CN116063666B - Multifunctional polyester material and preparation method and application thereof - Google Patents

Multifunctional polyester material and preparation method and application thereof Download PDF

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CN116063666B
CN116063666B CN202111289897.0A CN202111289897A CN116063666B CN 116063666 B CN116063666 B CN 116063666B CN 202111289897 A CN202111289897 A CN 202111289897A CN 116063666 B CN116063666 B CN 116063666B
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aryl
substituted
polyester material
multifunctional polyester
alkyl
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CN116063666A (en
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余达刚
王哲昊
刘毅
廖黎丽
于博
肖汉至
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Qingdao Sanli Bennuo New Materials Ltd By Share Ltd
Sichuan University
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Qingdao Sanli Bennuo New Materials Ltd By Share Ltd
Sichuan University
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    • 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
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/02Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
    • C08G63/12Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from polycarboxylic acids and polyhydroxy compounds
    • C08G63/16Dicarboxylic acids and dihydroxy compounds
    • C08G63/18Dicarboxylic acids and dihydroxy compounds the acids or hydroxy compounds containing carbocyclic rings
    • C08G63/19Hydroxy compounds containing aromatic rings
    • C08G63/193Hydroxy compounds containing aromatic rings containing two or more aromatic rings
    • 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
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/02Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
    • C08G63/12Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from polycarboxylic acids and polyhydroxy compounds
    • C08G63/16Dicarboxylic acids and dihydroxy compounds
    • C08G63/18Dicarboxylic acids and dihydroxy compounds the acids or hydroxy compounds containing carbocyclic rings
    • C08G63/181Acids containing aromatic rings
    • C08G63/185Acids containing aromatic rings containing two or more aromatic rings
    • 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
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/02Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
    • C08G63/12Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from polycarboxylic acids and polyhydroxy compounds
    • C08G63/16Dicarboxylic acids and dihydroxy compounds
    • C08G63/18Dicarboxylic acids and dihydroxy compounds the acids or hydroxy compounds containing carbocyclic rings
    • C08G63/199Acids or hydroxy compounds containing cycloaliphatic rings
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    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/68Polyesters containing atoms other than carbon, hydrogen and oxygen
    • C08G63/682Polyesters containing atoms other than carbon, hydrogen and oxygen containing halogens
    • C08G63/6824Polyesters containing atoms other than carbon, hydrogen and oxygen containing halogens derived from polycarboxylic acids and polyhydroxy compounds
    • C08G63/6826Dicarboxylic acids and dihydroxy 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
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/68Polyesters containing atoms other than carbon, hydrogen and oxygen
    • C08G63/688Polyesters containing atoms other than carbon, hydrogen and oxygen containing sulfur
    • C08G63/6884Polyesters containing atoms other than carbon, hydrogen and oxygen containing sulfur derived from polycarboxylic acids and polyhydroxy compounds
    • C08G63/6886Dicarboxylic acids and dihydroxy 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
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/78Preparation processes
    • 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
    • C08G2230/00Compositions for preparing biodegradable polymers
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/54Improvements relating to the production of bulk chemicals using solvents, e.g. supercritical solvents or ionic liquids

Abstract

The invention discloses a multifunctional polyester material, a preparation method and application thereof, and belongs to the technical field of polyester materials and synthesis thereof.

Description

Multifunctional polyester material and preparation method and application thereof
Technical Field
The invention relates to the technical field of polyester materials and synthesis thereof, in particular to a multifunctional polyester material and a preparation method and application thereof.
Background
The ongoing development of the modern industry has resulted in substantial emissions of CO 2, whereas CO 2, as a greenhouse gas, directly or indirectly results in global warming. Therefore, the development of emission reduction and utilization of the corresponding CO 2 is significant. How to change low-value CO 2 into a product with high added value is always the direction of the endeavor pursuit of the scientific community. However, the effective utilization of CO 2, especially in terms of industrialization, is often not satisfactory. The reason for this is that CO 2 has kinetic inert and thermodynamic stability characteristics.
The polymer material plays an important role in our daily life and production process as one of three branches in the material field. However, the production of the traditional high polymer material is seriously dependent on petrochemical raw materials, which is very unfavorable for China relying on petroleum import, and the petroleum-based high polymer material is difficult to recover and degrade after the service life is finished. Therefore, the development of a series of polymer materials with green sources has important significance. If the dimethyl ester monomer derived from CO 2 can be used as a monomer source in the field of high polymer materials, the high additional value utilization of CO 2 can be realized, and a new idea can be provided for the green development in the field of high polymer materials. Meanwhile, the degradable material can effectively reduce white pollution, and has important significance for developing environment-friendly materials.
At present, a series of CO 2 -based degradable multifunctional polyester materials prepared by taking CO 2 -based dimethyl glutarate as a high polymer material monomer are not reported.
Disclosure of Invention
Aiming at the defects, the invention aims to provide a multifunctional polyester material and a preparation method and application thereof. According to the invention, the CO 2 dimethyl glutarate compound is used as a high molecular material monomer to carry out melt polymerization with a functional diol monomer, so that a series of multifunctional degradable polyester materials with excellent self-repairing, ultraviolet shielding and hydrophobic performances on the CO 2 base are prepared.
In order to achieve the above purpose, the invention adopts the following technical scheme:
the invention provides a multifunctional polyester material, which comprises the following repeated structural units:
Wherein R 1 is aryl, aryl substituted with one or more R 1a, or electron withdrawing group; r 2 is hydrogen, alkyl or alkyl substituted with one or more R 1a; r 3 is aryl, aryl substituted with one or more R 1a, heteroaryl substituted with one or more R 1a, or electron withdrawing group; r 4 is hydrogen, alkyl substituted with one or more R 1a, heteroaryl substituted with one or more R 1a, aryl, or aryl substituted with one or more R 1a; r 5 is at least one of substituted aryl, heteroaryl, and alkyl; r 6 is formyl, acetyl, butyryl, pentanoyl, hexanoyl, propionyl, benzoyl, phenylacetyl, phenylpropionyl, phenylbutyryl, phenylpentanoyl, phenylhexanoyl, bromobenzoyl, chlorobenzoyl, fluorobenzoyl, trifluoromethylbenzoyl, naphthoyl, biphenyl acyl, methylbenzoyl, pyridine acyl, thiophene acyl or furan acyl; r 7、R8 and R 9 are each aryl, aryl substituted with one or more R 1a, heteroaryl, or heteroaryl substituted with one or more R 1a; r 1a is C 1~C10 alkyl, halogen, ester group, cyano or amide group, etc.; the polymerization degrees a, b and c are natural numbers in the range of 2 to 130.
Further, the preferred structural formula of the above aryl group is as follows:
further, the preferred structural formula of the electron withdrawing group is as follows:
The invention also provides a preparation method of the multifunctional polyester material, which comprises the following steps: adding a CO 2 -yl dimethyl glutarate compound and a functional diol monomer into a reaction device, continuously stirring under the protection of inert gas, heating to melt, and carrying out heat preservation reaction for 3-12 h; then heating to 200-240 ℃, reacting for 0.5-3 h under the vacuum degree of 450-500 Pa, continuing to react under the vacuum degree of 40-50 Pa until the pole climbing phenomenon occurs, and separating and purifying to obtain the multifunctional polyester material;
Wherein, the mol ratio of the CO 2 dimethyl glutarate compound to the functional diol monomer is 1:1-3;
the structural general formula of the CO 2 -yl dimethyl glutarate compound is shown as follows:
Wherein R 1 is aryl, aryl substituted with one or more R 1a, or electron withdrawing group; r 2 is hydrogen, alkyl or alkyl substituted with one or more R 1a; r 3 is aryl, aryl substituted with one or more R 1a, heteroaryl substituted with one or more R 1a, or electron withdrawing group; r 4 is hydrogen, alkyl substituted with one or more R 1a, heteroaryl substituted with one or more R 1a, aryl, or aryl substituted with one or more R 1a; r 5 is at least one of substituted aryl, heteroaryl, and alkyl; r 1a is C 1~C10 alkyl, halogen, ester group, cyano or amide group, etc.
The pole climbing phenomenon is referred to as Weissenberg effect (normal stress effect) of the polymer melt, and is also referred to as a wraparound phenomenon.
Further, the preferred structural formula of the above aryl group is as follows:
further, the preferred structural formula of the electron withdrawing group is as follows:
further, the molar ratio of the CO 2 dimethyl glutarate compound to the functional diol monomer is 1:1-1.6.
Further, the structural formula of the functional diol monomer is shown as follows:
further, the melting temperature is preferably 170 to 190 ℃.
Further, the temperature is raised to melt, and the reaction time is preferably 5 to 8 hours, more preferably 6 hours.
Further, the specific process of separation and purification is as follows: completely dissolving a product obtained by the reaction in a solvent to obtain a product solution; then dripping the mixture into a precipitator with the volume 5 to 7 times of that of the product solution, stirring to obtain a powdery product, filtering the powdery product, and drying the powdery product in a vacuum drying oven at the temperature of between 40 and 60 ℃ for 12 to 48 hours.
Further, the solvent of the dissolved product is selected from mixed solvent or chloroform composed of chloroform/trifluoroacetic acid with the volume ratio of 4-6:1-2.
Further, the precipitant is methanol, acetone or diethyl ether.
Further, in order to accelerate the reaction rate, the invention also comprises a catalyst in the reaction system, wherein the catalyst is zinc acetate/antimonous oxide, tetrabutyl titanate, manganese acetate, cobalt acetate or ethylene glycol antimony. Preferably zinc acetate/antimony trioxide or tetrabutyl titanate; wherein the dosage of the catalyst is 0.1 to 0.5 weight percent of the total mass of the reaction monomers.
The invention also provides application of the multifunctional polyester material in preparing an ultraviolet shielding agent and/or a hydrophobic agent and/or a self-repairing preparation.
A self-repairing agent adopts the multifunctional polyester material as a main component.
An ultraviolet shielding preparation adopts the multifunctional polyester material as a main component.
A hydrophobic preparation comprises the multifunctional polyester material as main ingredient.
In summary, the invention has the following advantages:
1. The invention provides a multifunctional polyester material, which is prepared by using a CO 2 dimethyl glutarate compound as a high polymer material monomer to carry out melt polymerization with a functional diol monomer, introducing a plurality of benzene ring structures into a main chain and a side chain of the multifunctional polyester material, so that pi-pi interaction occurs between molecular chains of the polyester material, and simultaneously, the pi-pi interaction is further enhanced along with mutual entanglement of chain segments, thereby realizing the function of self-repairing when the polyester material is subjected to external physical damage; the invention also introduces the diaryl ketone structure and a plurality of fluorine atom substituents into the polyester chain segment structure at the same time, thereby realizing the effective shielding of the polyester material on ultraviolet and excellent hydrophobic performance, and finally preparing a series of multifunctional degradable polyester materials with excellent self-repairing, ultraviolet shielding and hydrophobic performance on CO 2 groups.
2. The invention provides a method for green synthesis of polyester, which is derived from a raw material monomer-CO 2 -yl dimethyl glutarate compound serving as carbon dioxide and has important significance for realizing 'carbon reaching peak' and 'carbon neutralization' targets in China. Meanwhile, the preparation method has the characteristics of simplicity, easiness in operation, high efficiency and high yield.
Drawings
FIG. 1 is a self-healing diagram of a polyester material of the present invention;
FIG. 2 is a graph showing the results of a self-healing tensile test of a polyester material of the present invention;
FIG. 3 is a graph showing the ultraviolet absorption curve of the polyester material of the present invention;
FIG. 4 is a graph showing the water contact angle test results of the polyester material of the present invention;
FIG. 5 shows GPC test results of polyester materials of the present invention.
Detailed Description
The present invention will be described in further detail with reference to the following examples in order to make the objects, technical solutions and advantages of the present invention more apparent. It should be understood that the particular embodiments described herein are illustrative only and are not intended to limit the invention, i.e., the embodiments described are merely some, but not all, of the embodiments of the invention.
Thus, the following detailed description of the embodiments of the invention, as provided, is not intended to limit the scope of the invention, as claimed, but is merely representative of selected embodiments of the invention. All other embodiments, which can be made by a person skilled in the art without making any inventive effort, are intended to be within the scope of the present invention.
The preferred embodiments of the present invention are illustrated below.
Example 1
In order to obtain higher reaction conversion and polymer molecular weight, the polymerization conditions were subjected to condition screening using diol monomer-compound a and diacid monomer-compound B as reaction monomers in this example, and the specific results are shown in table 1 below.
TABLE 1
Note that: reaction conditions: diacid monomer (15 mmol), diol monomer (15 mmol), zinc acetate (0.2 wt%), antimony trioxide (0.3 wt%), prepolymerization time: 12h, polycondensation time: 12h; a, catalyst tetrabutyl titanate; and b, prepolymerizing for 6h. c, prepolymerizing for 18h; d, e number average molecular weight and molecular weight distribution were determined by GPC.
Example 2
The reaction formula of this example is as follows:
In a 50mL polymerization flask equipped with a nitrogen inlet and outlet and a mechanical stirrer, glycol (15 mmol) and dimethyl ester (15 mmol) monomers, zinc acetate (0.2 wt%) and antimony trioxide (0.3 wt%) were added as catalysts; placing the polymerization bottle on a double-row pipe, pumping and replacing nitrogen for three times, heating to 190 ℃ under the protection of nitrogen, and stirring for about 12 hours under the condition; then the temperature is increased to 240 ℃, and the mixture is stirred for 0.5 to 1 hour under the vacuum degree with the pressure of about 500 Pa; stirring is continued under the vacuum degree with the pressure of 50Pa until the pole climbing phenomenon appears. The solid product obtained was dissolved in 50mL of a chloroform/trifluoroacetic acid (volume ratio: 5:1) mixed solvent, and then the solution was added dropwise to 100mL of glacial methanol for precipitation, and the solid was filtered to obtain pale yellow powder. And then dried in a vacuum oven at 60 ℃ for 24 hours. The specific results are as follows:
Wherein the structure of PBH-1 is characterized as follows :1H NMR(400MHz,DMSO-d6)δ7.65–7.00(m,18H),3.95(br,8H),3.60–3.44(m,8H),1.75–1.19(m,16H);13C NMR(101MHz,DMSO-d6)δ193.09,172.57,172.54,172.49,161.93,138.21,138.14,129.86,127.75,127.44,114.10,67.65,67.03,64.30,48.87,48.57,36.02,28.38,27.87,25.14,24.96.
Example 3
The reaction formula of this example is as follows:
In a 50mL polymerization flask equipped with a nitrogen inlet and outlet and a mechanical stirrer, glycol (15 mmol) and dimethyl ester (15 mmol) monomers, zinc acetate (0.2 wt%) and antimony trioxide (0.3 wt%) were added as catalysts; placing the polymerization bottle on a double-row pipe, pumping and replacing nitrogen for three times, heating to 190 ℃ under the protection of nitrogen, and stirring for about 12 hours under the condition; then the temperature is increased to 240 ℃, and the mixture is stirred for 0.5 to 1 hour under the vacuum degree with the pressure of about 500 Pa; stirring is continued under the vacuum degree with the pressure of 50Pa until the pole climbing phenomenon appears. The solid product obtained was dissolved in 15mL of a chloroform/trifluoroacetic acid (volume ratio: 5:1) mixed solvent, and then the solution was added dropwise to 100mL of glacial methanol for precipitation, and the solid was filtered to obtain pale yellow powder. And then dried in a vacuum oven at 60 ℃ for 24 hours. The specific results are as follows:
Example 4
The reaction equation of this example is as follows:
In a 50mL polymerization flask equipped with a nitrogen inlet and outlet and a mechanical stirrer, diol (1.1025 g) and dimethyl ester (1.2495 g) monomers and tetrabutyl titanate (8. Mu.L) were added as catalysts; placing the polymerization bottle on a double-row pipe, pumping and replacing nitrogen for three times, heating to 190 ℃ under the protection of nitrogen, and stirring for about 12 hours under the condition; then the temperature is increased to 230 ℃ and stirred for 2 hours under the vacuum degree with the pressure of about 500 Pa; stirring is continued under the vacuum degree with the pressure of 50Pa until the pole climbing phenomenon appears. The solid product obtained was dissolved in 15mL of a chloroform/trifluoroacetic acid (volume ratio: 5:1) mixed solvent, and then the solution was added dropwise to 100mL of glacial methanol for precipitation, and the solid was filtered to obtain pale yellow powder. And then dried in a vacuum oven at 60 ℃ for 24 hours. M n=29700,Mw/Mn=1.39,T5%=346℃,Tg = 75 ℃ of the resulting polyester.
Example 5
The reaction equation of this example is as follows:
In a 50mL polymerization flask equipped with a nitrogen inlet and outlet and a mechanical stirrer, glycol (0.2122 g) and dimethyl ester (0.9371 g) monomers, zinc acetate (2.3 mg) and antimony trioxide (3.5 mg) were added as catalysts; placing the polymerization bottle on a double-row pipe, pumping and replacing nitrogen for three times, heating to 190 ℃ under the protection of nitrogen, and stirring for 12 hours under the condition; then the temperature is increased to 240 ℃ and stirred for 2 hours under the vacuum degree with the pressure of 500 Pa; continuously stirring under the vacuum degree with the pressure of 50Pa until the pole climbing phenomenon occurs; the obtained solid product is dissolved by 15mL of mixed solvent of chloroform/trifluoroacetic acid (volume ratio is 5:1), then the solution is dripped into 100mL of glacial methanol for precipitation, and the solid is filtered to obtain light yellow powder; drying in a vacuum drying oven at 60 ℃ for 24 hours; m n=43500,Mw/Mn = 1.64 of the resulting polyester.
Examples
In order to examine the properties of the polyesters obtained according to the invention in terms of self-repair, UV-shielding and hydrophobicity. Some of the polyesters obtained in examples 1 to 3 were now subjected to self-healing, UV shielding and hydrophobic testing.
The test instrument and instrument use procedure were as follows:
Gel chromatograph (GPC): the polymer molecular weight and its distribution were measured by gel permeation chromatograph model 2414 from Waters company, and the sample was dissolved in chromatographically pure tetrahydrofuran at a concentration of about 5mg/mL. Polystyrene was used as a standard, tetrahydrofuran was used as the mobile phase, the flow rate was 1.0mL/Min, and the test temperature was 30 ℃.
Dynamic thermo-mechanical test (DMA): the test was performed on a DMA242C analyzer manufactured by the german relaxation company. The stretching mode is selected, the experimental temperature is from room temperature to 60 ℃, the heating rate is 5 ℃/min, and the testing frequency is 1Hz.
Ultraviolet visible absorption (UV-Vis): in the preparation process, firstly, a sample to be tested is prepared into a DMF solution of 0.1mg/mL, then ultrasonic treatment is carried out for 5min, after the sample is uniformly dispersed, the suspension is poured into a quartz cuvette, and finally, instrument parameters are adjusted, wherein the wavelength range is 200-800nm.
Hot stage polarization microscope (POM): the self-repairing process of the PBH-1 thin film was observed using a polarization microscope of ECLIPSE LV POL (transmission/epi-illumination) in Japanese.
Mechanical strength test: the tensile strength and the elongation at break of the polyester are tested according to national standard GB1040-2006, a miniature injection molding machine which is newly filled in Shanghai is adopted to prepare the polyester according to a 1BA type spline in the national standard, the tensile strength and the elongation at break are tested on a universal mechanical machine, and the tensile rate is 10mm/min.
Contact angle test (WCA): the static contact angle of the test sample was measured using DCAT meter/interface tensiometer from delfei, germany, using water as the test liquid.
The resulting polyester materials were found to contain multiple benzene ring structures in the backbone structure,
Self-repair test
The self-repairing test polyester has the following structure:
First, a dumbbell bar (35 mm x 5mm x 0.5 mm) was cut into two sections from the middle. And then spliced together. Then put into an oven for repair for 5 hours at 50 ℃. During which no external force is applied. The self-repairing sample can bear a weight of 250 times its own weight without breaking (fig. 1a and 1 c). To further confirm the self-healing ability of the material, scratches were made on the film surface with a blade, and then the samples were placed on a heated table at 50 ℃ and the change in scratches was detected with POM (fig. 1 b). It can be seen that the scratches on the film gradually become narrower as the heating time is prolonged, and eventually the scratches disappear after heating for 90 minutes. The self-repairing efficiency of PBH-1 is tested by a tensile experiment, and the result shows that: the stress and the strain of the initial material are respectively 14.1MPa and 136.5%, and after repair, the stress and the strain are respectively 6.0MPa and 121.9%, and can be respectively recovered to 42.6% and 89.3% of the initial material, so that the material PBH-1 has good self-repair capability (figure 2).
Ultraviolet shielding test
The structure of the ultraviolet shielding test polyester is as follows:
The UV absorption capacity of the selected polyesters (PBH-1) was examined by the UV-Vis test, and commercial cosmetics, PBHG and PBHT were selected as controls. The test results show that PBH-1 has stronger absorption capacity to UVB wave band ultraviolet rays (figure 3). The data obtained by further calculation according to the relevant ultraviolet shielding formula show that: the UV absorption of PBH-1 in the UVB (280-320 nm) region was more than 2 times that of commercial materials and was superior to that of PBHG and PBHT (Table 2).
Table 2 PBH-1 ultraviolet shielding
Note that: commercial cosmetics use functionalized cinnamic acid nanofibers as a matrix, and sun-screening active ingredients: zinc oxide (14.5% wt%), octylmethoxy cinnamate (7.5% wt%) and caprylate (5% wt%).
Hydrophobic Property test
The structure of the hydrophobic property test polyester is as follows:
through the water contact angle test, it was found that the hydrophobic property was significantly improved with an increase in the number of fluorine atoms in the polyester (FIG. 4)
Degradation test
The structure of the degradation test polyester is as follows:
The degradation degree of the polyester material was tested by GPC after 15 days with a small amount of PTD with M n =29700 in phosphate buffer solution with ph=2 with stirring at room temperature for 15 days (fig. 5). The number average molecular weight of the polyester material is changed from 29700 to 19900, and the molecular weight distribution is changed from 1.39 to 2.08 (table 3), so that the polyester material has the degradable performance.
TABLE 3 specific data for polyester degradation
The foregoing is merely illustrative and explanatory of the invention as it is claimed, as modifications and additions may be made to, or similar to, the particular embodiments described, without the benefit of the inventors' inventive effort, and as alternatives to those of skill in the art, which remain within the scope of this patent.

Claims (9)

1. A multifunctional polyester material characterized in that the multifunctional polyester material has the following repeating structural units:
Wherein R 1 is aryl, aryl substituted with one or more R 1a, or electron withdrawing group; r 2 is hydrogen, alkyl or alkyl substituted with one or more R 1a; r 3 is aryl, aryl substituted with one or more R 1a, heteroaryl substituted with one or more R 1a, or electron withdrawing group; r 4 is hydrogen, alkyl substituted with one or more R 1a, heteroaryl substituted with one or more R 1a, aryl, or aryl substituted with one or more R 1a; r 5 is at least one of substituted aryl, heteroaryl, and alkyl; r 6 is formyl, acetyl, butyryl, pentanoyl, hexanoyl, propionyl, benzoyl, phenylacetyl, phenylpropionyl, phenylbutyryl, phenylpentanoyl, phenylhexanoyl, bromobenzoyl, chlorobenzoyl, fluorobenzoyl, trifluoromethylbenzoyl, naphthoyl, biphenyl acyl, methylbenzoyl, pyridine acyl, thiophene acyl or furan acyl; r 7、R8 and R 9 are each aryl, aryl substituted with one or more R 1a, heteroaryl, or heteroaryl substituted with one or more R 1a; r 1a is C 1~C10 alkyl, halogen, ester, cyano or amide; a. b and c are natural numbers in the range of 2 to 130.
2. The multifunctional polyester material of claim 1, wherein the aryl group has the structural formula:
3. the multifunctional polyester material of claim 1, wherein the electron withdrawing group has a structural formula as follows:
4. A method for producing a multifunctional polyester material according to any one of claims 1 to 3, comprising the steps of: adding a CO 2 -yl dimethyl glutarate compound and a functional diol monomer into a reaction device, continuously stirring under the protection of inert gas, heating to melt, and carrying out heat preservation reaction for 3-12 h; then heating to 200-240 ℃, reacting for 0.5-3 h under the vacuum degree of 450-500 Pa, continuing to react under the vacuum degree of 40-50 Pa until the pole climbing phenomenon occurs, and separating and purifying to obtain the multifunctional polyester material;
Wherein, the mol ratio of the CO 2 dimethyl glutarate compound to the functional diol monomer is 1:1-3;
the structural general formula of the CO 2 -yl dimethyl glutarate compound is shown as follows:
wherein R 1 is aryl, aryl substituted with one or more R 1a, or electron withdrawing group; r 2 is hydrogen, alkyl or alkyl substituted with one or more R 1a; r 3 is aryl, aryl substituted with one or more R 1a, heteroaryl substituted with one or more R 1a, or electron withdrawing group; r 4 is hydrogen, alkyl substituted with one or more R 1a, heteroaryl substituted with one or more R 1a, aryl, or aryl substituted with one or more R 1a; r 1a is C 1~C10 alkyl, halogen, ester, cyano or amide;
The structural formula of the functional diol monomer is shown as follows:
5. The method for producing a multifunctional polyester material according to claim 4, wherein the molar ratio of the CO 2 -yldimethyl glutarate compound to the functional diol monomer is 1:1 to 1.6.
6. Use of the multifunctional polyester material according to any of claims 1 to 3 for the preparation of uv-screening agents and/or for the preparation of hydrophobing agents and/or for the preparation of self-healing formulations.
7. A self-repairing agent characterized by using the multifunctional polyester material according to any one of claims 1 to 3 as a main component.
8. An ultraviolet shielding preparation characterized in that the multifunctional polyester material according to any one of claims 1 to 3 is used as a main component.
9. A hydrophobic preparation characterized by using the multifunctional polyester material according to any one of claims 1 to 3 as a main component.
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