阅读说明：本技术 一种以采用1-丁基-3-甲基咪唑溴盐制备的聚醚醚酮作为原料的选择性激光烧结的应用 (Application of selective laser sintering by using polyether-ether-ketone prepared from 1-butyl-3-methylimidazole bromine salt as raw material ) 是由 尤庆亮 肖标 钱新华 周瑞雪 何丹 邹立勇 于 2017-11-24 设计创作，主要内容包括：本发明公开了一种以采用1-丁基-3-甲基咪唑溴盐制备的聚醚醚酮作为原料的选择性激光烧结的应用,属于耐热高分子材料领域。一种以采用1-丁基-3-甲基咪唑溴盐制备的聚醚醚酮作为原料的选择性激光烧结的应用,所述应用包括：将1-丁基-3-甲基咪唑溴盐作为溶剂合成聚醚醚酮。将合成的聚醚醚酮作为选择性激光烧结技术的原料时,可得到粒径分布在30～70μm的粉末状的聚醚醚酮得纯净的产物,且聚醚醚酮的表面光滑,为类球形,且具有高粉料流动性,这使得该聚醚醚酮符合选择性激光烧结技术的要求。(The invention discloses application of selective laser sintering by taking polyether-ether-ketone prepared from 1-butyl-3-methylimidazolium bromide as a raw material, belonging to the field of heat-resistant high polymer materials. Use of a selective laser sintering starting from polyetheretherketone prepared with 1-butyl-3-methylimidazolium bromide, said use comprising: taking 1-butyl-3-methylimidazole bromine salt as a solvent to synthesize the polyetheretherketone. When the synthesized polyetheretherketone is used as a raw material of a selective laser sintering technology, a pure product of powdered polyetheretherketone with the particle size distribution of 30-70 mu m can be obtained, and the polyetheretherketone has a smooth surface, is spherical-like and has high powder fluidity, so that the polyetheretherketone meets the requirements of the selective laser sintering technology.)

1. Use of a selective laser sintering starting from polyetheretherketone prepared with 1-butyl-3-methylimidazolium bromide, characterized in that it comprises the following steps:

(1) under inert gas, adding a difluoro monomer into a solvent, continuously stirring at 25-60 ℃ to fully dissolve the difluoro monomer into the solvent to obtain a difluoro solution, and synthesizing polyether-ether-ketone by using 1-butyl-3-methylimidazole bromine salt as the solvent;

(2) under inert gas, uniformly mixing a diphenol monomer, anhydrous potassium carbonate and anhydrous sodium carbonate, adding the mixture into the difluoro solution, fully dissolving the diphenol monomer, the anhydrous potassium carbonate and the anhydrous sodium carbonate in the difluoro solution to obtain a mixed solution, heating the mixed solution to 140-200 ℃, reacting until no carbon dioxide gas is generated, finishing the reaction to obtain a reaction product, and purifying the reaction product to obtain the polyether-ether-ketone with the particle size distribution of 30-70 mu m.

2. The use of claim 1, wherein in the step (2), the specific method for adding the diphenol monomer, anhydrous potassium carbonate and anhydrous sodium carbonate into the difluoro solution after uniformly mixing comprises the following steps: uniformly mixing diphenol monomer, anhydrous potassium carbonate and anhydrous sodium carbonate, adding the mixture into the difluoro solution for 3-5 times respectively, wherein the interval time between two adjacent times of adding is 20-40 min, and continuously stirring after each time of adding.

3. The use of claim 1, wherein in the step (2), the specific method for obtaining the mixed solution is as follows: uniformly mixing the diphenol monomer, the anhydrous potassium carbonate and the anhydrous sodium carbonate, adding the mixture into the difluoro solution, heating to 120-140 ℃, and preserving heat for 1-3 hours to fully dissolve the diphenol monomer, the anhydrous potassium carbonate and the anhydrous sodium carbonate in the difluoro solution to obtain a mixed solution.

4. The use of claim 3, wherein the specific method of step (2) comprises: uniformly mixing the diphenol monomer, the anhydrous potassium carbonate and the anhydrous sodium carbonate, adding the mixture into the difluoro solution, heating the mixture from room temperature to 120-140 ℃ at the speed of 5-20 ℃/min, preserving the heat for 1-3 hours, fully dissolving the diphenol monomer, the anhydrous potassium carbonate and the anhydrous sodium carbonate in the difluoro solution to obtain a mixed solution, and heating the mixed solution to 140-200 ℃ at the speed of 2-10 ℃/min.

5. The use according to claim 1, wherein said difluoro monomer is 4,4 '-difluorobenzophenone, 3' -difluorobenzophenone, 2, 3-difluorobenzophenone, 2, 5-difluorobenzaldehyde, 2, 6-difluorobenzaldehyde, bis (4-fluorophenyl) ether, 4 '-difluorodiphenylmethane, 2, 5-difluoroanisole, 2, 5-difluorobenzophenone, 3, 5-difluorobenzonitrile, methyl 2, 5-difluorobenzoate, ethyl 2, 4-difluorobenzoate or 4,4' -difluorobenzylpiperazine.

6. Use according to claim 1, wherein the diphenol monomer is 1, 4-benzenediol, bisphenol a, 1, 5-naphthalenediol, 2, 6-naphthalenediol, tert-butylhydroquinone, 2-methoxyhydroquinone, trimethylhydroquinone, tetramethylhydroquinone, 2, 5-di-tert-octylhydroquinone, 2, 5-di-iso-octylhydroquinone, 2, 5-diphenylhydroquinone or 2, 5-di-tert-amylhydroquinone.

7. Use according to claim 1, wherein the purification comprises: filtration and washing, the filtration and washing comprising: adding ethanol into the reaction product, carrying out primary filtration to obtain primary filtered filter residue, washing the primary filtered filter residue with ethanol and acetone respectively for 1-2 times, then carrying out secondary filtration to obtain secondary filtered filter residue, and washing the secondary filtered filter residue with deionized water twice.

8. The use of claim 7, wherein the purifying further comprises: drying, the method of drying comprising: and (3) drying the washed product at 120 ℃ in vacuum to obtain the powdered polyether-ether-ketone.

Technical Field

The invention relates to the field of heat-resistant polymer materials, in particular to application of selective laser sintering by using polyether-ether-ketone prepared from 1-butyl-3-methylimidazolium bromide as a raw material.

Background

The Selective Laser Sintering (SLS) technique can print out the substituted skeleton which is completely consistent with the requirement of the physical characteristics of the patient, and the size precision and the shape matching degree of the substituted skeleton are far more than those of the prior alloy skeleton, so the selective Laser Sintering technique is valued and popularized by the medical field. According to the Frenkel sintering neck length equation, factors that affect the quality of sintering include the apparent density of the powder raw material and the particle size of the powder raw material. In order to ensure the quality of the selective laser sintering technology, the particle size of the raw material used as the selective laser sintering technology is required to be concentrated between 30 and 70 mu m, the particle appearance is close to spherical, and the apparent density is 0.3 to 0.5g/cm³If these requirements are not satisfied, the powder is unevenly spread during the sintering process, the surface of the sintered product is rough, and the shrinkage of each phase of the material is poor.

Polyether Ether Ketone (PEEK) is a special engineering plastic containing benzene rings, Ether bonds and carbonyl groups in a molecular main chain. Due to the excellent biocompatibility of the polyether-ether-ketone, the polyether-ether-ketone shows attractive application prospects in the fields of human bones and the like, and can be used as a selective laser sintering technical material for customizing a substitute bone consistent with the requirements of the physical characteristics of patients. The existing method for preparing polyether-ether-ketone adopts 4,4' -difluorobenzophenone and 1, 4-benzenediol as raw materials, anhydrous potassium carbonate and anhydrous sodium carbonate as catalysts, diphenyl sulfone (the melting point is 334 ℃) as a solvent, and starts to synthesize a product through nucleophilic substitution reaction at the initial temperature of 140-150 ℃, and the reaction is completed when the temperature is raised to 320 ℃. And (3) cooling the obtained product to room temperature, grinding, washing to obtain relatively pure polyetheretherketone, mechanically mixing the obtained polyetheretherketone with micron-sized hydroxyapatite together, and performing selective laser sintering forming to obtain the composite material with high porosity.

In the process of implementing the invention, the inventor finds that the prior art has at least the following problems:

when the polyether-ether-ketone is prepared, the obtained product needs to be ground, so that the polyether-ether-ketone prepared by the prior art has poor shape stability, less spherical particles, rough surface and wider particle size distribution, the prepared molded composite material has low size precision and poor quality, the mechanical property of the composite material prepared by the polyether-ether-ketone prepared by the prior art as a raw material through a selective laser sintering technology is much lower than that of the composite material prepared by the traditional injection molding or hot press molding method, and the application range of the composite material prepared by the prior art is very small.

Disclosure of Invention

In order to solve the problems of less spheroidal particles, rough surface and wide particle size distribution of the composite material in the prior art, the embodiment of the invention provides the application of selective laser sintering by taking polyether-ether-ketone prepared by 1-butyl-3-methylimidazolium bromide as a raw material. The technical scheme is as follows:

the embodiment of the invention provides an application of selective laser sintering by taking polyether-ether-ketone prepared from 1-butyl-3-methylimidazolium bromide as a raw material, which comprises the following steps: taking 1-butyl-3-methylimidazole bromine salt as a solvent to synthesize the polyetheretherketone.

Specifically, the application comprises the following steps:

(1) under the inert gas, adding a difluoro monomer into the solvent, and fully dissolving the difluoro monomer into the solvent to obtain a difluoro solution;

(2) under inert gas, uniformly mixing a diphenol monomer, anhydrous potassium carbonate and anhydrous sodium carbonate, adding the mixture into the difluoro solution, fully dissolving the diphenol monomer, the anhydrous potassium carbonate and the anhydrous sodium carbonate in the difluoro solution to obtain a mixed solution, heating the mixed solution to 140-200 ℃, reacting until no carbon dioxide gas is generated, finishing the reaction to obtain a reaction product, and purifying the reaction product to obtain the polyether-ether-ketone with the particle size distribution of 30-70 mu m.

Specifically, the specific method of step (1) is as follows: 1) and under the inert gas, adding a difluoro monomer into the solvent, and continuously stirring at 25-60 ℃ to fully dissolve the difluoro monomer into the solvent to obtain a difluoro solution.

Specifically, in the step (2), the specific method for adding the diphenol monomer, anhydrous potassium carbonate and anhydrous sodium carbonate into the difluoro solution after uniformly mixing the diphenol monomer, the anhydrous potassium carbonate and the anhydrous sodium carbonate comprises the following steps: uniformly mixing diphenol monomer, anhydrous potassium carbonate and anhydrous sodium carbonate, adding the mixture into the difluoro solution for 3-5 times respectively, wherein the interval time between two adjacent times of adding is 20-40 min, and continuously stirring after each time of adding.

Specifically, in the step (2), the specific method for obtaining the mixed solution is as follows: uniformly mixing the diphenol monomer, the anhydrous potassium carbonate and the anhydrous sodium carbonate, adding the mixture into the difluoro solution, heating to 120-140 ℃, and preserving heat for 1-3 hours to fully dissolve the diphenol monomer, the anhydrous potassium carbonate and the anhydrous sodium carbonate in the difluoro solution to obtain a mixed solution.

Further, the specific method of step (2) comprises: uniformly mixing the diphenol monomer, the anhydrous potassium carbonate and the anhydrous sodium carbonate, adding the mixture into the difluoro solution, heating the mixture from room temperature to 120-140 ℃ at the speed of 5-20 ℃/min, preserving the heat for 1-3 hours, fully dissolving the diphenol monomer, the anhydrous potassium carbonate and the anhydrous sodium carbonate in the difluoro solution to obtain a mixed solution, and heating the mixed solution to 140-200 ℃ at the speed of 2-10 ℃/min.

Further, the difluoro monomer is 4,4 '-difluorobenzophenone, 3' -difluorobenzophenone, 2, 3-difluorobenzophenone, 2, 5-difluorobenzaldehyde, 2, 6-difluorobenzaldehyde, bis (4-fluorophenyl) ether, 4 '-difluorodiphenylmethane, 2, 5-difluoroanisole, 2, 5-difluorobenzophenone, 3, 5-difluorobenzonitrile, 2, 5-difluorobenzoic acid methyl ester, 2, 4-difluorobenzoic acid ethyl ester or 4,4' -difluorobenzylpiperazine.

Preferably, the difluoro monomer is 4,4 '-difluorobenzophenone, 3' -difluorobenzophenone, and bis (4-fluorophenyl) ether.

Further, the diphenol monomer is 1, 4-benzenediol, bisphenol A, 1, 5-naphthalenediol, 2, 6-naphthalenediol, tert-butylhydroquinone, 2-methoxyhydroquinone, trimethylhydroquinone, tetramethylhydroquinone, 2, 5-di-tert-octylhydroquinone, 2, 5-diisooctylhydroquinone, 2, 5-diphenylhydroquinone or 2, 5-di-tert-amylhydroquinone.

Preferably, the diphenol monomers are 1, 4-benzenediol, bisphenol a and 2, 5-diphenylhydroquinone.

Specifically, the purification comprises: filtration and washing, the filtration and washing comprising: adding ethanol into the reaction product, carrying out primary filtration to obtain primary filtered filter residue, washing the primary filtered filter residue with ethanol and acetone respectively for 1-2 times, then carrying out secondary filtration to obtain secondary filtered filter residue, and washing the secondary filtered filter residue with deionized water twice.

Further, the purifying further comprises: drying, the method of drying comprising: and (3) drying the washed product at 120 ℃ in vacuum to obtain the powdered polyether-ether-ketone.

The technical scheme provided by the embodiment of the invention has the following beneficial effects: the embodiment of the invention provides application of selective laser sintering by taking polyether-ether-ketone prepared from 1-butyl-3-methylimidazole bromide as a raw material, wherein the application is to synthesize the polyether-ether-ketone by taking the 1-butyl-3-methylimidazole bromide as a solvent and take the synthesized polyether-ether-ketone as a raw material of a selective laser sintering technology. In the preparation process of the polyetheretherketone, the selected solvent is in a stable liquid state at room temperature or a high temperature close to room temperature to 300 ℃, so that the reaction temperature for synthesizing the polyetheretherketone can be reduced, the polyetheretherketone can be prepared at a relatively low temperature, the reaction is ensured to be always carried out in a liquid phase, meanwhile, the reaction system is still kept in the liquid phase state after the reaction is finished and the temperature is reduced to the room temperature, the subsequent treatment process of the polyetheretherketone is greatly facilitated, the problem that the polymer and the solvent are solidified into a group after the diphenyl sulfone is cooled in the synthesis process of the polyetheretherketone in the prior art is completely avoided, the synthesized polyetheretherketone can be directly used as a raw material of a selective laser sintering technology, the particle size of the prepared pure polyetheretherketone powder is distributed at 30-70 mu m through the detection of a dry-wet-cold-laser particle size analyzer, the surface of the prepared polyetheretherketone powder is smooth through the observation of a scanning electron microscope, and the polyether-ether-ketone is spherical-like and has high powder fluidity, so that the polyether-ether-ketone meets the requirements of a selective laser sintering technology.

Drawings

In order to more clearly illustrate the technical solutions in the embodiments of the present invention, the drawings needed to be used in the description of the embodiments will be briefly introduced below, and it is obvious that the drawings in the following description are only some embodiments of the present invention, and it is obvious for those skilled in the art to obtain other drawings based on these drawings without creative efforts.

FIG. 1 is an infrared spectrum of a polyetheretherketone powder according to an embodiment of the present invention, wherein the abscissa is light transmittance (in units%) and the ordinate is wavelength (in cm)^-1)；

FIG. 2 is a thermogravimetric analysis of a PEEK powder according to a first embodiment of the present invention, wherein the abscissa is temperature (unit ℃) and the ordinate is weight (unit%);

fig. 3 is a distribution diagram of the particle size of polyetheretherketone provided in the first embodiment of the present invention, in which the abscissa represents the particle size (in μm) and the ordinate represents the differential distribution (in%).

Fig. 4 is a scanning electron microscope image of peek according to an embodiment of the present invention.

Detailed Description

In order to make the objects, technical solutions and advantages of the present invention more apparent, embodiments of the present invention will be described in further detail below.

The 1-butyl-3-methylimidazolium bromide salt selected in this example is from Kaiyuan scientific and technological laboratory, Sanmenxia, Zhejiang province, with specification of CP and purity of 98%.

The difluoro monomers 4,4 '-difluorobenzophenone, 3' -difluorobenzophenone, 2, 3-difluorobenzophenone, 2, 5-difluorobenzaldehyde, 2, 6-difluorobenzaldehyde and bis (4-fluorophenyl) ether selected in the embodiment are all from Shanghai-sourced leaf Biotech limited, and the specification of the difluoro monomers is AR, and the purity of the difluoro monomers is more than or equal to 99.5%; 4,4 '-difluorodiphenylmethane, 2, 5-difluoroanisole, 2, 5-difluorobenzophenone, 3, 5-difluorobenzonitrile, 2, 5-difluorobenzoic acid methyl ester, 2, 4-difluorobenzoic acid ethyl ester and 4,4' -difluorobenzylpiperazine are all from the national pharmacy group, the specification of the compound is AR, and the purity is more than or equal to 99.5%.

The diphenol monomers selected in the embodiment are 1, 4-benzenediol, bisphenol A, 1, 5-naphthalenediol and 2, 6-naphthalenediol, the specification of which is AR from the national medicine group, and the purity of the diphenol monomers is more than or equal to 99.5 percent; tert-butylhydroquinone, 2-methoxyhydroquinone, trimethylhydroquinone, tetramethylhydroquinone, 2, 5-di-tert-octylhydroquinone, 2, 5-di-iso-octylhydroquinone, 2, 5-diphenylhydroquinone and 2, 5-di-tert-amylhydroquinone were all from Fuji film company, with specification AR and purity of not less than 99.5%.

Other reagents such as sodium carbonate and potassium carbonate were purchased from Shilang chemical with specification AR and purity > 99%.

Example one

Under the protection of nitrogen, 10.90g of 4,4 '-difluorobenzophenone is added into 218.00g of 1-butyl-3-methylimidazolium bromide solvent to obtain a 4,4' -difluorobenzophenone solution, wherein the structure of 1-butyl-3-methylimidazolium bromide is shown in the specificationHeating the 4,4' -difluorobenzophenone solution to 40 ℃, stirring the 4,4' -difluorobenzophenone solution to fully dissolve the 4,4' -difluorobenzophenone, and cooling to normal temperature for later use; under the protection of nitrogen, 5.50g of 1, 4-benzenediol and 0.69g of phenolUniformly mixing potassium carbonate hydrate and 4.77g of anhydrous sodium carbonate, dividing into four parts with equal mass, respectively adding the four parts into a 4,4' -difluorobenzophenone solution, continuously stirring at high speed (the stirring speed can be 100-500 r/min), keeping the stirring speed for 30min, heating the mixture to 140 ℃ from the normal temperature, the heating rate is 5 ℃/min, keeping the temperature for 2h, fully dissolving the 4,4' -difluorobenzophenone, the anhydrous potassium carbonate and the anhydrous sodium carbonate in the 4,4' -difluorobenzophenone solution, heating the mixture to 180 ℃, the heating rate is 2 ℃/min, after continuously reacting for 24h (no carbon dioxide gas is generated at the moment), naturally cooling the reaction system to the room temperature under the condition of keeping stirring to obtain a reaction product, adding 100ml of ethanol into the reaction product, and performing primary filtration by using a Buchner funnel to obtain primary filtration residue, and washing the primarily filtered filter residue with ethanol and acetone for 1-2 times respectively, then filtering again, washing the secondary filtered filter residue with 100ml of deionized water for two times, filtering, and then carrying out vacuum drying treatment at 120 ℃ to obtain 14.75g of polyether-ether-ketone powder with the yield of 90%.

The reaction is as follows:

the obtained polyetheretherketone powder was subjected to infrared spectroscopy, and the infrared spectrum is shown in FIG. 1, which is 1641.12cm^-1Corresponding to the stretching vibration peak of C ═ O, 1591.14cm^-1And 1492.31cm^-1Corresponding to the in-plane vibration peak of Ph-O-Ph benzene ring, 1296.66cm^-1Corresponding to a Ph-CO-Ph asymmetric stretching vibration peak of 1155.68cm^-1Corresponding to the bending vibration absorption peak in the C-H plane in the benzene ring structure, 922.96cm^-1Corresponding to a Ph-CO-Ph symmetrical telescopic vibration peak of 839.50cm^-1Corresponding to characteristic peak of para-substitution of benzene ring. Comparing the standard spectrum of the polyether-ether-ketone, the prepared product is the polyether-ether-ketone.

Thermogravimetric analysis is performed on the polyetheretherketone powder, as shown in fig. 2, the weight loss rates of the polyetheretherketone at 216 ℃, 371 ℃, and 416 ℃ are respectively 1%, 5%, and 10%, the temperature corresponding to the maximum weight loss rate is 453 ℃, and the carbon residue rate at 700 ℃ is 40.24%, which indicates that the polyetheretherketone prepared in this example has high thermal stability.

The polyetheretherketone obtained in this example was subjected to a particle size distribution test using a dry-wet cold-laser particle size analyzer, specifically using an instrument: dry-wet-cold-laser particle size analyzer, manufacturer: zhuhai Oumek, type: LS-CIII, the particle size distribution test method is as follows: 0.1g of the polyether-ether-ketone obtained in the first embodiment is dissolved in 5g of ethanol, and the solution is subjected to ultrasonic dispersion to prepare a suspension for testing, so that the particle size of the polyether-ether-ketone is normally distributed, the average particle size is mainly distributed in the range of 30-70 mu m, and the polyether-ether-ketone has better particle size distribution and uniformity. Meanwhile, apparent density detection is carried out on the polyether-ether-ketone powder, and a testing instrument: particle apparent density instrument, manufacturer: zhejiang ruike, type: FT-105C, method: selecting 50g of polyether-ether-ketone powder, placing the powder into an upper funnel, quickly drawing away a baffle plate of the funnel, freely stacking the powder into a measuring cup, measuring the volume of the powder in the measuring cup, and finally measuring that the apparent density of the polyether-ether-ketone powder is 0.40g/cm³The polyether-ether-ketone powder has good fluidity (the fluidity is determined by the shape and the roughness of the powder together and is comprehensively judged mainly by the shape, the particle size distribution, the apparent density and the powder laying efficiency of the powder), so that the ball bearing effect is generated in the powder laying process of the polyether-ether-ketone powder, and the quality of a selective laser sintering technical product is favorably improved. The observation result is shown in fig. 4 by observing with a scanning electron microscope (test instrument: ultra high resolution cold field scanning electron microscope, manufacturer: japanese hitachi, model: SU8010, magnification: 5000), and as can be seen from fig. 4, the polyetheretherketone powder is of a spheroidal structure, which makes the polyetheretherketone obtained meet the requirements of selective laser sintering technology.

The polyetheretherketone obtained in the first example is used as a raw material for a selective laser sintering technique, which specifically comprises the following steps: sieving the obtained polyetheretherketone powder by a 200-mesh sieve, taking 5kg of the sieved polyetheretherketone powder, carrying out selective laser sintering on a rapid forming machine, setting the scanning distance to be 0.1mm, the single-layer thickness to be 0.15mm, the scanning speed to be 1500mm/s, the preheating temperature to be 120-140 ℃, and the laser power to be 16W, preparing a complete polyetheretherketone tensile sample strip (the sample strip has the middle length of 60mm,full length 85mm, thickness 2mm) and impact bars (length × width × thickness: 125 mm. times.12 mm. times.5 mm), and the tensile specimen and the impact specimen were measured respectively to find a density of 0.723g/cm³Tensile strength of 80MPa and impact strength of 20KJ/m²Young modulus is 3GPa, the mechanical property of a sintered part is close to that of a polyether-ether-ketone molded part, wherein the polyether-ether-ketone molded part adopts the following equipment: TYU-2500 linkage mode-locking vertical injection molding machine; the manufacturer: giant Yu machine; the molding process comprises the following steps: adopting a double-screw extruder, wherein the temperature of a screw section is 350 ℃, the temperature of a nozzle is 380 ℃, the rotating speed of the screw is 100 r/min, and the injection pressure is 130MPa for injection molding.

The embodiment of the invention provides application of selective laser sintering by taking polyether-ether-ketone prepared from 1-butyl-3-methylimidazole bromide as a raw material, wherein the application is to synthesize the polyether-ether-ketone by taking the 1-butyl-3-methylimidazole bromide as a solvent and take the synthesized polyether-ether-ketone as a raw material of a selective laser sintering technology. In the preparation process of the polyetheretherketone, the selected solvent is in a stable liquid state at room temperature or a high temperature close to room temperature to 300 ℃, so that the reaction temperature for synthesizing the polyetheretherketone can be reduced, the polyetheretherketone can be prepared at a relatively low temperature, the reaction is ensured to be always carried out in a liquid phase, meanwhile, the reaction system is still kept in the liquid phase state after the reaction is finished and the temperature is reduced to the room temperature, the subsequent treatment process of the polyetheretherketone is greatly facilitated, the problem that a polymer and the solvent are solidified into a group after the diphenyl sulfone is cooled in the synthesis process of the polyetheretherketone in the prior art is completely avoided, the particle size distribution of a product of the powdered polyetheretherketone is detected to be 30-70 mu m by a dry-wet-cold-laser particle size analyzer when the synthesized polyetheretherketone can be directly used as a raw material of a selective laser sintering technology, and the surface of the polyetheretherketone is smooth by observation of a scanning electron microscope, and is spheroidal with an apparent density of 0.40g/cm³And the polyether-ether-ketone has high powder fluidity, so that the polyether-ether-ketone meets the requirements of selective laser sintering technology.

The above description is only for the purpose of illustrating the preferred embodiments of the present invention and is not to be construed as limiting the invention, and any modifications, equivalents, improvements and the like that fall within the spirit and principle of the present invention are intended to be included therein.