CN113308084A - Polyether ketone composite material and preparation method thereof - Google Patents
Polyether ketone composite material and preparation method thereof Download PDFInfo
- Publication number
- CN113308084A CN113308084A CN202110712724.9A CN202110712724A CN113308084A CN 113308084 A CN113308084 A CN 113308084A CN 202110712724 A CN202110712724 A CN 202110712724A CN 113308084 A CN113308084 A CN 113308084A
- Authority
- CN
- China
- Prior art keywords
- polyether ketone
- composite material
- liquid crystal
- thermotropic liquid
- crystal polymer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L61/00—Compositions of condensation polymers of aldehydes or ketones; Compositions of derivatives of such polymers
- C08L61/04—Condensation polymers of aldehydes or ketones with phenols only
- C08L61/16—Condensation polymers of aldehydes or ketones with phenols only of ketones with phenols
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L101/00—Compositions of unspecified macromolecular compounds
- C08L101/12—Compositions of unspecified macromolecular compounds characterised by physical features, e.g. anisotropy, viscosity or electrical conductivity
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Polyethers (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
Abstract
The invention relates to a polyether ketone composite material and a preparation method thereof, wherein the preparation method of the polyether ketone composite material comprises the following steps: adding thermotropic liquid crystal polymer with the particle size less than 100nm in the in-situ polymerization process of the polyether ketone to compound the polyether ketone and the thermotropic liquid crystal polymer to obtain a reactant; and separating the reactants to remove free thermotropic liquid crystal polymer and polyether ketone to obtain the polyether ketone composite material. The preparation method of the polyether ketone composite material can improve the compatibility of the polyether ketone and the thermotropic liquid crystal polymer, so that the polyether ketone composite material does not split phases and the melt viscosity is obviously reduced.
Description
Technical Field
The invention relates to the field of composite materials, in particular to a polyether ketone composite material and a preparation method thereof.
Background
Polyether ketone (PEKK) is a novel special engineering plastic, is known as a material of a pyramid tip, has excellent mechanical property, self-lubricating property, chemical corrosion resistance, high temperature resistance, radiation resistance and the like, is a thermoplastic semi-crystalline material, has multiple forming and processing modes and strong plasticity, and has extremely high requirements in the fields of chemical corrosion resistance, aerospace, electronic and electrical appliances, automobiles, medical appliances and the like. However, the chemical structure of polyetherketoneketone itself determines its high viscosity in the molten state, making its shaping and processing difficult, which limits its application to some extent.
Thermotropic Liquid Crystal Polymer (TLCP) is high-strength and high-modulus engineering plastic developed in the later 70 years of the last century, has a plurality of excellent properties, is usually compounded with thermoplastic materials to improve the properties of the thermoplastic materials, however, the thermotropic liquid crystal polymer has the problem of poor compatibility when compounded with the thermoplastic materials, is easy to generate phase separation, and is difficult to exert the modification effect of the thermotropic liquid crystal polymer on the thermoplastic materials.
Disclosure of Invention
Therefore, a polyether ketone composite material and a preparation method thereof are needed, wherein the compatibility of the polyether ketone and the thermotropic liquid crystal polymer can be improved, the polyether ketone composite material is free from phase separation, and the melt viscosity is remarkably reduced.
A preparation method of a polyether ketone composite material comprises the following steps:
mixing a thermotropic liquid crystal polymer with a reaction monomer of polyether ketone for in-situ polymerization to obtain a reactant, wherein the particle size of the thermotropic liquid crystal polymer is less than 100 nm;
and separating the reactants to remove the free thermotropic liquid crystal polymer and the free polyether ketone to obtain the polyether ketone composite material.
In one embodiment, the method further comprises the step of performing superfine treatment on the thermotropic liquid crystal polymer to obtain the thermotropic liquid crystal polymer with the particle size of less than 100 nm.
In one embodiment, the thermotropic liquid crystal polymer is ultrafined by at least one of jet milling, colloid milling and emulsification.
In one embodiment, the step of mixing the thermotropic liquid crystalline polymer with the reactive monomer of polyetherketoneketone for in situ polymerization comprises: mixing a catalyst, a solvent and the thermotropic liquid crystal polymer, cooling to-10 to-15 ℃, adding terephthaloyl chloride, isophthaloyl chloride and diphenyl ether, reacting for 1 to 2 hours, heating to 10 to 30 ℃, and continuing to react for 10 to 20 hours.
In one embodiment, the step of separating the reactants is performed by settling separation.
In one embodiment, the step of separating the reactants comprises:
providing a separation solution, wherein the separation solution is not reactive with both the polyetherketoneketone and the thermotropic liquid crystal polymer, and the density of the separation solution is between the density of the polyetherketoneketone and the density of the thermotropic liquid crystal polymer;
and (3) placing the reactants in the separation solution, stirring, standing for layering, and removing free thermotropic liquid crystal polymer and free polyether ketone.
In one embodiment, the separation solution is selected from at least one of an aqueous sodium hydroxide solution and an aqueous sodium chloride solution.
In one embodiment, in the polyether ketone composite material, the thermotropic liquid crystal polymer accounts for 1-50% by mass; and/or the presence of a catalyst in the reaction mixture,
the melting point temperature of the polyether ketone is in the liquid crystal state temperature interval of the thermotropic liquid crystal polymer; and/or the presence of a catalyst in the reaction mixture,
the thermotropic liquid crystal polymer has a density of 1.4g/cm3~1.7g/cm3The density of the polyether ketone is 1.2g/cm3~1.3g/cm3。
In one embodiment, the method further comprises the following steps: and extruding and granulating the polyether ketone composite material.
In one embodiment, before the step of separating the reactants, the method further comprises: and a step of pulverizing the reactant.
In one embodiment, the method further comprises the step of purifying the polyether ketone composite material.
In one embodiment, the step of purifying comprises: and respectively cleaning the polyether ketone composite material by adopting methanol and water, and then drying.
A polyether ketone composite material is prepared by the preparation method of the polyether ketone composite material.
The preparation method of the polyether ketone composite material comprises the steps of mixing the thermotropic liquid crystal polymer with the particle size smaller than 100nm with the reaction monomer of polyether ketone for in-situ polymerization, enabling the polymerization reaction to occur on the surface of the thermotropic liquid crystal polymer, and enabling the polyether ketone to deposit on the surface of the thermotropic liquid crystal polymer, so that the thermotropic liquid crystal polymer and the polyether ketone are compounded at the molecular level, the compatibility of the composite material is improved, and phase splitting is avoided. And then separating reactants, and removing free polyether ketone and free thermotropic liquid crystal polymer in the reaction, so as to avoid phase separation of the free polyether ketone and the free thermotropic liquid crystal polymer in the composite material and influence on the performance of the composite material, thereby utilizing the excellent melt fluidity of the thermotropic liquid crystal polymer, greatly reducing the melt viscosity of the whole composite material and improving the processing performance of the composite material. Therefore, the preparation method of the polyether ketone composite material can improve the compatibility of the polyether ketone and the thermotropic liquid crystal polymer, so that the polyether ketone composite material does not split phases and the melt viscosity is obviously reduced.
Drawings
FIG. 1 is a process flow diagram of one embodiment of a method for making a polyetherketoneketone composite;
FIG. 2 is a picture of the polyetherketoneketone composites prepared in example 4 and comparative example 2 under a microscope of come from super field depth;
FIG. 3 is a rheological profile of polyetherketoneketone prepared in example 2 and polyetherketoneketone composites prepared in examples 4-6, 10 and 1-3 at different shear rates;
FIG. 4 is a graph of the rheology of the polyetherketoneketone prepared in example 3 and the polyetherketoneketone composites prepared in examples 7-9 at different shear rates.
Detailed Description
In order that the invention may be more fully understood, reference will now be made to the following description taken in conjunction with the accompanying drawings. The detailed description sets forth the preferred embodiments of the invention. This invention may, however, be embodied in many different forms and should not be construed as limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete.
Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. The terminology used in the description of the invention herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the invention.
The thermotropic liquid crystal polymer is an engineering plastic with high strength and high modulus, the melt viscosity is low in a liquid crystal area, a molecular chain has high orientation, and the performance of the polymer is improved. Thermotropic liquid crystal polymers are thermoplastic, and the thermotropic liquid crystal polymers and thermoplastic materials are compounded to prepare the composite material, so that the fluidity of a polymer melt can be greatly improved, and simultaneously, the thermotropic liquid crystal polymers and the thermoplastic materials can form orientation and fiber formation to a certain extent under the action of external force in the processing processes of extrusion, injection molding and the like, thereby improving the processing performance and mechanical property of a matrix material.
However, when the thermotropic liquid crystal polymer and the polyether ketone are blended to prepare the composite material, the problems of poor compatibility and easy phase separation exist, so that the performance of the prepared composite material is poor. Therefore, in this embodiment, the inventors improve the method of compounding the thermotropic liquid crystal polymer with the polyetherketoneketone, so that the thermotropic liquid crystal polymer can be uniformly mixed and dispersed with the polyetherketoneketone, and the performance of the composite material is improved.
Specifically, referring to fig. 1, a preparation method of a polyetherketoneketone composite material according to an embodiment includes the following steps:
step S110: mixing the thermotropic liquid crystal polymer with a reaction monomer of polyether ketone for in-situ polymerization to obtain a reactant.
Wherein the particle size of the thermotropic liquid crystal polymer is less than 100 nm.
Specifically, the step of mixing the thermotropic liquid crystal polymer and the reaction monomer of polyether ketone for in-situ polymerization comprises the following steps: mixing a catalyst, a solvent and a thermotropic liquid crystal polymer, cooling to-10 to-15 ℃, adding terephthaloyl chloride, isophthaloyl chloride and diphenyl ether, reacting for 1 to 2 hours, and heating to 10 to 30 ℃ to continue reacting for 10 to 20 hours.
In one embodiment, the catalyst is aluminum chloride. The solvent is a mixture of dichloroethane and N-methylpyrrolidone. Furthermore, the mass ratio of the terephthaloyl chloride to the isophthaloyl chloride is 80: 20-60: 40. For example, the mass ratio of terephthaloyl chloride to isophthaloyl chloride is 80:20, 70:30, 60:40, etc. The crystallization behavior, the processing temperature, the melting point, the use temperature and the like of the material are changed by adjusting the mass ratio of the terephthaloyl chloride to the isophthaloyl chloride so as to meet different requirements.
Specifically, before step S110, the method further includes: the thermotropic liquid crystal polymer is subjected to superfine treatment to obtain the thermotropic liquid crystal polymer with the particle size less than 100 nm. In-situ polymerization is that reaction monomers, catalysts and the like are all added into a disperse phase, and because the monomers or prepolymers are soluble in a single phase and polymers of the monomers or prepolymers are insoluble in the whole system, polymerization reaction occurs on the disperse phase, and the polymers are deposited on the surface of the disperse phase.
Specifically, the thermotropic liquid crystal polymer is subjected to ultrafine processing by at least one of a jet milling method, a colloid mill method and an emulsification method. For example, the ultrafine treatment is carried out in a jet mill or an emulsifying machine. Preferably, the thermotropic liquid crystal polymer is subjected to superfine treatment by adopting a jet milling mode.
Further, the method further comprises a drying step after the step of performing ultrafine processing on the thermotropic liquid crystal polymer. Further, it was dried to constant weight.
The thermotropic liquid crystal polymer and polyether ketone composite material prepared by the in-situ polymerization method is compounded on a molecular level instead of the traditional physical blending, solves the problem of poor compatibility when the thermotropic liquid crystal polymer and a thermoplastic material are blended, avoids phase splitting, greatly reduces the melt viscosity of the whole composite material, improves the processing performance of the composite material, reduces the abrasion and energy consumption on equipment, greatly reduces the cost in molding processing, improves the mechanical property of the composite material, and has wide application prospect.
Step S120: and (4) crushing the reactant.
The reactant is crushed, so that on one hand, the composite material, the free polyether ketone and the free thermotropic liquid crystal polymer can be conveniently separated by a sedimentation method in the subsequent process, and on the other hand, impurities in the reactant can be conveniently removed by cleaning in the subsequent process, and the composite material can be conveniently purified.
Specifically, the reactant is pulverized until the particle size is 100nm or less.
Further, the pulverization treatment is at least one of colloid milling and emulsification.
Step S130: and separating the reactants to remove the free thermotropic liquid crystal polymer and the free polyether ketone to obtain the polyether ketone composite material.
In the step of separating the mixture, a settling separation method is adopted. Specifically, the sedimentation separation method may be gravity sedimentation or centrifugal sedimentation, and among them, gravity sedimentation is preferable.
Specifically, the step of separating the reactants comprises:
providing a separation solution, wherein the separation solution is not reacted with the polyether ketone and the thermotropic liquid crystal polymer, and the density of the separation solution is between that of the polyether ketone and that of the thermotropic liquid crystal polymer;
and (3) placing the reactants into a separation solution, stirring, standing for layering, and separating the free thermotropic liquid crystal polymer and the polyether ketone.
The settling separation method is to prepare a solution which does not react with two resins, control the density of the solution to be between the two pure resins and to be close to the density of the composite material resin, and then separate the two resins according to the phenomena of floating, suspending and settling caused by different densities.
Specifically, the thermotropic liquid crystalline polymer had a density of 1.4g/cm3~1.7g/cm3. Preferably, the thermotropic liquid crystalline polymer has a density of 1.7g/cm3. The density of the polyetherketoneketone is 1.2g/cm3~1.3g/cm3. The density difference between the thermotropic liquid crystal polymer with the density and the polyether ketone is large, and the thermotropic liquid crystal polymer with the density is convenient to separate by a sedimentation method.
In one embodiment, the polyetherketoneketone has a density of 1.3g/cm3The density of the thermotropic liquid crystal polymer used is 1.7g/cm3The density of the composite material is 1.5g/cm3And the density of the composite material resin can be changed according to the mass percent of the thermotropic liquid crystal polymer in the composite material, but is always positioned between the two polymers.
Specifically, the separation solution is at least one selected from an aqueous sodium hydroxide solution and an aqueous sodium chloride solution. Wherein the density of the separation solution can be changed by adjusting the content of the solute in the solution so that the density of the separation solution is similar to that of the composite material.
Step S140: and purifying the polyether ketone composite material.
Wherein the purification step comprises: and respectively cleaning the polyether ketone composite material by adopting methanol and water, and then drying. Impurities such as a catalyst remaining in the reaction can be removed by the purification treatment.
Step S150: and extruding and granulating the polyether ketone composite material.
Specifically, a twin-screw extruder is used for melt blending.
The polyether ketone composite material prepared by the steps S110 to S140 is a powder material, and the powder material has the problems of difficulty in transportation, difficulty in storage and the like, so that the polyether ketone composite material is extruded and granulated to obtain a granular composite material, and the problems of storage and transportation of the composite material are solved. In addition, the thermotropic liquid crystal polymer in the polyether ketone composite material is oriented and arranged orderly in the extrusion process, so that the mechanical property of the prepared composite material can be further improved. In addition, as the polyether ketone and the thermotropic liquid crystal polymer in the polyether ketone composite material are blended in a molecular level, the polyether ketone and the thermotropic liquid crystal polymer are directly melted and blended, and the problem of phase separation can not occur.
Specifically, the thermotropic liquid crystal polymer accounts for 1-50% of the composite material by mass percent. Preferably, the thermotropic liquid crystal polymer accounts for 20-30% of the composite material by mass percent.
Furthermore, the melting point temperature of the polyether ketone is in the liquid crystal state temperature interval of the thermotropic liquid crystal polymer, so that the thermotropic liquid crystal polymer is in a liquid crystal state in the melting and extruding process, is aligned and arranged orderly, and the mechanical property of the composite material is improved. For example, in the raw materials for preparing the polyether ketone, the mass ratio of the terephthaloyl chloride to the isophthaloyl chloride is 80:20, and the thermotropic liquid crystal polymer used can be a thermotropic liquid crystal polymer with the mark of KH of Jiangsu Wott special material manufacturing company Limited; in the raw materials for preparing the polyether ketone, the mass ratio of the terephthaloyl chloride to the isophthaloyl chloride is 70:30, and the used thermotropic liquid crystal polymer can be a thermotropic liquid crystal polymer with the brand number KDI of Jiangsu Wott special material manufacturing company Limited; in the raw materials for preparing the polyether ketone, the mass ratio of the terephthaloyl chloride to the isophthaloyl chloride is 60:40, and the thermotropic liquid crystal polymer used can be a thermotropic liquid crystal polymer with the brand of KD of Jiangsu Wott special material manufacturing company Limited.
The preparation method of the polyether ketone composite material at least has the following advantages:
(1) the method adopts an in-situ polymerization method to prepare the thermotropic liquid crystal polymer and polyether ketone composite material, is the composite on the molecular level rather than the traditional physical blending, solves the problem of poor compatibility when the thermotropic liquid crystal polymer and the thermoplastic material are blended, and avoids phase splitting.
(2) The preparation method of the polyether ketone composite material compounds polyether ketone and thermotropic liquid crystal polymer, utilizes the excellent melt fluidity of the thermotropic liquid crystal polymer, greatly reduces the melt viscosity of the whole composite material, improves the processing performance of the composite material, reduces the abrasion and energy consumption to equipment, and greatly reduces the cost in molding processing.
(3) The preparation method of the polyether ketone composite material can improve the mechanical property of the composite material and has wide application prospect.
The invention also provides the polyether ketone composite material of the embodiment, which is prepared by the preparation method of the polyether ketone composite material. The polyether ketone composite material has good uniformity, is not easy to phase split, has improved melt fluidity and processability, has excellent mechanical property, and has wide application prospect.
The following are specific examples:
the thermotropic liquid crystalline polymer used in the examples was obtained from Jiangsu Wott Special materials manufacturing Co., Ltd, and was of type KH or KDI.
Example 1
The embodiment provides a preparation method of an ultrafine thermotropic liquid crystal polymer, which comprises the following steps:
weighing thermotropic liquid crystal polymer (TLCP, the mark of which is KH), and performing superfine treatment by using an air flow pulverizer to obtain superfine thermotropic liquid crystal polymer, wherein the particle size of the superfine thermotropic liquid crystal polymer is less than 100 nm.
The thermotropic liquid crystal polymer with the mark KDI is weighed by the same method to be subjected to superfine treatment to obtain the superfine thermotropic liquid crystal polymer (with the mark KDI) with the grain diameter smaller than 100 nm.
Example 2
The embodiment provides a preparation method of polyether ketone powder, which comprises the following steps:
500g of AlCl are respectively added into a 1000mL three-neck bottle with a magnetic stirring and nitrogen guide pipe3500mL of dichloroethane and 125mL of N-methylpyrrolidone, reducing the temperature to-12 ℃, adding 162.4g of terephthaloyl chloride, 40.6g of isophthaloyl chloride and 160mL of diphenyl ether while stirring, reacting for 1.5 hours at the temperature, then heating to room temperature for reacting for 15 hours, and adding 100mL of methanol to quench after the reaction is finished to obtain the productTo a white colloid. Crushing the white colloid, sequentially washing the white colloid with methanol and deionized water, and finally putting the product in an oven to be dried to constant weight at 60 ℃ to obtain polyether ketone powder (T/I is 80/20).
Example 3
The embodiment provides a preparation method of polyether ketone powder, which comprises the following steps:
500g of AlCl are respectively added into a 1000mL three-neck bottle with a magnetic stirring and nitrogen guide pipe3500mL of dichloroethane and 125mL of N-methylpyrrolidone, cooling to-12 ℃ at low temperature, adding 142.1g of terephthaloyl chloride, 60.9g of isophthaloyl chloride and 160mL of diphenyl ether while stirring, reacting at the temperature for 1.5 hours, then heating to room temperature for reacting for 15 hours, and after the reaction is finished, adding 100mL of methanol to quench so as to obtain a white colloid. Crushing the white colloid, sequentially washing the white colloid with methanol and deionized water, and finally putting the product in an oven to be dried to constant weight at 60 ℃ to obtain polyether ketone powder (T/I is 70/30).
Example 4
The embodiment provides a preparation method of a polyether ketone composite material, which comprises the following steps:
41.4g of the ultrafine thermotropic liquid crystalline polymer (having a trade name of KH) prepared in example 1 and 500g of AlCl were charged into a 1000mL three-necked flask equipped with a magnetic stirrer and a nitrogen gas introduction tube, respectively3500mL of dichloroethane and 125mL of N-methylpyrrolidone, cooling to-12 ℃ at low temperature, adding 162.4g of terephthaloyl chloride, 40.6g of isophthaloyl chloride and 160mL of diphenyl ether while stirring, reacting at the temperature for 1.5 hours, then heating to room temperature for reacting for 15 hours, and after the reaction is finished, adding 100mL of methanol to quench so as to obtain a white colloid. And crushing the white colloid to obtain mixture powder.
The powder of the mixture was put into a mixer with a density of 1.5g/cm3The sodium hydroxide solution of (2) is separated by a sedimentation separation method, specifically, the mixture powder is put into a solution having a density of 1.5g/cm3Stirring and dispersing the sodium hydroxide aqueous solution, and standing to generate layering: floating on the upper layer was a density of 1.29g/cm3The middle layer is suspended with the density of 1.29g/cm3To 1.7g/cm3The lower layer is sinking and floating, and the density is 1.7g/cm3The thermotropic liquid crystal polymer and polyether ketone (TLCP/PEKK) composite material alloy is obtained after the thermotropic liquid crystal polymer powder is obtained, the thermotropic liquid crystal polymer and polyether ketone composite material powder is sequentially washed by methanol and deionized water, filtered, placed in a drying oven to be dried to constant weight at 120 ℃, finally melted and blended by a double-screw extruder and granulated.
Example 5
The embodiment provides a preparation method of a polyether ketone composite material, which comprises the following steps:
93.3g of the ultrafine thermotropic liquid crystalline polymer (having a trade name of KH) prepared in example 1 and 500g of AlCl were charged into a 1000mL three-necked flask equipped with a magnetic stirrer and a nitrogen gas introduction tube, respectively3500mL of dichloroethane and 125mL of N-methylpyrrolidone, cooling to-12 ℃ at low temperature, adding 162.4g of terephthaloyl chloride, 40.6g of isophthaloyl chloride and 160mL of diphenyl ether while stirring, reacting at the temperature for 1.5 hours, then heating to room temperature for reacting for 15 hours, and after the reaction is finished, adding 100mL of methanol to quench so as to obtain a white colloid. And crushing the white colloid to obtain mixture powder.
The powder of the mixture was put into a mixer with a density of 1.5g/cm3The sodium hydroxide solution of (2) is separated by a sedimentation separation method, specifically, the mixture powder is put into a solution having a density of 1.5g/cm3Stirring and dispersing the sodium hydroxide aqueous solution, and standing to generate layering: floating on the upper layer was a density of 1.29g/cm3The middle layer is suspended with the density of 1.29g/cm3To 1.7g/cm3The lower layer is sinking and floating, and the density is 1.7g/cm3The thermotropic liquid crystal polymer powder is prepared by obtaining pure thermotropic liquid crystal polymer and polyether ketone composite material powder, sequentially cleaning with methanol and deionized water, filtering, placing the powder in a drying oven to be dried to constant weight at 120 ℃, finally melting and blending by a double-screw extruder, and granulating to obtain the thermotropic liquid crystal polymer and polyether ketone (TLCP/PEKK) composite materialAnd (4) alloying the materials.
Example 6
The embodiment provides a preparation method of a polyether ketone composite material, which comprises the following steps:
159.9g of the ultrafine thermotropic liquid crystalline polymer (having a trade name of KH) prepared in example 1 and 500g of AlCl were charged into a 1000mL three-necked flask equipped with a magnetic stirrer and a nitrogen gas introduction tube, respectively3500mL of dichloroethane and 125mL of N-methylpyrrolidone, cooling to-12 ℃ at low temperature, adding 162.4g of terephthaloyl chloride, 40.6g of isophthaloyl chloride and 160mL of diphenyl ether while stirring, reacting at the temperature for 1.5 hours, then heating to room temperature for reacting for 15 hours, and after the reaction is finished, adding 100mL of methanol to quench so as to obtain a white colloid. The white colloid is smashed to obtain the reactant powder.
The reactant powder was charged to a density of 1.5g/cm3The reaction mixture was separated by sedimentation separation, and specifically, the reaction mixture powder was put into a reactor having a density of 1.5g/cm3Stirring and dispersing the sodium hydroxide aqueous solution, and standing to generate layering: floating on the upper layer was a density of 1.29g/cm3The middle layer is suspended with the density of 1.29g/cm3To 1.7g/cm3The lower layer is sinking and floating, and the density is 1.7g/cm3Separating the thermotropic liquid crystal polymer powder to obtain pure thermotropic liquid crystal polymer and polyether ketone composite material powder, sequentially cleaning with methanol and deionized water, carrying out suction filtration, placing the powder in a drying oven, drying to constant weight at 120 ℃, finally carrying out melt blending by using a double-screw extruder, and granulating to obtain the thermotropic liquid crystal polymer and polyether ketone (TLCP/PEKK) composite material alloy.
Example 7
This example provides a preparation method of a polyetherketoneketone composite material, which is similar to the preparation method of the polyetherketoneketone composite material of example 4, except that the mass of terephthaloyl chloride and isophthaloyl chloride is 142.1g and 60.9g, respectively, and the thermotropic liquid crystal polymer used is the ultrafine thermotropic liquid crystal polymer (brand KDI) prepared in example 1, and the obtained polyetherketoneketone composite material has T/I of 70/30.
Example 8
This example provides a preparation method of a polyetherketoneketone composite material, which is similar to the preparation method of the polyetherketoneketone composite material of example 5, except that the mass of terephthaloyl chloride and isophthaloyl chloride is 142.1g and 60.9g, respectively, and the thermotropic liquid crystal polymer used is the ultrafine thermotropic liquid crystal polymer (brand KDI) prepared in example 1, and the obtained polyetherketoneketone composite material has T/I of 70/30.
Example 9
This example provides a preparation method of a polyetherketoneketone composite material, which is similar to the preparation method of the polyetherketoneketone composite material of example 6, except that the mass of terephthaloyl chloride and isophthaloyl chloride is 142.1g and 60.9g, respectively, and the thermotropic liquid crystal polymer used is the ultrafine thermotropic liquid crystal polymer (brand KDI) prepared in example 1, and the obtained polyetherketoneketone composite material has T/I of 70/30.
Example 10
This example provides a preparation method of a polyetherketoneketone composite material, which is similar to the preparation method of the polyetherketoneketone composite material of example 4, except that the powder of the polyetherketoneketone composite material is purified and dried, and then is not subjected to extrusion granulation. The method comprises the following specific steps:
41.4g of the ultrafine thermotropic liquid crystalline polymer (having a trade name of KH) prepared in example 1 and 500g of AlCl were charged into a 1000mL three-necked flask equipped with a magnetic stirrer and a nitrogen gas introduction tube, respectively3500mL of dichloroethane and 125mL of N-methylpyrrolidone, cooling to-12 ℃ at low temperature, adding 162.4g of terephthaloyl chloride, 40.6g of isophthaloyl chloride and 160mL of diphenyl ether while stirring, reacting at the temperature for 1.5 hours, then heating to room temperature for reacting for 15 hours, and after the reaction is finished, adding 100mL of methanol to quench so as to obtain a white colloid. The white colloid is smashed to obtain the reactant powder.
The reactant powder was charged to a density of 1.5g/cm3The reaction mixture was separated by sedimentation separation, and specifically, the reaction mixture powder was put into a reactor having a density of 1.5g/cm3Stirring and dispersing the sodium hydroxide aqueous solution, and standing to generate layering: floating on the upper layer was a density of 1.29g/cm3The middle layer is suspended with the density of 1.29g/cm3To 1.7g/cm3The lower layer is sinking and floating, and the density is 1.7g/cm3Separating the thermotropic liquid crystal polymer powder to obtain pure thermotropic liquid crystal polymer and polyether ketone composite material powder, sequentially cleaning the powder by using methanol and deionized water, performing suction filtration, and placing the powder in a drying oven to dry the powder to constant weight at 120 ℃ to obtain the thermotropic liquid crystal polymer and polyether ketone (TLCP/PEKK) composite material.
Comparative example 1
Comparative example 1 provides a preparation method of a polyetherketoneketone composite material, similar to the preparation method of the polyetherketoneketone composite material of example 4, except that the thermotropic liquid crystalline polymer (having a trade name of KH) used in this example was not ultrafinely treated and had a particle size of 300 to 500 μm.
Comparative example 2
Comparative example 2 provides a method of preparing a polyetherketoneketone composite comprising the steps of:
373.24g of the polyether ketone powder prepared in the example 2 and 41.4g of the superfine thermotropic liquid crystal polymer (with the mark of KH) prepared in the example 1 are melted and blended by a double-screw extruder, and then the thermotropic liquid crystal polymer and polyether ketone (TLCP/PEKK) composite material alloy is obtained after granulation.
Comparative example 3
Comparative example 3 provides a method of preparing a polyetherketoneketone composite comprising the steps of:
41.4g of the ultrafine thermotropic liquid crystalline polymer (having a trade name of KH) prepared in example 1 and 500g of AlCl were charged into a 1000mL three-necked flask equipped with a magnetic stirrer and a nitrogen gas introduction tube, respectively3500mL of dichloroethane and 125mL of N-methylpyrrolidone, reducing the temperature to-12 ℃ while stirring, adding 162.4g of terephthaloyl chloride, 40.6g of isophthaloyl chloride and 160mL of diphenyl ether, reacting at the temperature for 1.5 hours, then heating to room temperature for reacting for 15 hours, and adding the mixture after the reaction is finishedQuenching with 100mL of methanol gave a white colloid. Crushing the white colloid to obtain reactant powder, sequentially cleaning with methanol and deionized water, performing suction filtration, placing the powder in an oven, drying to constant weight at 120 ℃, finally performing melt blending by using a double-screw extruder, and granulating to obtain the thermotropic liquid crystal polymer and polyether ketone (TLCP/PEKK) composite material alloy.
The following are test sections:
(1) the compatibility of the polyetherketoneketone composite materials prepared in example 4 and comparative example 2 was tested at 3000 times magnification using a superfield come microscope, and the experimental data shown in fig. 2 were obtained.
From the two photographs in fig. 2, it can be seen that the left side of the TLCP/PEKK composite material manufactured by the embodiment 4 of the present invention has particularly good compatibility, and the TLCP is arranged in the PEKK resin in an oriented state and has no phase separation structure; the right side of the TLCP/PEKK composite material prepared by adopting the conventional industrial physical blending of the comparative example 2 has an obvious two-phase structure and poor compatibility.
(2) Using 10 thermotropic liquid crystal polymer and polyetherketoneketone composites prepared in examples 4 to 10 and comparative examples 1 to 3 and 2 samples of different grades of polyetherketoneketone (PEKK, T/I: 80/20 and T/I: 70/30) pure resins in examples 2 to 3, rheological property tests were performed under different shear rates, the test data are shown in table 1 and table 2 below, and the test data in table 1 and table 2 were plotted to obtain the rheological curves of the PEKK and the TLCP/PEKK composites at different shear rates as shown in fig. 3 and fig. 4. The test conditions were: the temperature was 390 ℃; the shear rates were 1001/s, 2001/s, 5001/s, 8001/s, 10001/s and 15001/s, respectively.
TABLE 1
TABLE 2
As can be seen from fig. 3 and 4, in the polyetherketoneketone composite materials prepared in the examples, as the mass percentage of the TLCP in the composite material increases, the viscosity of the composite material has a significantly decreasing tendency.
(3) The thermotropic liquid crystal polymer and polyetherketoneketone composite materials prepared in examples 4 to 10 and comparative examples 1 to 3 and 2 pure resin samples of different brands of polyetherketoneketone (PEKK, T/I: 80/20 and T/I: 70/30, respectively) in examples 2 to 3 were subjected to tensile property test, bending property test and heat distortion temperature test to obtain experimental data shown in tables 3 and 4.
TABLE 3
TABLE 4
It can be seen from the table that as the mass percentage of the TLCP in the composite material increases, the tensile strength, tensile modulus, flexural strength, flexural modulus, and heat distortion temperature of the composite material all increase significantly, and the elongation at break decreases slightly.
The technical features of the embodiments described above may be arbitrarily combined, and for the sake of brevity, all possible combinations of the technical features in the embodiments described above are not described, but should be considered as being within the scope of the present specification as long as there is no contradiction between the combinations of the technical features.
The above-mentioned embodiments only express several embodiments of the present invention, so as to understand the technical solutions of the present invention specifically and in detail, but not to be understood as the limitation of the protection scope of the invention. It should be noted that, for a person skilled in the art, several variations and modifications can be made without departing from the inventive concept, which falls within the scope of the present invention. It should be understood that the technical solutions provided by the present invention, which are obtained by logical analysis, reasoning or limited experiments, are within the scope of the appended claims. Therefore, the protection scope of the present invention should be subject to the content of the appended claims, and the description and the drawings can be used for explaining the content of the claims.
Claims (13)
1. The preparation method of the polyether ketone composite material is characterized by comprising the following steps:
mixing a thermotropic liquid crystal polymer with a reaction monomer of polyether ketone for in-situ polymerization to obtain a reactant, wherein the particle size of the thermotropic liquid crystal polymer is less than 100 nm;
and separating the reactants to remove the free thermotropic liquid crystal polymer and the free polyether ketone to obtain the polyether ketone composite material.
2. The method of claim 1, further comprising the step of ultrafining the thermotropic liquid crystalline polymer to obtain a thermotropic liquid crystalline polymer having a particle size of less than 100 nm.
3. The method of claim 2, wherein the thermotropic liquid crystalline polymer is ultrafined by at least one of jet milling, colloid milling and emulsification.
4. The method of claim 1, wherein the step of mixing the thermotropic liquid crystal polymer with the polyether ketone reaction monomer for in situ polymerization comprises: mixing a catalyst, a solvent and the thermotropic liquid crystal polymer, cooling to-10 to-15 ℃, adding terephthaloyl chloride, isophthaloyl chloride and diphenyl ether, reacting for 1 to 2 hours, heating to 10 to 30 ℃, and continuing to react for 10 to 20 hours.
5. The method of claim 1, wherein the step of separating the reactants comprises a settling separation process.
6. The method of claim 5, wherein the step of separating the reactants comprises:
providing a separation solution, wherein the separation solution is not reactive with both the polyetherketoneketone and the thermotropic liquid crystal polymer, and the density of the separation solution is between the density of the polyetherketoneketone and the density of the thermotropic liquid crystal polymer;
and (3) placing the reactants in the separation solution, stirring, standing for layering, and removing free thermotropic liquid crystal polymer and free polyether ketone.
7. The method according to claim 6, wherein the separation solution is at least one selected from the group consisting of an aqueous sodium hydroxide solution and an aqueous sodium chloride solution.
8. The method for preparing the polyether ketone composite material according to any one of claims 1 to 7, wherein the mass percent of the thermotropic liquid crystal polymer in the polyether ketone composite material is 1-50%; and/or the presence of a catalyst in the reaction mixture,
the melting point temperature of the polyether ketone is in the liquid crystal state temperature interval of the thermotropic liquid crystal polymer; and/or the presence of a catalyst in the reaction mixture,
the thermotropic liquid crystal polymer has a density of 1.4g/cm3~1.7g/cm3The density of the polyether ketone is 1.2g/cm3~1.3g/cm3。
9. The method for preparing the polyether ketone composite material as claimed in any one of claims 1 to 7, further comprising: and extruding and granulating the polyether ketone composite material.
10. The method for preparing a polyetherketoneketone composite material as claimed in any one of claims 1 to 7, wherein the step of separating the reactants is preceded by the steps of: and a step of pulverizing the reactant.
11. The method for preparing a polyetherketoneketone composite material according to any one of claims 1 to 7, further comprising a step of purifying the polyetherketoneketone composite material.
12. The method of making a polyetherketoneketone composite material of claim 11 wherein the step of purifying comprises: and respectively cleaning the polyether ketone composite material by adopting methanol and water, and then drying.
13. A polyether ketone composite material, which is prepared by the preparation method of the polyether ketone composite material as claimed in any one of claims 1 to 12.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110712724.9A CN113308084B (en) | 2021-06-25 | 2021-06-25 | Polyether ketone composite material and preparation method thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110712724.9A CN113308084B (en) | 2021-06-25 | 2021-06-25 | Polyether ketone composite material and preparation method thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
CN113308084A true CN113308084A (en) | 2021-08-27 |
CN113308084B CN113308084B (en) | 2022-12-02 |
Family
ID=77380423
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202110712724.9A Active CN113308084B (en) | 2021-06-25 | 2021-06-25 | Polyether ketone composite material and preparation method thereof |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN113308084B (en) |
Citations (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5006402A (en) * | 1989-04-28 | 1991-04-09 | The University Of Akron | Wholly aromatic polyester fiber-reinforced high performance thermoplastic and process for preparing same |
CN1198453A (en) * | 1997-05-05 | 1998-11-11 | 中国科学院化学研究所 | Polyether ether ketone compound material modified by thermotropic liquid crystal polymer |
WO2008123449A1 (en) * | 2007-03-29 | 2008-10-16 | Asahi Kasei Chemicals Corporation | Resin pellet reinforced with long-fiber filler |
US20140243485A1 (en) * | 2013-02-22 | 2014-08-28 | Ticona Llc | High Performance Polymer Composition with Improved Flow Properties |
US20160102173A1 (en) * | 2014-10-08 | 2016-04-14 | Ticona Llc | Dispersant for Use in Synthesis of Polyaryletherketones |
CN105524409A (en) * | 2015-11-03 | 2016-04-27 | 南京肯特复合材料有限公司 | Potassium titanate whisker reinforced PEEK composite material and preparation method thereof |
CN105713343A (en) * | 2014-12-05 | 2016-06-29 | 黑龙江鑫达企业集团有限公司 | High-mobility TLCP/PES/PEEK composite material and preparation method thereof |
US20170145208A1 (en) * | 2015-11-20 | 2017-05-25 | Ticona Llc | High Flow Polyaryletherketone Composition |
CN107556696A (en) * | 2017-08-16 | 2018-01-09 | 宜宾天原集团股份有限公司 | A kind of high fluidity polyether-ether-ketone composite material formula and preparation method thereof |
JP6753550B2 (en) * | 2018-02-21 | 2020-09-09 | Dic株式会社 | Moisture curable polyurethane hot melt resin composition |
-
2021
- 2021-06-25 CN CN202110712724.9A patent/CN113308084B/en active Active
Patent Citations (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5006402A (en) * | 1989-04-28 | 1991-04-09 | The University Of Akron | Wholly aromatic polyester fiber-reinforced high performance thermoplastic and process for preparing same |
CN1198453A (en) * | 1997-05-05 | 1998-11-11 | 中国科学院化学研究所 | Polyether ether ketone compound material modified by thermotropic liquid crystal polymer |
WO2008123449A1 (en) * | 2007-03-29 | 2008-10-16 | Asahi Kasei Chemicals Corporation | Resin pellet reinforced with long-fiber filler |
US20140243485A1 (en) * | 2013-02-22 | 2014-08-28 | Ticona Llc | High Performance Polymer Composition with Improved Flow Properties |
US20160102173A1 (en) * | 2014-10-08 | 2016-04-14 | Ticona Llc | Dispersant for Use in Synthesis of Polyaryletherketones |
CN105713343A (en) * | 2014-12-05 | 2016-06-29 | 黑龙江鑫达企业集团有限公司 | High-mobility TLCP/PES/PEEK composite material and preparation method thereof |
CN105524409A (en) * | 2015-11-03 | 2016-04-27 | 南京肯特复合材料有限公司 | Potassium titanate whisker reinforced PEEK composite material and preparation method thereof |
US20170145208A1 (en) * | 2015-11-20 | 2017-05-25 | Ticona Llc | High Flow Polyaryletherketone Composition |
CN107556696A (en) * | 2017-08-16 | 2018-01-09 | 宜宾天原集团股份有限公司 | A kind of high fluidity polyether-ether-ketone composite material formula and preparation method thereof |
JP6753550B2 (en) * | 2018-02-21 | 2020-09-09 | Dic株式会社 | Moisture curable polyurethane hot melt resin composition |
Non-Patent Citations (4)
Title |
---|
NAFFAKH, M,等: "Kinetic analysis of thermo-oxidative degradation of PEEK/thermotropic liquid crystalline polymer blends", 《 POLYMER ENGINEERING AND SCIENCE》 * |
SON, Y,等: "Improvement of the processability of poly(ether ketone ketone) by the addition of a thermotropic liquid crystalline polymer", 《 POLYMER ENGINEERING AND SCIENCE》 * |
YAZAKI, H,等: "EFFECTS OF POLY(ETHER ETHER KETONE) OLIGOMERS ON THE MECHANICAL-PROPERTIES OF POLY(ETHER ETHER KETONE) - THERMOTROPIC LIQUID-CRYSTALLINE COPOLYESTER BLENDS", 《KOBUNSHI RONBUNSHU》 * |
李刚,等: "新型聚芳醚酮与热致性液晶高聚物共混物流变性能和力学性能的研究", 《高分子学报》 * |
Also Published As
Publication number | Publication date |
---|---|
CN113308084B (en) | 2022-12-02 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Chang et al. | An exfoliation of organoclay in thermotropic liquid crystalline polyester nanocomposites | |
Chang et al. | Poly (butylene terephthalate)/organoclay nanocomposites prepared by in situ interlayer polymerization and its fiber (II) | |
EP0044175B2 (en) | Blend of polycarbonate and wholly aromatic polyester | |
EP1621581A1 (en) | Liquid crystaline polyester resin composition | |
EP0154065B1 (en) | Blend of polyalkylene terephthalate and high molecular weight wholly aromatic polyester and process for producing the same | |
WO2010053110A1 (en) | Aliphatic polycarbonate complex derived from carbon dioxide, and process for producing same | |
DE69919450T2 (en) | Aromatic liquid crystalline polyesters and resin composition made therefrom | |
CN103088460B (en) | A kind of High-strength industrial polyester fiber and preparation method thereof | |
CN112980182B (en) | COFs/nylon 6 composite material and preparation method thereof | |
JP4034019B2 (en) | Method for producing liquid crystalline polyester | |
Reinaldo et al. | Rheological, mechanical and morphological properties of poly (methyl methacrylate)/poly (ethylene terephthalate) blend with dual reactive interfacial compatibilization | |
CN107236298B (en) | Modification and coloring method of nylon composite material | |
JPS60139754A (en) | Composition | |
CN113308084B (en) | Polyether ketone composite material and preparation method thereof | |
Sweah et al. | Preparation and study of mechanical and thermal properties of polymer blends from recycled materials of polystyrene and polymethylmethacryalate with different ratio of diethylmalonate | |
CN110951222A (en) | High-impact-resistance regenerated PET material and preparation method thereof | |
CN102260405A (en) | Preparation method of polylactic acid/attapulgite clay composite material | |
CN103074697A (en) | Melt direct spinning moderately strong polyster fiber and preparation method thereof | |
CN101759967A (en) | Halogen-free warp-resistant PBT of excellent electrical properties and preparing technique thereof | |
CN113493529B (en) | Preparation method of polybutadiene latex with double particle size distribution | |
Illescas et al. | The role of polyhedral oligomeric silsesquioxane on the thermo-mechanical properties of polyoxymethylene copolymer based nanocomposites | |
US11965089B2 (en) | Microspheric ionomer having cross-linked structure, preparation method therefor, applications thereof, and preparation system thereof | |
CN108530850B (en) | A kind of fire retardant PBT with no halogen/ASA alloy and preparation method thereof | |
Magagnini et al. | A study of polycarbonate‐liquid crystal polymer blends | |
JPH0127103B2 (en) |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |