• L*, a*, and b* in the CIE1976 (L*, a*, b*) color system were measured.
• ⁇ Refractive index (ne) and Abbe number ( ⁇ e) Using a Pulfrich refractometer KPR-30 manufactured by Shimadzu Corporation, at 20°C, the wavelength was 546.1 nm (mercury e-line), the wavelength 480.0 nm (Cd F' line), and the wavelength 643.9 nm (Cd C' line). The refractive index (ne, nF', nC') at each wavelength was measured. Based on these measurement results, the refractive index (ne) and Abbe number ( ⁇ e) were determined.
• Tg glass transition temperature
• TMA penetration method 50g load, pin tip 0.5mm ⁇ , heating rate 10°C/min
• TMA-60 thermomechanical analyzer
• ⁇ Specific gravity d It was measured by the Archimedes method at 20°C.
• the polythiol composition (A) one manufactured in Reference Production Example 3, which will be described later, was used.
• the polymerizable composition was filtered under reduced pressure using a PTFE (polytetrafluoroethylene) filter, and then sufficiently degassed under a reduced pressure of 600 Pa until no foaming was observed.
• This degassed polymerizable composition was injected between a pair of glass molds fixed with tape, and then the pair of glass molds were placed in an oven, and the temperature inside the oven was set at 10°C. Next, the temperature inside the oven was raised from 10°C to 120°C over 38 hours.
• the monomers (polyisocyanate compound and polythiol composition) in the degassed polymerizable composition are polymerized, and a molded article containing thiourethane resin R1 is placed between a pair of glass molds (9.0 mm thick). (that is, a cured product of the polymerizable composition) was formed. Subsequently, the inside of the oven was cooled, and after cooling, the pair of glass molds were taken out from the oven, and then the molded bodies were removed from the pair of glass molds to obtain molded bodies.
• the purity of polythiol component A1 in the polythiol composition (A) obtained in Reference Production Example 3 was 91.6%.
• Example 1 ⁇ Decomposition of thiourethane resin (aminolysis using ammonia as a decomposition agent represented by formula (1))>
• Thiourethane resin waste R1 (18.0 g) obtained in Reference Production Example 2
• Toluene (31.9g) and 25% ammonia water (10.1 g) (equivalent to 0.15 mol of ammonia as a decomposer represented by formula (1)), was added to obtain a reaction solution, and the reaction vessel was then sealed with nitrogen gas. Next, the reaction solution in the reaction container was heated to 90° C.
• the reaction solution was cooled to room temperature and filtered under reduced pressure. Through the vacuum filtration, 10.1 g (yield: 91.4%) of polyurea compound B1 was obtained as a filtrate, and a toluene solution containing a polythiol composition was obtained as a filtrate.
• the polyurea compound B1 and the polythiol composition are both decomposition products produced by amine decomposition of the thiourethane resin waste R1.
• ammonia as a decomposition agent represented by formula (1) was volatilized and easily removed from the reaction system.
• Acid washing was performed by adding 30.0 g of 35% hydrochloric acid aqueous solution to the above filtrate (ie, toluene solution containing the polythiol composition). After washing with water twice by adding 30.0 g of degassed water to the toluene solution after acid washing, 12.4 g of a 32% aqueous sodium hydroxide solution and 20 g of degassed water were sequentially added to form an aqueous phase. , an aqueous solution containing an alkali metal salt of polythiol was obtained. The aqueous solution containing the alkali metal salt of polythiol was washed twice with 20.0 g of toluene.
• Example 2 ⁇ Decomposition of thiourethane resin (aminolysis using methylamine as a decomposition agent represented by formula (1))>
• “25% ammonia water (10.1 g) (equivalent to 0.15 mol of ammonia as a decomposing agent expressed by formula (1))” was replaced with "40% methylamine aqueous solution (1.6 g) (formula ( The same operation as in Example 1 was performed except that the amount of methylamine (equivalent to 0.15 mol) as a decomposing agent represented by 1) was changed.
• Example 2 10.9 g (yield: 87.6%) of polyurea compound B2 was obtained as a filtrate by vacuum filtration after the completion of the decomposition reaction, and a toluene solution containing a polythiol composition was obtained as a filtrate. Ta.
• the polyurea compound B2 and the polythiol composition are both decomposition products produced by amine decomposition of the thiourethane resin waste R1.
• methylamine as a decomposer represented by formula (1) was volatilized and easily removed from the reaction system.
• polythiol component A1 4-mercaptomethyl-1,8-dimercapto-3,6-dithiaoctane (i.e., polythiol component A1) as the main component was obtained. 7.01 g (yield: 81.1%) of polythiol composition (A) was obtained.
• Example 3 ⁇ Decomposition of thiourethane resin (aminolysis using dimethylamine as a decomposition agent represented by formula (1))>
• “25% ammonia water (10.1 g) (equivalent to 0.15 mol of ammonia as a decomposing agent represented by formula (1))” was replaced with "13.4 g of 50% dimethylamine aqueous solution (formula (1)
• the same operation as in Example 1 was performed except for changing the amount of dimethylamine (corresponding to 0.15 mol of dimethylamine as a decomposing agent).
• Example 3 after the completion of the decomposition reaction, separation and extraction was performed to obtain an aqueous solution of polyurea compound B3, and water was distilled off from the obtained aqueous solution to obtain 12.8 g of polyurea compound B3 (yield: :95.0%) was obtained.
• a toluene solution containing a polythiol composition was obtained as an organic phase.
• the polyurea compound B2 and the polythiol composition are both decomposition products produced by amine decomposition of the thiourethane resin waste R1.
• dimethylamine as a decomposing agent represented by formula (1) was removed from the reaction system.
• Example 4 ⁇ Decomposition of thiourethane resin (alcohololysis using methanol as a decomposition agent represented by formula (2))>
• Thiourethane resin R1 (18.0 g) obtained in Reference Production Example 2, 31.8 g (1.0 mol) of methanol as a decomposing agent represented by formula (2), 1,4-diazabicyclo-[2,2,2]-octane (1.1 g; 0.010 mol) as a tertiary amine (decomposition aid), was added to obtain a reaction solution, and the reaction vessel was then sealed with nitrogen gas. Next, the reaction solution in the reaction container was heated to 150° C.
• an aqueous solution containing an alkali metal salt of polythiol was obtained as an aqueous phase.
• the aqueous solution containing the alkali metal salt of polythiol was washed twice with 20.0 g of toluene.
• 40.0 g of toluene was added to the aqueous solution after washing, and then 30.0 g of 35% hydrochloric acid aqueous solution was added to perform neutralization.
• the aqueous phase was extracted from the neutralized liquid, and 30.0 g of degassed water was added to the remaining organic phase to perform separation washing twice to obtain a toluene solution in which the polythiol composition was dissolved.
• Example 4 in the process of vacuum filtration after the completion of the decomposition reaction, methanol as a decomposition agent represented by formula (2) was volatilized and easily removed from the reaction system.
• the refractive index of the polythiol composition (A) was measured using a liquid refractometer RA600 manufactured by Kyoto Electronics Industry Co., Ltd.
• the thiol value of the polythiol composition (A) was determined by redox titration using a 0.05M iodine aqueous solution.
• Example 6 ⁇ Manufacture of molded object> The procedure was the same as in Reference Production Example 1 except that the thickness between the pair of glass molds was changed from 9.0 mm to 2.5 mm (i.e., the polythiol composition produced in Reference Production Example 3 was used as polythiol composition (A)). Using product (A)), a molded article containing a thiourethane resin was obtained.
• a molded article containing a thiourethane resin was produced in the same manner as above except that the polythiol composition (A) produced in Reference Production Example 3 was changed to the polythiol composition (A) produced in Examples 1 to 4. I got it.
• Refractive index (ne) and Abbe number ( ⁇ e) Using a Pulfrich refractometer KPR-30 manufactured by Shimadzu Corporation, at 20°C, the wavelength was 546.1 nm (mercury e-line), the wavelength 480.0 nm (Cd F' line), and the wavelength 643.9 nm (Cd C' line). The refractive index (ne, nF', nC') of the molded body at each wavelength was measured. Based on these measurement results, the refractive index (ne) and Abbe number ( ⁇ e) of the molded body were determined.
• thermomechanical analyzer TMA-60 manufactured by Shimadzu Corporation
• TMA penetration method 50 g load, pin tip 0.5 mm ⁇ , heating rate 10 ° C / min
• Example 6X In Example 6X, the same operations as in Example 6 were performed except for the following changes in the production of the molded body, and results similar to those in Example 6 (Table 2) were obtained.
• Example 6 m-xylylene diisocyanate (XDI) (52 parts by mass) was used in the production of the molded body, but in Example 6X, XDI (52 parts by mass) was used as the XDI composition as described above. The composition was changed to composition X1 (the amount of XDI contained was 52 parts by mass).
• XDI composition X1 was produced by adding a trace amount of compound (N1), a trace amount of compound (N2), and a trace amount of compound (N3) to XDI, which is the main component, and mixing these.
• the peak area of the compound (N1) is 0.20 ppm or more (specifically 600 ppm) with respect to the peak area 1 of xylylene diisocyanate
• the peak area of the compound (N2) is 0.05 ppm or more (specifically 18 ppm) with respect to the peak area 1 of xylylene diisocyanate
• the peak area of compound (N3) was 0.10 ppm or more (specifically 100 ppm) relative to the peak area 1 of xylylene diisocyanate.
• Example 7 ⁇ Production of polyamine compound by reaction of polyurea compound B1 obtained in Example 1 and ethylenediamine>
• Polyurea compound B1 2.0 g; 9.0 mmol obtained in Example 1
• Ethylenediamine 3.2 g; 54 mmol
• a decomposing agent represented by formula (3) was added to obtain a reaction solution, and the reaction vessel was then sealed with nitrogen gas.
• the reaction solution in the reaction vessel was heated to 145° C. under sealed conditions, and the reaction was carried out by stirring for 3 hours under pressure conditions higher than atmospheric pressure by 0.01 MPa or more.
• XDA xylylenediamine
• GC gas chromatography
• XDA xylylenediamine
• the mass of the reaction solution after the reaction was 4.9 g
• the concentration of XDA determined from the GC results was 18.6%
• the production yield was 74.6% (two-step yield from thiourethane resin R1). was 68.2%).
• the decomposing agent (ammonia) represented by formula (1) produced by decomposition of polyurea compound B1 was volatilized and easily removed from the reaction solution after the reaction.
• the decomposing agent (ethylenediamine) represented by formula (3) can also be easily removed from the reaction solution after the reaction by distillation.
• Example 8 ⁇ Production of polyamine compound by reaction of polyurea compound B2 obtained in Example 2 and ethylenediamine> Same as Example 7 except that polyurea compound B1 was changed to polyurea compound B2 (2.0 g; 8.0 mmol) obtained in Example 2, and the amount of ethylenediamine was changed to 2.9 g (48 mmol). The following operations were carried out. It was confirmed by gas chromatography (GC) that xylylenediamine (XDA), which is a polyamine compound, was produced by the reaction between polyurea compound B2 and ethylenediamine.
• GC gas chromatography
• the mass of the reaction solution after the reaction was 4.6 g, the concentration of XDA determined from the GC results was 18.2%, and the production yield was 75.6% (two-step yield from thiourethane resin R1). was 66.1%).
• the decomposing agent (methylamine) represented by formula (1) produced by the decomposition of polyurea compound B2 was volatilized and easily removed from the reaction solution after the reaction.
• the decomposing agent (ethylenediamine) represented by formula (3) can also be easily removed from the reaction solution after the reaction by distillation.
• Example 9 ⁇ Production of polyamine compound by reaction of polyurea compound B3 obtained in Example 3 and ethylenediamine> Same as Example 7 except that polyurea compound B1 was changed to polyurea compound B3 (2.0 g; 7.2 mmol) obtained in Example 3, and the amount of ethylenediamine was changed to 2.6 g (43 mmol). The operation was carried out. It was confirmed by gas chromatography (GC) that xylylenediamine (XDA), which is a polyamine compound, was produced by the reaction between polyurea compound B3 and ethylenediamine.
• GC gas chromatography
• the mass of the reaction solution after the reaction was 4.2 g, the concentration of XDA determined from the GC results was 19.3%, and the production yield was 81.9% (two-step yield from thiourethane resin R1). was 77.8%).
• the decomposing agent represented by formula (3) (ethylenediamine) and the decomposing agent represented by formula (1) produced by decomposition of polyurea compound B3 (dimethylamine) are extracted from the reaction solution after the reaction by distillation. can be easily removed.
• Example 10 ⁇ Production of polyamine compound using polycarbamate compound C1 obtained in Example 4> The same operation as in Example 7 except that polyurea compound B1 was changed to polycarbamate C1 (2.0 g; 79 mmol) obtained in Example 4, and the amount of ethylenediamine was changed to 2.9 g (48 mmol). was carried out.
• Gas chromatography (GC) confirmed that xylylenediamine (XDA), a polyamine compound, was produced by the reaction between polycarbamate C1 and ethylenediamine.
• the mass of the reaction solution after the reaction was 4.9 g, the concentration of XDA determined from the GC results was 15.6%, and the production yield was 70.4% (two-step yield from thiourethane resin R1).
• Example 11 ⁇ Production of polyamine compound by reaction of polyurea compound B1 obtained in Example 1 and N,N'-dimethylethylenediamine> 3.2 g (54 mmol) of ethylenediamine as a decomposing agent represented by formula (3) was changed to 4.8 g (54 mmol) of N,N'-dimethylethylenediamine as a decomposing agent represented by formula (3). The same operation as in Example 7 was performed except for this. It was confirmed by gas chromatography (GC) that xylylenediamine (XDA), a polyamine compound, was produced by the reaction between polyurea compound B1 and N,N'-dimethylethylenediamine.
• GC gas chromatography
• the mass of the reaction solution after the reaction was 6.7 g, the concentration of XDA determined from the GC results was 15.8%, and the production yield was 85.5% (two-step yield from thiourethane resin R1). was 78.1%).
• the decomposing agent (ammonia) represented by formula (1) produced by decomposition of polyurea compound B1 was volatilized and easily removed from the reaction solution after the reaction.
• the decomposer (N,N'-dimethylethylenediamine) represented by formula (3) can also be easily removed from the reaction solution after the reaction by distillation.
• Example 12 ⁇ Production of polyamine compound by reaction of polyurea compound B1 obtained in Example 1 and 2-aminoethanol> 3.2 g (54 mmol) of ethylenediamine as a decomposing agent represented by formula (3) was changed to 5.0 g (90 mmol) of 2-aminoethanol as a decomposing agent represented by formula (3), and the reaction temperature was changed. The same operation as in Example 7 was carried out except that the temperature was changed from 145°C to 180°C and the reaction time was changed from 3 hours to 6 hours. Gas chromatography (GC) confirmed that xylylenediamine (XDA), a polyamine compound, was produced by the reaction between polyurea compound B1 and 2-aminoethanol.
• GC Gas chromatography
• the mass of the reaction solution after the reaction was 6.7 g, the concentration of XDA determined from the GC results was 10.2%, and the production yield was 55.7% (two-step yield from thiourethane resin R1). was 50.9%).
• the decomposing agent (ammonia) represented by formula (1) produced by decomposition of polyurea compound B1 was volatilized and easily removed from the reaction solution after the reaction.
• the decomposing agent (2-aminoethanol) represented by formula (3) can also be easily removed from the reaction solution after the reaction by distillation.
• Example 13 ⁇ Production of polyamine compound by reaction of polyurea compound B1 obtained in Example 1 and ethylene glycol> The same operation as in Example 12 was carried out except that 3.2 g (54 mmol) of ethylene diamine as the decomposing agent represented by formula (3) was changed to 5.6 g (90 mmol) of ethylene glycol. It was confirmed by gas chromatography (GC) that xylylenediamine (XDA), which is a polyamine compound, was produced by the reaction between polyurea compound B1 and ethylene glycol. The mass of the reaction solution after the reaction was 6.9 g, the concentration of XDA determined from the GC results was 7.1%, and the production yield was 40.6% (two-step yield from thiourethane resin R1).
• GC gas chromatography
• the decomposing agent (ammonia) represented by formula (1) produced by decomposition of polyurea compound B1 was volatilized and easily removed from the reaction solution after the reaction.
• the decomposing agent (ethylene glycol) represented by formula (3) can also be easily removed from the reaction solution after the reaction by distillation.
• polyamine compounds could be produced using polyurea compounds or polycarbamate compounds produced by decomposition of thiourethane resins as raw materials.
• a polyisocyanate compound can be produced by reacting at least one of the produced polyamine compounds and nitrates of these polyamine compounds with carbonyl dichloride.
• a polymerizable composition can be produced by mixing the obtained polyisocyanate compound and an active hydrogen compound. The obtained polymerizable composition can be used for producing thiourethane resin or urethane resin.

Landscapes

• Chemical & Material Sciences (AREA)
• Organic Chemistry (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Medicinal Chemistry (AREA)
• Polymers & Plastics (AREA)
• Health & Medical Sciences (AREA)
• Sustainable Development (AREA)
• Life Sciences & Earth Sciences (AREA)
• Physics & Mathematics (AREA)
• General Physics & Mathematics (AREA)
• Optics & Photonics (AREA)
• Inorganic Chemistry (AREA)
• Polyurethanes Or Polyureas (AREA)
• Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Priority Applications (4)

Applications Claiming Priority (2)

Publications (1)

Family

ID=90099610

Family Applications (1)

Country Status (5)

Cited By (2)

Citations (10)

Family Cites Families (2)

• 2023
  • 2023-08-23 CN CN202380060599.5A patent/CN119731153A/zh active Pending
  • 2023-08-23 KR KR1020257006347A patent/KR20250047758A/ko active Pending
  • 2023-08-23 WO PCT/JP2023/030285 patent/WO2024048389A1/ja not_active Ceased
  • 2023-08-23 JP JP2024544165A patent/JPWO2024048389A1/ja active Pending
  • 2023-08-23 EP EP23860152.0A patent/EP4582411A1/en active Pending

Patent Citations (12)

Non-Patent Citations (1)

Also Published As

Similar Documents

Legal Events