CN115286655A - Bio-based epoxy resin suitable for wet-process winding carbon fiber hydrogen storage bottle and preparation method thereof - Google Patents

Bio-based epoxy resin suitable for wet-process winding carbon fiber hydrogen storage bottle and preparation method thereof Download PDF

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CN115286655A
CN115286655A CN202210915119.6A CN202210915119A CN115286655A CN 115286655 A CN115286655 A CN 115286655A CN 202210915119 A CN202210915119 A CN 202210915119A CN 115286655 A CN115286655 A CN 115286655A
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epoxy resin
bio
based epoxy
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wet
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尚垒
陈雪
敖玉辉
郑勇
朱承双
张春红
何嘉欢
陈艺静
刘浩
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Changchun University of Technology
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    • C07F7/00Compounds containing elements of Groups 4 or 14 of the Periodic Table
    • C07F7/02Silicon compounds
    • C07F7/08Compounds having one or more C—Si linkages
    • C07F7/18Compounds having one or more C—Si linkages as well as one or more C—O—Si linkages
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    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F7/00Compounds containing elements of Groups 4 or 14 of the Periodic Table
    • C07F7/02Silicon compounds
    • C07F7/08Compounds having one or more C—Si linkages
    • C07F7/18Compounds having one or more C—Si linkages as well as one or more C—O—Si linkages
    • C07F7/1804Compounds having Si-O-C linkages
    • C07F7/1872Preparation; Treatments not provided for in C07F7/20
    • C07F7/188Preparation; Treatments not provided for in C07F7/20 by reactions involving the formation of Si-O linkages
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    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F7/00Compounds containing elements of Groups 4 or 14 of the Periodic Table
    • C07F7/02Silicon compounds
    • C07F7/08Compounds having one or more C—Si linkages
    • C07F7/18Compounds having one or more C—Si linkages as well as one or more C—O—Si linkages
    • C07F7/1804Compounds having Si-O-C linkages
    • C07F7/1872Preparation; Treatments not provided for in C07F7/20
    • C07F7/1892Preparation; Treatments not provided for in C07F7/20 by reactions not provided for in C07F7/1876 - C07F7/1888
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    • C08G59/00Polycondensates containing more than one epoxy group per molecule; Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups
    • C08G59/18Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing
    • C08G59/20Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing characterised by the epoxy compounds used
    • C08G59/22Di-epoxy compounds
    • C08G59/30Di-epoxy compounds containing atoms other than carbon, hydrogen, oxygen and nitrogen
    • C08G59/306Di-epoxy compounds containing atoms other than carbon, hydrogen, oxygen and nitrogen containing silicon
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C1/00Pressure vessels, e.g. gas cylinder, gas tank, replaceable cartridge
    • F17C1/02Pressure vessels, e.g. gas cylinder, gas tank, replaceable cartridge involving reinforcing arrangements
    • F17C1/04Protecting sheathings
    • F17C1/06Protecting sheathings built-up from wound-on bands or filamentary material, e.g. wires
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
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    • F17C2203/06Materials for walls or layers thereof; Properties or structures of walls or their materials
    • F17C2203/0634Materials for walls or layers thereof
    • F17C2203/0658Synthetics
    • F17C2203/0663Synthetics in form of fibers or filaments
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2221/00Handled fluid, in particular type of fluid
    • F17C2221/01Pure fluids
    • F17C2221/012Hydrogen
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/32Hydrogen storage

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  • General Engineering & Computer Science (AREA)
  • Epoxy Resins (AREA)

Abstract

The invention provides a bio-based epoxy resin suitable for a wet-process winding carbon fiber hydrogen storage bottle and a preparation method thereof, belonging to the technical field of epoxy resin preparation. The structural formula of the bio-based epoxy resin is shown as a formula (1), the invention also provides a preparation method of the bio-based epoxy resin, the method utilizes eugenol and dichlorodiphenylsilane as raw materials for preparing epoxy monomers, the thermal stability of the materials can be improved due to more aromatic structures of the bio-based epoxy resin, the reaction raw materials belong to renewable resources, the cost is low, the quality is excellent and non-toxic, the reaction process does not need too harsh reaction conditions, and the prepared resin has good mechanical property, thermal stability and excellent fluidity, has good application value in industry and can be suitable for winding carbon fiber hydrogen storage bottles by a wet method.

Description

Bio-based epoxy resin suitable for wet-process winding carbon fiber hydrogen storage bottle and preparation method thereof
Technical Field
The invention belongs to the technical field of epoxy resin preparation, and particularly relates to bio-based epoxy resin suitable for a wet-process winding carbon fiber hydrogen storage bottle and a preparation method thereof.
Background
The epoxy resin is a high molecular oligomer which contains two or more epoxy groups, takes aliphatic or aromatic groups as a framework, and can generate a thermosetting product through the reaction of the epoxy groups and other active groups. The epoxy resin has a large amount of active and polar groups, and as a thermosetting resin, the epoxy resin is widely applied to the fields of coatings, composite materials, adhesives, electronic packaging materials, engineering plastics, civil engineering and building materials and the like due to excellent comprehensive performance, good cohesiveness, excellent mechanical property, small curing shrinkage, good manufacturability, excellent electric insulation property and corrosion resistance.
However, the development of high performance epoxy resins faces two obstacles (1) the unsustainability of their petroleum-based raw materials in the life cycle, from production, use to disposal; (2) The special properties such as dielectric property and flame retardant property are further improved. At present, most of epoxy resin is derived from petroleum resources, particularly bisphenol A epoxy resin, and petroleum resources are non-renewable resources, and the cost of high polymer materials derived from petroleum resources is increased along with the gradual reduction of reserves of the petroleum resources. In addition, bisphenol a is suspected of having physiological toxicity and has been restricted in use in many countries such as europe, and thus under the current situation of increasingly depleted petroleum resources, there is an urgent need to use raw materials from other sources to produce epoxy resins, and to reduce the dependence on petroleum resources. The search for sustainable, high-quality, inexpensive, non-toxic alternatives to petroleum is a key to the existence and development of the polymer industry, and it is particularly important to develop alternatives with renewable resources and possessing comparable properties. In the past, halogenated organic additives such as polybrominated biphenyls and polybrominated diphenyl ethers have been widely used in the production of flame retardant epoxy materials. Unfortunately, these halogenated additives have proven to be harmful to the human endocrine system. Under such circumstances, the development of low flammability bio-based epoxy resins, while avoiding the introduction of halogen elements, is very important for reducing potential fire and health hazards. Some researchers have introduced organophosphate groups into epoxy molecules to improve their flame retardancy, but have resulted in high hygroscopicity and low thermal stability, resulting in poor processability of coatings, adhesives and fiber-reinforced composites. In addition, in view of the use of epoxy resins, a particularly low dielectric constant is also necessary because they are widely used as insulating materials for electronic devices (e.g., central processing units) and exhibit good dielectric properties. However, the research on bio-based epoxy resins has rarely solved this problem.
At present, almost all epoxy resins are completely dependent on petroleum resources. With the increasing consumption of petroleum resources and energy, the replacement of traditional petroleum-based epoxy resins with renewable epoxy resins, particularly bio-based epoxy resins, is imminent. Many different plant sources are obtained through fermentation and chemical transformation, such as epoxidized vegetable oils, isosorbide, cardanol, vanillin, itaconic acid, and lignin derivatives, to synthesize bio-based epoxy thermosets. So as to meet the requirement of serving as a starting material for preparing the bio-based epoxy monomer. In recent years, the shift from petroleum-based to bio-based materials in combination with inorganic nano-molecules to the synthesis of new resins is currently a major goal.
The carbon fiber winding forming process can be divided into wet winding and dry winding, wherein the wet winding is widely applied due to low cost and good manufacturability, and the wet winding equipment mainly comprises a fiber frame, tension control equipment, a glue dipping tank, a silk spinning nozzle and a rotary core mold structure. The international advanced six-dimensional winding technology can well control the trend of the fiber and realize the combination of annular winding, spiral winding and plane winding. The mode that combines together is wound to the spiral direction and hoop winding to the adoption in the actual production more, and hoop winding can eliminate the gas cylinder and receive the hoop stress that internal pressure and produced, and the spiral direction winding can provide longitudinal stress, promotes gas cylinder wholeness ability. The carbon fiber hydrogen storage cylinder resin matrix not only needs to meet the requirements of the cylinder on mechanical strength and toughness, but also needs a high-strength, high-toughness and fatigue-resistant resin system to ensure the service life of the cylinder because the matrix is easy to generate fatigue damage in the use environment of long-term inflation and deflation. Resin matrices for wet winding molding are required to have a low initial viscosity at a working temperature and a long pot life at that temperature, in addition to satisfying the respective properties.
Disclosure of Invention
The invention aims to solve the problems that the existing resin system is difficult to impregnate carbon fibers and raw materials are non-renewable, and provides a bio-based epoxy resin suitable for a wet-process winding carbon fiber hydrogen storage bottle and a preparation method thereof.
In order to achieve the purpose, the technical scheme adopted by the invention comprises the following steps:
the invention firstly provides a bio-based epoxy resin suitable for a wet-process winding carbon fiber hydrogen storage bottle, which has a structural formula shown in a formula (1):
Figure BDA0003775392560000031
the invention also provides a preparation method of the bio-based epoxy resin suitable for the wet-process winding carbon fiber hydrogen storage bottle shown in the formula (1), which comprises the following steps:
step one, adding eugenol, triethylamine and a solvent into a reaction vessel, and then adding dichlorodiphenylsilane to obtain an intermediate product DSi;
and step two, dripping the intermediate product DSi obtained in the step one into a suspension of meta-hydroperoxybenzoic acid, keeping the temperature of a reaction mixture below-5 ℃ in the dripping process, slowly heating to room temperature, stirring, and performing post-treatment to obtain the bio-based epoxy resin which is shown in the formula (1) and is suitable for the wet-process winding carbon fiber hydrogen storage bottle.
Preferably, the mol ratio of the eugenol, the triethylamine and the dichlorodiphenylsilane in the step one is (3-5): (1-3).
Preferably, the solvent of the first step is dichloromethane.
Preferably, the reaction temperature of the first step is 30-90 ℃, and the reaction time is 2-8h.
Preferably, the molar ratio of the intermediate product DSi to the m-chloroperoxybenzoic acid in the second step is 1 (3-5).
Preferably, the stirring time of the second step is 24-150h.
Preferably, the post-treatment in the second step is to filter the obtained mixture, and the filtrate is washed by saturated sodium thiosulfate solution and saturated sodium bicarbonate solution in sequence. The mixture was then dried over anhydrous sodium sulfate and the reaction product was filtered and rotary evaporated to remove CH 2 C1 2 Thereafter, further drying at 30-90 ℃ under vacuum.
The invention has the advantages of
The invention provides a bio-based epoxy resin suitable for a wet-process winding carbon fiber hydrogen storage bottle and a preparation method thereof, the structural formula of the bio-based epoxy resin is shown as a formula (1), and a siloxane-containing chain segment in the structure has the characteristics of low polarity, high dissociation energy, spiral molecular structure, large molecular volume and the like, so that the bio-based epoxy resin has excellent fluidity; the invention also provides a preparation method of the bio-based epoxy resin, which uses eugenol and dichlorodiphenylsilane as raw materials for preparing epoxy monomers, and because the aromatic structures are more, the thermal stability of the materials can be improved, the reaction raw materials belong to renewable resources, the price is low, the quality is excellent and non-toxic, the reaction process does not need too harsh reaction conditions, and the prepared resin has good mechanical properties, thermal stability and excellent fluidity, has good application value in industry, and can be suitable for winding carbon fiber hydrogen storage bottles by a wet method.
Drawings
FIG. 1 is an infrared spectrum of the bio-based epoxy resin prepared in example 1;
FIG. 2 is a nuclear magnetic resonance hydrogen spectrum of the bio-based epoxy resin of example 1;
FIG. 3 is a NMR spectrum of a bio-based epoxy resin of example 2;
FIG. 4 is a differential thermogravimetric analysis plot of the bio-based epoxy resin of example 1;
FIG. 5 is a graph of viscosity analysis of the bio-based epoxy resin of example 1.
Detailed Description
The invention firstly provides a bio-based epoxy resin suitable for a wet-process winding carbon fiber hydrogen storage bottle, which has a structural formula shown in a formula (1),
Figure BDA0003775392560000041
the invention also provides a preparation method of the bio-based epoxy resin suitable for the wet-process winding carbon fiber hydrogen storage bottle shown in the formula (1), which comprises the following steps:
adding eugenol, triethylamine and a solvent into a reaction vessel, wherein the solvent is preferably dichloromethane, then dissolving dichlorodiphenylsilane into dichloromethane to obtain a dichlorodiphenylsilane solution, slowly dripping the dichlorodiphenylsilane solution into the reaction vessel, wherein the reaction temperature is preferably 30-90 ℃, the reaction time is preferably 2-8h, the obtained product is preferably filtered, washing the filtrate with deionized water, and drying with sodium sulfate. After filtration, dichloromethane was removed from the organic layer by rotary evaporation. Finally, drying in a vacuum oven to obtain an intermediate product DSi; the mol ratio of the eugenol, the triethylamine and the dichlorodiphenylsilane is preferably (3-5) to (1-3). The reaction process is as follows:
Figure BDA0003775392560000051
step two, dripping the intermediate product DSi obtained in the step one into the suspension of m-chloroperoxybenzoic acid, and keeping the temperature of the reaction mixture in the dripping processSlowly heating to room temperature below 5 ℃, stirring for 24-150h, and performing post-treatment to obtain the bio-based epoxy resin shown in the formula (1) and suitable for the wet-process winding carbon fiber hydrogen storage bottle; the mol ratio of the intermediate product DSi to the m-chloroperoxybenzoic acid is preferably 1 (3-5), the post-treatment is preferably that the obtained mixture is filtered, the filtrate is washed by saturated sodium thiosulfate solution and saturated sodium bicarbonate solution in sequence, then the mixture is dried on anhydrous sodium sulfate, and the reaction product is filtered and rotary evaporated to remove CH 2 C1 2 Thereafter, further drying is carried out at 30-90 ℃ under vacuum. The reaction process is as follows:
Figure BDA0003775392560000052
the present invention is further illustrated by reference to the following specific examples, in which the starting materials are all commercially available.
Example 1
Step 1 eugenol (0.03 mol), triethylamine (0.03 mol) and dichloromethane (70 mL) were introduced into a 250mL three-necked round bottom flask equipped with a magnetic stirrer and reflux condenser. Dichlorodiphenylsilane (0.01 mol g) was then dissolved in dichloromethane (20 mL) and slowly added dropwise to the flask. Heating at 40 deg.C under reflux for 3 hr, filtering, washing the filtrate with deionized water for 3 times, and drying with sodium sulfate. After filtration, dichloromethane was removed from the organic layer by rotary evaporation. Finally, drying overnight in a vacuum oven gave a yellow liquid.
Step 2, under the nitrogen atmosphere, mixing the intermediate product and m-chloroperoxybenzoic acid in a molar ratio of 1:3, slowly dropping the intermediate product into the suspension of the m-chloroperoxybenzoic acid. During the dropwise addition, the temperature of the reaction mixture was kept below-5 ℃ and then slowly raised to room temperature and stirred for 48h. The reaction mixture was then filtered to remove m-chlorobenzoic acid, and the filtrate was washed successively with a saturated sodium thiosulfate solution and a saturated sodium bicarbonate solution. Subsequently, the mixture was dried over anhydrous sodium sulfate. The reaction product is filtered and rotary evaporated to remove CH 2 Cl 2 Thereafter, further drying was carried out at 40 ℃ under vacuum. Finally, a brown viscous liquid was obtained as the final product.
The infrared spectrum of the flame-retardant bio-based epoxy resin prepared in example 1 is shown in figure 1, and 3535cm of eugenol curve -1 Disappearance of the-OH peak at (C) and 773cm in the DSi curve of the novel intermediate -1 The disappearance of the Si-Cl bond signal peak represents the successful reaction of eugenol and dichlorodiphenylsilane, and 1122cm are shown in the ESR curve of the novel epoxy resin -1 This was also demonstrated by the formation of Si-O-C bonds, 1645cm in the eugenol feedstock curve -1 Peak value of (2) is represented by CH = CH 2 Caused by stretching vibration of the groups, disappears in the ESR curve of the novel epoxy resin, and simultaneously the ESR of the product is 909cm -1 And 829cm -1 The signal peak at the epoxy group confirms the formation of the epoxy group in EUEP.
The nuclear magnetic resonance hydrogen spectrum of the flame-retardant bio-based epoxy resin prepared in example 1 is shown in fig. 2, and the chemical shifts and the integral areas of all peaks are well matched with protons in the chemical structure of the novel epoxy resin ESR, which indicates that the target compound is successfully synthesized.
Example 1 differential thermogravimetric analysis graph of bio-based epoxy resin as shown in fig. 4, TGA curves of DDM cured bisphenol a type epoxy resin and novel epoxy resin ESR under nitrogen atmosphere, bisphenol a type epoxy resin has slightly higher initial decomposition temperature than novel epoxy resin ESR, but carbon residue rate of novel epoxy resin ESR is much higher than that of bisphenol a type epoxy resin, and excellent thermal stability is shown.
Example 1 the viscosity analysis profile of the bio-based epoxy resin is shown in FIG. 5, wherein a is a shear rate of 50rpm s -1 When the viscosity is changed with the temperature at 30-100 ℃, the viscosity of the bisphenol A type epoxy resin is firstly sharply reduced along with the temperature rise within 25-65 ℃; then keeping the temperature from 65 to 100 ℃ stable; in contrast, the viscosity of the ESR of the novel epoxy resin of the present invention is not significantly reduced from 25 to 100 ℃ and the viscosity of the ESR of the novel epoxy resin at 100 ℃ is still lower than that of the commercial bisphenol A type epoxy resin.
b is the viscosity at 25 ℃ with shear rate from 1 to 10 rpm.s -1 According to the change rule, the viscosity of the novel epoxy resin ESR and the viscosity of the bisphenol A epoxy resin are basically kept unchanged under different shear rates, and the constant viscosity is respectively 3.2130 Pa · s and 8.2144Pa · s. The viscosity of commercial bisphenol A is 2.6 times of ESR of the novel epoxy resin synthesized by the invention, which shows that the resin of the invention is beneficial to improving the processing performance.
Example 2
Step 1 eugenol (0.035 mol), triethylamine (0.035 mol) and dichloromethane (70 mL) were introduced into a 250mL three-necked round bottom flask equipped with a magnetic stirrer and reflux condenser. Dichlorodiphenylsilane (0.012 mol) was then dissolved in dichloromethane (20 mL) and slowly charged dropwise into the flask. Heating at 50 deg.C under reflux for 4 hr, filtering, washing the filtrate with deionized water for 3 times, and drying with sodium sulfate. After filtration, dichloromethane was removed from the organic layer by rotary evaporation. Finally, drying overnight in a vacuum oven gave a yellow liquid.
Step 2, under the nitrogen atmosphere, mixing the intermediate product and m-chloroperoxybenzoic acid in a molar ratio of 1:3, slowly dropping the intermediate product into the suspension of the m-chloroperoxybenzoic acid. During the dropwise addition, the temperature of the reaction mixture was kept below-5 ℃ and then slowly raised to room temperature and stirred for 72h. The reaction mixture was then filtered to remove m-chlorobenzoic acid, and the filtrate was washed successively with a saturated sodium thiosulfate solution and a saturated sodium bicarbonate solution. Subsequently, the mixture was dried over anhydrous sodium sulfate. The reaction product is filtered and rotary evaporated to remove CH 2 Cl 2 Thereafter, further drying was carried out under vacuum at 50 ℃. Finally, a brown viscous liquid was obtained as the final product.
The nuclear magnetic resonance hydrogen spectrum of the bio-based epoxy resin prepared in example 2 is shown in fig. 3, and the chemical shifts and the integral areas of all peaks are well matched with the protons in the chemical structure of the ESR of the novel epoxy resin, which indicates that the target compound is successfully synthesized.
Example 3
Step 1 eugenol (0.034 mol), triethylamine (0.04 mol) and dichloromethane (80 mL) were introduced into a 250mL three-necked round bottom flask equipped with a magnetic stirrer and reflux condenser. Dichlorodiphenylsilane (0.02 mol) was then dissolved in dichloromethane (20 mL) and slowly charged dropwise into the flask. Heating at 60 deg.C under reflux for 5 hr, filtering, washing the filtrate with deionized water for 3 times, and drying with sodium sulfate. After filtration, dichloromethane was removed from the organic layer by rotary evaporation. Finally, drying overnight in a vacuum oven gave a yellow liquid.
Step 2, under the nitrogen atmosphere, mixing the intermediate product and m-chloroperoxybenzoic acid in a molar ratio of 1:4, slowly dropping the intermediate product into the suspension of the m-chloroperoxybenzoic acid. During the dropwise addition, the temperature of the reaction mixture was kept below-5 ℃ and then slowly raised to room temperature and stirred for 96h. The reaction mixture was then filtered to remove m-chlorobenzoic acid, and the filtrate was washed successively with a saturated sodium thiosulfate solution and a saturated sodium bicarbonate solution. Subsequently, the mixture was dried over anhydrous sodium sulfate. The reaction product is filtered and rotary evaporated to remove CH 2 Cl 2 Thereafter, further drying was carried out under vacuum at 60 ℃. Finally, a brown viscous liquid was obtained as the final product.
Example 4
Step 1 eugenol (0.045 mol), triethylamine (0.045 mol) and dichloromethane (80 mL) were introduced into a 250mL three-necked round bottom flask equipped with a magnetic stirrer and a reflux condenser. Dichlorodiphenylsilane (0.0225 mol) was then dissolved in dichloromethane (20 mL) and slowly added dropwise to the flask. Heating at 70 deg.C under reflux for 6 hr, filtering, washing the filtrate with deionized water for 3 times, and drying with sodium sulfate. After filtration, dichloromethane was removed from the organic layer by rotary evaporation. Finally, drying overnight in a vacuum oven gave a yellow liquid.
Step 2, under the nitrogen atmosphere, mixing the intermediate product and m-chloroperoxybenzoic acid in a molar ratio of 1:4, slowly dropping the intermediate product into the suspension of the m-chloroperoxybenzoic acid. During the dropwise addition, the temperature of the reaction mixture was kept below-5 ℃ and then slowly raised to room temperature and stirred for 120h. The reaction mixture was then filtered to remove m-chlorobenzoic acid, and the filtrate was washed successively with a saturated sodium thiosulfate solution and a saturated sodium bicarbonate solution. Subsequently, the mixture was dried over anhydrous sodium sulfate. The reaction product is filtered and rotary evaporated to remove CH 2 Cl 2 Thereafter, further drying was carried out at 70 ℃ under vacuum. Finally, a brown viscous liquid was obtained as the final product.
Example 5
Step 1 eugenol (0.05 mol), triethylamine (0.05 mol) and dichloromethane (90 mL) were introduced into a 250mL three-necked round bottom flask equipped with a magnetic stirrer and reflux condenser. Dichlorodiphenylsilane (0.03 mol) was then dissolved in dichloromethane (20 mL) and slowly charged dropwise into the flask. Heating at 80 deg.C under reflux for 7 hr, filtering, washing the filtrate with deionized water for 3 times, and drying with sodium sulfate. After filtration, dichloromethane was removed from the organic layer by rotary evaporation. Finally, drying overnight in a vacuum oven gave a yellow liquid.
Step 2, under the nitrogen atmosphere, mixing the intermediate product and m-chloroperoxybenzoic acid in a molar ratio of 1:5, the intermediate product is slowly dropped into the suspension of m-chloroperoxybenzoic acid. During the dropwise addition, the temperature of the reaction mixture was kept below-5 ℃ and then slowly raised to room temperature and stirred for 144h. The reaction mixture was then filtered to remove m-chlorobenzoic acid, and the filtrate was washed successively with a saturated sodium thiosulfate solution and a saturated sodium bicarbonate solution. Subsequently, the mixture was dried over anhydrous sodium sulfate. The reaction product is filtered and rotary evaporated to remove CH 2 Cl 2 Thereafter, further drying was carried out under vacuum at 80 ℃. Finally, a brown viscous liquid was obtained as the final product.

Claims (8)

1. The bio-based epoxy resin suitable for the wet-process winding carbon fiber hydrogen storage bottle is characterized in that the structural formula is shown as the formula (1):
Figure FDA0003775392550000011
2. the method for preparing bio-based epoxy resin suitable for wet-winding carbon fiber hydrogen storage bottle as shown in formula (1) of claim 1, comprising:
step one, adding eugenol, triethylamine and a solvent into a reaction container, and then adding dichlorodiphenylsilane to obtain an intermediate product DSi;
and step two, dripping the intermediate product DSi obtained in the step one into a suspension of meta-hydroperoxybenzoic acid, keeping the temperature of a reaction mixture below-5 ℃ in the dripping process, slowly heating to room temperature, stirring, and performing post-treatment to obtain the bio-based epoxy resin which is shown in the formula (1) and is suitable for the wet-process winding carbon fiber hydrogen storage bottle.
3. The method as set forth in claim 2, wherein the molar ratio of eugenol, triethylamine and dichlorodiphenylsilane in the first step is (3-5): (3-5): 1-3.
4. The method according to claim 2, wherein the solvent used in the first step is dichloromethane.
5. The preparation method of claim 2, wherein the reaction temperature of the first step is 30-90 ℃ and the reaction time is 2-8h.
6. The preparation method of claim 2, wherein the molar ratio of the intermediate product DSi to the m-chloroperoxybenzoic acid in the second step is 1 (3-5).
7. The preparation method according to claim 2, wherein the stirring time of the second step is 24-150h.
8. The preparation method according to claim 2, wherein the post-treatment in the second step is to filter the obtained mixture, and the filtrate is washed with saturated sodium thiosulfate solution and saturated sodium bicarbonate solution in sequence. The mixture was then dried over anhydrous sodium sulfate and the reaction product was filtered and rotary evaporated to remove CH 2 C1 2 Thereafter, further drying is carried out at 30-90 ℃ under vacuum.
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106589317A (en) * 2016-12-03 2017-04-26 苏州大学 Biomass-based epoxy resin and preparation method thereof
CN110835402A (en) * 2019-11-20 2020-02-25 长春工业大学 Low-viscosity bio-based epoxy resin based on vanillin and preparation method thereof
US20200062888A1 (en) * 2016-12-03 2020-02-27 Soochow University Biomass-based epoxy resin and preparation method thereof
CN113583216A (en) * 2021-09-15 2021-11-02 福建蓝海黑石新材料科技有限公司 Bio-based epoxy resin containing silicon-oxygen bond and preparation and application methods thereof

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106589317A (en) * 2016-12-03 2017-04-26 苏州大学 Biomass-based epoxy resin and preparation method thereof
US20200062888A1 (en) * 2016-12-03 2020-02-27 Soochow University Biomass-based epoxy resin and preparation method thereof
CN110835402A (en) * 2019-11-20 2020-02-25 长春工业大学 Low-viscosity bio-based epoxy resin based on vanillin and preparation method thereof
CN113583216A (en) * 2021-09-15 2021-11-02 福建蓝海黑石新材料科技有限公司 Bio-based epoxy resin containing silicon-oxygen bond and preparation and application methods thereof

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