WO2023284618A1 - Resin composition, polyurethane material, polyurethane composite material, and preparation methods - Google Patents

Resin composition, polyurethane material, polyurethane composite material, and preparation methods Download PDF

Info

Publication number
WO2023284618A1
WO2023284618A1 PCT/CN2022/104319 CN2022104319W WO2023284618A1 WO 2023284618 A1 WO2023284618 A1 WO 2023284618A1 CN 2022104319 W CN2022104319 W CN 2022104319W WO 2023284618 A1 WO2023284618 A1 WO 2023284618A1
Authority
WO
WIPO (PCT)
Prior art keywords
resin composition
polyurethane
reactive component
active hydrogen
acrylate
Prior art date
Application number
PCT/CN2022/104319
Other languages
French (fr)
Chinese (zh)
Inventor
吉明磊
姜磊
季刚
陈翠萍
Original Assignee
道生天合材料科技(上海)股份有限公司
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 道生天合材料科技(上海)股份有限公司 filed Critical 道生天合材料科技(上海)股份有限公司
Publication of WO2023284618A1 publication Critical patent/WO2023284618A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F299/00Macromolecular compounds obtained by interreacting polymers involving only carbon-to-carbon unsaturated bond reactions, in the absence of non-macromolecular monomers
    • C08F299/02Macromolecular compounds obtained by interreacting polymers involving only carbon-to-carbon unsaturated bond reactions, in the absence of non-macromolecular monomers from unsaturated polycondensates
    • C08F299/06Macromolecular compounds obtained by interreacting polymers involving only carbon-to-carbon unsaturated bond reactions, in the absence of non-macromolecular monomers from unsaturated polycondensates from polyurethanes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/04Polymeric products of isocyanates or isothiocyanates with vinyl compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/67Unsaturated compounds having active hydrogen
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/67Unsaturated compounds having active hydrogen
    • C08G18/6795Unsaturated polyethers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K7/00Use of ingredients characterised by shape
    • C08K7/02Fibres or whiskers
    • C08K7/04Fibres or whiskers inorganic
    • C08K7/14Glass
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L75/00Compositions of polyureas or polyurethanes; Compositions of derivatives of such polymers
    • C08L75/04Polyurethanes
    • C08L75/06Polyurethanes from polyesters
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L75/00Compositions of polyureas or polyurethanes; Compositions of derivatives of such polymers
    • C08L75/04Polyurethanes
    • C08L75/08Polyurethanes from polyethers

Definitions

  • the invention relates to the technical field of polyurethane materials, in particular to a resin composition, a polyurethane material, a polyurethane composite material and a preparation method.
  • the resin composition When the resin composition is in a liquid state, it is used to wet the reinforcing material, such as glass fiber cloth, and the simultaneous addition polymerization reaction and free radical polymerization reaction gradually generate a solid polyurethane matrix, which is fused with the wetted reinforcing material. Integrate to form a polyurethane composite material.
  • the water sensitivity of the resin composition is critical to the resulting polyurethane composite properties. If the water sensitivity is too high, it is easy to produce foaming reaction with water vapor. During the curing process of the resin, these newly generated air bubbles will remain in the interface between the resin and the composite material. After curing, the final composite product will contain many holes and cause product defects, which will significantly reduce the mechanical properties of the material and deteriorate the product quality. It is difficult to effectively control, which increases the risk of product quality accidents, and will also lead to a decrease in the yield of composite products.
  • the viscosity of the resin composition is critical to the properties of the resulting polyurethane composite. If the viscosity is too low and easy to flow, the resin composition cannot be effectively absorbed by the glass fiber cloth, and the resin composition will be lost and the glass fiber cloth will lack glue. This phenomenon will leave a lot of pores in the glass fiber cloth, and will The final composite product contains a lot of holes and produces product defects, which is not suitable for hand lay-up, winding and other processes.
  • the object of the present invention is to provide a resin composition, a polyurethane material prepared from the resin composition, a polyurethane composite material comprising the polyurethane material, and the resin composition, the polyurethane material and the polyurethane
  • the preparation method of the composite material is to effectively reduce the water sensitivity of the resin composition, further improve product performance, and avoid foaming problems in the subsequent production, preparation and processing of the composite material to the greatest extent.
  • the resin composition of the present invention comprises an isocyanate component, a reactive component and a free radical initiator; the isocyanate component comprises at least one organic isocyanate; in the reactive component: an average of each The molecule contains at least one acrylate double bond, either a double bond on an acrylic group or a methacrylic group, for free radical polymerization under the action of said free radical initiator double bond; each molecule contains at least one active hydrogen to react with the at least one organic isocyanate addition polymerization; the average number of acrylate double bonds and active hydrogen contained in each molecule is not less in 2.1.
  • the beneficial effect of the resin composition of the present invention is that: in the reactive components, the sum of the number of acrylate double bonds and active hydrogen contained in each molecule on average is not less than 2.1, and the acrylate The double bond is the double bond on the acrylic group or the double bond on the methacrylic group, which not only helps to improve product performance, but also can effectively reduce the water sensitivity of the resin composition, and avoid subsequent composite material production to the greatest extent. Foaming problems occurred during preparation and processing.
  • each molecule of the reactive component contains 1-4 acrylate groups on average, and each of the acrylate groups contains the acrylate double bond.
  • the beneficial effect is that: the addition of the at least one active hydrogen helps to improve product performance, and can effectively reduce the water sensitivity of the resin composition.
  • the reactive component contains 1.1-4.9 hydroxyl groups on average per molecule, and each of the hydroxyl groups contains the active hydrogen.
  • the beneficial effect is that: the combination of the at least one acrylate double bond helps to improve product performance, and can effectively reduce the water sensitivity of the resin composition.
  • the reactive component comprises an ester product obtained by esterification reaction of at least one organic polyol with an acrylic substance, and the at least one organic polyol has an average of at least 2.1 active components per molecule. hydrogen.
  • the beneficial effect is that it helps to improve product performance and can effectively reduce the water sensitivity of the resin composition.
  • the at least one organic polyol comprises at least one polyether polyol comprising the active hydrogens.
  • the average functionality of the at least one polyether polyol is 2.1-6, and the hydroxyl value is 25-1100 mg potassium hydroxide/g.
  • the content of the free radical initiator is 0.01%-7%.
  • the beneficial effect is that it helps to improve product performance and can effectively reduce the water sensitivity of the resin composition.
  • a catalyst is also included to accelerate the cross-linking reaction of the carbamate group, and the content of the catalyst is greater than 0 and less than or equal to 5% based on the mass percentage of the reactive component, and the carbamic acid
  • the ester group is obtained by the addition polymerization reaction between the active hydrogen and the at least one organic isocyanate.
  • auxiliary agents are also included to facilitate regulation and control of the physical and chemical properties of the polyurethane material prepared by the resin composition.
  • the polyurethane material of the present invention comprises a polyurethane matrix, and the polyurethane matrix is prepared from the resin composition. Due to the reactive components of the resin composition, the average number of acrylate double bonds contained in each molecule The sum of the number of active hydrogen and the number of active hydrogen is not less than 2.1, and the double bond of the acrylate type is a double bond on the acrylic acid group or a double bond on the methacrylic acid group, which can help improve product performance and effectively reduce the The water sensitivity of the above-mentioned resin composition can be avoided to the greatest extent to avoid foaming problems in the subsequent production, preparation and processing of composite materials.
  • the preparation method of the polyurethane material of the present invention includes: providing the resin composition, the resin composition includes a reactive component, a free radical initiator and at least one organic isocyanate, and the average amount of the reactive component is Each molecule contains at least one acrylate double bond and at least one active hydrogen; the free radical polymerization reaction of the at least one acrylate double bond is initiated by the free radical initiator, and the at least one active hydrogen is combined with the at least one active hydrogen An organic isocyanate undergoes addition polymerization.
  • the preparation method of the polyurethane material uses the resin composition as a raw material, because in the reactive components of the resin composition, the average number of acrylate double bonds and active hydrogen contained in each molecule is quite a lot In 2.1, the acrylate double bond is a double bond on an acrylic acid group or a double bond on a methacrylic group, which can help improve product performance and effectively reduce the water sensitivity of the resin composition, Minimize the lack of glue in the subsequent preparation and processing of composite materials, making the finished product prone to foaming problems.
  • the resin composition further includes a catalyst, and the mass percentage of the catalyst in the reactive component is controlled to be greater than 0 and less than or equal to 5%, so as to accelerate the reaction between the active hydrogen and the at least one organic isocyanate.
  • the cross-linking reaction of the carbamate group obtained by the addition polymerization reaction is that it can help improve product performance and effectively reduce the water sensitivity of the resin composition.
  • the resin composition further includes additives to regulate the physical and chemical properties of the polyurethane material.
  • the average functionality of the at least one organic isocyanate is 2.0-3.6.
  • the beneficial effect is that it can help improve product performance and effectively reduce the water sensitivity of the resin composition.
  • said at least one organic isocyanate has a viscosity measured according to DIN 53019-1-3 at 25° C. of 4-2500 mPa.s. The beneficial effect is that it can help improve product performance and effectively reduce the water sensitivity of the resin composition.
  • the polyurethane composite material of the present invention comprises a reinforcing material and the polyurethane material. Since the polyurethane material is prepared from the resin composition, in the reactive components of the resin composition, the average number of acrylate double bonds and active hydrogen contained in each molecule is not less than 2.1 , the acrylate double bond is a double bond on an acrylic acid group or a double bond on a methacrylic acid group, which can help improve product performance and effectively reduce the water sensitivity of the resin composition to the greatest extent Avoid foaming problems in the subsequent preparation and processing of composite materials.
  • the reinforcing material accounts for 1-91% by mass of the polyurethane composite material.
  • the beneficial effect is that the mechanical strength can be flexibly adjusted according to the use requirements.
  • the preparation method of the polyurethane composite material of the present invention uses reinforcing materials and the polyurethane material as raw materials, through vacuum introduction process, pultrusion forming process, winding forming process, resin transfer process, hand lay-up forming process, compression molding process and spray forming Prepared by at least one of the techniques.
  • the preparation method of the polyurethane composite material uses the polyurethane material as one of the raw materials, in the reactive components of the resin composition, the sum of the number of acrylate double bonds and active hydrogen contained in each molecule on average is not equal to Less than 2.1, the acrylate double bond is a double bond on the acrylic acid group or a double bond on the methacrylic group, which can help improve product performance and effectively reduce the water sensitivity of the resin composition , to avoid foaming problems in the subsequent production, preparation and processing of composite materials to the greatest extent.
  • An embodiment of the present invention provides a resin composition, which includes an isocyanate component, a reactive component and a free radical initiator.
  • the isocyanate component includes at least one organic isocyanate.
  • the at least one organic isocyanate is at least one of any chain aliphatic isocyanate, alicyclic isocyanate and aromatic isocyanate known to be used in the preparation of polyurethane.
  • the at least one organic isocyanate is 2,2'-diphenylmethane diisocyanate, 2,4'-diphenylmethane diisocyanate, 4,4'-diphenylmethane diisocyanate , a mixture of monomeric diphenylmethane diisocyanate and higher homologues of diphenylmethane diisocyanate (abbreviated as polymeric MDI), isophorone diisocyanate (IPDI) or its oligomers, 2,4-toluene Diisocyanate or 2,6-toluene diisocyanate (TDI) or mixtures thereof; tetramethylene diisocyanate or its oligomers; pentamethylene diisocyanate or its oligomers; hexamethylene diisocyanate (HDI) or its oligomers; 4,4'-dicyclohexylmethane diisocyanate (HMDI), methylcyclo
  • At least one of the at least one organic isocyanate exists in the form of a polyisocyanate prepolymer, and the polyisocyanate prepolymer is an isocyanate dimer, trimer, tetramer, and pentamer any kind of body.
  • the NCO weight percentage of the polyisocyanate prepolymer is 10-48%. In other specific embodiments, the NCO weight percentage of the polyisocyanate prepolymer is any one of 16-38% and 19-33%.
  • the at least one organic isocyanate is diphenylmethane diisocyanate (MDI), polyphenylmethane polyisocyanate (PMDI), and their multimers, prepolymers or combinations thereof.
  • the at least one organic isocyanate has an average functionality of 2.0-3.6. In some other embodiments, the average functionality of the at least one organic isocyanate is 2.1-2.8.
  • the viscosity of the at least one organic isocyanate measured according to DIN53019-1-3 at 25° C. is 4-2500 mPa.s.
  • the at least one organic isocyanate has a viscosity measured according to DIN53019-1-3 at 25° C. in any one of 5-800 mPa.s and 10-300 mPa.s.
  • each molecule of the reactive component contains at least one acrylate double bond and at least one active hydrogen, and the average number of acrylate double bonds and active hydrogen contained in each molecule is the sum of Not less than 2.1.
  • the at least one acrylate double bond undergoes a radical polymerization reaction under the action of the radical initiator, and the at least one active hydrogen undergoes an addition polymerization reaction with the at least one organic isocyanate.
  • the acrylate double bond is a double bond on an acrylic group or a double bond on a methacrylic group.
  • the reactive component comprises 1-4 acrylate groups per molecule on average, each of the acrylate groups comprising the acrylate double bond.
  • the number of acrylate groups contained in each molecule of the reactive component is any one of 1.05-3, 1.1-2.5, 1.15-2.4 and 1.2-2.3.
  • the reactive component comprises, on average, 1.1-4.9 hydroxyl groups per molecule, each of the hydroxyl groups comprising the active hydrogen.
  • the number of hydroxyl groups contained in each molecule of the reactive component is any one of 1.2-4, 1.25-3.5, 1.3-3, 1.35-2.6, 1.4-2.5 and 1.5-2.4 kind.
  • the reactive component is an ester product obtained through an esterification reaction of at least one organic polyol and an acrylic substance, and the at least one organic polyol has an average of at least 2.1 the active hydrogen.
  • the acrylic substance is acrylic anhydride, methacrylic anhydride, acryloyl chloride, methacryloyl chloride, acryloyl bromide, methacryloyl bromide, acrylic acid, methacrylic acid, methyl acrylate, methacrylic acid Methyl acrylate, ethyl methacrylate, propyl acrylate, propyl methacrylate, isopropyl acrylate, isopropyl methacrylate, butyl acrylate, butyl methacrylate, tert-butyl acrylate and At least one kind of tert-butyl methacrylate.
  • said at least one organic polyol comprises at least one polyether polyol comprising said active hydrogen.
  • the at least one organic polyol is at least one of polyether polyol, polyether carbonate polyol, polyester polyol, polycarbonate diol, polymer polyol, and vegetable oil-based polyol .
  • the at least one organic polyol is polyoxypropylene diol, polyether triol, polyether tetraol, polyether pentaol, polyurea polyol, polytetrahydrofuran diol, adipate polyester At least one of diol, aromatic polyester polyol, polycaprolactone polyol, polycarbonate diol, polyacrylate polyol, and polyolefin polyol.
  • the average functionality of the at least one polyether polyol is 2.1-6, and the hydroxyl value is 25-1100 mg potassium hydroxide/g.
  • the average functionality of the at least one polyether polyol is 2.5-5, and the hydroxyl value is 35-800 mg potassium hydroxide/g.
  • the average functionality of the at least one polyether polyol is 2.7-4.6, and the hydroxyl value is 50-660 mg potassium hydroxide/g.
  • the average functionality of the at least one polyether polyol is 2.8-4.4, and the hydroxyl number is 80-630 mg potassium hydroxide/g.
  • the average functionality of the at least one polyether polyol is 3.0-4.3, and the hydroxyl value is 100-600 mg potassium hydroxide/g.
  • the average functionality of the at least one polyether polyol is 3.1-4.2, and the hydroxyl number is 110-570 mg potassium hydroxide/g.
  • the reactive component is obtained by esterifying at least one organic polyol with at least one acrylic or methacrylic group.
  • the reactive component is obtained by esterifying at least one organic polyol with at least one acrylic anhydride or methacrylic anhydride.
  • the reactive component is obtained by esterifying at least one organic polyol with at least one acryloyl halide or methacryloyl halide.
  • the acryloyl halide is any one of acryloyl chloride and acryloyl bromide.
  • the methacryloyl halide is any one of methacryloyl chloride and methacryloyl bromide.
  • the reactive component is obtained by esterifying at least one organic polyol with at least one acrylic acid or methacrylic acid under catalyst conditions.
  • the reactive component is obtained by transesterifying at least one organic polyol with at least one methacrylate or acrylate under catalyst conditions.
  • the acrylate is any one of methyl acrylate, ethyl acrylate, propyl acrylate, isopropyl acrylate, butyl acrylate and tert-butyl acrylate.
  • the methacrylate is any one of methyl methacrylate, ethyl methacrylate, propyl methacrylate, isopropyl methacrylate, butyl methacrylate and tert-butyl methacrylate.
  • esterification reaction of at least one organic polyhydric alcohol with acrylic anhydride or methacrylic anhydride the esterification reaction with acryloyl halide or methacryloyl halide, the esterification reaction with acrylic acid or methacrylic acid, and the For the transesterification reaction of acrylate or methacrylate, those skilled in the art are familiar with the specific operation methods of these reactions.
  • Some esterification methods can refer to the records in CN101983959B or CN101475502B.
  • the content of the free radical initiator is 0.01%-7%.
  • the free radical initiator is a free radical initiator capable of initiating curing of the double bond-containing compound.
  • the free radical initiator is added to at least one of the at least one organic isocyanate and the reactive component.
  • the free radical initiator is any one of peroxide, persulfide, peroxycarbonate, peroxyboric acid and azo compound.
  • the free radical initiator is tert-butyl isopropyl carbonate, tert-butyl peroxy-3,5,5-trimethylhexanoate, methyl ethyl ketone peroxide, cumene peroxide Hydrogen peroxide, persulfate, azobisisobutyronitrile, azobisisoheptanonitrile, dimethyl azobisisobutyrate, benzoyl peroxide, benzoyl tert-butyl peroxide and hydrogen peroxide at least one of .
  • the resin composition further includes a catalyst to accelerate the crosslinking reaction of the carbamate group, and the content of the catalyst is greater than 0 and less than or equal to 5%, the urethane group is obtained by the addition polymerization of the active hydrogen and the at least one organic isocyanate.
  • the mass percentage of the catalyst in the reactive component is 0.001-2%.
  • the catalyst is 2,3-dimethyl-3,4,5,6-tetrahydropyrimidine, triethylamine, tributylamine, triethylenediamine, dimethylbenzylamine, N-methylmorpholine, N-ethylmorpholine, N-cyclohexylmorpholine, N,N,N',N'-tetramethylethylenediamine, N,N,N',N'-tetramethyl butyldiamine, N,N,N',N'-tetramethylhexamethylenediamine, pentamethyldiethylenetriamine, tetramethyldiaminoethylether, bis(dimethylaminopropyl)urea, Any of dimethylpiperazine, 1,2-dimethylimidazole, and 1-azabicyclo(3,3,0)octane.
  • the catalyst is 1,4-diazabicyclo(2,2,2)octane, triethanolamine, triisopropanolamine, N-methyldiethanolamine, N-ethyldiethanolamine and Any one of dimethylethanolamine.
  • the catalyst is an organometallic compound. In some other embodiments, the catalyst consists of the organometallic compound and a strongly basic amine.
  • the organometallic compound is tin(II) acetate, tin(II) octoate, tin(II) ethylhexanoate, tin(II) laurate, dibutyltin diacetate, dilaurate dilaurate Any of butyltin, dibutyltin maleate, and dioctyltin diacetate.
  • the organometallic compound is bismuth (III) neodecanoate, bismuth 2-ethylhexanoate, bismuth octoate or mixtures thereof.
  • the resin composition also includes several additives to facilitate regulation and control of the physical and chemical properties of the polyurethane material prepared by the resin composition, the physical and chemical properties include viscosity, degree of crosslinking, waterproof performance, flame retardant At least one of performance, anti-smoke performance, anti-staining performance, antistatic performance, anti-oxidation performance, ultraviolet stability performance, leveling performance and adsorption performance.
  • the several auxiliary agents are fillers, internal release agents, flame retardants, smoke suppressants, dyes, pigments, antistatic agents, antioxidants, UV stabilizers, diluents, defoamers , coupling agent, surface wetting agent, leveling agent, water remover, catalyst, molecular sieve, thixotropic agent, plasticizer and free radical reaction inhibitor.
  • the filler is aluminum hydroxide, bentonite, fly ash, wollastonite, perlite powder, floating beads, calcium carbonate, talcum powder, mica powder, china clay, fumed silica, expandable Microspheres, diatomaceous earth, volcanic ash, barium sulfate, calcium sulfate, solid and/or hollow glass microspheres, stone powder, wood flour, wood chips, bamboo powder, bamboo chips, rice grains, straw chips, coffee grounds, sorghum stalks At least one of scrap, graphite powder, metal powder, recycled thermosetting composite powder, plastic granules or powder.
  • the embodiment of the present invention also provides a polyurethane material, the polyurethane material includes a polyurethane matrix, the polyurethane matrix is prepared from the resin composition, because in the reactive components of the resin composition, the average The sum of the number of acrylate double bonds and active hydrogen contained is not less than 2.1, and the acrylate double bonds are double bonds on acrylic acid groups or double bonds on methacrylic acid groups, which can help to improve The product performance is improved, and the water sensitivity of the resin composition is effectively reduced, so as to avoid foaming problems in the production, preparation and processing of subsequent composite materials to the greatest extent.
  • the preparation method of the polyurethane material includes: providing the resin composition, the resin composition includes a reactive component, a free radical initiator and at least one organic isocyanate, and the reactive component On average, each molecule of the fraction contains at least one acrylate double bond and at least one active hydrogen; the free radical polymerization reaction of the at least one acrylate double bond is initiated by the free radical initiator, and the at least one active hydrogen Addition polymerization takes place with the at least one organic isocyanate.
  • the preparation method of the polyurethane material uses the resin composition as a raw material, because in the reactive components of the resin composition, the average number of acrylate double bonds and active hydrogen contained in each molecule is quite a lot In 2.1, the acrylate double bond is a double bond on an acrylic acid group or a double bond on a methacrylic group, which can help improve product performance and effectively reduce the water sensitivity of the resin composition, To avoid foaming problems in the subsequent production, preparation and processing of composite materials to the greatest extent.
  • the mass percentage of the catalyst in the reactive component is controlled to be greater than 0 and less than or equal to 5%, so as to accelerate the addition polymerization reaction of the active hydrogen and the at least one organic isocyanate to obtain The crosslinking reaction of the carbamate group.
  • the additive regulates the physical and chemical properties of the polyurethane material, and the physical and chemical properties include viscosity, degree of crosslinking, waterproof performance, flame retardant performance, smoke-proof performance, anti-dyeing performance, antistatic performance, oxidation resistance At least one of performance, UV stability performance, leveling performance and adsorption performance.
  • the embodiment of the invention also provides the polyurethane composite material and its preparation method.
  • the polyurethane composite material of the embodiment of the present invention includes a reinforcing material and the polyurethane material. Since the polyurethane material is prepared from the resin composition, in the reactive components of the resin composition, the average number of acrylate double bonds and active hydrogen contained in each molecule is not less than 2.1 , the acrylate double bond is a double bond on an acrylic acid group or a double bond on a methacrylic acid group, which can help improve product performance and effectively reduce the water sensitivity of the resin composition to the greatest extent Avoid foaming problems in the subsequent preparation and processing of composite materials.
  • the mass percentage of the reinforcing material in the polyurethane composite material is any one of 1-91%, 15-90%, 35-85%, 45-83% and 50-81%.
  • the reinforcing material includes glass fiber, carbon fiber, carbon nanotube, polyester fiber, aramid fiber, nylon fiber, natural fiber, basalt fiber, silicon carbide fiber, boron fiber, asbestos fiber, whisker , at least one of hard particles and metal fibers.
  • polyurethane addition polymerization that is, addition polymerization of isocyanate groups and hydroxyl groups, and free radical polymerization occur simultaneously.
  • the resin composition is in a liquid state, it is used to wet the reinforcing material, and the simultaneous addition polymerization reaction and free radical polymerization reaction gradually generate the solid polyurethane matrix, and the wetted reinforcing material integrated to form the polyurethane composite.
  • the preparation method of the polyurethane composite material in the embodiment of the present invention uses the reinforcing material and the polyurethane material as raw materials, through vacuum introduction process, pultrusion forming process, winding forming process, resin transfer process, hand lay-up forming process, compression molding process and Prepared by at least one of the injection molding processes.
  • the preparation method of the polyurethane composite material uses the polyurethane material as one of the raw materials, in the reactive components of the resin composition, the sum of the number of acrylate double bonds and active hydrogen contained in each molecule on average is not equal to Less than 2.1, the acrylate double bond is a double bond on the acrylic acid group or a double bond on the methacrylic group, which can help improve product performance and effectively reduce the water sensitivity of the resin composition , to avoid foaming problems in the subsequent production, preparation and processing of composite materials to the greatest extent.
  • Resin tensile properties of specific examples were determined according to ISO 527-2.
  • the tensile properties of the polyurethane composites of the specific examples were determined according to ISO 527-5.
  • Isocyanate components isocyanate PM200 and isocyanate WANNATE MDI-50;
  • the raw materials for preparing the reactive components are polyether polyol P1, polyether polyol P2, polyether polyol P3 and polyether polyol P4. in:
  • Polyether polyol P1 is a trifunctional polyol prepared with glycerin as the initiator and propylene oxide as the main body of the polymerization reaction, with a hydroxyl value of 235 mg KOH/g;
  • Polyether polyol P2 is a trifunctional polyol prepared with glycerin as the initiator and propylene oxide as the main body of the polymerization reaction, with a hydroxyl value of 330 mgKOH/g;
  • Polyether polyol P3 is a tetrafunctional polyol prepared by using pentaerythritol as the initiator and propylene oxide as the main body of the polymerization reaction, with a hydroxyl value of 450mgKOH/g;
  • Polyether polyol P4 is a six-functional polyol prepared with sorbitol as the initiator and propylene oxide as the main body of the polymerization reaction, with a hydroxyl value of 430 mgKOH/g;
  • Free radical initiators benzoyl peroxide (PERKADOX CH-50L) and methyl ethyl ketone peroxide (Butanox M-50), purchased from Nouryon.
  • the additives are 5A molecular sieve activated powder and defoamer BYKA560.
  • the 5A molecular sieve activated powder is purchased from Xintao Technology, and the defoamer is purchased from BYK Chemicals.
  • At least one organic polyol and the acrylic substance are subjected to an esterification reaction in an organic solvent under the action of a catalyst until no more water is produced in the esterification reaction.
  • the temperature of the esterification reaction is 60-140 degrees Celsius.
  • the at least one organic polyol is 30-100 parts, the acrylic substance is 3-35 parts, the solvent is 3-55 parts, the catalyst is 0.05-1 part, and the polymerization inhibitor is 0.03-0.5 parts.
  • the acrylic substance is mixed with at least one organic polyol, a solvent, a catalyst, etc. under the condition of ice bath and stirring, and then the esterification reaction is carried out under ice bath for 3-8 hours.
  • the at least one organic polyol is 60-90 parts
  • the acrylic substance is 20-60 parts
  • the solvent is 200-500 parts
  • the auxiliary agent is 30-150 parts
  • the polymerization inhibition The quality of the agent is 0.03-0.45 parts.
  • Embodiments provide several reactive components, and the reactive components used in different embodiments are combined from at least one of the several reactive components.
  • each reactive component among the several reactive components is abbreviated as B-P1-1, B-P1-2, B-P2-1, B-P2-2, B -P3-1 and B-P4-1.
  • Each molecule of B-P1-1 contains 2 methacrylates and 1 hydroxyl group.
  • the preparation method is as follows: polyether polyol P1 and hydroquinone, the masses are 71.6g and 0.1g respectively, and hydroquinone is used as Inhibitor; methacrylic acid is an acrylic substance with a mass of 20.7g; 30g of cyclohexane is a solvent with a mass of 30g; p-toluenesulfonic acid is a catalyst with a mass of 0.8g; the above mixture is reacted at 80°C until water separation When the water in the vessel is no longer produced, the reaction is finished, and the solvent is removed by vacuum rotation, and the resulting mixture can be purified to obtain the product B-P1-1.
  • Each molecular structure of B-P1-2 contains 1 methacrylate and 2 hydroxyl groups.
  • the preparation method is as follows: polyether polyol P1 is 71.6g, methacrylic acid is 10.3g, 15g cyclohexane, 0.4g P-toluenesulfonic acid and 0.08g of hydroquinone are mixed and reacted at 80°C until water in the water separator no longer occurs, then the reaction is completed, the solvent is removed by vacuum rotation, and the obtained mixture is purified to obtain the product B-P1-2.
  • Each molecular structure of B-P2-1 contains 2 acrylates and 1 hydroxyl group.
  • the preparation method is as follows: 51g of polyether polyol P2, 17.3g of acrylic acid, 22g of cyclohexane, 0.8g of p-toluenesulfonic acid and 0.1g of hydroquinone was reacted at 80°C until the water in the water separator was no longer produced, then the reaction was completed, the solvent was removed by vacuum rotation, and the obtained mixture was purified to obtain the product B-P2-1.
  • Each molecular structure of B-P2-2 contains 1 acrylate and 2 hydroxyl groups.
  • the preparation method is as follows: 51g of polyether polyol P2, 8.7g of acrylic acid, 11g of cyclohexane, 0.4g of p-toluenesulfonic acid and 0.08g of hydroquinone is reacted at 80°C until the water in the water separator is no longer produced, then the reaction is complete, the solvent is removed by vacuum rotation, and the obtained mixture is purified to obtain the product B-P2-2.
  • Each molecular structure of B-P3-1 contains 2 acrylates and 2 hydroxyl groups.
  • the preparation method is as follows: 50g of polyether polyol P3, 17.3g of acrylic acid, 22g of cyclohexane, 0.8g of p-toluenesulfonic acid and 0.1g of hydroquinone is reacted at 80°C until the water in the water separator no longer produces, then the reaction is completed, the solvent is removed by vacuum rotation, and the obtained mixture is purified to obtain the product B-P3-1.
  • Each molecular structure of B-P4-1 contains 5 acrylates and 1 hydroxyl group.
  • the preparation method is as follows: slowly add 42.5ml of acryloyl chloride dropwise to 78.3 g polyether polyol P4, 0.2 g of hydroquinone and 100 g of triethylamine in dichloromethane 350 ml solution, the dropwise addition was completed in 60 minutes, and triethylamine was used as an auxiliary agent. The reaction was continued for another 5 hours under ice-bath conditions. Stop stirring and let stand overnight. After standing overnight, the reaction was terminated, and unreacted products and other impurities were removed by washing successively with water, 1M hydrochloric acid, and 1M NaOH solution. The solvent was spun off in vacuo, and the resulting mixture was purified to obtain the product B-P4-1.
  • test methods for which specific conditions are not indicated in the following examples are generally in accordance with conventional conditions, or in accordance with the conditions suggested by the manufacturer. All percentages and parts are by weight unless otherwise indicated.
  • Another example is that when large-scale products such as blades and yachts are prepared by the vacuum introduction process, it takes a long time for resin introduction. If the gel time is less than 150 minutes, it is far from enough. Therefore, the comparative examples 1-3 based on the traditional polyurethane system do not meet the requirements of many kinds of composite material production processes. Comparative Example 4 shows that even with the addition of partially reactive component (B), the requirements are not met. However, Examples 1-5 show that the gel time is significantly prolonged, all above 200 minutes, far higher than the requirement of 150 minutes, so it can better adapt to the time operation requirements of many composite material production processes; and its mechanical properties be greatly improved.
  • the improvement of mechanical properties helps to further reduce the weight of the composite material based on this thermosetting resin on the premise of meeting the requirements of actual use, so that it can meet the requirements of lighter weight.
  • the shrinkage rate of the resin after curing was too large, resulting in brittleness and cracking of the resin plate sample, and a satisfactory test sample could not be obtained.
  • the reason is that the content of acrylate is too high, resulting in too high free radical polymerization crosslinking density of active double bonds, so that the cured resin shrinkage rate is too large and internal cracking occurs.
  • the average number of (meth)acrylate functional groups in its molecular structure should have a preferred range; If it is low, the gel time and mechanical properties cannot be significantly prolonged, but if it is too high, adverse effects such as shrinkage and cracking will occur.
  • polyol, isocyanate component (A), reactive component (B), free radical initiator (C) and other additives are made into resin mixed liquid, and stirred under vacuum condition Breathe for 5 minutes. Then put the resin mixed liquid into the casting body mold that has been kept in a constant temperature oven at 35°C, and keep the constant temperature for 2 hours, then raise the temperature of the oven to 80°C and keep it for 4 hours, and then turn off the heating. After cooling to room temperature, the cured sample can be taken out to obtain the thermosetting polyurethane resin matrix of Comparative Example 5 and Example 6.
  • Table 2 The specific test results are shown in Table 2.
  • thermosetting polyurethane resin matrix introduced with the reactive component (B) has better comprehensive properties than ordinary polyurethane resins.
  • the polyurethane composite material in this embodiment is based on the polyurethane compositions of comparative example 6, comparative example 7 and embodiment 7 in table 3, prepared by hand lay-up process in the laboratory, to be used to compare the process of its actual operation properties and observe its cured effect including composite quality.
  • the operation is carried out on glass plates: place four layers of uniaxial glass fiber cloth (Hengshi, E61200, UD, ⁇ 1200g/m2) on the upper surfaces of three glass plates sprayed with release agent respectively, at 25°C and 50% Place in a relative humidity environment for 24 hours for temperature and humidity balance.
  • Table 3 After preparing the three types of resins, slowly pour them on the upper surface of their respective glass fiber cloths, so that the liquid resins naturally penetrate into the glass fiber cloths from top to bottom, and wait for 6 minutes to fully absorb them. Soak the glass fiber, then cover the upper surface of the glass fiber cloth with a layer of transparent plastic film, and then use a hand lay-up roller to squeeze out all the air in the soaked glass fiber cloth.
  • the sheet quality based on comparative example 6 resin-impregnated glass fiber cloth is unqualified, because the foaming problem is very serious, indicating that its water sensitivity is high; the sheet quality based on comparative example 7 resin-impregnated glass fiber cloth is not up to standard Qualified, because although its foaming problem has declined to some extent, it is still obvious, indicating that although the components are adjusted in Comparative Example 7, the water-sensitive foaming problem cannot be completely avoided; The sheets of cloth are of good quality, uniform and complete, and there is no foaming problem.
  • the experimental results are listed in Table 3.
  • the tensile modulus and tensile strength are the modulus and strength measured in the 90° direction, which mainly reflect the resin strength and the bonding strength of the resin and fiber interface.
  • thermosetting polyurethane resin matrix introduced with reactive component (B) has better operability in composite material technology than ordinary polyurethane resin and other modified Polyurethane can be used to prepare hand lay-up products.
  • the polyurethane composite material of this example is based on the polyurethane resin compositions of Comparative Example 5 and Example 6 in Table 2, respectively, and the composite product is prepared through a vacuum introduction process, and its properties are tested.
  • the composite material of comparative example 8 uses the resin of comparative example 5; the composite material of embodiment 8 uses the resin of embodiment 6)
  • the operation is carried out on the glass plate: place the Hengshi uniaxial glass fiber cloth (E61200, UD, ⁇ 1200g/m2) on the upper surface of the glass plate sprayed with the release agent, and then put the release cloth and the flow guide on it in turn. Netting and vacuum bags.
  • the front position of this device is connected to the vacuum, and the rear position is connected to the liquid resin through the guide tube.
  • the properties of the polyurethane composite material of the present invention are shown in Table 4.
  • the tensile modulus and tensile strength shown in Table 4 are the modulus and strength measured under the tensile condition of 0° direction.
  • thermosetting polyurethane resin matrix containing the reactive component (B) is suitable for the composite material process and prepares qualified composite products.
  • the operation is carried out on the glass plate: place the Hengshi uniaxial glass fiber cloth (E61200, UD, ⁇ 1200g/m2) on the upper surface of the glass plate sprayed with the release agent, and then put the release cloth and the flow guide on it in turn. Netting and vacuum bags.
  • the front position of this device is connected to the vacuum, and the rear position is connected to the liquid resin through the guide tube. After all these are set, the tube of the draft tube is bent and blocked, and then the tube connected to the vacuum is connected to the vacuum pump, so that the whole setup is kept in a vacuum state.
  • the resin mixed liquid is introduced into the glass fiber cloth of the above-mentioned device under vacuum condition. After the glass fiber cloth is fully soaked, bend the guide tube and the tube connected to the vacuum to block, so that the whole system soaked by all the liquid resin is still kept in a vacuum state; then start to gradually increase the temperature within 1 hour. 80°C, then keep at 80°C for 2 hours, accelerate the curing of the resin by heating at high temperature, and then turn off the heat.
  • thermosetting polyurethane resin matrix containing reactive component (B) is suitable for the composite process and can be used to prepare qualified composite products.

Abstract

The present invention provides a resin composition comprising an isocyanate component, a reactive component, and a free radical initiator. In the reactive component, the sum of the average number of acrylate double bonds and active hydrogen contained in each molecule is not less than 2.1. The acrylate double bonds are double bonds on acrylic acid groups or on methacrylic acid groups, and can help improve product performance, and effectively reduce the water sensitivity of the resin composition, thereby avoiding, to the greatest extent, a foaming problem in the subsequent production, preparation, and processing process of the composite material. The present invention further provides a polyurethane material, which is prepared from the resin composition, a polyurethane composite material comprising the polyurethane material, and preparation methods for the resin composition, the polyurethane material, and the polyurethane composite material.

Description

树脂组合物、聚氨酯材料和聚氨酯复合材料以及制备方法Resin composition, polyurethane material, polyurethane composite material and preparation method
交叉引用cross reference
本申请要求申请日为2021年07月15日,申请号为2021108009470,发明名称为“树脂组合物、聚氨酯材料和聚氨酯复合材料以及制备方法”的中国专利申请的优先权。申请号为2021108009470且发明名称为“树脂组合物、聚氨酯材料和聚氨酯复合材料以及制备方法”的中国专利申请的全部内容以引用方式并入本申请。This application claims the priority of a Chinese patent application with an application date of July 15, 2021, an application number of 2021108009470, and an invention title of "resin composition, polyurethane material, polyurethane composite material and preparation method". The entire content of the Chinese patent application with the application number 2021108009470 and the invention title "resin composition, polyurethane material and polyurethane composite material and preparation method" is incorporated into this application by reference.
技术领域technical field
本发明涉及聚氨酯材料技术领域,尤其涉及树脂组合物、聚氨酯材料和聚氨酯复合材料以及制备方法。The invention relates to the technical field of polyurethane materials, in particular to a resin composition, a polyurethane material, a polyurethane composite material and a preparation method.
技术背景technical background
传统聚氨酯树脂基于异氰酸酯基团与羟基的加成聚合反应,发生交联固化;但由于这类树脂反应性偏快,使操作时间偏短,且其水敏感性偏高,使用过程中需要非常严格的湿度控制,因此不太适合用于各类复材工艺制备产品。新型的聚氨酯复合材料制备过程中,异氰酸酯基团与羟基的加成聚合反应与自由基聚合反应同时存在。树脂组合物在液态时,被用来润湿所述增强材料,例如玻纤布,同时发生的加成聚合反应与自由基聚合反应逐渐生成固体的聚氨酯基体,与已经被润湿的增强材料融为一体,从而形成聚氨酯复合材料。Traditional polyurethane resins are based on the addition polymerization reaction of isocyanate groups and hydroxyl groups, and cross-linking and curing occur; however, due to the fast reactivity of this type of resin, the operation time is relatively short, and its water sensitivity is relatively high, so it needs to be very strict during use. Humidity control, so it is not suitable for all kinds of composite materials to prepare products. In the preparation process of the new polyurethane composite material, the addition polymerization reaction of isocyanate group and hydroxyl group and free radical polymerization reaction exist at the same time. When the resin composition is in a liquid state, it is used to wet the reinforcing material, such as glass fiber cloth, and the simultaneous addition polymerization reaction and free radical polymerization reaction gradually generate a solid polyurethane matrix, which is fused with the wetted reinforcing material. Integrate to form a polyurethane composite material.
树脂组合物的水敏感性对得到的聚氨酯复合材料性能至关重要。如果水敏感性过高,则易与水汽产生发泡反应。在树脂固化的过程中,这些新产生的气泡会留在树脂和复材界面中,固化后会使最终的复材产品含有很多孔洞而导致产品缺陷,会显著降低材料的力学性能,使产品质量难以有效控制,增加了发生产品质量事故的风险,也会导致复材产品良品率降低。The water sensitivity of the resin composition is critical to the resulting polyurethane composite properties. If the water sensitivity is too high, it is easy to produce foaming reaction with water vapor. During the curing process of the resin, these newly generated air bubbles will remain in the interface between the resin and the composite material. After curing, the final composite product will contain many holes and cause product defects, which will significantly reduce the mechanical properties of the material and deteriorate the product quality. It is difficult to effectively control, which increases the risk of product quality accidents, and will also lead to a decrease in the yield of composite products.
树脂组合物的粘度对得到的聚氨酯复合材料性能至关重要。若粘度过低易流淌,导致树脂组合物不能被玻纤布有效吸附,产生树脂组合物流失而使玻纤布缺胶,此缺胶现象会在玻纤布里留下很多孔隙,固化后会使最终的复材产品含有很多孔洞而产生产品缺陷,不适合用于手糊、缠绕等工艺。The viscosity of the resin composition is critical to the properties of the resulting polyurethane composite. If the viscosity is too low and easy to flow, the resin composition cannot be effectively absorbed by the glass fiber cloth, and the resin composition will be lost and the glass fiber cloth will lack glue. This phenomenon will leave a lot of pores in the glass fiber cloth, and will The final composite product contains a lot of holes and produces product defects, which is not suitable for hand lay-up, winding and other processes.
因此,有必要开发新型的树脂组合物以解决现有技术存在的上述问题。Therefore, it is necessary to develop novel resin compositions to solve the above-mentioned problems existing in the prior art.
发明概要Summary of the invention
本发明的目的在于提供一种树脂组合物,由所述树脂组合物制备而成的聚氨酯材料,包含所述聚氨酯材料的聚氨酯复合材料,以及所述树脂组合物、所述聚氨酯材料和所述聚氨酯复合材料的制备方法,以有效降低所述树脂组合物的水敏感性,进一步提高产品性能,且最大程度避免后续复合材料生产制备和加工过程中出现发泡问题。The object of the present invention is to provide a resin composition, a polyurethane material prepared from the resin composition, a polyurethane composite material comprising the polyurethane material, and the resin composition, the polyurethane material and the polyurethane The preparation method of the composite material is to effectively reduce the water sensitivity of the resin composition, further improve product performance, and avoid foaming problems in the subsequent production, preparation and processing of the composite material to the greatest extent.
为实现上述目的,本发明的树脂组合物包含异氰酸酯组分、反应性组分和自由基起始剂;所述异氰酸酯组分包含至少一种有机异氰酸酯;所述反应性组分中:平均每个分子包含至少一个丙烯酸酯类双键,以在所述自由基起始剂的作用下发生自由基聚合反应,所述丙烯酸酯类双键为丙烯酸基团上的双键或甲基丙烯酸基团上的双键;平均每个分子包含至少一个活性氢,以与所述至少一种有机异氰酸酯发生加成聚合反应;平均每个分子所含有的丙烯酸酯类双键和活性氢的数目之和不少于2.1。To achieve the above object, the resin composition of the present invention comprises an isocyanate component, a reactive component and a free radical initiator; the isocyanate component comprises at least one organic isocyanate; in the reactive component: an average of each The molecule contains at least one acrylate double bond, either a double bond on an acrylic group or a methacrylic group, for free radical polymerization under the action of said free radical initiator double bond; each molecule contains at least one active hydrogen to react with the at least one organic isocyanate addition polymerization; the average number of acrylate double bonds and active hydrogen contained in each molecule is not less in 2.1.
本发明的所述树脂组合物的有益效果在于:所述反应性组分中,平均每个分子所含有的丙烯酸酯类双键和活性氢的数目之和不少于2.1,所述丙烯酸酯类双键为丙烯酸基团上的双键或甲基丙烯酸基团上的双键,不仅有助于提高产品性能,还能够有效降低所述树脂组合物的水敏感性,最大程度避免后续复合材料生产制备和加工过程中出现发泡问题。The beneficial effect of the resin composition of the present invention is that: in the reactive components, the sum of the number of acrylate double bonds and active hydrogen contained in each molecule on average is not less than 2.1, and the acrylate The double bond is the double bond on the acrylic group or the double bond on the methacrylic group, which not only helps to improve product performance, but also can effectively reduce the water sensitivity of the resin composition, and avoid subsequent composite material production to the greatest extent. Foaming problems occurred during preparation and processing.
优选的,所述反应性组分的平均每个分子包含1-4个丙烯酸酯类基团,每个所述丙烯酸酯类基团包含所述丙烯酸酯类双键。其有益效果在于:配合所述至少一个活性氢,有助于提高产品性能,且能够有效降低所述树脂组合物 的水敏感性。Preferably, each molecule of the reactive component contains 1-4 acrylate groups on average, and each of the acrylate groups contains the acrylate double bond. The beneficial effect is that: the addition of the at least one active hydrogen helps to improve product performance, and can effectively reduce the water sensitivity of the resin composition.
优选的,所述反应性组分的平均每个分子包含1.1-4.9个羟基,每个所述羟基包含所述活性氢。其有益效果在于:配合所述至少一个丙烯酸酯类双键,有助于提高产品性能,且能够有效降低所述树脂组合物的水敏感性。Preferably, the reactive component contains 1.1-4.9 hydroxyl groups on average per molecule, and each of the hydroxyl groups contains the active hydrogen. The beneficial effect is that: the combination of the at least one acrylate double bond helps to improve product performance, and can effectively reduce the water sensitivity of the resin composition.
优选的,所述反应性组分包含至少一种有机多元醇与丙烯酸类物质通过酯化反应得到的酯类产物,所述至少一种有机多元醇的平均每个分子具有至少2.1个所述活性氢。其有益效果在于:有助于提高产品性能,且能够有效降低所述树脂组合物的水敏感性。Preferably, the reactive component comprises an ester product obtained by esterification reaction of at least one organic polyol with an acrylic substance, and the at least one organic polyol has an average of at least 2.1 active components per molecule. hydrogen. The beneficial effect is that it helps to improve product performance and can effectively reduce the water sensitivity of the resin composition.
进一步优选的,所述至少一种有机多元醇包含至少一种聚醚多元醇,所述聚醚多元醇包含所述活性氢。Further preferably, the at least one organic polyol comprises at least one polyether polyol comprising the active hydrogens.
进一步优选的,所述至少一种聚醚多元醇的平均官能度为2.1-6,羟值为25-1100毫克氢氧化钾/克。Further preferably, the average functionality of the at least one polyether polyol is 2.1-6, and the hydroxyl value is 25-1100 mg potassium hydroxide/g.
优选的,以占所述反应性组分的质量百分比计,所述自由基起始剂的含量为0.01%-7%。其有益效果在于:有助于提高产品性能,且能够有效降低所述树脂组合物的水敏感性。Preferably, based on the mass percentage of the reactive components, the content of the free radical initiator is 0.01%-7%. The beneficial effect is that it helps to improve product performance and can effectively reduce the water sensitivity of the resin composition.
优选的,还包含催化剂,以加速氨基甲酸酯类基团的交联反应,以占所述反应性组分的质量百分比计,所述催化剂的含量大于0并小于等于5%,所述氨基甲酸酯类基团由所述活性氢与所述至少一种有机异氰酸酯发生所述加成聚合反应得到。其有益效果在于:有助于提高产品性能,且能够有效降低所述树脂组合物的水敏感性。Preferably, a catalyst is also included to accelerate the cross-linking reaction of the carbamate group, and the content of the catalyst is greater than 0 and less than or equal to 5% based on the mass percentage of the reactive component, and the carbamic acid The ester group is obtained by the addition polymerization reaction between the active hydrogen and the at least one organic isocyanate. The beneficial effect is that it helps to improve product performance and can effectively reduce the water sensitivity of the resin composition.
优选的,还包含若干助剂,以利于调控通过所述树脂组合物所制备的聚氨酯材料的理化性能。Preferably, several auxiliary agents are also included to facilitate regulation and control of the physical and chemical properties of the polyurethane material prepared by the resin composition.
本发明的所述聚氨酯材料包含聚氨酯基体,所述聚氨酯基体由所述树脂组合物制备而成,由于所述树脂组合物的反应性组分中,平均每个分子所含有的丙烯酸酯类双键和活性氢的数目之和不少于2.1,所述丙烯酸酯类双键为丙烯酸基团上的双键或甲基丙烯酸基团上的双键,能够有助于提高产品性能, 且有效降低所述树脂组合物的水敏感性,最大程度避免后续复合材料生产制备和加工过程中出现发泡问题。The polyurethane material of the present invention comprises a polyurethane matrix, and the polyurethane matrix is prepared from the resin composition. Due to the reactive components of the resin composition, the average number of acrylate double bonds contained in each molecule The sum of the number of active hydrogen and the number of active hydrogen is not less than 2.1, and the double bond of the acrylate type is a double bond on the acrylic acid group or a double bond on the methacrylic acid group, which can help improve product performance and effectively reduce the The water sensitivity of the above-mentioned resin composition can be avoided to the greatest extent to avoid foaming problems in the subsequent production, preparation and processing of composite materials.
本发明的所述聚氨酯材料制备方法包括:提供所述树脂组合物,所述树脂组合物包含反应性组分、自由基起始剂以及至少一种有机异氰酸酯,所述反应性组分的平均每个分子包含至少一个丙烯酸酯类双键以及至少一个活性氢;通过所述自由基起始剂引发所述至少一个丙烯酸酯类双键的自由基聚合反应,所述至少一个活性氢与所述至少一种有机异氰酸酯发生加成聚合反应。The preparation method of the polyurethane material of the present invention includes: providing the resin composition, the resin composition includes a reactive component, a free radical initiator and at least one organic isocyanate, and the average amount of the reactive component is Each molecule contains at least one acrylate double bond and at least one active hydrogen; the free radical polymerization reaction of the at least one acrylate double bond is initiated by the free radical initiator, and the at least one active hydrogen is combined with the at least one active hydrogen An organic isocyanate undergoes addition polymerization.
所述聚氨酯材料制备方法使用了所述树脂组合物作为原料,由于所述树脂组合物的反应性组分中,平均每个分子所含有的丙烯酸酯类双键和活性氢的数目之和不少于2.1,所述丙烯酸酯类双键为丙烯酸基团上的双键或甲基丙烯酸基团上的双键,能够有助于提高产品性能,且有效降低所述树脂组合物的水敏感性,最大程度避免后续复合材料生产制备和加工过程中出现缺胶问题使得成品易于出现发泡问题。The preparation method of the polyurethane material uses the resin composition as a raw material, because in the reactive components of the resin composition, the average number of acrylate double bonds and active hydrogen contained in each molecule is quite a lot In 2.1, the acrylate double bond is a double bond on an acrylic acid group or a double bond on a methacrylic group, which can help improve product performance and effectively reduce the water sensitivity of the resin composition, Minimize the lack of glue in the subsequent preparation and processing of composite materials, making the finished product prone to foaming problems.
优选的,所述树脂组合物还包括催化剂,控制所述催化剂占所述反应性组分的质量百分比大于0并小于等于5%,以加速由所述活性氢与所述至少一种有机异氰酸酯发生所述加成聚合反应得到的氨基甲酸酯类基团的交联反应。其有益效果在于:能够有助于提高产品性能,且有效降低所述树脂组合物的水敏感性。Preferably, the resin composition further includes a catalyst, and the mass percentage of the catalyst in the reactive component is controlled to be greater than 0 and less than or equal to 5%, so as to accelerate the reaction between the active hydrogen and the at least one organic isocyanate. The cross-linking reaction of the carbamate group obtained by the addition polymerization reaction. The beneficial effect is that it can help improve product performance and effectively reduce the water sensitivity of the resin composition.
优选的,所述树脂组合物还包含助剂,以调控所述聚氨酯材料的理化性能。Preferably, the resin composition further includes additives to regulate the physical and chemical properties of the polyurethane material.
优选的,所述至少一种有机异氰酸酯的平均官能度为2.0-3.6。其有益效果在于:能够有助于提高产品性能,且有效降低所述树脂组合物的水敏感性。优选的,所述至少一种有机异氰酸酯在25℃下根据DIN 53019-1-3测定的粘度为4-2500毫帕斯卡.秒。其有益效果在于:能够有助于提高产品性能,且有效降低所述树脂组合物的水敏感性。Preferably, the average functionality of the at least one organic isocyanate is 2.0-3.6. The beneficial effect is that it can help improve product performance and effectively reduce the water sensitivity of the resin composition. Preferably, said at least one organic isocyanate has a viscosity measured according to DIN 53019-1-3 at 25° C. of 4-2500 mPa.s. The beneficial effect is that it can help improve product performance and effectively reduce the water sensitivity of the resin composition.
本发明的聚氨酯复合材料包含增强材料和所述聚氨酯材料。由于所述聚氨酯材料由所述树脂组合物制备而成,所述树脂组合物的反应性组分中,平均 每个分子所含有的丙烯酸酯类双键和活性氢的数目之和不少于2.1,所述丙烯酸酯类双键为丙烯酸基团上的双键或甲基丙烯酸基团上的双键,能够有助于提高产品性能,且有效降低所述树脂组合物的水敏感性,最大程度避免后续复合材料生产制备和加工过程中出现发泡问题。The polyurethane composite material of the present invention comprises a reinforcing material and the polyurethane material. Since the polyurethane material is prepared from the resin composition, in the reactive components of the resin composition, the average number of acrylate double bonds and active hydrogen contained in each molecule is not less than 2.1 , the acrylate double bond is a double bond on an acrylic acid group or a double bond on a methacrylic acid group, which can help improve product performance and effectively reduce the water sensitivity of the resin composition to the greatest extent Avoid foaming problems in the subsequent preparation and processing of composite materials.
优选的,所述增强材料占所述聚氨酯复合材料的质量百分比为1-91%。其有益效果在于:使力学强度可根据使用需求灵活调控。Preferably, the reinforcing material accounts for 1-91% by mass of the polyurethane composite material. The beneficial effect is that the mechanical strength can be flexibly adjusted according to the use requirements.
本发明的所述聚氨酯复合材料制备方法以增强材料和所述聚氨酯材料为原料,通过真空导入工艺、拉挤成型工艺、缠绕成型工艺、树脂传递工艺、手糊成型工艺、模压成型工艺和喷射成型工艺的至少一种制备而成。由于所述聚氨酯复合材料制备方法以所述聚氨酯材料为原料之一,所述树脂组合物的反应性组分中,平均每个分子所含有的丙烯酸酯类双键和活性氢的数目之和不少于2.1,所述丙烯酸酯类双键为丙烯酸基团上的双键或甲基丙烯酸基团上的双键,能够有助于提高产品性能,且有效降低所述树脂组合物的水敏感性,最大程度避免后续复合材料生产制备和加工过程中出现发泡问题。The preparation method of the polyurethane composite material of the present invention uses reinforcing materials and the polyurethane material as raw materials, through vacuum introduction process, pultrusion forming process, winding forming process, resin transfer process, hand lay-up forming process, compression molding process and spray forming Prepared by at least one of the techniques. Since the preparation method of the polyurethane composite material uses the polyurethane material as one of the raw materials, in the reactive components of the resin composition, the sum of the number of acrylate double bonds and active hydrogen contained in each molecule on average is not equal to Less than 2.1, the acrylate double bond is a double bond on the acrylic acid group or a double bond on the methacrylic group, which can help improve product performance and effectively reduce the water sensitivity of the resin composition , to avoid foaming problems in the subsequent production, preparation and processing of composite materials to the greatest extent.
发明内容Contents of the invention
为使本发明实施例的目的、技术方案和优点更加清楚,下面将对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有作出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。除非另外定义,此处使用的技术术语或者科学术语应当为本发明所属领域内具有一般技能的人士所理解的通常意义。本文中使用的“包括”等类似的词语意指出现该词前面的元件或者物件涵盖出现在该词后面列举的元件或者物件及其等同,而不排除其他元件或者物件。In order to make the purpose, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below. Obviously, the described embodiments are part of the embodiments of the present invention, not all of them. the embodiment. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without creative efforts fall within the protection scope of the present invention. Unless otherwise defined, the technical terms or scientific terms used herein shall have the usual meanings understood by those skilled in the art to which the present invention belongs. As used herein, "comprising" and similar words mean that the elements or items appearing before the word include the elements or items listed after the word and their equivalents, without excluding other elements or items.
本发明实施例提供了一种树脂组合物,包含异氰酸酯组分、反应性组分和自由基起始剂。An embodiment of the present invention provides a resin composition, which includes an isocyanate component, a reactive component and a free radical initiator.
本发明实施例中,对有机多异氰酸酯、聚醚多元醇、聚酯多元醇、其它 类多元醇及含活性氢低聚物的具体描述,可以参考文献“《聚氨酯原料及助剂手册》第二版,刘益军编著,2013年,化学工业出版社”的第1、2、3、4章,将上述公开的全部内容以引用的方式合并入本文。In the embodiment of the present invention, for the specific description of organic polyisocyanates, polyether polyols, polyester polyols, other polyols and active hydrogen-containing oligomers, reference can be made to the second part of "Handbook of Polyurethane Raw Materials and Auxiliaries" Edition, edited by Liu Yijun, 2013, Chapters 1, 2, 3, and 4 of "Chemical Industry Press", the entire content of the above disclosure is incorporated herein by reference.
本发明实施例中,所述异氰酸酯组分包含至少一种有机异氰酸酯。In an embodiment of the present invention, the isocyanate component includes at least one organic isocyanate.
一些实施例中,所述至少一种有机异氰酸酯为用于制备聚氨酯的已知任何链状脂肪族异氰酸酯、脂环族异氰酸酯和芳香族异氰酸酯的至少一种。In some embodiments, the at least one organic isocyanate is at least one of any chain aliphatic isocyanate, alicyclic isocyanate and aromatic isocyanate known to be used in the preparation of polyurethane.
一些具体的实施例中,所述至少一种有机异氰酸酯为2,2'-二苯基甲烷二异氰酸酯、2,4'-二苯基甲烷二异氰酸酯、4,4'-二苯基甲烷二异氰酸酯、单体二苯基甲烷二异氰酸酯和二苯基甲烷二异氰酸酯的高级同系物(简记为聚合MDI)的混合物,异佛尔酮二异氰酸酯(IPDI)或其低聚物,2,4-甲苯二异氰酸酯或2,6-甲苯二异氰酸酯(TDI)或其混合物;四亚甲基二异氰酸酯或其低聚物;五亚甲基二异氰酸酯或其低聚物;六亚甲基二异氰酸酯(HDI)或其低聚物;4,4’-二环己基甲烷二异氰酸酯(HMDI)、甲基环己基二异氰酸酯(HTDI)、1,5-萘基二异氰酸酯(NDI)或其混合物、对苯二异氰酸酯(PPDI)、对苯二亚甲基二异氰酸酯(XDI)、四甲基二亚甲基二异氰酸酯(TMXDI)以及它们的多聚体或其组合。In some specific embodiments, the at least one organic isocyanate is 2,2'-diphenylmethane diisocyanate, 2,4'-diphenylmethane diisocyanate, 4,4'-diphenylmethane diisocyanate , a mixture of monomeric diphenylmethane diisocyanate and higher homologues of diphenylmethane diisocyanate (abbreviated as polymeric MDI), isophorone diisocyanate (IPDI) or its oligomers, 2,4-toluene Diisocyanate or 2,6-toluene diisocyanate (TDI) or mixtures thereof; tetramethylene diisocyanate or its oligomers; pentamethylene diisocyanate or its oligomers; hexamethylene diisocyanate (HDI) or its oligomers; 4,4'-dicyclohexylmethane diisocyanate (HMDI), methylcyclohexyl diisocyanate (HTDI), 1,5-naphthyl diisocyanate (NDI) or mixtures thereof, p-phenylene diisocyanate (PPDI), p-xylylene diisocyanate (XDI), tetramethyl dimethylene diisocyanate (TMXDI) and their multimers or combinations thereof.
一些实施例中,所述至少一种有机异氰酸酯的至少一种以多异氰酸酯预聚物的形式存在,所述多异氰酸酯预聚物为异氰酸酯的二聚体、三聚体、四聚体和五聚体的任意一种。In some embodiments, at least one of the at least one organic isocyanate exists in the form of a polyisocyanate prepolymer, and the polyisocyanate prepolymer is an isocyanate dimer, trimer, tetramer, and pentamer any kind of body.
一些具体的实施例中,所述多异氰酸酯预聚物的NCO重量百分比为10-48%。另一些具体的实施例中,所述多异氰酸酯预聚物的NCO重量百分比为16-38%和19-33%的任意一种。In some specific embodiments, the NCO weight percentage of the polyisocyanate prepolymer is 10-48%. In other specific embodiments, the NCO weight percentage of the polyisocyanate prepolymer is any one of 16-38% and 19-33%.
一些具体的实施例中,所述至少一种有机异氰酸酯为二苯基甲烷二异氰酸酯(MDI)、多苯基甲烷多异氰酸酯(PMDI)、以及它们的多聚体、预聚体或其组合。In some specific embodiments, the at least one organic isocyanate is diphenylmethane diisocyanate (MDI), polyphenylmethane polyisocyanate (PMDI), and their multimers, prepolymers or combinations thereof.
一些实施例中,所述至少一种有机异氰酸酯的平均官能度为2.0-3.6。另 一些实施例中,所述至少一种有机异氰酸酯的平均官能度为2.1-2.8。In some embodiments, the at least one organic isocyanate has an average functionality of 2.0-3.6. In some other embodiments, the average functionality of the at least one organic isocyanate is 2.1-2.8.
一些实施例中,所述至少一种有机异氰酸酯在25℃下根据DIN53019-1-3测定的粘度为4-2500mPa.s。In some embodiments, the viscosity of the at least one organic isocyanate measured according to DIN53019-1-3 at 25° C. is 4-2500 mPa.s.
一些实施例中,所述至少一种有机异氰酸酯在25℃下根据DIN53019-1-3测定的粘度范围为5-800mPa.s和10-300mPa.s的任意一种。In some embodiments, the at least one organic isocyanate has a viscosity measured according to DIN53019-1-3 at 25° C. in any one of 5-800 mPa.s and 10-300 mPa.s.
本发明实施例中,所述反应性组分的平均每个分子包含至少一个丙烯酸酯类双键和至少一个活性氢,平均每个分子所含有的丙烯酸酯类双键和活性氢的数目之和不少于2.1。In an embodiment of the present invention, each molecule of the reactive component contains at least one acrylate double bond and at least one active hydrogen, and the average number of acrylate double bonds and active hydrogen contained in each molecule is the sum of Not less than 2.1.
具体的,所述至少一个丙烯酸酯类双键在所述自由基起始剂的作用下发生自由基聚合反应,所述至少一个活性氢与所述至少一种有机异氰酸酯发生加成聚合反应。Specifically, the at least one acrylate double bond undergoes a radical polymerization reaction under the action of the radical initiator, and the at least one active hydrogen undergoes an addition polymerization reaction with the at least one organic isocyanate.
一些实施例中,所述丙烯酸酯类双键为丙烯酸基团上的双键或甲基丙烯酸基团上的双键。In some embodiments, the acrylate double bond is a double bond on an acrylic group or a double bond on a methacrylic group.
一些实施例中,所述反应性组分的平均每个分子包含1-4个丙烯酸酯类基团,每个所述丙烯酸酯类基团包含所述丙烯酸酯类双键。In some embodiments, the reactive component comprises 1-4 acrylate groups per molecule on average, each of the acrylate groups comprising the acrylate double bond.
一些实施例中,所述反应性组分的平均每个分子包含的丙烯酸酯类基团的数值范围为1.05-3,1.1-2.5,1.15-2.4以及1.2-2.3的任意一种。In some embodiments, the number of acrylate groups contained in each molecule of the reactive component is any one of 1.05-3, 1.1-2.5, 1.15-2.4 and 1.2-2.3.
一些实施例中,所述反应性组分的平均每个分子包含1.1-4.9个羟基,每个所述羟基包含所述活性氢。In some embodiments, the reactive component comprises, on average, 1.1-4.9 hydroxyl groups per molecule, each of the hydroxyl groups comprising the active hydrogen.
一些实施例中,所述反应性组分的平均每个分子所包含的羟基的数值范围为1.2-4,1.25-3.5,1.3-3,1.35-2.6,1.4-2.5以及1.5-2.4的任意一种。In some embodiments, the number of hydroxyl groups contained in each molecule of the reactive component is any one of 1.2-4, 1.25-3.5, 1.3-3, 1.35-2.6, 1.4-2.5 and 1.5-2.4 kind.
一些实施例中,所述反应性组分为至少一种有机多元醇与丙烯酸类物质通过酯化反应得到的酯类产物,所述至少一种有机多元醇的平均每个分子具有至少2.1个所述活性氢。In some embodiments, the reactive component is an ester product obtained through an esterification reaction of at least one organic polyol and an acrylic substance, and the at least one organic polyol has an average of at least 2.1 the active hydrogen.
一些实施例中,所述丙烯酸类物质为丙烯酸酐、甲基丙烯酸酐、丙烯酰氯、甲基丙烯酰氯、丙烯酰溴、甲基丙烯酰溴、丙烯酸、甲基丙烯酸、丙烯 酸甲酯、甲基丙烯酸甲酯、丙烯酸乙酯、甲基丙烯酸乙酯、丙烯酸丙酯、甲基丙烯酸丙酯、丙烯酸异丙酯、甲基丙烯酸异丙酯、丙烯酸丁酯、甲基丙烯酸丁酯、丙烯酸叔丁酯和甲基丙烯酸叔丁酯的至少一种。In some embodiments, the acrylic substance is acrylic anhydride, methacrylic anhydride, acryloyl chloride, methacryloyl chloride, acryloyl bromide, methacryloyl bromide, acrylic acid, methacrylic acid, methyl acrylate, methacrylic acid Methyl acrylate, ethyl methacrylate, propyl acrylate, propyl methacrylate, isopropyl acrylate, isopropyl methacrylate, butyl acrylate, butyl methacrylate, tert-butyl acrylate and At least one kind of tert-butyl methacrylate.
一些实施例中,所述至少一种有机多元醇包含至少一种聚醚多元醇,所述聚醚多元醇包含所述活性氢。In some embodiments, said at least one organic polyol comprises at least one polyether polyol comprising said active hydrogen.
一些实施例中,所述至少一种有机多元醇为聚醚多元醇、聚醚碳酸酯多元醇、聚酯多元醇、聚碳酸酯二醇、聚合物多元醇和基于植物油的多元醇的至少一种。In some embodiments, the at least one organic polyol is at least one of polyether polyol, polyether carbonate polyol, polyester polyol, polycarbonate diol, polymer polyol, and vegetable oil-based polyol .
一些实施例中,所述至少一种有机多元醇为聚氧化丙烯二醇、聚醚三醇、聚醚四醇、聚醚五醇、聚脲多元醇、聚四氢呋喃二醇、己二酸聚酯二醇、芳香族聚酯多元醇、聚己内酯多元醇、聚碳酸酯二醇、聚丙烯酸酯多元醇和聚烯烃多元醇的至少一种。In some embodiments, the at least one organic polyol is polyoxypropylene diol, polyether triol, polyether tetraol, polyether pentaol, polyurea polyol, polytetrahydrofuran diol, adipate polyester At least one of diol, aromatic polyester polyol, polycaprolactone polyol, polycarbonate diol, polyacrylate polyol, and polyolefin polyol.
一些实施例中,所述至少一种聚醚多元醇的平均官能度为2.1-6,羟值为25-1100毫克氢氧化钾/克。In some embodiments, the average functionality of the at least one polyether polyol is 2.1-6, and the hydroxyl value is 25-1100 mg potassium hydroxide/g.
一些实施例中,所述至少一种聚醚多元醇的平均官能度为2.5-5,羟值为35-800毫克氢氧化钾/克。In some embodiments, the average functionality of the at least one polyether polyol is 2.5-5, and the hydroxyl value is 35-800 mg potassium hydroxide/g.
一些实施例中,所述至少一种聚醚多元醇的平均官能度为2.7-4.6,羟值为50-660毫克氢氧化钾/克。In some embodiments, the average functionality of the at least one polyether polyol is 2.7-4.6, and the hydroxyl value is 50-660 mg potassium hydroxide/g.
一些实施例中,所述至少一种聚醚多元醇的平均官能度为2.8-4.4,羟值为80-630毫克氢氧化钾/克。In some embodiments, the average functionality of the at least one polyether polyol is 2.8-4.4, and the hydroxyl number is 80-630 mg potassium hydroxide/g.
一些实施例中,所述至少一种聚醚多元醇的平均官能度为3.0-4.3,羟值为100-600毫克氢氧化钾/克。In some embodiments, the average functionality of the at least one polyether polyol is 3.0-4.3, and the hydroxyl value is 100-600 mg potassium hydroxide/g.
一些实施例中,所述至少一种聚醚多元醇的平均官能度为3.1-4.2,羟值为110-570毫克氢氧化钾/克。In some embodiments, the average functionality of the at least one polyether polyol is 3.1-4.2, and the hydroxyl number is 110-570 mg potassium hydroxide/g.
一些实施例中,所述反应性组分由至少一种有机多元醇与至少一种丙烯酸基团或甲基丙烯酸基团进行酯化得到。In some embodiments, the reactive component is obtained by esterifying at least one organic polyol with at least one acrylic or methacrylic group.
一些实施例中,所述反应性组分由至少一种有机多元醇与至少一种丙烯酸酐或甲基丙烯酸酐发生酯化反应得到。In some embodiments, the reactive component is obtained by esterifying at least one organic polyol with at least one acrylic anhydride or methacrylic anhydride.
一些实施例中,所述反应性组分由至少一种有机多元醇与至少一种丙烯酰卤或甲基丙烯酰卤发生酯化反应得到。In some embodiments, the reactive component is obtained by esterifying at least one organic polyol with at least one acryloyl halide or methacryloyl halide.
具体的,丙烯酰卤为丙烯酰氯和丙烯酰溴的任意一种。Specifically, the acryloyl halide is any one of acryloyl chloride and acryloyl bromide.
具体的,甲基丙烯酰卤为甲基丙烯酰氯和甲基丙烯酰溴的任意一种。Specifically, the methacryloyl halide is any one of methacryloyl chloride and methacryloyl bromide.
一些实施例中,所述反应性组分由至少一种有机多元醇与至少一种丙烯酸或甲基丙烯酸在催化剂条件下发生酯化反应得到。In some embodiments, the reactive component is obtained by esterifying at least one organic polyol with at least one acrylic acid or methacrylic acid under catalyst conditions.
一些实施例中,所述反应性组分由至少一种有机多元醇与至少一种甲基丙烯酸酯或丙烯酸酯在催化剂条件下发生酯交换反应得到。In some embodiments, the reactive component is obtained by transesterifying at least one organic polyol with at least one methacrylate or acrylate under catalyst conditions.
具体的,丙烯酸酯为丙烯酸甲酯、丙烯酸乙酯、丙烯酸丙酯、丙烯酸异丙酯、丙烯酸丁酯和丙烯酸叔丁酯的任意一种。Specifically, the acrylate is any one of methyl acrylate, ethyl acrylate, propyl acrylate, isopropyl acrylate, butyl acrylate and tert-butyl acrylate.
具体的,甲基丙烯酸酯为甲基丙烯酸甲酯、甲基丙烯酸乙酯、甲基丙烯酸丙酯、甲基丙烯酸异丙酯、甲基丙烯酸丁酯和甲基丙烯酸叔丁酯的任意一种。Specifically, the methacrylate is any one of methyl methacrylate, ethyl methacrylate, propyl methacrylate, isopropyl methacrylate, butyl methacrylate and tert-butyl methacrylate.
上述至少一种有机多元醇与丙烯酸酐或甲基丙烯酸酐发生的酯化反应、与丙烯酰卤或甲基丙烯酰卤发生的酯化反应、与丙烯酸或甲基丙烯酸发生的酯化反应以及与丙烯酸酯或甲基丙烯酸酯发生的酯交换反应,本领域普通技术人员熟知这些反应的具体操作方法。一些酯化方法可以参考CN101983959B或CN101475502B中的记载。The esterification reaction of at least one organic polyhydric alcohol with acrylic anhydride or methacrylic anhydride, the esterification reaction with acryloyl halide or methacryloyl halide, the esterification reaction with acrylic acid or methacrylic acid, and the For the transesterification reaction of acrylate or methacrylate, those skilled in the art are familiar with the specific operation methods of these reactions. Some esterification methods can refer to the records in CN101983959B or CN101475502B.
一些实施例中,以占所述反应性组分的质量百分比计,所述自由基起始剂的含量为0.01%-7%。In some embodiments, based on the mass percentage of the reactive component, the content of the free radical initiator is 0.01%-7%.
一些实施例中,所述自由基起始剂为可引发含双键化合物固化的自由基引发剂。In some embodiments, the free radical initiator is a free radical initiator capable of initiating curing of the double bond-containing compound.
一些实施例中,所述自由基起始剂添加于所述至少一种有机异氰酸酯和所述反应性组分的至少一种。In some embodiments, the free radical initiator is added to at least one of the at least one organic isocyanate and the reactive component.
一些实施例中,所述自由基起始剂为过氧化物、过硫化物、过氧化碳酸酯、过氧化硼酸和偶氮化合物的任意一种。In some embodiments, the free radical initiator is any one of peroxide, persulfide, peroxycarbonate, peroxyboric acid and azo compound.
一些具体的实施例中,所述自由基起始剂为氧化异丙基碳酸叔丁酯、过氧化-3,5,5-三甲基己酸叔丁酯、过氧化甲乙酮、异丙苯过氧化氢、过硫酸盐、偶氮二异丁腈、偶氮二异庚腈、偶氮二异丁酸二甲酯、过氧化苯甲酰、过氧化苯甲酰叔丁酯和过氧化氢中的至少一种。In some specific embodiments, the free radical initiator is tert-butyl isopropyl carbonate, tert-butyl peroxy-3,5,5-trimethylhexanoate, methyl ethyl ketone peroxide, cumene peroxide Hydrogen peroxide, persulfate, azobisisobutyronitrile, azobisisoheptanonitrile, dimethyl azobisisobutyrate, benzoyl peroxide, benzoyl tert-butyl peroxide and hydrogen peroxide at least one of .
一些实施例中,所述树脂组合物还包含催化剂,以加速氨基甲酸酯类基团的交联反应,以占所述反应性组分的质量百分比计,所述催化剂的含量大于0并小于等于5%,所述氨基甲酸酯类基团由所述活性氢与所述至少一种有机异氰酸酯发生所述加成聚合反应得到。In some embodiments, the resin composition further includes a catalyst to accelerate the crosslinking reaction of the carbamate group, and the content of the catalyst is greater than 0 and less than or equal to 5%, the urethane group is obtained by the addition polymerization of the active hydrogen and the at least one organic isocyanate.
一些实施例中,所述催化剂占所述反应性组分的质量百分比为0.001-2%。In some embodiments, the mass percentage of the catalyst in the reactive component is 0.001-2%.
一些具体的实施例中,所述催化剂为2,3-二甲基-3,4,5,6-四氢嘧啶、三乙胺、三丁胺、三乙烯二胺、二甲基苄胺、N-甲基吗啉、N-乙基吗啉、N-环己基吗啉、N,N,N',N'-四甲基乙二胺、N,N,N',N'-四甲基丁二胺、N,N,N',N'-四甲基己二胺、五甲基二亚乙基三胺、四甲基二氨基乙醚、双(二甲基氨基丙基)脲、二甲基哌嗪、1,2-二甲基咪唑和1-氮杂双环(3,3,0)辛烷的任意一种。In some specific embodiments, the catalyst is 2,3-dimethyl-3,4,5,6-tetrahydropyrimidine, triethylamine, tributylamine, triethylenediamine, dimethylbenzylamine, N-methylmorpholine, N-ethylmorpholine, N-cyclohexylmorpholine, N,N,N',N'-tetramethylethylenediamine, N,N,N',N'-tetramethyl butyldiamine, N,N,N',N'-tetramethylhexamethylenediamine, pentamethyldiethylenetriamine, tetramethyldiaminoethylether, bis(dimethylaminopropyl)urea, Any of dimethylpiperazine, 1,2-dimethylimidazole, and 1-azabicyclo(3,3,0)octane.
一些实施例中,所述催化剂为1,4-二氮杂双环(2,2,2)辛烷、三乙醇胺、三异丙醇胺、N-甲基二乙醇胺、N-乙基二乙醇胺和二甲基乙醇胺的任意一种。In some embodiments, the catalyst is 1,4-diazabicyclo(2,2,2)octane, triethanolamine, triisopropanolamine, N-methyldiethanolamine, N-ethyldiethanolamine and Any one of dimethylethanolamine.
一些实施例中,所述催化剂为有机金属化合物。另一些实施例中,所述催化剂由所述有机金属化合物和强碱性胺组成。In some embodiments, the catalyst is an organometallic compound. In some other embodiments, the catalyst consists of the organometallic compound and a strongly basic amine.
一些具体的实施例中,所述有机金属化合物为乙酸锡(II)、辛酸锡(II)、乙基己酸锡(II)、月桂酸锡(II)、二乙酸二丁基锡、二月桂酸二丁基锡、马来酸二丁基锡、二乙酸二辛基锡的任意一种。In some specific embodiments, the organometallic compound is tin(II) acetate, tin(II) octoate, tin(II) ethylhexanoate, tin(II) laurate, dibutyltin diacetate, dilaurate dilaurate Any of butyltin, dibutyltin maleate, and dioctyltin diacetate.
一些具体的实施例中,所述有机金属化合物为新癸酸铋(III)、2-乙基己酸铋和辛酸铋或其混合物。In some specific embodiments, the organometallic compound is bismuth (III) neodecanoate, bismuth 2-ethylhexanoate, bismuth octoate or mixtures thereof.
一些实施例中,所述树脂组合物还包含若干助剂,以利于调控通过所述树脂组合物所制备的聚氨酯材料的理化性能,所述理化性能包括粘度、交联度、防水性能、阻燃性能、防烟性能、防染性能、抗静电性能、抗氧化性能、紫外稳定性能、流平性能和吸附性能的至少一种。In some embodiments, the resin composition also includes several additives to facilitate regulation and control of the physical and chemical properties of the polyurethane material prepared by the resin composition, the physical and chemical properties include viscosity, degree of crosslinking, waterproof performance, flame retardant At least one of performance, anti-smoke performance, anti-staining performance, antistatic performance, anti-oxidation performance, ultraviolet stability performance, leveling performance and adsorption performance.
一些具体的实施例中,所述若干助剂为填料、内脱模剂、阻燃剂、防烟剂、染料、颜料、抗静电剂、抗氧剂、UV稳定剂、稀释剂、消泡剂、偶联剂、表面润湿剂、流平剂、除水剂、催化剂、分子筛、触变剂、增塑剂和自由基反应抑制剂的至少一种。In some specific embodiments, the several auxiliary agents are fillers, internal release agents, flame retardants, smoke suppressants, dyes, pigments, antistatic agents, antioxidants, UV stabilizers, diluents, defoamers , coupling agent, surface wetting agent, leveling agent, water remover, catalyst, molecular sieve, thixotropic agent, plasticizer and free radical reaction inhibitor.
一些具体的实施例中,所述填料为氢氧化铝、膨润土、粉煤灰、硅灰石、珍珠岩粉、漂珠、碳酸钙、滑石粉、云母粉、瓷土、气相白炭黑、可膨胀微球、硅藻土、火山灰、硫酸钡、硫酸钙、实心和/或空心的玻璃微球、石粉、木粉、木屑、竹粉、竹屑、稻粒、秸秆碎屑、咖啡渣、高粱杆碎屑、石墨粉、金属粉末、热固性复合材料回收粉料、塑料颗粒或粉末的至少一种。In some specific embodiments, the filler is aluminum hydroxide, bentonite, fly ash, wollastonite, perlite powder, floating beads, calcium carbonate, talcum powder, mica powder, china clay, fumed silica, expandable Microspheres, diatomaceous earth, volcanic ash, barium sulfate, calcium sulfate, solid and/or hollow glass microspheres, stone powder, wood flour, wood chips, bamboo powder, bamboo chips, rice grains, straw chips, coffee grounds, sorghum stalks At least one of scrap, graphite powder, metal powder, recycled thermosetting composite powder, plastic granules or powder.
本发明实施例中关于催化剂、阻燃剂、脱模剂、防老化助剂和稳定剂、偶联剂、填料和增强材料等的具体描述,也可以参考文献“《聚氨酯原料及助剂手册》第二版,刘益军编著,2013年,化学工业出版社”的第6、7、8、9、11、12章,将上述公开的全部内容以引用的方式合并入本文。For specific descriptions of catalysts, flame retardants, mold release agents, anti-aging additives and stabilizers, coupling agents, fillers, and reinforcing materials in the embodiments of the present invention, you can also refer to the "Handbook of Polyurethane Raw Materials and Auxiliaries" The second edition, edited by Liu Yijun, 2013, Chapters 6, 7, 8, 9, 11, and 12 of "Chemical Industry Press", the entire content of the above disclosure is incorporated into this article by reference.
本发明实施例还提供了聚氨酯材料,所述聚氨酯材料包含聚氨酯基体,所述聚氨酯基体由所述树脂组合物制备而成,由于所述树脂组合物的反应性组分中,平均每个分子所含有的丙烯酸酯类双键和活性氢的数目之和不少于2.1,所述丙烯酸酯类双键为丙烯酸基团上的双键或甲基丙烯酸基团上的双键,能够有助于提高产品性能,且有效降低所述树脂组合物的水敏感性,最大程度避免后续复合材料生产制备和加工过程中出现发泡问题。The embodiment of the present invention also provides a polyurethane material, the polyurethane material includes a polyurethane matrix, the polyurethane matrix is prepared from the resin composition, because in the reactive components of the resin composition, the average The sum of the number of acrylate double bonds and active hydrogen contained is not less than 2.1, and the acrylate double bonds are double bonds on acrylic acid groups or double bonds on methacrylic acid groups, which can help to improve The product performance is improved, and the water sensitivity of the resin composition is effectively reduced, so as to avoid foaming problems in the production, preparation and processing of subsequent composite materials to the greatest extent.
本发明实施例还提供了所述聚氨酯材料制备方法包括:提供所述树脂组合物,所述树脂组合物包含反应性组分、自由基起始剂以及至少一种有机异氰酸酯,所述反应性组分的平均每个分子包含至少一个丙烯酸酯类双键以及 至少一个活性氢;通过所述自由基起始剂引发所述至少一个丙烯酸酯类双键的自由基聚合反应,所述至少一个活性氢与所述至少一种有机异氰酸酯发生加成聚合反应。The embodiment of the present invention also provides that the preparation method of the polyurethane material includes: providing the resin composition, the resin composition includes a reactive component, a free radical initiator and at least one organic isocyanate, and the reactive component On average, each molecule of the fraction contains at least one acrylate double bond and at least one active hydrogen; the free radical polymerization reaction of the at least one acrylate double bond is initiated by the free radical initiator, and the at least one active hydrogen Addition polymerization takes place with the at least one organic isocyanate.
所述聚氨酯材料制备方法使用了所述树脂组合物作为原料,由于所述树脂组合物的反应性组分中,平均每个分子所含有的丙烯酸酯类双键和活性氢的数目之和不少于2.1,所述丙烯酸酯类双键为丙烯酸基团上的双键或甲基丙烯酸基团上的双键,能够有助于提高产品性能,且有效降低所述树脂组合物的水敏感性,最大程度避免后续复合材料生产制备和加工过程中出现发泡问题。The preparation method of the polyurethane material uses the resin composition as a raw material, because in the reactive components of the resin composition, the average number of acrylate double bonds and active hydrogen contained in each molecule is quite a lot In 2.1, the acrylate double bond is a double bond on an acrylic acid group or a double bond on a methacrylic group, which can help improve product performance and effectively reduce the water sensitivity of the resin composition, To avoid foaming problems in the subsequent production, preparation and processing of composite materials to the greatest extent.
一些实施例中,控制所述催化剂占所述反应性组分的质量百分比大于0并小于等于5%,以加速由所述活性氢与所述至少一种有机异氰酸酯发生所述加成聚合反应得到的氨基甲酸酯类基团的交联反应。In some embodiments, the mass percentage of the catalyst in the reactive component is controlled to be greater than 0 and less than or equal to 5%, so as to accelerate the addition polymerization reaction of the active hydrogen and the at least one organic isocyanate to obtain The crosslinking reaction of the carbamate group.
一些实施例中,所述助剂调控所述聚氨酯材料的理化性能,所述理化性能包括粘度、交联度、防水性能、阻燃性能、防烟性能、防染性能、抗静电性能、抗氧化性能、紫外稳定性能、流平性能和吸附性能的至少一种。In some embodiments, the additive regulates the physical and chemical properties of the polyurethane material, and the physical and chemical properties include viscosity, degree of crosslinking, waterproof performance, flame retardant performance, smoke-proof performance, anti-dyeing performance, antistatic performance, oxidation resistance At least one of performance, UV stability performance, leveling performance and adsorption performance.
本发明实施例还提供了聚氨酯复合材料及其制备方法。The embodiment of the invention also provides the polyurethane composite material and its preparation method.
本发明实施例的聚氨酯复合材料包含增强材料和所述聚氨酯材料。由于所述聚氨酯材料由所述树脂组合物制备而成,所述树脂组合物的反应性组分中,平均每个分子所含有的丙烯酸酯类双键和活性氢的数目之和不少于2.1,所述丙烯酸酯类双键为丙烯酸基团上的双键或甲基丙烯酸基团上的双键,能够有助于提高产品性能,且有效降低所述树脂组合物的水敏感性,最大程度避免后续复合材料生产制备和加工过程中出现发泡问题。The polyurethane composite material of the embodiment of the present invention includes a reinforcing material and the polyurethane material. Since the polyurethane material is prepared from the resin composition, in the reactive components of the resin composition, the average number of acrylate double bonds and active hydrogen contained in each molecule is not less than 2.1 , the acrylate double bond is a double bond on an acrylic acid group or a double bond on a methacrylic acid group, which can help improve product performance and effectively reduce the water sensitivity of the resin composition to the greatest extent Avoid foaming problems in the subsequent preparation and processing of composite materials.
一些实施例中,所述增强材料占所述聚氨酯复合材料的质量百分比为l-91%,15-90%,35-85%,45-83%和50-81%的任意一种。In some embodiments, the mass percentage of the reinforcing material in the polyurethane composite material is any one of 1-91%, 15-90%, 35-85%, 45-83% and 50-81%.
一些实施例中,所述增强材料包括玻璃纤维、碳纤维、碳纳米管、聚酯纤维、芳香族聚酰胺纤维、尼龙纤维、天然纤维、玄武岩纤维、碳化硅纤维、 硼纤维、石棉纤维、晶须、硬质颗粒和金属纤维的至少一种。In some embodiments, the reinforcing material includes glass fiber, carbon fiber, carbon nanotube, polyester fiber, aramid fiber, nylon fiber, natural fiber, basalt fiber, silicon carbide fiber, boron fiber, asbestos fiber, whisker , at least one of hard particles and metal fibers.
一些实施例中,聚氨酯加成聚合反应,即异氰酸酯基团与羟基的加成聚合反应与自由基聚合反应同时存在。所述树脂组合物在液态时,被用来润湿所述增强材料,同时发生的加成聚合反应与自由基聚合反应逐渐生成固体的所述聚氨酯基体,与已经被润湿的所述增强材料融为一体,从而形成所述聚氨酯复合材料。In some embodiments, polyurethane addition polymerization, that is, addition polymerization of isocyanate groups and hydroxyl groups, and free radical polymerization occur simultaneously. When the resin composition is in a liquid state, it is used to wet the reinforcing material, and the simultaneous addition polymerization reaction and free radical polymerization reaction gradually generate the solid polyurethane matrix, and the wetted reinforcing material integrated to form the polyurethane composite.
本发明实施例的所述聚氨酯复合材料制备方法以增强材料和所述聚氨酯材料为原料,通过真空导入工艺、拉挤成型工艺、缠绕成型工艺、树脂传递工艺、手糊成型工艺、模压成型工艺和喷射成型工艺的至少一种制备而成。由于所述聚氨酯复合材料制备方法以所述聚氨酯材料为原料之一,所述树脂组合物的反应性组分中,平均每个分子所含有的丙烯酸酯类双键和活性氢的数目之和不少于2.1,所述丙烯酸酯类双键为丙烯酸基团上的双键或甲基丙烯酸基团上的双键,能够有助于提高产品性能,且有效降低所述树脂组合物的水敏感性,最大程度避免后续复合材料生产制备和加工过程中出现发泡问题。The preparation method of the polyurethane composite material in the embodiment of the present invention uses the reinforcing material and the polyurethane material as raw materials, through vacuum introduction process, pultrusion forming process, winding forming process, resin transfer process, hand lay-up forming process, compression molding process and Prepared by at least one of the injection molding processes. Since the preparation method of the polyurethane composite material uses the polyurethane material as one of the raw materials, in the reactive components of the resin composition, the sum of the number of acrylate double bonds and active hydrogen contained in each molecule on average is not equal to Less than 2.1, the acrylate double bond is a double bond on the acrylic acid group or a double bond on the methacrylic group, which can help improve product performance and effectively reduce the water sensitivity of the resin composition , to avoid foaming problems in the subsequent production, preparation and processing of composite materials to the greatest extent.
上述真空导入工艺、拉挤成型工艺、缠绕成型工艺、树脂传递工艺、手糊成型工艺、模压成型工艺和喷射成型工艺均为本领域技术人员的常规技术手段。The above-mentioned vacuum introduction process, pultrusion forming process, winding forming process, resin transfer process, hand lay-up process, compression molding process and spray forming process are all conventional technical means for those skilled in the art.
以下通过具体的实施例对本发明实施例技术方案进行详细阐述。The technical solutions of the embodiments of the present invention will be described in detail below through specific examples.
具体实施例的树脂拉伸性能根据ISO 527-2测定。Resin tensile properties of specific examples were determined according to ISO 527-2.
具体实施例的聚氨酯复合材料拉伸性能根据ISO 527-5测定。The tensile properties of the polyurethane composites of the specific examples were determined according to ISO 527-5.
具体实施例所用原材料如下:The raw materials used in specific embodiments are as follows:
异氰酸酯组分:异氰酸酯PM200和异氰酸酯WANNATE MDI-50;Isocyanate components: isocyanate PM200 and isocyanate WANNATE MDI-50;
制备反应性组分的原料为聚醚多元醇P1、聚醚多元醇P2、聚醚多元醇P3和聚醚多元醇P4。其中:The raw materials for preparing the reactive components are polyether polyol P1, polyether polyol P2, polyether polyol P3 and polyether polyol P4. in:
聚醚多元醇P1以甘油作为起始剂,环氧丙烷为聚合反应的主体制得的3官能度多元醇,羟值235mg KOH/g;Polyether polyol P1 is a trifunctional polyol prepared with glycerin as the initiator and propylene oxide as the main body of the polymerization reaction, with a hydroxyl value of 235 mg KOH/g;
聚醚多元醇P2以甘油作为起始剂,环氧丙烷为聚合反应的主体制得的3官能度多元醇,羟值330mgK0H/g;Polyether polyol P2 is a trifunctional polyol prepared with glycerin as the initiator and propylene oxide as the main body of the polymerization reaction, with a hydroxyl value of 330 mgKOH/g;
聚醚多元醇P3以季戊四醇作为起始剂,环氧丙烷为聚合反应的主体制得的4官能度多元醇,羟值450mgK0H/g;Polyether polyol P3 is a tetrafunctional polyol prepared by using pentaerythritol as the initiator and propylene oxide as the main body of the polymerization reaction, with a hydroxyl value of 450mgKOH/g;
聚醚多元醇P4以山梨醇作为起始剂,环氧丙烷为聚合反应的主体制得的6官能度多元醇,羟值430mgK0H/g;Polyether polyol P4 is a six-functional polyol prepared with sorbitol as the initiator and propylene oxide as the main body of the polymerization reaction, with a hydroxyl value of 430 mgKOH/g;
自由基起始剂:过氧化苯甲酰(PERKADOX CH-50L)和过氧化甲乙酮(Butanox M-50),购自诺力昂。Free radical initiators: benzoyl peroxide (PERKADOX CH-50L) and methyl ethyl ketone peroxide (Butanox M-50), purchased from Nouryon.
助剂为5A分子筛活化粉和消泡剂BYKA560,其中的5A分子筛活化粉购自鑫陶科技,消泡剂购自毕克化学。The additives are 5A molecular sieve activated powder and defoamer BYKA560. The 5A molecular sieve activated powder is purchased from Xintao Technology, and the defoamer is purchased from BYK Chemicals.
一些实施例中,至少一种有机多元醇和丙烯酸类物质在催化剂的作用下在有机溶剂中进行酯化反应直至酯化反应不再有水产生。酯化反应的温度为60-140摄氏度。In some embodiments, at least one organic polyol and the acrylic substance are subjected to an esterification reaction in an organic solvent under the action of a catalyst until no more water is produced in the esterification reaction. The temperature of the esterification reaction is 60-140 degrees Celsius.
具体的,按质量份数计,所述至少一种有机多元醇为30-100份,丙烯酸类物质为3-35份,溶剂为3-55份,催化剂为0.05-1份,阻聚剂为0.03-0.5份。Specifically, in parts by mass, the at least one organic polyol is 30-100 parts, the acrylic substance is 3-35 parts, the solvent is 3-55 parts, the catalyst is 0.05-1 part, and the polymerization inhibitor is 0.03-0.5 parts.
一些实施例中,在冰浴和搅拌的条件下将丙烯酸类物质与至少一种有机多元醇、溶剂和催化剂等混合后在冰浴下进行3-8小时的酯化反应。In some embodiments, the acrylic substance is mixed with at least one organic polyol, a solvent, a catalyst, etc. under the condition of ice bath and stirring, and then the esterification reaction is carried out under ice bath for 3-8 hours.
具体的,按质量份数计,所述至少一种有机多元醇为60-90份,丙烯酸类物质为20-60份,溶剂为200-500份,助剂质量为30-150份,阻聚剂的质量为0.03-0.45份。Specifically, in terms of parts by mass, the at least one organic polyol is 60-90 parts, the acrylic substance is 20-60 parts, the solvent is 200-500 parts, the auxiliary agent is 30-150 parts, and the polymerization inhibition The quality of the agent is 0.03-0.45 parts.
具体实施例提供了若干反应性组分,不同具体实施例所使用的反应性组分由所述若干反应性组分中的至少一种组合而成。Embodiments provide several reactive components, and the reactive components used in different embodiments are combined from at least one of the several reactive components.
一些具体的实施例中,所述若干反应性组分中的各反应性组分分别简记为B-P1-1、B-P1-2、B-P2-1、B-P2-2、B-P3-1和B-P4-1。In some specific examples, each reactive component among the several reactive components is abbreviated as B-P1-1, B-P1-2, B-P2-1, B-P2-2, B -P3-1 and B-P4-1.
B-P1-1的每个分子含2个甲基丙烯酸酯和1个羟基,制备方法如下:聚 醚多元醇P1和对苯二酚,质量分别为71.6g和0.1g,对苯二酚作为阻聚剂;甲基丙烯酸为丙烯酸类物质,质量为20.7g;30g环己烷为溶剂,质量为30g;对甲苯磺酸为催化剂,质量为0.8g;上述混合物在80℃下反应至分水器中的水不再产生则反应结束,真空旋去溶剂,所得混合物经提纯即可得到产物B-P1-1。Each molecule of B-P1-1 contains 2 methacrylates and 1 hydroxyl group. The preparation method is as follows: polyether polyol P1 and hydroquinone, the masses are 71.6g and 0.1g respectively, and hydroquinone is used as Inhibitor; methacrylic acid is an acrylic substance with a mass of 20.7g; 30g of cyclohexane is a solvent with a mass of 30g; p-toluenesulfonic acid is a catalyst with a mass of 0.8g; the above mixture is reacted at 80°C until water separation When the water in the vessel is no longer produced, the reaction is finished, and the solvent is removed by vacuum rotation, and the resulting mixture can be purified to obtain the product B-P1-1.
B-P1-2的每个分子结构中含1个甲基丙烯酸酯和2个羟基,制备方法如下:聚醚多元醇P1为71.6g,甲基丙烯酸为10.3g,15g环己烷,0.4g对甲苯磺酸以及0.08g对苯二酚混合后于80℃反应至分水器中的水不再产生则反应结束,真空旋去溶剂,所得混合物经提纯即可得到产物B-P1-2。Each molecular structure of B-P1-2 contains 1 methacrylate and 2 hydroxyl groups. The preparation method is as follows: polyether polyol P1 is 71.6g, methacrylic acid is 10.3g, 15g cyclohexane, 0.4g P-toluenesulfonic acid and 0.08g of hydroquinone are mixed and reacted at 80°C until water in the water separator no longer occurs, then the reaction is completed, the solvent is removed by vacuum rotation, and the obtained mixture is purified to obtain the product B-P1-2.
B-P2-1的每个分子结构中含2个丙烯酸酯和1个羟基,制备方法如下:聚醚多元醇P2为51g,丙烯酸为17.3g,22g环己烷,0.8g对甲苯磺酸以及0.1g对苯二酚于80℃反应至分水器中的水不再产生则反应结束,真空旋去溶剂,所得混合物经提纯即可得到产物B-P2-1。Each molecular structure of B-P2-1 contains 2 acrylates and 1 hydroxyl group. The preparation method is as follows: 51g of polyether polyol P2, 17.3g of acrylic acid, 22g of cyclohexane, 0.8g of p-toluenesulfonic acid and 0.1g of hydroquinone was reacted at 80°C until the water in the water separator was no longer produced, then the reaction was completed, the solvent was removed by vacuum rotation, and the obtained mixture was purified to obtain the product B-P2-1.
B-P2-2的每个分子结构中含1个丙烯酸酯和2个羟基,制备方法如下:聚醚多元醇P2为51g,丙烯酸为8.7g,11g环己烷,0.4g对甲苯磺酸以及0.08g对苯二酚于80℃反应至分水器中的水不再产生则反应结束,真空旋去溶剂,所得混合物经提纯即可得到产物B-P2-2。Each molecular structure of B-P2-2 contains 1 acrylate and 2 hydroxyl groups. The preparation method is as follows: 51g of polyether polyol P2, 8.7g of acrylic acid, 11g of cyclohexane, 0.4g of p-toluenesulfonic acid and 0.08g of hydroquinone is reacted at 80°C until the water in the water separator is no longer produced, then the reaction is complete, the solvent is removed by vacuum rotation, and the obtained mixture is purified to obtain the product B-P2-2.
B-P3-1的每个分子结构中含2个丙烯酸酯和2个羟基,制备方法如下:聚醚多元醇P3为50g,丙烯酸为17.3g,22g环己烷,0.8g对甲苯磺酸以及0.1g对苯二酚于80℃反应至分水器中的水不再产生则反应结束,真空旋去溶剂,所得混合物经提纯即可得到产物B-P3-1。Each molecular structure of B-P3-1 contains 2 acrylates and 2 hydroxyl groups. The preparation method is as follows: 50g of polyether polyol P3, 17.3g of acrylic acid, 22g of cyclohexane, 0.8g of p-toluenesulfonic acid and 0.1g of hydroquinone is reacted at 80°C until the water in the water separator no longer produces, then the reaction is completed, the solvent is removed by vacuum rotation, and the obtained mixture is purified to obtain the product B-P3-1.
B-P4-1的每个分子结构中含5个丙烯酸酯和1个羟基,制备方法如下:在冰浴(0-4℃)和搅拌条件下,将丙烯酰氯42.5ml缓慢滴加到含有78.3g聚醚多元醇P4、0.2g对苯二酚和100g三乙胺的二氯甲烷350ml溶液中,60分钟滴加完毕,三乙胺作为助剂。再在冰浴条件下继续反应5小时。停止搅拌,静置过夜。静置过夜后结束反应,先后用水、1M盐酸、1M的NaOH溶 液洗涤除去未反应产物和其它杂质。真空旋去溶剂,所得混合物经提纯即可得到产物B-P4-1。Each molecular structure of B-P4-1 contains 5 acrylates and 1 hydroxyl group. The preparation method is as follows: slowly add 42.5ml of acryloyl chloride dropwise to 78.3 g polyether polyol P4, 0.2 g of hydroquinone and 100 g of triethylamine in dichloromethane 350 ml solution, the dropwise addition was completed in 60 minutes, and triethylamine was used as an auxiliary agent. The reaction was continued for another 5 hours under ice-bath conditions. Stop stirring and let stand overnight. After standing overnight, the reaction was terminated, and unreacted products and other impurities were removed by washing successively with water, 1M hydrochloric acid, and 1M NaOH solution. The solvent was spun off in vacuo, and the resulting mixture was purified to obtain the product B-P4-1.
下列实施例中未注明具体条件的试验方法,通常按照常规条件,或按照制造厂商所建议的条件。除非另有说明,所有的百分比和份数按重量计。The test methods for which specific conditions are not indicated in the following examples are generally in accordance with conventional conditions, or in accordance with the conditions suggested by the manufacturer. All percentages and parts are by weight unless otherwise indicated.
实施例1-5Example 1-5
首先将浇注体模具放入150℃的烘箱中恒温,然后将表1所列的各组分按比例配制成树脂混合液体,均匀混合后将此树脂液体迅速倒入模具中,并在150℃下保持25分钟。然后停止烘箱的加热使之慢慢降温,等冷却到室温后就可以取出固化的样品,得到对比实施例1-4和实施例1-5的热固聚氨酯树脂基体。具体测试结果见表1。First, put the mold of the casting body in an oven at 150°C to keep the temperature constant, then prepare the components listed in Table 1 into a resin mixed liquid in proportion, and after uniform mixing, quickly pour the resin liquid into the mold, and heat it at 150°C Leave on for 25 minutes. Then the heating of the oven was stopped to lower the temperature slowly, and after cooling to room temperature, the cured sample could be taken out to obtain the thermosetting polyurethane resin matrix of Comparative Examples 1-4 and Examples 1-5. The specific test results are shown in Table 1.
表1Table 1
Figure PCTCN2022104319-appb-000001
Figure PCTCN2022104319-appb-000001
Figure PCTCN2022104319-appb-000002
Figure PCTCN2022104319-appb-000002
从上表1的对比实施例1-4和实施例1-5各项数据分析可以看到,引入了同时含有(甲基)丙烯酸酯和羟基官能团的反应性组分,不仅可以使凝胶时间显著延长,还可以进一步提高固化树脂的力学性能。长的凝胶时间有利于复材行业生产的需要。例如,在拉挤生产工艺中,设备发生故障需要停机修理的时候,如果凝胶时间不够长的话,注胶盒和模具通常就会被固化的树脂堵塞,发生堵模生产事故。这个时候,就需要拆开注胶盒和模具进行清理。不仅浪费时间,降低生产效率,还会产生大量玻纤和树脂固废。又例如,真空导入工艺制备叶片和游艇等大型产品时,需要树脂导入的时间很长。凝胶时间如果低于150分钟,是远远不够的。所以,基于传统聚氨酯体系的对比实施例1-3不适应很多种复材生产工艺的要求。对比实施例4显示,即使加入部分反应性组分(B),也不能满足要求。而实施例1-5则显示凝胶时间被显著延长,均在200分钟以上,远高于150分钟的要求,所以能更好地适应很多种复材生产工艺的时间操作要求;且其力学性能得到很大提高。力学性能提高,有助于在满足实际使用要求的前提下,还可对基于此热固树脂的复合材料进一步减重,使之满足更加轻量化的要求。实施例5中,树脂固化以后收缩率过大,导致树脂板样品发脆和开裂,无法得到满意的测试样品。原因是丙烯酸酯的含量过高,导致活性双键的自由基聚合交联密度过高,使固化树脂收缩率过大而发生内开裂。所以,反应性组分(B)的使用虽然会带来长凝胶时间、优异力学性能等优点,但其分子结构中的平均(甲基)丙烯酸酯官能团个数应该有个优选范围;如果过低的话,则不能显著延长凝胶时间和提高力学性能,但如果过高的化,就会产生收缩开裂等不利影响。It can be seen from the data analysis of comparative examples 1-4 and examples 1-5 in the above table 1 that the introduction of reactive components containing (meth)acrylate and hydroxyl functional groups can not only make the gel time Significantly extended, can also further improve the mechanical properties of the cured resin. The long gel time is beneficial to the production needs of the composite material industry. For example, in the pultrusion production process, when the equipment fails and needs to be shut down for repairs, if the gel time is not long enough, the injection box and the mold will usually be blocked by the cured resin, resulting in a blocked production accident. At this time, it is necessary to disassemble the injection box and mold for cleaning. Not only waste time, reduce production efficiency, but also generate a lot of glass fiber and resin solid waste. Another example is that when large-scale products such as blades and yachts are prepared by the vacuum introduction process, it takes a long time for resin introduction. If the gel time is less than 150 minutes, it is far from enough. Therefore, the comparative examples 1-3 based on the traditional polyurethane system do not meet the requirements of many kinds of composite material production processes. Comparative Example 4 shows that even with the addition of partially reactive component (B), the requirements are not met. However, Examples 1-5 show that the gel time is significantly prolonged, all above 200 minutes, far higher than the requirement of 150 minutes, so it can better adapt to the time operation requirements of many composite material production processes; and its mechanical properties be greatly improved. The improvement of mechanical properties helps to further reduce the weight of the composite material based on this thermosetting resin on the premise of meeting the requirements of actual use, so that it can meet the requirements of lighter weight. In Example 5, the shrinkage rate of the resin after curing was too large, resulting in brittleness and cracking of the resin plate sample, and a satisfactory test sample could not be obtained. The reason is that the content of acrylate is too high, resulting in too high free radical polymerization crosslinking density of active double bonds, so that the cured resin shrinkage rate is too large and internal cracking occurs. Therefore, although the use of the reactive component (B) will bring advantages such as long gel time and excellent mechanical properties, the average number of (meth)acrylate functional groups in its molecular structure should have a preferred range; If it is low, the gel time and mechanical properties cannot be significantly prolonged, but if it is too high, adverse effects such as shrinkage and cracking will occur.
实施例6Example 6
按照表2的配比,将多元醇、异氰酸酯组分(A)、反应性组分(B)、自由基起始剂(C)和其它助剂配成树脂混合液体,在真空条件下搅拌脱气5分钟。再将此树脂混合液体放入已在35℃烘箱中恒温的浇注体模具,继续恒温保持2小时,然后烘箱升温到80℃并保持4小时,再关掉加热。等冷却到室温后就可以取出固化的样品,得到对比实施例5和实施例6的热固聚氨酯树脂基体。具体测试结果见表2。According to the ratio in Table 2, polyol, isocyanate component (A), reactive component (B), free radical initiator (C) and other additives are made into resin mixed liquid, and stirred under vacuum condition Breathe for 5 minutes. Then put the resin mixed liquid into the casting body mold that has been kept in a constant temperature oven at 35°C, and keep the constant temperature for 2 hours, then raise the temperature of the oven to 80°C and keep it for 4 hours, and then turn off the heating. After cooling to room temperature, the cured sample can be taken out to obtain the thermosetting polyurethane resin matrix of Comparative Example 5 and Example 6. The specific test results are shown in Table 2.
表2Table 2
Figure PCTCN2022104319-appb-000003
Figure PCTCN2022104319-appb-000003
从上表2所列对比实施例5和实施例6的数据比较,说明反应性组分(B)的引入,可以使树脂的凝胶时间、力学性能等显著提高。通过比较对比实施例5和实施例6,说明引入反应性组分(B)的热固聚氨酯树脂基体,其综合性能已经优于普通聚氨酯树脂。From the comparison of the data of Comparative Example 5 and Example 6 listed in Table 2 above, it shows that the introduction of the reactive component (B) can significantly improve the gel time and mechanical properties of the resin. By comparing Example 5 and Example 6, it is shown that the thermosetting polyurethane resin matrix introduced with the reactive component (B) has better comprehensive properties than ordinary polyurethane resins.
实施例7Example 7
本实施例中的聚氨酯复合材料,树脂基于表3中对比实施例6、对比实施例7和实施例7的聚氨酯组合物,通过实验室的手糊工艺制备,以用来比较其实际操作的工艺性并观察其固化后的效果包括复材质量。The polyurethane composite material in this embodiment, the resin is based on the polyurethane compositions of comparative example 6, comparative example 7 and embodiment 7 in table 3, prepared by hand lay-up process in the laboratory, to be used to compare the process of its actual operation properties and observe its cured effect including composite quality.
操作在玻璃平板上进行:将四层单轴玻纤布(恒石,E61200,UD,~1200g/m2)分别放置在喷过脱模剂的三块玻璃平板上表面,在25℃和50%相对湿度的环境下放置24小时进行温湿度平衡。依照表3的组分和比例,将三类树脂各自配制好后,分别缓慢倒在各自玻纤布的上表面,使液态树脂从上向下自然渗入玻纤布,并等待6分钟使其充分浸润玻纤,然后在玻纤布上表面覆盖一层透明塑料膜,再使用手糊滚筒将浸润后的玻纤布里面的空气都挤出。(实际操作过程中发现,由于对比实施例7的树脂粘度过低,所以易流淌,导致树脂不能被玻纤布有效吸附,产生树脂流失而使玻纤布缺胶,此缺胶现象会在玻纤布里留下很多孔隙,固化后会使最终的复材产品含有很多孔洞而产生产品缺陷;而对比实施例6和实施例7的树脂粘度适中,可以被玻纤布有效吸附,不会产生缺胶问题。树脂如果粘度过低,就不适合用于手糊、缠绕等工艺,因为会发生滴胶、缺胶等问题,这也是复材行业的共识,而对比实施例7也验证了这一点。)然后将其整体都放入80℃的烘箱,固化3小时。停止烘箱加热,使温度慢慢降至室温,再分别取出三块已经固化好的复材片材。经观察,基于对比实施例6树脂浸润玻纤布的片材质量不合格,因为发泡问题很严重,说明其水敏感性高;基于对比实施例7树脂浸润玻纤布的片材质量也不合格,因为其发泡问题虽然有所下降,但仍旧明显,说明对比实施例7中虽然在组分上进行调整,但仍然不能完全避免水敏感发泡问题;而基于实施例7树脂浸润玻纤布的片材质量好,均匀完整,没有发泡问题。实验结果列于表3。拉伸模量和拉伸强度为90°方向测得的模量和强度,主要反映的是树脂强度以及树脂和纤维界面的结合强度。The operation is carried out on glass plates: place four layers of uniaxial glass fiber cloth (Hengshi, E61200, UD, ~1200g/m2) on the upper surfaces of three glass plates sprayed with release agent respectively, at 25°C and 50% Place in a relative humidity environment for 24 hours for temperature and humidity balance. According to the components and proportions in Table 3, after preparing the three types of resins, slowly pour them on the upper surface of their respective glass fiber cloths, so that the liquid resins naturally penetrate into the glass fiber cloths from top to bottom, and wait for 6 minutes to fully absorb them. Soak the glass fiber, then cover the upper surface of the glass fiber cloth with a layer of transparent plastic film, and then use a hand lay-up roller to squeeze out all the air in the soaked glass fiber cloth. (During the actual operation, it was found that because the viscosity of the resin in Comparative Example 7 was too low, it was easy to flow, and the resin could not be effectively absorbed by the glass fiber cloth, resulting in resin loss and the lack of glue in the glass fiber cloth. The fiber cloth leaves a lot of pores, and after curing, the final composite product will contain many holes and cause product defects; while the resins in Comparative Example 6 and Example 7 have moderate viscosity and can be effectively absorbed by the glass fiber cloth without producing Lack of glue. If the viscosity of the resin is too low, it is not suitable for hand lay-up, winding and other processes, because problems such as dripping and lack of glue will occur. This is also the consensus of the composite material industry, and Comparative Example 7 also verifies this A little.) Then put the whole in an oven at 80°C and cure for 3 hours. Stop the oven heating, let the temperature drop to room temperature slowly, and then take out three cured composite sheets respectively. After observation, the sheet quality based on comparative example 6 resin-impregnated glass fiber cloth is unqualified, because the foaming problem is very serious, indicating that its water sensitivity is high; the sheet quality based on comparative example 7 resin-impregnated glass fiber cloth is not up to standard Qualified, because although its foaming problem has declined to some extent, it is still obvious, indicating that although the components are adjusted in Comparative Example 7, the water-sensitive foaming problem cannot be completely avoided; The sheets of cloth are of good quality, uniform and complete, and there is no foaming problem. The experimental results are listed in Table 3. The tensile modulus and tensile strength are the modulus and strength measured in the 90° direction, which mainly reflect the resin strength and the bonding strength of the resin and fiber interface.
表3table 3
Figure PCTCN2022104319-appb-000004
Figure PCTCN2022104319-appb-000004
从上表3所列对比实施例6、对比实施例7和实施例7的数据比较,说明反应性组分(B)的引入,可以使树脂的水敏感性显著降低,在50%的湿度下甚至都可以适用于手糊工艺制备复材产品。基于复材的力学性能测试也可以看出,对比实施例6和对比实施例7由于水敏感性高,导致片材含有很多气泡,所以显著降低了其片材的力学性能。通过综合比较对比实施例6、对比实施例7和实施例7,说明引入反应性组分(B)的热固聚氨酯树脂基体,其复材工艺可操作性能已经优于普通聚氨酯树脂和其它改性的聚氨酯,可以用于制备手糊产品。From the comparison of the data of comparative example 6, comparative example 7 and embodiment 7 listed in the above table 3, it is shown that the introduction of reactive component (B) can significantly reduce the water sensitivity of the resin, under 50% humidity It can even be applied to the hand lay-up process to prepare composite products. Based on the mechanical property test of the composite material, it can also be seen that due to the high water sensitivity of Comparative Example 6 and Comparative Example 7, the sheet contains many bubbles, which significantly reduces the mechanical properties of the sheet. Through a comprehensive comparison of Comparative Example 6, Comparative Example 7 and Example 7, it is shown that the thermosetting polyurethane resin matrix introduced with reactive component (B) has better operability in composite material technology than ordinary polyurethane resin and other modified Polyurethane can be used to prepare hand lay-up products.
实施例8Example 8
本实施例的聚氨酯复合材料分别基于表2中的对比实施例5和实施例6的聚氨酯树脂组合物,通过真空导入工艺制备复材产品,并测试其性质。(对比实施例8的复材使用对比实施例5的树脂;实施例8的复材使用实施例6的树脂)The polyurethane composite material of this example is based on the polyurethane resin compositions of Comparative Example 5 and Example 6 in Table 2, respectively, and the composite product is prepared through a vacuum introduction process, and its properties are tested. (the composite material of comparative example 8 uses the resin of comparative example 5; the composite material of embodiment 8 uses the resin of embodiment 6)
操作在玻璃平板上进行:将恒石单轴玻纤布(E61200,UD,~1200g/m2)放置在喷过脱模剂的玻璃平板上表面,再在上面依次放上脱模布、导流网和真空袋。这个装置的前部位置与真空相连,后部位置通过导流管接入液体树脂中。这些都设置好以后,将导流管的管子弯折堵住,再将整个装置放入加热到60℃的烘箱,并将连接真空的管子接通真空泵,在抽真空条件下加热除湿2个小时,以尽量除去玻纤和导流网等辅材上的湿气,然后再关掉烘箱加热,使整个设置在保持真空状态下自然降到室温。The operation is carried out on the glass plate: place the Hengshi uniaxial glass fiber cloth (E61200, UD, ~1200g/m2) on the upper surface of the glass plate sprayed with the release agent, and then put the release cloth and the flow guide on it in turn. Netting and vacuum bags. The front position of this device is connected to the vacuum, and the rear position is connected to the liquid resin through the guide tube. After all these are set up, bend and block the tube of the guide tube, then put the whole device into an oven heated to 60°C, connect the tube connected to the vacuum to the vacuum pump, and heat and dehumidify under vacuum for 2 hours , in order to remove the moisture on auxiliary materials such as glass fiber and guide net as much as possible, and then turn off the oven to heat, so that the whole device will naturally drop to room temperature while maintaining a vacuum state.
然后按照表2的配比,将异氰酸酯组分(A)、反应性组分(B)、自由基起始剂(C)和其它助剂混合,在真空条件下搅拌脱气6分钟后,立即将此树脂混合液体在真空条件下将其导入上述装置的玻纤布中。待玻纤布被全部浸润后,将导流管和连接真空的管子均弯折堵住,使整个被全部液态树脂浸润的体系仍继续保持在真空状态下;接着开始在1小时内逐步升温到80℃,再在80℃下保持2小时,通过高温加热促进树脂的固化,然后关掉加热,并自然降温至室温后,将已固化产品脱模,得到玻纤布增强的聚氨酯复合材料。所得聚氨酯复合材料的性能参数见表4。Then mix the isocyanate component (A), reactive component (B), free radical starter (C) and other additives according to the proportioning in Table 2, and stir and degas under vacuum for 6 minutes, immediately This resin mixed liquid is introduced into the glass fiber cloth of the above-mentioned device under vacuum condition. After the glass fiber cloth is fully soaked, bend the guide tube and the tube connected to the vacuum to block, so that the whole system soaked by all the liquid resin is still kept in a vacuum state; then start to gradually increase the temperature within 1 hour. 80°C, then keep at 80°C for 2 hours, accelerate the curing of the resin by heating at a high temperature, then turn off the heating, and cool down to room temperature naturally, then demould the cured product to obtain a polyurethane composite material reinforced with glass fiber cloth. The performance parameters of the obtained polyurethane composite materials are shown in Table 4.
本发明聚氨酯复合材料的性能如表4所示。表4所示的拉伸模量和拉伸强度为0°方向拉伸条件下测得的模量和强度。The properties of the polyurethane composite material of the present invention are shown in Table 4. The tensile modulus and tensile strength shown in Table 4 are the modulus and strength measured under the tensile condition of 0° direction.
表4Table 4
Figure PCTCN2022104319-appb-000005
Figure PCTCN2022104319-appb-000005
Figure PCTCN2022104319-appb-000006
Figure PCTCN2022104319-appb-000006
通过比较表4中所列对比实施例8与实施例8的力学性能,说明引入反应性组分(B)后的热固聚氨酯树脂基体制备的复合材料,其力学性能优于现有的普通聚氨酯树脂制备的复合材料。上述结果表明,这种含有反应性组分(B)的热固聚氨酯树脂基体适用于复材工艺,制备合格的复材产品。By comparing the mechanical properties of Comparative Example 8 and Example 8 listed in Table 4, it is shown that the composite material prepared by introducing the thermosetting polyurethane resin matrix after the reactive component (B) has better mechanical properties than the existing common polyurethane Composite materials made of resin. The above results show that the thermosetting polyurethane resin matrix containing the reactive component (B) is suitable for the composite material process and prepares qualified composite products.
实施例9和实施例10Example 9 and Example 10
为了进一步验证反应性组分(B)的引入有助于显著降低热固聚氨酯树脂组合物水敏感性并优于其它种类的改性聚氨酯树脂,我们对真空导入工艺做了一些调整。和实施例8相比,直接跳过了真空加热除湿的过程,以验证几种树脂对水汽敏感的程度。In order to further verify that the introduction of the reactive component (B) helps to significantly reduce the water sensitivity of the thermosetting polyurethane resin composition and is superior to other types of modified polyurethane resins, we made some adjustments to the vacuum introduction process. Compared with Example 8, the process of vacuum heating and dehumidification was directly skipped to verify the sensitivity of several resins to water vapor.
操作在玻璃平板上进行:将恒石单轴玻纤布(E61200,UD,~1200g/m2)放置在喷过脱模剂的玻璃平板上表面,再在上面依次放上脱模布、导流网和真空袋。这个装置的前部位置与真空相连,后部位置通过导流管接入液体树脂中。这些都设置好以后,将导流管的管子弯折堵住,再将连接真空的管子接通真空泵,使整个设置一直保持在真空状态下。The operation is carried out on the glass plate: place the Hengshi uniaxial glass fiber cloth (E61200, UD, ~1200g/m2) on the upper surface of the glass plate sprayed with the release agent, and then put the release cloth and the flow guide on it in turn. Netting and vacuum bags. The front position of this device is connected to the vacuum, and the rear position is connected to the liquid resin through the guide tube. After all these are set, the tube of the draft tube is bent and blocked, and then the tube connected to the vacuum is connected to the vacuum pump, so that the whole setup is kept in a vacuum state.
接着马上按照表5的配比,将异氰酸酯组分(A)、反应性组分(B)、自由基起始剂(C)和其它助剂混合,在真空条件下搅拌脱气6分钟。紧接着再将此树脂混合液体在真空条件下将其导入上述装置的玻纤布中。待玻纤布被全部浸润后,将导流管和连接真空的管子均弯折堵住,使整个被全部液态树脂浸润的体系仍继续保持在真空状态下;接着开始在1小时内逐步升温到80℃,再在80℃下保持2小时,通过高温加热促进树脂的固化,然后关掉加热。自然降到室温后,将已固化产品脱模,得到玻纤布增强的聚氨酯复合材料。可以观察到,对比实施例9的复材板仍有少量气泡,且玻纤有白丝现象;这是由于树脂对水汽敏感导致的。而实施例9和10却没有此类气泡和白丝现 象,说明相应的树脂在这种条件下已经有效克服了水敏感性的问题。具体结果和测试数据见下表5。拉伸模量和拉伸强度为90°方向测得的模量和强度。Then immediately mix the isocyanate component (A), reactive component (B), free radical initiator (C) and other additives according to the ratio in Table 5, and stir and degas under vacuum for 6 minutes. Next, the resin mixed liquid is introduced into the glass fiber cloth of the above-mentioned device under vacuum condition. After the glass fiber cloth is fully soaked, bend the guide tube and the tube connected to the vacuum to block, so that the whole system soaked by all the liquid resin is still kept in a vacuum state; then start to gradually increase the temperature within 1 hour. 80°C, then keep at 80°C for 2 hours, accelerate the curing of the resin by heating at high temperature, and then turn off the heat. After naturally cooling down to room temperature, the cured product is demolded to obtain a polyurethane composite material reinforced with glass fiber cloth. It can be observed that the composite board of Comparative Example 9 still has a small amount of bubbles, and the glass fiber has white silk phenomenon; this is caused by the resin being sensitive to water vapor. And embodiment 9 and 10 do not have this kind of bubble and white silk phenomenon, illustrate that corresponding resin has effectively overcome the problem of water sensitivity under this condition. The specific results and test data are shown in Table 5 below. Tensile modulus and tensile strength are the modulus and strength measured in the 90° direction.
表5table 5
Figure PCTCN2022104319-appb-000007
Figure PCTCN2022104319-appb-000007
通过综合比较表5中所列对比实施例9与实施例9、10的固化效果和力学性能数据,说明引入反应性组分(B)后的热固聚氨酯树脂,其水敏感性优于其它方式改进的聚氨酯树脂,且其力学性能也优于其它方式改进的聚氨酯树脂制备的复合材料。上述结果表明,这种含有反应性组分(B)的热固聚氨酯树脂基体适用于复材工艺,可用于制备合格的复材产品。By comprehensively comparing the curing effect and mechanical property data of Comparative Example 9 and Examples 9 and 10 listed in Table 5, it is shown that the water sensitivity of the thermosetting polyurethane resin after introducing the reactive component (B) is better than that of other methods Improved polyurethane resin, and its mechanical properties are also superior to composite materials prepared by other improved polyurethane resins. The above results show that this thermosetting polyurethane resin matrix containing reactive component (B) is suitable for the composite process and can be used to prepare qualified composite products.
虽然在上文中详细说明了本发明的实施方式,但是对于本领域的技术人员来说显而易见的是,能够对这些实施方式进行各种修改和变化。但是,应理解,这种修改和变化都属于权利要求书中所述的本发明的范围和精神之内。 而且,在此说明的本发明可有其它的实施方式,并且可通过多种方式实施或实现。Although the embodiments of the present invention have been described in detail above, it will be apparent to those skilled in the art that various modifications and changes can be made to the embodiments. However, it should be understood that such modifications and changes are within the scope and spirit of the present invention described in the claims. Furthermore, the invention described herein is capable of other embodiments and of being practiced or carried out in various ways.

Claims (17)

  1. 一种树脂组合物,其特征在于,包含异氰酸酯组分、反应性组分和自由基起始剂;A resin composition, characterized in that, comprising an isocyanate component, a reactive component and a free radical initiator;
    所述异氰酸酯组分包含至少一种有机异氰酸酯;The isocyanate component comprises at least one organic isocyanate;
    所述反应性组分中:Among the reactive components:
    平均每个分子包含至少一个丙烯酸酯类双键,以在所述自由基起始剂的作用下发生自由基聚合反应,所述丙烯酸酯类双键为丙烯酸基团上的双键或甲基丙烯酸基团上的双键;On average, each molecule contains at least one acrylate double bond, which is a double bond on an acrylic group or a methacrylic acid group, for free-radical polymerization to occur under the action of said free-radical initiator the double bond on the group;
    平均每个分子包含至少一个活性氢,以与所述至少一种有机异氰酸酯发生加成聚合反应;comprising on average at least one active hydrogen per molecule for addition polymerization with said at least one organic isocyanate;
    平均每个分子所含有的丙烯酸酯类双键和活性氢的数目之和不少于2.1。The average sum of the number of acrylate double bonds and active hydrogen contained in each molecule is not less than 2.1.
  2. 根据权利要求1所述的树脂组合物,其特征在于,所述反应性组分的平均每个分子包含1-4个丙烯酸酯类基团,每个所述丙烯酸酯类基团包含所述丙烯酸酯类双键。The resin composition according to claim 1, wherein the reactive component comprises 1-4 acrylate groups per molecule on average, and each of the acrylate groups comprises the acrylic acid ester double bond.
  3. 根据权利要求1所述的树脂组合物,其特征在于,所述反应性组分的平均每个分子包含1.1-4.9个羟基,每个所述羟基包含所述活性氢。The resin composition according to claim 1, wherein the reactive component contains 1.1-4.9 hydroxyl groups on average per molecule, and each of the hydroxyl groups contains the active hydrogen.
  4. 根据权利要求1所述的树脂组合物,其特征在于,所述反应性组分包含至少一种有机多元醇与丙烯酸类物质通过酯化反应得到的酯类产物,所述至少一种有机多元醇的平均每个分子具有至少2.1个所述活性氢。The resin composition according to claim 1, wherein the reactive component comprises an ester product obtained by esterification reaction of at least one organic polyol and an acrylic substance, and the at least one organic polyol has an average of at least 2.1 of said active hydrogens per molecule.
  5. 根据权利要求4所述的树脂组合物,其特征在于,所述至少一种有机多元醇包含至少一种聚醚多元醇,所述聚醚多元醇包含所述活性氢。The resin composition according to claim 4, wherein said at least one organic polyol comprises at least one polyether polyol comprising said active hydrogen.
  6. 根据权利要求5所述的树脂组合物,其特征在于,所述至少一种聚醚多元醇的平均官能度为2.1-6,羟值为25-1100毫克氢氧化钾/克。The resin composition according to claim 5, characterized in that, the average functionality of the at least one polyether polyol is 2.1-6, and the hydroxyl value is 25-1100 mg potassium hydroxide/g.
  7. 根据权利要求1所述的树脂组合物,其特征在于,以占所述反应性组 分的质量百分比计,所述自由基起始剂的含量为0.01%-7%。The resin composition according to claim 1, characterized in that, based on the mass percentage of the reactive components, the content of the free radical initiator is 0.01%-7%.
  8. 根据权利要求1所述的树脂组合物,其特征在于,还包含催化剂,以加速生成氨基甲酸酯类基团的交联反应,以占所述反应性组分的质量百分比计,所述催化剂的含量大于0并小于等于5%,所述氨基甲酸酯类基团由所述活性氢与所述至少一种有机异氰酸酯发生所述加成聚合反应得到。Resin composition according to claim 1, is characterized in that, also comprises catalyst, to accelerate the cross-linking reaction that generates carbamate group, accounts for the mass percent of described reactive component, and the mass percent of described catalyst The content is greater than 0 and less than or equal to 5%, and the urethane group is obtained by the addition polymerization reaction of the active hydrogen and the at least one organic isocyanate.
  9. 根据权利要求1所述的树脂组合物,其特征在于,还包含若干助剂,以利于调控通过所述树脂组合物所制备的聚氨酯材料的理化性能。The resin composition according to claim 1, characterized in that, it also comprises several auxiliary agents to facilitate the regulation and control of the physical and chemical properties of the polyurethane material prepared by the resin composition.
  10. 根据权利要求1所述的树脂组合物,其特征在于,所述至少一种有机异氰酸酯的平均官能度为2.0-3.6。The resin composition according to claim 1, wherein the average functionality of the at least one organic isocyanate is 2.0-3.6.
  11. 根据权利要求1所述的树脂组合物,其特征在于,所述至少一种有机异氰酸酯在25℃下根据DIN 53019-1-3测定的粘度为4-2500毫帕斯卡.秒。The resin composition according to claim 1, characterized in that the at least one organic isocyanate has a viscosity of 4-2500 mPa.s at 25° C. as measured according to DIN 53019-1-3.
  12. 一种聚氨酯材料,其特征在于,包含聚氨酯基体,所述聚氨酯基体由权利要求1-11任一项所述的树脂组合物制备而成。A polyurethane material, characterized in that it comprises a polyurethane matrix prepared from the resin composition according to any one of claims 1-11.
  13. 一种聚氨酯材料制备方法,其特征在于,包括:A method for preparing a polyurethane material, characterized in that it comprises:
    提供如权利要求1-11任一项所述的树脂组合物,所述树脂组合物包含反应性组分、自由基起始剂以及至少一种有机异氰酸酯,所述反应性组分的平均每个分子包含至少一个丙烯酸酯类双键以及至少一个活性氢;Resin composition as described in any one of claim 1-11 is provided, and described resin composition comprises reactive component, radical initiator and at least one organic isocyanate, and the average of each of described reactive component The molecule contains at least one acrylate double bond and at least one active hydrogen;
    通过所述自由基起始剂引发所述至少一个丙烯酸酯类双键的自由基聚合反应,所述至少一个活性氢与所述至少一种有机异氰酸酯发生加成聚合反应。The free radical polymerization reaction of the at least one acrylate double bond is initiated by the free radical initiator, and the at least one active hydrogen undergoes an addition polymerization reaction with the at least one organic isocyanate.
  14. 根据权利要求13所述的聚氨酯材料制备方法,其特征在于,所述树脂组合物还包括催化剂,控制所述催化剂占所述反应性组分的质量百分比大于0并小于等于5%,以加速由所述活性氢与所述至少一种有机异氰酸酯发生所述加成聚合反应得到的氨基甲酸酯类基团的交联反应。The method for preparing a polyurethane material according to claim 13, wherein the resin composition further comprises a catalyst, and the mass percentage of the catalyst in the reactive component is controlled to be greater than 0 and less than or equal to 5%, so as to accelerate the process by The active hydrogen reacts with the at least one organic isocyanate to undergo a cross-linking reaction of urethane groups obtained by the addition polymerization reaction.
  15. 一种聚氨酯复合材料,其特征在于,包含增强材料和权利要求12所述的聚氨酯材料。A polyurethane composite material, characterized in that it comprises a reinforcing material and the polyurethane material according to claim 12.
  16. 根据权利要求15所述的聚氨酯复合材料,其特征在于,所述增强材料占所述聚氨酯复合材料的质量百分比为1-91%。The polyurethane composite material according to claim 15, characterized in that the reinforcing material accounts for 1-91% by mass of the polyurethane composite material.
  17. 一种聚氨酯复合材料制备方法,其特征在于,以增强材料和权利要求12所述的聚氨酯材料为原料,通过真空导入工艺、拉挤成型工艺、缠绕成型工艺、树脂传递工艺、手糊成型工艺、模压成型工艺和喷射成型工艺的至少一种制备而成。A method for preparing a polyurethane composite material, characterized in that, using the reinforcing material and the polyurethane material described in claim 12 as raw materials, through a vacuum introduction process, a pultrusion process, a winding process, a resin transfer process, a hand lay-up process, It is prepared by at least one of a compression molding process and an injection molding process.
PCT/CN2022/104319 2021-07-15 2022-07-07 Resin composition, polyurethane material, polyurethane composite material, and preparation methods WO2023284618A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN202110800947.0 2021-07-15
CN202110800947.0A CN115612041A (en) 2021-07-15 2021-07-15 Resin composition, polyurethane material, polyurethane composite material and preparation method

Publications (1)

Publication Number Publication Date
WO2023284618A1 true WO2023284618A1 (en) 2023-01-19

Family

ID=84855953

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2022/104319 WO2023284618A1 (en) 2021-07-15 2022-07-07 Resin composition, polyurethane material, polyurethane composite material, and preparation methods

Country Status (2)

Country Link
CN (1) CN115612041A (en)
WO (1) WO2023284618A1 (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102585157A (en) * 2012-03-13 2012-07-18 广东深展实业有限公司 Ultraviolet light polymerization polyfunctionality polyurethane acrylate vacuum coating surface coating resin
CN105859585A (en) * 2016-04-15 2016-08-17 江苏利田科技股份有限公司 Tri-functionality urethane acrylate based on glycerin and preparation method and application of tri-functionality urethane acrylate
CN105859587A (en) * 2016-04-15 2016-08-17 江苏利田科技股份有限公司 Tetra-functionality urethane acrylate based on pentaerythritol and preparation method and application tetra-functionality urethane acrylate
CN105859584A (en) * 2016-04-15 2016-08-17 江苏利田科技股份有限公司 Tri-functionality urethane acrylate based on trimethylolethane/trimethylolpropane and preparation method and application of tri-functionality urethane acrylate
US20180250434A1 (en) * 2016-03-02 2018-09-06 The Board Of Trustees Of The Leland Stanford Junior University Bone-tendon graft biomaterial, use as a medical device and method of making same

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102585157A (en) * 2012-03-13 2012-07-18 广东深展实业有限公司 Ultraviolet light polymerization polyfunctionality polyurethane acrylate vacuum coating surface coating resin
US20180250434A1 (en) * 2016-03-02 2018-09-06 The Board Of Trustees Of The Leland Stanford Junior University Bone-tendon graft biomaterial, use as a medical device and method of making same
CN105859585A (en) * 2016-04-15 2016-08-17 江苏利田科技股份有限公司 Tri-functionality urethane acrylate based on glycerin and preparation method and application of tri-functionality urethane acrylate
CN105859587A (en) * 2016-04-15 2016-08-17 江苏利田科技股份有限公司 Tetra-functionality urethane acrylate based on pentaerythritol and preparation method and application tetra-functionality urethane acrylate
CN105859584A (en) * 2016-04-15 2016-08-17 江苏利田科技股份有限公司 Tri-functionality urethane acrylate based on trimethylolethane/trimethylolpropane and preparation method and application of tri-functionality urethane acrylate

Also Published As

Publication number Publication date
CN115612041A (en) 2023-01-17

Similar Documents

Publication Publication Date Title
US10683403B2 (en) Polyurethane composite material and process of preparing same
US11667824B2 (en) Adhesive and its preparation and application
CN105778005B (en) Free-radically polymerizable polyurethane composition
EP1591491B1 (en) A urethane acrylate composite structure
US9181380B2 (en) Thermosetting resin composition
CN101049747A (en) Composite parts comprising sprayed polyurethaneureas
JP2019510848A (en) Curable urethane acrylate composition
CN102432805A (en) Photo-curable polyurethane acrylate vinyl/propenyl ether heterozygous pre-polymer and preparation method thereof
JP5336730B2 (en) Adhesive structure bonded using radical polymerizable adhesive for fiber reinforced plastic and method for producing the same
CN111748073A (en) Method for preparing polyurethane pultrusion composite material
WO2023030454A1 (en) Thermosetting resin composition, and epoxy resin material, composite material thereof, and preparation method therefor
CN115768809A (en) Polyurethane composition for producing composite materials
CN113527628B (en) Thermosetting polyurethane acrylic resin and application thereof
WO2023284618A1 (en) Resin composition, polyurethane material, polyurethane composite material, and preparation methods
JPH08259643A (en) Resin composition, construction and building material and coating material
CN111825822A (en) Method for storing isocyanate reactive component
EP3549670A1 (en) Manufacturing method for a polyurethane-poly(meth)acrylate resin
US20220184901A1 (en) Method for preparing a pultruded polyurethane composite
EP3733729A1 (en) Method for preparing a pultruded polyurethane composite
CN114437310B (en) Modified polyurethane composition and application thereof
EP4021714A1 (en) Method for producing a spar cap, trailing edge and/or other reinforced laminate structural parts of wind turbine blade
CN101649176A (en) Unsaturated aliphatic polyester type polyurethane adhesive
CN114316188B (en) Phenolic resin modified polyurethane and composite board thereof
CN113563789B (en) Moisture-curing hot-melt paint for wood veneers and preparation method thereof
CN114507330B (en) Polyurethane composition

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 22841255

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE