Disclosure of Invention
The invention aims to provide a biology-based semi-aromatic polyamide and a preparation method thereof aiming at the defects of the prior art, and the biology-based semi-aromatic polyamide is characterized in that a monomer, furan dicarboxylic acid diester, sebacic acid and diamine are taken as raw materials, a biology-based semi-aromatic polyamide prepolymer is generated by polymerization under the action of a catalyst, and the high molecular weight biology-based semi-aromatic polyamide resin is obtained by further polycondensation at high temperature after the prepolymer is dried; the method has the advantages of easily obtained raw materials, simple operation and high yield, and the carbon element of the obtained resin is a complete bio-based source and has the advantages of low water absorption, easy processing and high mechanical strength.
The technical scheme of the invention is as follows:
the first technical problem to be solved by the invention is to provide a bio-based semi-aromatic polyamide, which has a structural formula as follows:
wherein n is 10-200, x + y is more than 0 and less than or equal to 1, x is not equal to 0, and y is not equal to 0;
R1=-(CH2)8CH3、-(CH2)10CH3、-(CH2)12CH3、-(CH2)14CH3、-(CH2)15CH3、-(CH2)16CH3、-(CH2)18CH3、-(CH2)20CH3、-(CH2)22CH3、-(CH2)24CH3、-(CH2)26CH3or- (CH)2)28CH3At least one of;
R2=-(CH2)5-and/or- (CH)2)10-。
Further, the bio-based semi-aromatic polyamide is prepared by adopting the following method: preparing amidated glutamic acid monomer with sodium glutamate and long-chain fatty acyl chloride as material; mixing the amidated glutamic acid monomer with furan dicarboxylic acid diester, sebacic acid and diamine, and preparing a bio-based semi-aromatic polyamide prepolymer by adopting a high-temperature solution polymerization method; and further performing polycondensation on the prepolymer to obtain the bio-based semi-aromatic polyamide.
Further, in the method for preparing the bio-based semi-aromatic polyamide, the long-chain fatty acid chloride is any one of decanoyl chloride, dodecanoyl chloride, tetradecanoyl chloride, hexadecanoyl chloride, heptadecanoyl chloride, octadecanoyl chloride, eicosanoyl chloride, docosanoyl chloride, tetracosanoyl chloride, hexacosanoyl chloride, octacosanoyl chloride or triacontanoyl chloride.
Further, in the above method for producing a bio-based semi-aromatic polyamide, the furandicarboxylic acid diester is at least one of dimethyl 2, 5-furandicarboxylate, diethyl 2, 5-furandicarboxylate, di-n-propyl 2, 5-furandicarboxylate, diisopropyl 2, 5-furandicarboxylate, di-n-butyl 2, 5-furandicarboxylate, diisobutyl 2, 5-furandicarboxylate, and di-sec-butyl 2, 5-furandicarboxylate.
Further, in the method for preparing the bio-based semi-aromatic polyamide, the diamine is pentamethylene diamine and/or decamethylene diamine.
Further, the bio-based semi-aromatic polyamide prepolymer is prepared by the following preparation steps:
(1) adding 301-581 parts of monomer, 184-2260 parts of furan dicarboxylic acid diester, 0-1010 parts of sebacic acid, 210-2800 parts of diamine, 1-30 parts of catalyst, 5-80 parts of molecular weight regulator and 100-2000 parts of alcohol into a reaction kettle, introducing nitrogen, stirring, heating to 60-90 ℃ within 0.5-1 hour
(2) Stopping introducing nitrogen, sealing the reaction kettle, heating to 180-240 ℃ within 1-3 hours, and maintaining the temperature for reaction for 2-5 hours;
(3) opening an exhaust valve, discharging mixed steam of alcohol and water within 0.5-2 hours to reduce the pressure in the kettle to 0.5-1.5 MPa, and maintaining the temperature to be not more than 240-260 ℃;
(4) closing an exhaust valve, and continuously stirring and reacting at 240-260 ℃ for 0.5-2 hours to homogenize the materials; then cooling to room temperature, discharging, drying the product until the water content is less than or equal to 0.3 percent, and obtaining the bio-based semi-aromatic polyamide prepolymer;
in the step (1), the structural formula of the monomer is as follows:
wherein:
R1=-(CH2)8CH3、-(CH2)10CH3、-(CH2)12CH3、-(CH2)14CH3、-(CH2)15CH3、-(CH2)16CH3、-(CH2)18CH3、-(CH2)20CH3、-(CH2)22CH3、-(CH2)24CH3、-(CH2)26CH3or- (CH)2)28CH3Any one of the above.
Further, in the preparation method of the bio-based semi-aromatic polyamide prepolymer, the monomer is prepared by the following method, and the method comprises the following steps:
1) adding 190.5-470.5 parts of long-chain fatty acyl chloride and 100-1000 parts of solvent into a dissolving kettle, and uniformly stirring to obtain an acyl chloride solution;
2) adding 169 parts of sodium glutamate, 80-138 parts of alkaline compound and 200-2000 parts of deionized water into a reactor with a stirrer, a thermometer, a condenser and a freezing water cooling device; introducing chilled water, and stirring and reacting for 1-3 hours at 0-30 ℃; maintaining stirring and temperature, and dropwise adding the acyl chloride solution obtained in the step 1) into the reactor within 0.5-2 hours; after the dropwise addition is finished, continuously maintaining the temperature for reaction for 0.5-1 hour;
3) heating to 36-81 ℃, and evaporating the solvent; continuously heating to age the reaction solution at 50-90 ℃ for 1-2 hours;
4) filtering while the mixture is hot, and then cooling to 20-40 ℃; adding acid with the concentration of 1.0-12.0 mol/L into the filtrate until the pH value is 0-3, standing at room temperature for 6-24 hours, and fully precipitating a product; the monomer is obtained by filtering, washing and drying.
Further, in the above method for preparing the monomer, the solvent in step 1) is any one of dichloromethane, n-pentane, n-hexane or cyclohexane.
Further, in the above method for preparing a monomer, the basic compound in step 2) is any one of sodium hydroxide, potassium hydroxide, sodium carbonate or potassium carbonate.
Further, in the above method for producing a monomer, the acid in step 4) is any one of hydrochloric acid, sulfuric acid, or phosphoric acid.
Further, in the preparation method of the bio-based semi-aromatic polyamide prepolymer, in the step (1), the catalyst is at least one of phosphoric acid, pyrophosphoric acid, polyphosphoric acid, phosphorous acid, sodium phosphate, sodium phosphite, sodium hypophosphite or sodium tripolyphosphate.
Further, in the preparation method of the bio-based semi-aromatic polyamide prepolymer, in the step (1), the molecular weight regulator is any one of acetic acid, caproic acid, caprylic acid, capric acid, dodecanoic acid, tetradecanoic acid, hexadecanoic acid, heptadecanoic acid, octadecanoic acid, eicosanoic acid, docosanoic acid, tetracosanoic acid, hexacosanoic acid, octacosanoic acid and triacontanoic acid.
Further, in the preparation method of the bio-based semi-aromatic polyamide prepolymer, in the step (1), the alcohol is any one of methanol, ethanol, n-propanol, isopropanol, n-butanol, isobutanol or sec-butanol; methanol is preferred.
Further, in the preparation method of the bio-based semi-aromatic polyamide, the bio-based semi-aromatic polyamide prepolymer is subjected to polycondensation reaction at 220-330 ℃ to obtain the bio-based semi-aromatic polyamide.
Further, in the preparation method of the bio-based semi-aromatic polyamide, the method for further polycondensing the bio-based semi-aromatic polyamide prepolymer at high temperature is at least one of vacuum solid-phase polycondensation, solid-phase polycondensation under the protection of water vapor and/or inert gas, solid-phase polycondensation under the protection of inert liquid, solid-phase reaction extrusion, melt polycondensation under the protection of water vapor and/or inert gas, melt polycondensation under the protection of inert liquid, vacuum melt polycondensation or melt reaction extrusion; wherein the inert gas is at least one of nitrogen, argon or helium; the inert liquid is at least one of diphenyl ether, diphenyl sulfone, dimethyl silicone oil or diphenyl silicone oil.
The second technical problem to be solved by the present invention is to provide a method for preparing the above bio-based semi-aromatic polyamide, the method comprising: preparing amidated glutamic acid monomer with sodium glutamate and long-chain fatty acyl chloride as material; mixing the amidated glutamic acid monomer with furan dicarboxylic acid diester, sebacic acid and diamine, and preparing a bio-based semi-aromatic polyamide prepolymer by adopting a high-temperature solution polymerization method; and further performing polycondensation on the prepolymer to obtain the bio-based semi-aromatic polyamide.
Further, in the above method for producing a bio-based semi-aromatic polyamide, the long-chain fatty acid chloride may be any one of decanoyl chloride, dodecanoyl chloride, tetradecanoyl chloride, hexadecanoyl chloride, heptadecanoyl chloride, octadecanoyl chloride, eicosanoyl chloride, docosanoyl chloride, tetracosanoyl chloride, hexacosanoyl chloride, octacosanoyl chloride, or triacontanoyl chloride.
Further, in the above method for producing a bio-based semi-aromatic polyamide, the furandicarboxylic acid diester is at least one of dimethyl 2, 5-furandicarboxylate, diethyl 2, 5-furandicarboxylate, di-n-propyl 2, 5-furandicarboxylate, diisopropyl 2, 5-furandicarboxylate, di-n-butyl 2, 5-furandicarboxylate, diisobutyl 2, 5-furandicarboxylate, and di-sec-butyl 2, 5-furandicarboxylate.
Further, in the above method for preparing bio-based semi-aromatic polyamide, the diamine is pentamethylenediamine and/or decamethylenediamine.
Further, the bio-based semi-aromatic polyamide prepolymer is prepared by the following preparation steps:
(1) adding 301-581 parts of monomer, 184-2260 parts of furan dicarboxylic acid diester, 0-1010 parts of sebacic acid, 210-2800 parts of diamine, 1-30 parts of catalyst, 5-80 parts of molecular weight regulator and 100-2000 parts of alcohol into a reaction kettle, introducing nitrogen, stirring, heating to 60-90 ℃ within 0.5-1 hour
(2) Stopping introducing nitrogen, sealing the reaction kettle, heating to 180-240 ℃ within 1-3 hours, and maintaining the temperature for reaction for 2-5 hours;
(3) opening an exhaust valve, discharging mixed steam of alcohol and water within 0.5-2 hours to reduce the pressure in the kettle to 0.5-1.5 MPa, and maintaining the temperature to be not more than 240-260 ℃;
(4) closing an exhaust valve, and continuously stirring and reacting at 240-260 ℃ for 0.5-2 hours to homogenize the materials; then cooling to room temperature, discharging, drying the product until the water content is less than or equal to 0.3 percent, and obtaining the bio-based semi-aromatic polyamide prepolymer;
in the step (1), the structural formula of the monomer is as follows:
wherein:
R1=-(CH2)8CH3、-(CH2)10CH3、-(CH2)12CH3、-(CH2)14CH3、-(CH2)15CH3、-(CH2)16CH3、-(CH2)18CH3、-(CH2)20CH3、-(CH2)22CH3、-(CH2)24CH3、-(CH2)26CH3or- (CH)2)28CH3Any one of the above.
Further, in the preparation method of the bio-based semi-aromatic polyamide prepolymer, the monomer is prepared by the following method, and the method comprises the following steps:
1) adding 190.5-470.5 parts of long-chain fatty acyl chloride and 100-1000 parts of solvent into a dissolving kettle, and uniformly stirring to obtain an acyl chloride solution;
2) adding 169 parts of sodium glutamate, 80-138 parts of alkaline compound and 200-2000 parts of deionized water into a reactor with a stirrer, a thermometer, a condenser and a freezing water cooling device; introducing chilled water, and stirring and reacting for 1-3 hours at 0-30 ℃; maintaining stirring and temperature, and dropwise adding the acyl chloride solution obtained in the step 1) into the reactor within 0.5-2 hours; after the dropwise addition is finished, continuously maintaining the temperature for reaction for 0.5-1 hour;
3) heating to 36-81 ℃, and evaporating the solvent; continuously heating to age the reaction solution at 50-90 ℃ for 1-2 hours;
4) filtering while the mixture is hot, and then cooling to 20-40 ℃; adding acid with the concentration of 1.0-12.0 mol/L into the filtrate until the pH value is 0-3, standing at room temperature for 6-24 hours, and fully precipitating a product; the monomer is obtained by filtering, washing and drying.
Further, in the above method for preparing the monomer, the solvent in step 1) is any one of dichloromethane, n-pentane, n-hexane or cyclohexane.
Further, in the above method for preparing a monomer, the basic compound in step 2) is any one of sodium hydroxide, potassium hydroxide, sodium carbonate or potassium carbonate.
Further, in the above method for producing a monomer, the acid in step 4) is any one of hydrochloric acid, sulfuric acid, or phosphoric acid.
Further, in the preparation method of the bio-based semi-aromatic polyamide prepolymer, in the step (1), the catalyst is at least one of phosphoric acid, pyrophosphoric acid, polyphosphoric acid, phosphorous acid, sodium phosphate, sodium phosphite, sodium hypophosphite or sodium tripolyphosphate.
Further, in the preparation method of the bio-based semi-aromatic polyamide prepolymer, in the step (1), the molecular weight regulator is any one of acetic acid, caproic acid, caprylic acid, capric acid, dodecanoic acid, tetradecanoic acid, hexadecanoic acid, heptadecanoic acid, octadecanoic acid, eicosanoic acid, docosanoic acid, tetracosanoic acid, hexacosanoic acid, octacosanoic acid and triacontanoic acid.
Further, in the preparation method of the bio-based semi-aromatic polyamide prepolymer, in the step (1), the alcohol is any one of methanol, ethanol, n-propanol, isopropanol, n-butanol, isobutanol or sec-butanol; methanol is preferred.
Further, in the preparation method of the bio-based semi-aromatic polyamide, the bio-based semi-aromatic polyamide prepolymer is subjected to polycondensation reaction at 220-330 ℃ to obtain the bio-based semi-aromatic polyamide.
Further, in the preparation method of the bio-based semi-aromatic polyamide, the method for further polycondensing the bio-based semi-aromatic polyamide prepolymer at high temperature is at least one of vacuum solid-phase polycondensation, solid-phase polycondensation under the protection of water vapor and/or inert gas, solid-phase polycondensation under the protection of inert liquid, solid-phase reaction extrusion, melt polycondensation under the protection of water vapor and/or inert gas, melt polycondensation under the protection of inert liquid, vacuum melt polycondensation or melt reaction extrusion; wherein the inert gas is at least one of nitrogen, argon or helium; the inert liquid is at least one of diphenyl ether, diphenyl sulfone, dimethyl silicone oil or diphenyl silicone oil.
In the invention, the raw materials are in parts by weight except for special specifications.
The invention has the beneficial effects that:
1. the invention takes sodium glutamate and long-chain fatty acyl chloride as raw materials, firstly amidated glutamic acid monomer is prepared; and mixing the monomer with furan dicarboxylic acid diester, sebacic acid and diamine, preparing a bio-based semi-aromatic polyamide prepolymer by adopting high-temperature solution polymerization, and further performing polycondensation to prepare the bio-based semi-aromatic polyamide. The method uses less raw materials from petroleum sources, and has the advantages of energy conservation and environmental protection.
2. The main raw material sodium glutamate of the invention is the main component of monosodium glutamate, is a product which is produced and used in large scale at present, and has the advantages of low price, wide raw material source and low cost.
3. The bio-based semi-aromatic polyamide obtained by the invention is a complete bio-based high polymer material, has low water absorption rate and has the advantage of good dimensional stability.
4. The invention adopts various polymerization methods to prepare the bio-based semi-aromatic polyamide, has simple operation and mature process, and the obtained product has stable quality.
Detailed Description
The present invention is described in detail below by way of examples, it should be noted that the examples are only for the purpose of further illustrating the present invention and are not to be construed as limiting the scope of the present invention, and that those skilled in the art can make insubstantial modifications and adaptations to the invention described above based on the disclosure of the present invention.
Example 1
1905g of decanoyl chloride and 2000g of dichloromethane were added to the dissolution kettle and stirred uniformly to obtain an acid chloride solution. 1690g of sodium glutamate, 800g of sodium hydroxide and 4000g of deionized water are added into a reactor with a stirrer, a thermometer, a condenser and a frozen water cooling device; introducing chilled water, and stirring and reacting for 2 hours at 20 ℃; maintaining stirring and temperature, and dropwise adding the acyl chloride solution into the reactor within 1 hour; after the dropwise addition is finished, the temperature is continuously maintained for reaction for 0.5 hour; heating to 40 ℃, and distilling off dichloromethane; continuing to heat up, and aging the reaction solution at 60 ℃ for 1 hour; filtering while the solution is hot, and cooling to 35 ℃; adding hydrochloric acid with the concentration of 5.0mol/L into the filtrate until the PH value is 1, standing for 15 hours at room temperature, and fully separating out a product; the monomer is obtained by filtering, washing and drying.
Adding 1505g of the monomer, 920g of 2, 5-furandicarboxylic acid dimethyl ester, 1050g of pentamethylene diamine, 10g of polyphosphoric acid, 60g of octadecanoic acid and 800g of methanol into a reaction kettle, introducing nitrogen, stirring, and heating to 60 ℃ within 0.5 hour; stopping introducing nitrogen, sealing the reaction kettle, heating to 220 ℃ within 2 hours, and maintaining the temperature for reaction for 3 hours; opening an exhaust valve, discharging mixed steam of alcohol and water within 1 hour to reduce the pressure in the kettle to 1.2MPa, and maintaining the temperature not to exceed 240 ℃; closing an exhaust valve, heating to 240 ℃, and maintaining the temperature for reaction for 2 hours to homogenize the materials; then cooling to room temperature, discharging, and drying the product until the water content is less than or equal to 0.3 percent to obtain the bio-based semi-aromatic polyamide prepolymer.
2200g of the prepolymer is added into a solid phase polycondensation kettle, and the mixture is vacuumized to-0.08 MPa; gradually heating to 240 ℃ under continuous stirring, and reacting for 8 hours under heat preservation; cooling and discharging to obtain high molecular weight bio-based semi-aromatic polyamide resin with intrinsic viscosity [ eta ]]=0.81dL·g-1Melt index 84 g.10 min-1. The performance parameters of each example are shown in table 1.
And (3) performance testing: the thermogravimetric analysis adopts the company of NETZSCH TG 209, and the heating rate is 10 ℃ min-1Nitrogen atmosphere, test temperature range: the temperature is between room temperature and 600 ℃, and the 5 percent weight loss temperature is taken as the thermal decomposition temperature; FIG. 1 is a thermogravimetric analysis of the bio-based semi-aromatic polyamide obtained in example 1; as is clear from FIG. 1, the thermal decomposition temperature of the bio-based semi-aromatic polyamide obtained in example 1 was 394.2 ℃.
Example 2
Adding 3025g of octadecanoyl chloride and 4000g of n-hexane into a dissolving kettle, and uniformly stirring to obtain an acyl chloride solution. 1690g of sodium glutamate, 1380g of potassium carbonate and 12000g of deionized water were added to a reactor equipped with a stirrer, a thermometer, a condenser and a chilled water cooling device; introducing chilled water, and stirring and reacting for 3 hours at the temperature of 30 ℃; maintaining stirring and temperature, and dropwise adding the acyl chloride solution into the reactor within 1.5 hours; after the dropwise addition is finished, the temperature is continuously maintained for reaction for 1 hour; heating to 70 ℃, and evaporating n-hexane; continuing to heat up, and aging the reaction solution at 80 ℃ for 2 hours; filtering while the solution is hot, and cooling to 25 ℃; adding sulfuric acid with the concentration of 2.0mol/L into the filtrate until the pH value is 3, standing for 18 hours at room temperature, and fully separating out a product; the monomer is obtained by filtering, washing and drying.
2065g of the monomer, 2970g of diethyl 2, 5-furandicarboxylate, 1010g of sebacic acid, 4430g of decanediamine, 20g of sodium hypophosphite, 100g of hexadecanoic acid and 2200g of ethanol are added into a reaction kettle, nitrogen is introduced, stirring is carried out, and the temperature is raised to 65 ℃ within 1 hour; stopping introducing nitrogen, sealing the reaction kettle, heating to 230 ℃ within 3 hours, and maintaining the temperature for reaction for 4 hours; opening an exhaust valve, discharging mixed steam of alcohol and water within 2 hours to reduce the pressure in the kettle to 1.0MPa, and maintaining the temperature not to exceed 245 ℃; closing an exhaust valve, heating to 250 ℃, and maintaining the temperature for reaction for 1 hour to homogenize the materials; then cooling to room temperature, discharging, and drying the product until the water content is less than or equal to 0.3 percent to obtain the bio-based semi-aromatic polyamide prepolymer.
6500g of the prepolymer is added into a solid phase polycondensation kettle, the temperature is raised to 100 ℃, and nitrogen is introduced: taking mixed gas with the volume ratio of water vapor of 8:2 as protective gas; gradually heating to 250 ℃ under continuous stirring, and reacting for 6 hours under heat preservation; vacuumizing to-0.09 MPa, heating to 260 ℃, and reacting for 4 hours in a heat preservation way; cooling and discharging to obtain high molecular weight bio-based semi-aromatic polyamide resin with intrinsic viscosity [ eta ]]=0.83dL·g-1Melt index 302 g.10 min-1。
Example 3
Adding 274.5g of hexadecanoyl chloride and 500g of n-pentane into a dissolving kettle, and uniformly stirring to obtain an acyl chloride solution. 169g of sodium glutamate, 106g of sodium carbonate and 900g of deionized water were added to a reactor equipped with a stirrer, a thermometer, a condenser and a chilled water cooling device; introducing chilled water, and stirring and reacting for 1 hour at 10 ℃; maintaining stirring and temperature, and dropwise adding the acyl chloride solution into the reactor within 0.5 hour; after the dropwise addition is finished, the temperature is continuously maintained for reaction for 1 hour; heating to 36 deg.c to evaporate n-pentane; continuing to heat up, and aging the reaction solution at 50 ℃ for 1.5 hours; filtering while the solution is hot, and cooling to 20 ℃; adding hydrochloric acid with the concentration of 12.0mol/L into the filtrate until the PH value is 0, standing for 24 hours at room temperature, and fully separating out a product; the monomer is obtained by filtering, washing and drying.
192.5g of the above monomer, 206.5g of the monomer prepared in example 2, 678g of di-n-butyl 2, 5-furandicarboxylate, 101g of sebacic acid, 430g of pentanediamine, 86g of decanediamine, 3g of phosphoric acid, 1g of sodium triphosphate, 5g of acetic acid and 600g of n-butanol were added to a reaction vessel, nitrogen was introduced, stirring was carried out, and the temperature was raised to 90 ℃ within 0.5 hour; stopping introducing nitrogen, sealing the reaction kettle, heating to 200 ℃ within 1 hour, and maintaining the temperature for reaction for 5 hours; opening an exhaust valve, discharging mixed steam of alcohol and water within 0.5 hour to reduce the pressure in the kettle to 0.5MPa, and maintaining the temperature to be not more than 250 ℃; closing an exhaust valve, heating to 255 ℃, and maintaining the temperature for reaction for 1.5 hours to homogenize the materials; then cooling to room temperature, discharging, and drying the product until the water content is less than or equal to 0.3 percent to obtain the bio-based semi-aromatic polyamide prepolymer.
Adding 200g of the prepolymer and 240g of dimethyl silicone oil into a reaction kettle, and replacing air in the kettle with nitrogen for 3 times; gradually heating to 250 ℃ under continuous stirring, and reacting for 7 hours under heat preservation; cooling, discharging, filtering, washing the solid with dichloromethane and water in sequence, drying to obtain high molecular weight biological radical semi-aromatic polyamide resin with intrinsic viscosity [ eta ]]=0.73dL·g-1Melt index 96 g.10 min-1。
Example 4
Adding 33.05g of eicosanoyl chloride and 60g of cyclohexane into a dissolving kettle, and uniformly stirring to obtain an acyl chloride solution. 16.9g of sodium glutamate, 11.2g of potassium hydroxide and 130g of deionized water are added to a reactor with a stirrer, a thermometer, a condenser and a chilled water cooling device; introducing chilled water, and stirring and reacting for 2 hours at 25 ℃; maintaining stirring and temperature, and dropwise adding the acyl chloride solution into the reactor within 1 hour; after the dropwise addition is finished, the temperature is continuously maintained for reaction for 1 hour; heating to 81 ℃, and evaporating cyclohexane; continuing to heat up, and aging the reaction solution for 1 hour at 90 ℃; filtering while the solution is hot, and cooling to 30 ℃; adding phosphoric acid with the concentration of 1.0mol/L into the filtrate until the PH value is 1, standing for 12 hours at room temperature, and fully separating out a product; the monomer is obtained by filtering, washing and drying.
Adding 22.05g of the monomer, 84.8g of diisopropyl 2, 5-furandicarboxylate, 83.4g of decamethylenediamine, 1.5g of sodium phosphate, 2.5g of decanoic acid and 75g of isopropanol into a reaction kettle, introducing nitrogen, stirring, and heating to 60 ℃ within 0.5 hour; stopping introducing nitrogen, sealing the reaction kettle, heating to 210 ℃ within 2 hours, and maintaining the temperature for reaction for 4 hours; opening an exhaust valve, discharging mixed steam of alcohol and water within 2 hours to reduce the pressure in the kettle to 0.8MPa, and maintaining the temperature not to exceed 245 ℃; closing an exhaust valve, heating to 260 ℃, and maintaining the temperature for reaction for 1 hour to homogenize the materials; then cooling to room temperature, discharging, and drying the product until the water content is less than or equal to 0.3 percent to obtain the bio-based semi-aromatic polyamide prepolymer.
Adding 20g of the prepolymer into a quartz reaction tube, gradually heating to 260 ℃ under the protection of argon, and carrying out heat preservation reaction for 8 hours; cooling and discharging to obtain high molecular weight bio-based semi-aromatic polyamide resin with intrinsic viscosity [ eta ]]=0.98dL·g-1。
Example 5
Adding 19.05kg of decanoyl chloride and 12.00kg of dichloromethane into a dissolving kettle, and uniformly stirring to obtain an acyl chloride solution. 16.90kg of sodium glutamate, 8.00kg of sodium hydroxide and 35.00kg of deionized water were added to a reactor equipped with a stirrer, a thermometer, a condenser and a chilled water cooling device; introducing chilled water, and stirring and reacting for 2 hours at the temperature of 30 ℃; maintaining stirring and temperature, and dropwise adding the acyl chloride solution into the reactor within 2 hours; after the dropwise addition is finished, the temperature is continuously maintained for reaction for 1 hour; heating to 40 ℃, and distilling off dichloromethane; continuing to heat up, and aging the reaction solution at 60 ℃ for 1 hour; filtering while the solution is hot, and cooling to 25 ℃; adding hydrochloric acid with the concentration of 6.0mol/L into the filtrate until the PH value is 1, standing for 24 hours at room temperature, and fully separating out a product; the monomer is obtained by filtering, washing and drying.
Adding 24.08kg of the monomer, 14.72kg of dimethyl 2, 5-furandicarboxylate, 16.80kg of pentanediamine, 0.12kg of sodium tripolyphosphate, 0.60kg of octadecanoic acid and 7.50kg of methanol into a reaction kettle, introducing nitrogen, stirring, and heating to 60 ℃ within 0.5 hour; stopping introducing nitrogen, sealing the reaction kettle, heating to 225 ℃ within 3 hours, and maintaining the temperature for reaction for 3 hours; opening an exhaust valve, discharging mixed steam of alcohol and water within 2 hours to reduce the pressure in the kettle to 0.9MPa, and maintaining the temperature to be not more than 240 ℃; closing an exhaust valve, heating to 250 ℃, and maintaining the temperature for reaction for 2 hours to homogenize the materials; then cooling to room temperature, discharging, and drying the product until the water content is less than or equal to 0.3 percent to obtain the bio-based semi-aromatic polyamide prepolymer.
Adding 35.00kg of the bio-based semi-aromatic polyamide into a reaction extruder, and performing melt extrusion at 320 ℃ and under vacuum of-0.08 MPa; the yield is 10kg/h, and the material retention time is 9 min; cooling, drawing, granulating and drying the extrudate to obtain the high molecular weight bio-based semi-aromatic polyamide resin with intrinsic viscosity [ eta ])]=0.84dL·g-1Melt index 103 g.10 min-1。
TABLE 1 Performance parameters of the bio-based semi-aromatic polyamides obtained in examples 1 to 5
|
Intrinsic viscosity (dL g)-1)
|
Melting Point (. degree.C.)
|
Melt index (g 10 min)-1)
|
Example 1
|
0.81
|
306
|
84
|
Example 2
|
0.83
|
287
|
302
|
Example 3
|
0.73
|
312
|
96
|
Example 4
|
0.98
|
311
|
-
|
Example 5
|
0.84
|
304
|
103 |
a. Intrinsic viscosity test: and (3) dissolving the sample in concentrated sulfuric acid at the temperature of 30 +/-0.1 ℃, testing in an Ubbelohde viscometer, and calculating by adopting a one-point method.
b. Melting point test: in the nitrogen atmosphere, the heating rate and the cooling rate are both 10 ℃/min, and a melting peak of a DSC second heating curve is taken.
c. Melt index test conditions: capillary diameter 2.095mm, 5kg load. Examples 1, 2,5 were tested at 325 ℃, example 3 at 335 ℃ and example 4 was not enough tested.