CN114045102A - Fuel steam isolation coating for carrying traffic fuel tank and preparation method thereof - Google Patents
Fuel steam isolation coating for carrying traffic fuel tank and preparation method thereof Download PDFInfo
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- CN114045102A CN114045102A CN202111216865.8A CN202111216865A CN114045102A CN 114045102 A CN114045102 A CN 114045102A CN 202111216865 A CN202111216865 A CN 202111216865A CN 114045102 A CN114045102 A CN 114045102A
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D175/00—Coating compositions based on polyureas or polyurethanes; Coating compositions based on derivatives of such polymers
- C09D175/04—Polyurethanes
- C09D175/08—Polyurethanes from polyethers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/4009—Two or more macromolecular compounds not provided for in one single group of groups C08G18/42 - C08G18/64
- C08G18/4045—Mixtures of compounds of group C08G18/58 with other macromolecular compounds
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/48—Polyethers
- C08G18/4804—Two or more polyethers of different physical or chemical nature
- C08G18/4812—Mixtures of polyetherdiols with polyetherpolyols having at least three hydroxy groups
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/58—Epoxy resins
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D5/00—Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes
- C09D5/08—Anti-corrosive paints
Abstract
The invention mainly aims at the air tightness requirement of a fuel vapor of a carrying traffic fuel tank, develops a fuel vapor isolation coating with excellent comprehensive performance, can adapt to harsh working conditions and multiphase corrosion environment of the fuel tank, and provides a lasting protection and isolation effect. The fuel steam isolation coating is composed of a component A and a component B. The component A consists of polyurethane modified epoxy resin, a wetting agent, a flatting agent, a defoaming agent and a diluent, wherein the polyurethane modified epoxy resin is self-made and is prepared from polyether polyol, epoxy resin, polyisocyanate, epoxy propanol, a catalyst and a mixed solvent through a specific synthesis process; the component B consists of polyether amine resin, polyamide resin and diluent.
Description
Technical Field
The invention relates to a coating, in particular to a fuel steam isolation coating with excellent comprehensive performance and a preparation method thereof, and belongs to the field of materials.
Background
With the rapid development of economy in China, the carrying traffic industry is also rapidly developed. Airplanes, automobiles, and the like have become indispensable vehicles in human life. The oil tank is used as a main component for carrying traffic, and the oil storage capacity of the oil tank determines the cruising ability and is increasingly concerned. It is known that the assembly gap of the carrying traffic fuel tank prevents the leakage of fuel by an oil-resistant sealant or the like. However, after a long service time, the oil-resistant sealant is often aged, and the oil tank structure is greatly deformed under the frequent vibration impact environment in the driving process of the vehicle, so that the original sealing system has fine defects. In addition, vehicles are usually exposed outdoors for a long time, the fuel temperature is high under the conditions of sunshine and the like, a large amount of fuel vapor can be generated inside the fuel tank, and the fuel vapor and the fuel have strong permeability and can be diffused to adjacent structures through fine defects in the oil-resistant sealant. Fuel vapor and fuel oil can be accumulated into oil drops when penetrating into the closed structure, so that potential safety hazards of vehicles are caused, if leakage happens carelessly, on one hand, fire disasters are easy to cause, and on the other hand, the comfort of members is adversely affected.
According to the relevant data show, some aircraft tank structures are the component part of gas-tight cabin, when taking place the fuel infiltration, oil droplet, fuel steam can directly get into in the gas-tight cabin, and outside parcel has multiple sheltering from such as heat insulation layer, decorative board, can't observe oil seepage situation, easily takes place the oil leak accumulation, is difficult to clear away the fuel of seepage simultaneously, consequently can only reduce to break down through strengthening the measure of preventing fuel infiltration. The oil-resistant sealant has low bonding strength, cannot effectively isolate fuel vapor permeation on the outer side, and cannot meet the use requirement. Therefore, the fuel steam isolation coating with excellent comprehensive performance is developed and used for carrying structural members such as an external traffic oil tank and the like, the fuel steam permeation is prevented, and the fuel steam isolation coating has very important influence on the improvement of safety, stability and member comfort.
Because of the objective factors of higher development difficulty, small dosage and the like, the product varieties and specifications of the existing fuel steam isolation coating are less, no manufacturers develop and produce the coating at home, the used products depend on the import at home and abroad, the comprehensive performance cannot completely meet the practical application due to the small dosage of the fuel steam isolation coating, the condition of fuel leakage still exists, the test method and the important technical indexes for checking the fuel steam permeation are not given in various domestic and foreign standard specifications, and the key technical indexes and the test method of the coating need to be explored and researched by themselves. This poses certain difficulties for the development of such coatings.
Disclosure of Invention
The purpose of the invention is as follows: aiming at the problems that the oil vapor leakage and diffusion are caused by the aging of the oil-resistant sealing agent in the assembly gap after the oil tank of the transportation vehicle is used for a period of time and the fine defect is generated in the original sealing system due to the large deformation of the oil tank structure under the frequent vibration and strong impact, so that the multi-aspect potential safety hazard is easily caused, the fuel vapor isolation coating with excellent comprehensive performance is developed, the relevant theoretical basis and key technology are mastered, the corresponding technical difficulty is broken through, the functional research of the fuel vapor isolation coating is completed, and the mass and stable production supply capacity is formed.
The invention mainly aims at the air tightness requirement of a fuel vapor of a carrying traffic fuel tank, carries out professional technical research, develops a fuel vapor isolation coating with excellent comprehensive performance, can adapt to harsh working conditions and multiphase corrosion environment of the fuel tank, and provides a lasting protection and isolation effect.
The fuel steam isolation coating is composed of a component A and a component B. The component A consists of polyurethane modified epoxy resin, a wetting agent, a flatting agent, a defoaming agent and a diluent, wherein the polyurethane modified epoxy resin is self-made and is prepared from polyether polyol, epoxy resin, polyisocyanate, epoxy propanol, a catalyst and a mixed solvent through a specific synthesis process; the component B consists of polyether amine resin, polyamide resin and diluent.
The formula of the polyurethane modified epoxy resin contained in the fuel steam isolation coating A component comprises the following components in percentage by mass:
the formula of the fuel steam isolation coating A component comprises the following components in percentage by mass:
the polyether polyol is a mixture of at least one difunctional polyether polyol and at least one trifunctional polyether polyol in a certain proportion. The amount of the difunctional polyether polyol is not less than 75% of the total amount calculated by the molar amount.
The epoxy resin is bisphenol A epoxy resin, the middle of a chain segment at least contains more than two hydroxyl active groups, the molecular weight is less than or equal to 1000, and the structural formula is as follows:
the polyisocyanate is one or a mixture of more than two of polyisocyanate compounds containing two or more NCO active groups.
The catalyst is any one of dibutyltin dilaurate, stannous octoate and metal naphthenate in a metal salt catalyst.
The mixed solvent is one or a mixture of more than two of ether ester solvents, ketone solvents and ester solvents.
The wetting agent is at least one of polyether modified polydimethylsiloxane and polyester modified polydimethylsiloxane.
The leveling agent is at least one of polyacrylate solution and polyether modified polymethyl alkyl siloxane.
The defoaming agent is at least one of foam-breaking polysiloxane, foam-breaking polymer and polysiloxane.
The diluent is one or a mixture of more than two of ether ester solvents, ketone solvents and ester solvents.
The formula of the fuel steam isolation coating B comprises the following components in percentage by mass:
30 to 47 percent of polyether amine resin
35 to 52 percent of polyamide resin
15 to 23 percent of diluent
The polyether amine is one or a mixture of more than two of bifunctional polyether amine and trifunctional polyether amine.
The polyamide is one or a mixture of more than two of 100mg KOH/g to 400mg KOH/g of active hydrogen equivalent.
The diluent is one or a mixture of more than two of ether alcohol solvents, ether ester solvents, benzene solvents, ketone solvents and ester solvents.
The preparation method of the fuel steam isolation coating of the invention prepares materials according to the formula, and the preparation process of the component A comprises the following steps:
adding stoichiometric polyether polyol into a reaction kettle for dehydration treatment, adding a certain amount of epoxy resin to increase the cross-linking point of a polymer, adding theoretical stoichiometric polyisocyanate into the reaction kettle, adding a proper amount of catalyst, and reacting at 60-80 ℃ for 5 hours to obtain the isocyanate-terminated polyurethane prepolymer.
Adding the polyurethane prepolymer and epoxy propanol into a reaction kettle according to a metering ratio under the condition of normal temperature, fully stirring, after one hour, raising the reaction temperature to 80-90 ℃ after the system temperature is stable, and reacting at constant temperature until no isocyanate group (-NCO) is actually measured, thereby obtaining the self-made polyurethane modified epoxy resin.
And (3) sequentially adding a wetting agent, a flatting agent, a defoaming agent and a mixed solvent into the self-made polyurethane modified epoxy resin solution under the stirring state, uniformly stirring at a high speed, filtering and discharging to obtain the component A.
The preparation method of the fuel steam isolation coating of the invention prepares materials according to the formula, and the preparation process of the component B comprises the following steps:
and mixing the polyether amine, the polyamide and the mixed solvent under the stirring state, uniformly stirring and filtering to obtain the component B.
According to the preparation process of the components A and B, the components A and B are weighed and uniformly mixed according to the mass ratio of 10:1 according to related calculation, and a proper amount of diluent is added to adjust the mixture to reach the construction viscosity, so that the finished paint is obtained.
The key points of the technology of the invention are as follows: synthesizing fuel steam insulating paint A component resin and preparing fuel steam insulating paint B component. The coating is particularly characterized in that the type and the proportion of the resin are mixed, so that the coating can adapt to the harsh working condition and multiphase corrosion environment of an oil tank and provide a lasting protection and isolation effect.
The invention relates to a preparation method of a fuel steam insulating coating. The method has the following beneficial effects:
(1) after the fuel steam barrier coating is formed into a film, the film has good adhesive force and high crosslinking degree so as to form a compact low-permeability paint film, and simultaneously, the flexibility of the coating is also considered, so that the problem that the paint film has insufficient flexibility due to overlarge internal stress of a high-crosslinking system is solved.
The polyurethane-epoxy resin graft copolymerization method is adopted, firstly, polyhydroxy compound and polyisocyanate are polymerized into polyurethane prepolymer, and the polyurethane prepolymer is terminated by epoxy propanol to obtain polyurethane modified epoxy resin, wherein the epoxy resin has the characteristics of high solid content and low viscosity, integrates the advantages of the epoxy resin and the polyurethane resin, has higher crosslinking degree, and greatly enhances the adhesion and bonding performance of the system; excellent tensile strength and extremely high elongation at break are also ensured.
(2) The selected base resin should have a durable corrosion resistance to ensure that the coating has excellent resistance to strong corrosive media such as fuel oil, fuel vapor and salt water and excellent shielding effect.
Polyether polyol and polyester polyol are two types of raw materials commonly used for preparing elastic polyurethane, and the prepared polyurethane has outstanding characteristics in the aspects of low temperature resistance, flexibility, water resistance and damp-heat resistance due to the action of ether bonds in the polyether polyol. The method selects difunctional/trifunctional polyether polyol to compound, and then prepares polyurethane prepolymer with isocyanate. The prepolymer has high branching degree, more active sites, compact structure after reaction with a curing agent, good water resistance of a coating and excellent oil resistance.
In addition, the molecular chain segment of the hydroxyl epoxy resin contains active secondary hydroxyl, a small amount of hydroxyl epoxy resin can be introduced to further improve active crosslinking points in a resin structure when the polyurethane prepolymer is prepared, and-NCO groups in isocyanate react with-OH groups of the epoxy resin to generate strongly polar urethane bonds (-NHCOO-) which are bonded with a base material to form a rigid structure, so that the heat stability of the coating is improved, the resistance of the coating to a hot corrosion medium is enhanced, the cured coating has excellent chemical resistance, and the coating has excellent corrosion resistance to salt solutions and oils.
(3) The prepared fuel steam isolation coating has the characteristics of high solid content and low viscosity, and ensures that the comprehensive performance of the coating is not influenced by the construction process.
Polyisocyanates have excellent chemical resistance, variability in the-NCO active sites, and are a common monomer for the synthesis of isocyanate prepolymers. By utilizing the activity difference of active sites, particularly under the use of a proper catalyst, the reaction activity difference is increased, the selectivity is high, the reaction temperature can be selected to be lower, the prepolymer with narrow molecular weight distribution is easy to manufacture, and good reproducibility is shown; the generated resin has uniform relative molecular mass distribution and good stability, and is beneficial to preparing high-solid low-viscosity products. In the synthesis process, by controlling the proportion, introducing epoxypropanol and other operations, the epoxy group is introduced into the system, the active sites are increased, the branching degree of the system is improved, and the coating has more excellent adhesion and medium resistance. The glycidol is a monomer with double functional groups, and as the glycidol molecule contains two functional groups of epoxy group and hydroxyl group, the glycidol is used for blocking isocyanate to obtain polyurethane modified epoxy resin, and is an important component in preparing the polyurethane modified epoxy resin.
Detailed Description
This example demonstrates the preparation of a fuel vapor barrier coating for a fuel tank of a transportation vehicle.
The first embodiment is as follows:
(1) preparing a fuel steam isolation coating component A for a carrying traffic oil tank: under the stirring state, 0.5kg of wetting agent BYK-330, 0.5kg of flatting agent BYK-320, 0.4kg of defoaming agent BYK-066N and 11.6kg of diluent (xylene: cyclohexanone: butanone: 2:1:1) are sequentially added into 87kg of self-made polyurethane modified epoxy resin solution, the mixture is stirred at a high speed and dispersed uniformly, and the component A is obtained after filtering and discharging.
The preparation method of the self-made polyurethane modified epoxy resin comprises the following steps: adding 18kg of difunctional polyether polyol D210 and 12kg of trifunctional polyether polyol G303 into a reaction kettle for dehydration, adding 14.6kg of epoxy resin E-44 to increase the cross-linking point of the polymer, fully and uniformly stirring, adding 24.6kg of polyisocyanate IPDI into the reaction kettle, adding 0.7kg of catalyst dibutyltin dilaurate, and reacting at 60-80 ℃ for 5 hours to obtain the isocyanate-terminated polyurethane prepolymer. And after the temperature is reduced to the normal temperature, putting 17.7kg of epoxy propanol into a reaction kettle, adding 12.4kg of mixed solvent (xylene: cyclohexanone: butanone: 2:1:1), fully stirring, after one hour, raising the reaction temperature to 80-90 ℃ after the system temperature is stable, and reacting at constant temperature until no isocyanate group (-NCO) is actually measured, thereby obtaining the self-made polyurethane modified epoxy resin.
(2) Preparing a fuel steam isolation coating component B for a carrying traffic oil tank: adding 45kg of polyetheramine SD-2001, 42kg of polyamide 300# and 13kg of diluent (xylene: cyclohexanone: butanone: 2:1:1) into a pulling cylinder under a stirring state, uniformly mixing, stirring for 25 minutes, and filtering and discharging to obtain a component B.
Example two:
(1) preparing a fuel steam isolation coating component A for a carrying traffic oil tank: 0.6kg of wetting agent BYK-310, 0.6kg of flatting agent BYK-358N, 0.5kg of defoaming agent BYK-A530 and 8.3kg of diluent (xylene: cyclohexanone: butanone: 2:1:1) are sequentially added into 90kg of self-made polyurethane modified epoxy resin solution under the stirring state, the mixture is stirred at a high speed and dispersed uniformly, and the component A is obtained after filtering and discharging.
The preparation method of the self-made polyurethane modified epoxy resin comprises the following steps: adding 15kg of difunctional polyether polyol D210 and 15kg of trifunctional polyether polyol G303 into a reaction kettle for dehydration, adding 13.8kg of epoxy resin E-44 to increase the cross-linking point of the polymer, fully and uniformly stirring, adding 25.2kg of polyisocyanate IPDI into the reaction kettle, adding 0.7kg of catalyst dibutyltin dilaurate, and reacting at 60-80 ℃ for 5 hours to obtain the isocyanate-terminated polyurethane prepolymer. And after the temperature is reduced to the normal temperature, 16.7kg of epoxy propanol is put into a reaction kettle, 13.6kg of mixed solvent (xylene: cyclohexanone: butanone: 2:1:1) is added and fully stirred, after one hour, the reaction temperature is increased to 80-90 ℃ after the system temperature is stable, and the reaction is carried out at constant temperature until no isocyanate group (-NCO) is actually measured, so that the self-made polyurethane modified epoxy resin is obtained.
(2) Preparing a fuel steam isolation coating component B for a carrying traffic oil tank: adding 38.6kg of polyetheramine SD-2001, 51.4kg of polyamide 300# and 10kg of diluent (xylene: cyclohexanone: butanone: 2:1:1) into a drawn cylinder under the stirring state, uniformly mixing, stirring for 25 minutes, and filtering and discharging to obtain a component B.
Example three:
(1) preparing a fuel steam isolation coating component A for a carrying traffic oil tank: 0.7kg of wetting agent BYK-330, 0.7kg of flatting agent BYK-358N, 0.4kg of defoaming agent BYK-066N and 8.2kg of diluent (xylene: cyclohexanone: butanone 2:1:1) are sequentially added into 90kg of self-made polyurethane modified epoxy resin solution under the stirring state, the mixture is stirred at a high speed and dispersed uniformly, and the component A is obtained after filtering and discharging.
The preparation method of the self-made polyurethane modified epoxy resin comprises the following steps: adding 24kg of difunctional polyether polyol D204 and 6kg of trifunctional polyether polyol G4030 into a reaction kettle for dehydration, adding 15kg of epoxy resin E-44 to increase the crosslinking point of the polymer, fully and uniformly stirring, adding 23.4kg of polyisocyanate IPDI into the reaction kettle, adding 0.9kg of catalyst dibutyltin dilaurate, and reacting at 60-80 ℃ for 5 hours to obtain the isocyanate-terminated polyurethane prepolymer. And after the temperature is reduced to the normal temperature, 18.3kg of epoxy propanol is put into a reaction kettle, 12.4kg of mixed solvent (xylene: cyclohexanone: butanone: 2:1:1) is added and fully stirred, after one hour, the reaction temperature is increased to 80-90 ℃ after the system temperature is stable, and the reaction is carried out at constant temperature until no isocyanate group (-NCO) is actually measured, so that the self-made polyurethane modified epoxy resin is obtained.
(2) Preparing a fuel steam isolation coating component B for a carrying traffic oil tank: adding 46.5kg of polyetheramine SD-2001, 38.2kg of polyamide 300# and 15.3kg of diluent (xylene: cyclohexanone: butanone: 2:1:1) into a drawn cylinder under a stirring state, uniformly mixing, stirring for 25 minutes, and filtering and discharging to obtain a component B.
Effects of the implementation
The performance of the fuel vapor barrier coatings of examples 1-3 were tested and the results were as follows:
Claims (10)
1. a fuel steam insulating paint is characterized in that,
the formula of the fuel steam isolation coating A component comprises the following components in percentage by mass:
the formula of the fuel steam isolation coating B comprises the following components in percentage by mass:
30 to 47 percent of polyether amine resin
35 to 52 percent of polyamide resin
15 to 23 percent of diluent.
3. the fuel vapor barrier coating of claim 1 wherein the polyether polyol is a mixture of at least one difunctional polyether polyol and at least one trifunctional polyether polyol in proportions such that the amount of difunctional polyether polyol is not less than 75% by mole of the total.
4. The fuel vapor barrier coating of claim 1, wherein the epoxy resin is bisphenol a epoxy resin, and the middle of the chain segment contains at least one of more than two hydroxyl active groups and the molecular weight is less than or equal to 1000.
5. The fuel steam isolating paint as set forth in claim 1, wherein the wetting agent is at least one of polyether modified polydimethylsiloxane and polyester modified polydimethylsiloxane, the leveling agent is at least one of polyacrylate solution and polyether modified polymethylalkylsiloxane, the defoaming agent is at least one of defoaming polysiloxane, defoaming polymer and polysiloxane, and the diluent is one or a mixture of more than two of ether ester solvents, ketone solvents and ester solvents.
6. The fuel vapor barrier coating according to claim 2, wherein the polyisocyanate is one or a mixture of two or more of polyisocyanate compounds containing two or more NCO reactive groups, and the mixed solvent is one or a mixture of two or more of ether ester solvents, ketone solvents and ester solvents.
7. The fuel steam isolation coating as claimed in claim 1, wherein the polyetheramine is one or a mixture of two or more of bifunctional polyetheramine and trifunctional polyetheramine, the polyamide is one or a mixture of two or more of active hydrogen equivalent weight of 100mg KOH/g-400 mg KOH/g, and the diluent is one or a mixture of two or more of ether alcohol solvent, ether ester solvent, benzene solvent, ketone solvent and ester solvent.
8. The fuel steam isolation coating as claimed in claim 2, wherein the polyurethane modified epoxy resin is prepared by adding stoichiometric polyether polyol into a reaction kettle for dehydration treatment, adding a certain amount of epoxy resin to increase the cross-linking point of the polymer, adding stoichiometric polyisocyanate into the reaction kettle, adding a proper amount of catalyst, reacting at 60-80 ℃ for 5 hours to obtain isocyanate group-terminated polyurethane prepolymer, adding the polyurethane prepolymer and epoxypropanol into the reaction kettle according to a stoichiometric ratio under normal temperature conditions, fully stirring, after one hour, raising the reaction temperature to 80-90 ℃ after the system temperature is stable, and reacting at constant temperature until no isocyanate group (-NCO) is actually measured to obtain the polyurethane modified epoxy resin.
9. The fuel steam isolating paint as set forth in claim 1, wherein the component A is prepared through adding wetting agent, leveling agent, defoaming agent and mixed solvent successively into the modified polyurethane epoxy resin solution while stirring, high speed stirring, filtering and discharging.
10. The fuel steam barrier coating of claim 1, wherein the component b is prepared by mixing the polyetheramine, the polyamide and the mixed solvent under stirring, stirring uniformly, and filtering to obtain the component b.
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CN114644746A (en) * | 2022-04-21 | 2022-06-21 | 韶关东森合成材料有限公司 | Polyurethane modified epoxy resin and preparation method and application thereof |
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