KR100552131B1 - Aromatic polyimide composite powders with low crystallinity and method for preparing them - Google Patents

Abstract

The present invention relates to an aromatic polyimide composite powder material by one-step direct polymerization and a method for preparing the same, and more particularly, to a monomer of tetracarboxylic dianhydride and an aromatic diamine in a phenolic organic polar solvent in which inorganic particle powder is dispersed. Conventional aromatic polyimide prepared by a two-step process in a conventional low temperature process by producing a polyimide-based composite powder material in which inorganic particle powder is uniformly dispersed by a one-step heat polymerization process of mixing and then raising the temperature to specific conditions The present invention relates to an aromatic polyimide composite powder material by one-step direct polymerization which can improve a manufacturing process of a resin powder and to provide a molded article having excellent heat resistance, abrasion resistance, thermal expansion resistance, and the like, and a manufacturing method thereof.

Single Step, Inorganic Particle Powder, Polyimide

Description

Aromatic polyimide composite powders with low crystallinity and method for preparing them}             

Figure 1 shows a particle distribution of the polyimide composite powder containing graphite (Graphite).

FIG. 2 is a SEM photograph (× 1,500, × 30,000) of the polyimide composite powder surface form according to Example 1. FIG.

Figure 3 is a SEM photograph (x 1,500, x 30,000) of the surface of the polyimide composite powder by physical mixing according to Comparative Example 2.

The present invention relates to an aromatic polyimide composite powder material by one-step direct polymerization and a method for preparing the same, and more particularly, a monomer of tetracarboxylic dianhydride and a monomer of aromatic diamine in a phenolic organic polar solvent in which inorganic particle powder is dispersed. Conventional aromatic polyimide prepared by a two-step process in a conventional low temperature process by producing a polyimide-based composite powder material in which inorganic particle powder is uniformly dispersed by a one-step heat polymerization process of mixing and then raising the temperature to specific conditions The present invention relates to an aromatic polyimide composite powder material by one-step direct polymerization which can improve a manufacturing process of a resin powder and to provide a molded article having excellent heat resistance, abrasion resistance, thermal expansion resistance, and the like, and a manufacturing method thereof.

In general, the polyimide (hereinafter referred to as "PI") resin refers to a high heat-resistant resin prepared by imidating an aromatic tetracarboxylic acid or a derivative thereof and an aromatic diamine or an aromatic diisocyanate. However, these PI resins have insolubility that does not dissolve in a solvent and insolubility that does not melt by heating. In addition, the PI resin may have various molecular structures depending on the type of monomer used. Generally, pyromellitic dianhydride (PMDA) or biphenyltetracarboxylic dianhydride (BPDA) is used as the aromatic tetracarboxylic acid component, and oxydianiline (ODA) or p -phenylene diamine ( p- PDA) is used as the aromatic diamine component. ) Is prepared by condensation polymerization, and the most typical PI resin has the structure of Formula 1 as a repeating unit.

The PI resin having the above formula 1 as a repeating unit is an insoluble and insoluble ultra high heat resistant resin, and has the following characteristics:

(1) Excellent heat oxidation resistance, (2) Extremely high usable heat resistance, long term use temperature of about 260 ℃, short term use temperature of 480 ℃, (3) Excellent electrochemical and mechanical properties, (4 ) Excellent radiation resistance and low temperature characteristics, (5) Intrinsic flame retardancy, (6) Excellent chemical resistance.

However, the PI resin as described above has the advantage of having excellent heat resistance characteristics, on the other hand, due to the properties of insoluble and insoluble, there is a disadvantage that processing is very difficult.

In particular, the degree of imidization and crystallinity of the polymer powder has an effect on the processability and mechanical properties of the resin. If the degree of imidization of the PI resin is too low, water may be generated as a byproduct of the imidization reaction during the processing to generate bubbles. In addition, when the degree of crystallinity of the PI resin is too high, the interaction between the powders is insufficient in the heat treatment of the molded body, and this has been pointed out that the mechanical properties of the molded body are degraded. Cause. Therefore, the control of the degree of imidization and crystallinity in the appropriate range can be said to be a very important factor in improving the moldability and mechanical properties of the polymer powder.

On the other hand, the PI resin is an organic compound made of carbon, and has a disadvantage in that heat resistance and thermal expansion properties are inferior to inorganic compounds. Therefore, many studies have been made for the improvement thereof, and a representative example may be the formation of a composite material by a complex reaction with an inorganic compound having a layered structure. That is, in the case of Canadian Patent Application No. 1035150, Japanese Patent Publication No. 58-160350, Japanese Patent Publication No. 63-095264, Japanese Patent Publication No. 62-127314, and Japanese Patent Publication No. 02-058538, etc. As one of the methods for producing a powder material, the compounding was carried out by dry blending polyamic acid (PAA) with inorganic particles of various types, and as a result, the wear resistance and thermal expansion properties of the conventional PI resin were greatly improved. I was. However, in the above case, since the polyimide powder was prepared and then simply mixed with the additive by a physical method, the additive was not evenly dispersed in the polyimide powder and coated on the surface to reduce the fusion characteristics between the powders, thereby reducing the mechanical properties of the PI molded article. It has a disadvantage that can lead to the deterioration.

Therefore, research on the production of PI-based composite materials, in which inorganic powders are evenly dispersed in the polymer matrix, while maintaining almost all properties of existing PI resins, has been particularly demanded. Thus, Japanese Patent Publication No. 63-081160 et al. After dispersing in an aprotic polar solvent such as N-methylpyrrolidone (NMP) and performing a polymerization reaction, the dispersion characteristics of the inorganic particles were improved in the polyimide particles, but in this case, the low temperature via the production of polyamic acid There is a disadvantage that the two-stage polymerization has to be carried out, and also because the PI resin powder prepared in the aprotic polar solvent shows a relatively high crystallinity, there is a problem that the molding process properties are reduced as a result.

Accordingly, the inventors of the present invention have made efforts to solve the above problems, and as a result, the aromatic diamine monomer and the tetracarboxylic dianhydride monomer are added in a phenol-based organic polar solvent in which inorganic particle powder is dispersed, and then a specific temperature range and temperature increase rate Simultaneously carrying out the imid polymerization and complexing reaction by gradually raising the temperature in the temperature rising condition that is specifically configured, the inorganic particles used are uniformly dispersed in the polyimide powder, while maintaining the crystallinity and heat resistance characteristics of the existing polyimide resin. Compounded at the molecular level, it is possible to manufacture polyamide-based composite materials with improved heat resistance, abrasion resistance, thermal expansion and mechanical properties that can be used as core heat-resistant materials in high-tech industries such as electric, electronic, aerospace and aviation. Knowing to complete the present invention.

Accordingly, an object of the present invention is to provide an aromatic polyimide composite powder material and a manufacturing method thereof by one-step direct polymerization capable of providing a molded article excellent in heat resistance, abrasion resistance and thermal expansion resistance.

In the present invention, a mixture of a tetracarboxylic dianhydride monomer and an aromatic diamine monomer is added to a phenolic organic polar solvent in which inorganic particle powder is dispersed, and then heated to 60 to 80 ° C. over a period of 2 to 3 hours, and the temperature range is 2 to 2 °. After maintaining for 3 hours, the mixture is heated to 160-200 ° C. over 2 to 3 hours, and then prepared by reacting under reflux for 5 minutes to 6 hours while maintaining the temperature range thereof. The manufacturing method of the composite material powder comprised as a polyimide resin and an inorganic material is characterized by the above-mentioned.

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The present invention will be described in detail as follows.

In the present invention, the inorganic particles are uniform by a simple heating process in which the monomers of tetracarboxylic dianhydride and the monomers of aromatic diamine are added to the phenolic organic polar solvent in which the inorganic particle powder is dispersed, and then the temperature is raised within a specific temperature rising rate and temperature range. By producing the dispersed polyimide composite material powder, it improves the manufacturing process of the conventional aromatic polyimide resin powder produced by the two-step process in the existing low temperature process, and excellent in heat resistance, wear resistance and thermal expansion resistance The present invention relates to an aromatic polyimide composite material powder by a one-step direct polymerization capable of providing a molded article, and a method of manufacturing the same.

In the present invention, tetracarboxylic dianhydride and aromatic diamine are used as the monomer for producing polyimide. As tetracarboxylic dianhydride, pyromellitic dianhydride, benzophenonetetracarboxylic dianhydride, oxydiphthalic dianhydride, nonphthalic dianhydride and hexafluoroisopropylidenediphthalic dianhydride, 1,2,3,4-cyclobutane Tetracarboxylic dianhydride (CBDA), 1,2,3,4-cyclopentanetetracarboxylic dianhydride (CPDA), 4- (2,5-dioxotetrahydrofuryl) -3-methylcyclohexane-1,2- Dicarboxylic dianhydride (DOCDA), 4- (2,5-dioxotetrahydrofuryl-3-yl) -tetraline-1,2-dicarboxylic dianhydride (DOTDA) and bicyclooctene-2,3, One or two or more selected from 5,6-tetracarboxylic dianhydride (BODA) may be used as essential components, and common tetracarboxylic acid monomers used for other polyimide polymerization may be used together. As the aromatic diamine, para-phenylenediamine (p-PDA), meta-phenylenediamine (m-PDA), 4,4-oxydianiline (ODA), 4,4-methylenedianiline (MDA), 2 , 2-bisaminophenylhexafluoropropane (HFDA), metabisaminophenoxydiphenylsulfone (m-BAPS), parabisaminophenoxydiphenylsulfone (p-BAPS), 1,4-bisaminophenoxybenzene (TPE-Q), 1,3-bisaminophenoxybenzene (TPE-R), 2,2-bisaminophenoxyphenylpropane (BAPP), 2,2-bisaminophenoxyphenylhexafuluropropane ( HFBAPP), and one, two or more selected from 4,4-benzanilide (DABA) are used as essential ingredients, and other diamine monomers that have been used in other polyimide polymerizations may be used together.

The polyimide or polyamic acid resin prepared as the repeating unit of Formula 2, prepared by polymerization of the above monomer mixture, has a weight average molecular weight (Mw) in the range of 10,000 to 300,000 g / mol, and is in the range of 0.1 to 2.0 dl / g. It maintains intrinsic viscosity and has a glass transition temperature of 200 to 400 ° C.

The present invention uses a phenolic organic polar solvent in which inorganic particle powder is dispersed as a solvent for the polymerization of the monomer mixture. As a result of the technical construction, it is possible to use polyphenol containing conventional inorganic particles using a phenolic organic polar solvent. The problem by mid resin manufacture was solved. The phenolic organic polar solvent selected and used in the present invention has a low plasticizing effect compared to the aprotic polar solvent, and thus the polyimide composite resin produced has a low crystallinity, a high specific surface area, and a non-aggregated spherical shape. Powder properties. Specifically, as the phenolic organic polar solvent, a single solvent or a mixed solvent of two or more selected from methacresol, paracresol, metachlorophenol and parachlorophenol may be used.

Since the aprotic polar solvent, a solvent for preparing polyimide composite powders, has been previously reported, it is difficult to remove by-product water completely out of the reaction system during the polymerization reaction because of its high compatibility with water. Moisture participates in the hydrolysis of the polyamic acid resulting in a decrease in polymer molecular weight. In contrast, since the phenolic organic polar solvent used as the polymerization solvent in the present invention is a polar solvent exhibiting incompatibility with water, water generated during the reaction can be easily removed out of the reaction system, and the molecular weight reduction reaction of the polymer by hydrolysis This can be minimized. In addition, a high molecular weight polyimide composite powder is reproducibly prepared by dehydration of tetracarboxylic acid, which is a trace amount of impurities present in the acid dianhydride, during the high temperature reaction carried out under the phenolic organic polar solvent to generate an acid dianhydride as a monomer.

In the present invention, by using the above-described specific phenolic organic polar solvent and dispersing the inorganic particles therein, the mechanical properties deteriorated due to the low compatibility of the polyimide composite resin prepared by dispersing the existing inorganic particles. The above problems can be solved in the present invention. In the present invention, the inorganic particle powder to be dispersed and used in the phenolic organic polar solvent may be selected from layered graphite powder, molybdenum sulfide (MoS ₂ ), silica, and aluminum nitride (AlN). When the graphite powder is used, the most preferable effect can be obtained. The inorganic particles as described above are used having a size in the range of 0.5 to 30 ㎛, and if the size of the inorganic particles is out of the above range has a problem in compatibility with the polyimide powder. In addition, the inorganic particle powder may be used in an amount of 5 to 50% by weight based on the total amount of the monomer 100, and when the amount of the inorganic particle powder exceeds the above range, a smooth polymerization reaction may not be performed.

In the present invention, a polyamide composite powder may be produced, if necessary, using the polyimide resin or the polyamic acid as a precursor of the polyimide.

On the other hand, the present invention is to specifically configure the temperature raising conditions in the polymerization process of the monomer mixture in the phenolic organic polar solvent in which the inorganic particle powder as described above is characterized in another technical configuration of the present invention, polyamic After the acid is prepared, a polyimide composite powder is prepared by a single step simple heating condition in which the temperature is raised at a constant rate using a specific solvent in which inorganic particles are dispersed, without undergoing a conventional two-step polymerization reaction in which an imidation reaction proceeds. There is a difference from the existing method, it is possible to manufacture a high molecular weight polyimide composite powder.

In the present invention, a mixture of a tetracarboxylic dianhydride monomer and an aromatic diamine monomer is added to a phenolic organic polar solvent in which inorganic particle powder is dispersed for the production of a polyimide composite powder, and the temperature is raised to 60 to 80 ° C. over 2 to 3 hours. It was then maintained for 2 to 3 hours in the temperature range, and then heated to 160 to 200 ℃ over 2 hours, and then characterized in that the reaction is refluxed for 5 minutes to 6 hours in this temperature range. The reason for limiting the temperature raising condition as described above is to prepare a polyimide resin powder having a linear structure, and may cause some crosslinking reaction when the temperature range and the temperature increase rate are out of the above range.

In addition, in carrying out the polymerization reaction, phthalic anhydride, maleic acid, aniline can be used within the range of less than 10 mol% as a molecular weight regulator, trimethylamine, triethylamine, pyridine, isoquinoline and It is also possible to use one selected from quinoline, and the catalyst is more preferably used within the range of less than 10 mol%.

As a result, the PI-based composite powder produced by the production method according to the present invention maintains its intrinsic viscosity in the range of 0.1 to 2.0 dl / g, maintains the molecular weight distribution in the range of 200,000 to 300,000 g / mol, and has a crystallinity of 10 to It is 25%, the degree of imidization is in the range of 70 to 90%, the specific surface area is maintained in the range of 50 to 200 m 2 / g, and is easily dissolved by concentrated sulfuric acid at room temperature.

As described above, in the present invention, by changing the production conditions of the composite material, the inorganic particles used are uniformly dispersed in the powder of the polyamic acid or polyimide resin having the formula (2) as a repeating unit, and the existing polyimide resin Polyamide compounded at the molecular level while maintaining the crystallinity and heat resistance characteristics of the polyamide, and improved in heat resistance, abrasion resistance, thermal expansion characteristics, and mechanical properties that can be used as core heat resistance materials for high-tech industries such as electric, electronics, space, and aviation. Composite materials can now be manufactured.

The present invention will be described in more detail based on the following examples, but the present invention is not limited by the following examples.

Example 1 Preparation of Polyimide Composite Powder (PI-G1)

50 ml of mixed cresol (paracresol: metacresol = 33: 67, molar ratio) were placed in a 500 ml four-necked flask equipped with a mechanical stirrer, thermometer, Dean Stark trap, nitrogen gas inlet and outlet, 200 ml of mixed cresol (paracresol: metacresol = 33:67, molar ratio) was dispersed evenly by adding g (10% by weight) graphite powder [Komex, particle size 5 μm]. And 20.0 g (0.1 mol) of oxydianiline (ODA) were completely dissolved. Subsequently, 21.8 g (0.1 mol) of pyromellitic dianhydride (PMDA) was added slowly to dissolve, and then the reaction temperature was raised to 75 ° C. over 2 hours and then maintained for 2 hours. Then, after raising the temperature to 200 ° C. over 2 hours, the mixture was refluxed for 2 hours. At this time, the solid content concentration was 10% by weight, the stirring speed was maintained at 500 rpm.

After completion of the reaction, the precipitated powder was filtered and washed with methanol to remove impurities and the remaining reaction solvent, and dried in a vacuum oven at 100 ° C. for 12 hours to quantitatively obtain polyimide composite powder PI-G1.

Example 2. Preparation of Polyimide Composite Powder (PI-G2)

Into a 500 ml four-necked flask equipped with a mechanical stirrer, thermometer, Dean Stark trap, nitrogen gas inlet and outlet, 50 ml of mixed cresol (paracresol: metacresol = 33: 67, molar ratio) was added and 9.55 g (20% by weight). ) Disperse evenly by adding graphite powder [Komex, particle size 5㎛] and 20.024 g (0.1 mol) with 200 ml of mixed cresol (paracresol: metacresol = 33:67, molar ratio) while passing through nitrogen gas. ) ODA was completely dissolved. Then 21.812 g (0.1 mol) of PMDA was added slowly to dissolve, and then the reaction temperature was raised to 75 ° C. over 2 hours and then maintained for 2 hours. Then, after raising the temperature to 200 ° C. over 2 hours, the mixture was refluxed for 2 hours. At this time, the solid content concentration was 10% by weight, the stirring speed was maintained at 500 rpm.

After completion of the reaction, the precipitated powder was filtered and then washed with methanol to remove impurities and the remaining reaction solvent, and dried for 12 hours in a vacuum oven at 100 ℃ to obtain a polyimide composite powder PI-G2 quantitatively.

Example 3. Preparation of Polyimide Composite Powder (PI-G3)

50 ml of mixed cresol (paracresol: metacresol = 33: 67, molar ratio) was placed in a 500 ml four-necked flask equipped with a mechanical stirrer, thermometer, Dean Stark trap, nitrogen gas inlet and outlet, and 16.4 g (30% by weight). ) Disperse evenly by adding graphite powder [Komex, particle size 5㎛] and 20.024 g (0.1 mol) with 200 ml of mixed cresol (paracresol: metacresol = 33:67, molar ratio) while passing through nitrogen gas. ) ODA was completely dissolved. Then 21.812 g (0.1 mol) of PMDA was added slowly to dissolve, and then the reaction temperature was raised to 75 ° C. over 2 hours and then maintained for 2 hours. Then, after raising the temperature to 200 ° C. over 2 hours, the mixture was refluxed for 2 hours. At this time, the solid content concentration was 10% by weight, the stirring speed was maintained at 500 rpm.

After completion of the reaction, the precipitated powder was filtered and washed with methanol to remove impurities and the remaining reaction solvent, and dried in a vacuum oven at 100 ° C. for 12 hours to quantitatively obtain polyimide composite powder PI-G3.

Example 4. Preparation of Polyimide Composite Powder (PI-G4)

50 ml of mixed cresol (paracresol: metacresol = 33:67, molar ratio) was placed in a 500 ml four-necked flask equipped with a mechanical stirrer, thermometer, Dean Stark trap), nitrogen gas inlet and outlet, and 25.4 g (40 weight) %) Graphite powder [Komex, particle size 5㎛] was added and dispersed evenly, and 20 ml of mixed cresol (paracresol: metacresol = 33:67, molar ratio) and 20.024 g (0.1 mol) of ODA was completely dissolved. Then 21.812 g (0.1 mol) of PMDA was added slowly to dissolve, and then the reaction temperature was raised to 75 ° C. over 2 hours and then maintained for 2 hours. Then, after raising the temperature to 200 ° C. over 2 hours, the mixture was refluxed for 2 hours. At this time, the solid content concentration was 10% by weight, the stirring speed was maintained at 500 rpm.

After completion of the reaction, the precipitated powder was filtered and washed with methanol to remove impurities and the remaining reaction solvent, and dried in a vacuum oven at 100 ° C. for 12 hours to quantitatively obtain polyimide composite powder PI-G4.

Example 5. Preparation of Polyimide Composite Powder (PI-G5)

50 ml of mixed cresol (paracresol: metacresol = 33: 67, molar ratio) was placed in a 500 ml four-necked flask equipped with a mechanical stirrer, thermometer, Dean Stark trap, nitrogen gas inlet and outlet, and 38.2 g (50% by weight). ) Disperse evenly by adding graphite powder [Komex, particle size 5㎛] and 20.024 g (0.1 mol) with 200 ml of mixed cresol (paracresol: metacresol = 33:67, molar ratio) while passing through nitrogen gas. ) ODA was completely dissolved. Then 21.812 g (0.1 mol) of PMDA was added slowly to dissolve, and then the reaction temperature was raised to 75 ° C. over 2 hours and then maintained for 2 hours. Then, after raising the temperature to 200 ° C. over 2 hours, the mixture was refluxed for 2 hours. At this time, the solid content concentration was 10% by weight, the stirring speed was maintained at 500 rpm.

After completion of the reaction, the precipitated powder was filtered and then washed with methanol to remove impurities and the remaining reaction solvent, and dried for 12 hours in a vacuum oven at 100 ℃ to obtain a polyimide composite powder PI-G5 quantitatively.

Comparative Example 1. Preparation of Polyimide Powder (PI-N)

In a 500 ml four-necked flask equipped with a mechanical stirrer, thermometer, Dean stock trap, nitrogen gas inlet and outlet, 20.024 g (0.1 mol) of ODA was mixed as a reaction solvent (paracresol: metacresol = 33: 67, molar ratio). After complete dissolution), 21.812 g (0.1 mol) of solid PMDA was slowly added while passing nitrogen gas at room temperature. The solution was heated to 200 ° C. for 2 hours and then refluxed at 200 ° C. for 2 hours, at which time the concentration of solids was 10% by weight and the stirring rate was maintained at 500 rpm.

After completion of the reaction, the precipitated powder was filtered and washed with methanol to remove impurities and the remaining reaction solvent, and the purified polyimide powder (PI) was dried in a vacuum oven at 100 ° C. for 12 hours.

Comparative Example 2. Preparation of Polyimide Composite Powder by Physical Mixing (PI-G6)

A physical mixture was prepared by simply stirring 8.367 g (15 wt%) graphite powder [Komex, particle size 5 μm] and 85 wt% of the polyimide powder prepared from Comparative Example 1. At this time, a magnetic bar or a mechanical stirrer was used as the mixing method, and the mixing time was fixed at 24 hours.

Comparative Example 3

A polyimide composite powder was prepared in the same manner as in Example 1, but using N-methyl-2-pyrrolidone, without using a phenolic organic polar solvent used in the present invention.

Experimental Example: Preparation of PI Composite Powder and Evaluation of Powder Properties

[Production of PI Composite Powder]

Types of the polyimide composite powders prepared according to Examples 1 to 5 and Comparative Examples 1 to 3 are shown in the following Table 1, and the characteristics of the polyimide composite powder were evaluated by the following methods, and are shown in Table 2 below. It was.

division Polyimide Content of Graphite Powder (%) Example 1 PI-G1 10 Example 2 PI-G2 20 Example 3 PI-G3 30 Example 4 PI-G4 40 Example 5 PI-G5 50 Comparative Example 1 PI-N 0 Comparative Example 2 PI-G6 10 Comparative Example 3 PI-G7 10

[Characteristic Evaluation of PI Composite Powder]

1) Structure Identification

Structural analysis of the prepared polyimide resin powder was confirmed using an FT-IR spectrometer (Bio-rad Digi-Lab division FTS 20/80) and a ¹ H-NMR spectrometer (Bruker AMX500). In addition, the degree of imidization (DI) of the resin was determined by comparing the characteristic band sizes of the FT-IR spectrum. In other words, the relative absorption of the imide CN of 1380 cm ⁻¹ with respect to the directional C = C stretch band at 1500 cm ⁻¹ was compared. In this case, as a standard sample (100% imidized sample), 1 at 400 ° C. A PI film cured over time was used. The degree of imidization was calculated by the following equation.

Here, DI is the degree of imidization, Iν ₁₃₈₀ is the imide CN absorbance at 1380 cm ⁻¹ , and Iν ₁₅₀₀ shows the elongation band of directional C = C at 1500 cm ⁻¹ .

2) Molecular Weight Measurement

The polyimide resin powder was dissolved in concentrated sulfuric acid at a concentration of 0.5 g / kL, and the inherent viscosity (η _inh ) of the solution was measured using a viscosity meter (Canon Fenske Viscometer; size 150) at a temperature of 30 ° C.

3) Thermal Property

The thermal properties of the polymers were measured using a TGA (Thermo Gravimetric Analyzer: DuPont 9900), wherein the temperature increase rate was 10 ℃ / min, the nitrogen flow rate was fixed at 50 cc / min.

4) Particle Size Analysis

The particle size of the polyimide resin powders was dispersed in distilled water, treated in a sonicator for 30 minutes, and measured using a particle size analyzer ( Mastersizer χ ). 1 shows a size distribution diagram of graphite powder, PI-G1 prepared according to Example 1, and powder particles of PI-G6 prepared according to Comparative Example 2, and prepared according to Example 1 of the present invention. It can be seen that graphite particles are more uniformly dispersed in PI-G1.

5) Particle Shape Measurement

Particle shape and size of the polyimide resin powders were analyzed using a scanning electron microscope (SEM). Figure 2 shows the surface shape of the PI-G1 powder particles prepared according to Example 1, Figure 3 shows the surface shape of the PI-G6 powder particles prepared according to Comparative Example 2. That is, it can be seen that the powder particles of the polyimide resin prepared according to Example 1 appear more uniformly and densely.

6) Degree of Crystallinity

Crystallinity of the prepared polymers was determined using XRD (X-ray Diffractometer), it was calculated by the following equation.

Where X _c is It is the degree of crystallinity, I _a is the area of amorphous scattering, and I _c is the area of crystalline scattering peaks.

7) bulk density

In order to measure the density of the polyimide resin powders, the powder was charged in a 5 mL measuring cylinder, and the weight thereof was calculated by the following equation.

Where p is the bulk density, M is the weight of the powder, and V is the volume of the powder.

division Example 1 (PI-G1) Example 2 (PI-G2) Example 3 (PI-G3) Example 4 (PI-G4) Comparative Example 1 (PI-N) Comparative Example 2 (PI-G6) Comparative Example 3 PI-G7 Imidization degree (%) 70.4 78.0 77.5 76.7 82.0 76.4 85 Crystallinity (%) 19.0 19.3 17.5 18.0 26.0 25.8 35 Bulk Density (g / Cm ² ) 0.30 0.32 0.35 0.36 0.36 0.31 0.35 Average particle size (㎛) 11.6 12.0 12.4 13.4 13.0 10.30 11.00

As shown in Table 2, the polyimide composite powders prepared according to Examples 1 to 4 of the present invention were all insoluble in general organic solvents, like polyimide powders, and dissolved only in concentrated sulfuric acid. Therefore, after dissolving the obtained polymers in sulfuric acid, the intrinsic viscosity of the obtained polymers was in the range of 0.4 to 0.7 dl / g. When the polyimide composite powder prepared according to Examples 1 to 4 was compared to the polyimide powder without the additive (Comparative Example 1), the intrinsic viscosity and the imidization degree were slightly decreased, and the crystallinity was similar. . In the case of the size of the powder particles, in the case of PI-G6, a polyimide powder composite prepared by physical mixing of Comparative Example 2, the size of the particles was slightly increased by forming a thin coating film on the surface of the polyimide powder. On the other hand, PI-G1 to G5, which is a powder prepared by one-step polymerization according to Examples 1 to 4 of the present invention, showed a similar pattern to that of the polyimide powder to which no additive was added.

As described above, according to the method of the present invention, imide polymerization and complexation by dissolving a mixture of an aromatic diamine monomer and a tetracarboxylic dianhydride monomer in a phenolic organic polar solvent in which inorganic particle powder is dispersed, and then gradually raising the temperature. The reaction can be performed simultaneously to shorten the manufacturing process, and the inorganic particles used are uniformly dispersed in the polyimide powder, and complexed at the molecular level while maintaining the crystallinity and heat resistance characteristics of the existing polyimide resin. do. Therefore, the heat resistance, abrasion resistance, thermal expansion and mechanical properties are improved, and the low crystallinity can be used as an advanced core heat-resistant material such as mechanical components and semiconductor equipment components in high-tech industries such as electric, electronics, aerospace and aviation. have.

Claims (6)

The inorganic particle powder is dispersed in two or more phenolic organic polar mixed solvents selected from methacresol, para cresol, metachlorophenol and parachlorophenol, and then dissolved by adding a tetracarboxylic dianhydride monomer to the aromatic diamine monomer. After dissolving, the mixed solution was heated to 60 to 80 ° C. over 2 to 3 hours, maintained for 2 to 3 hours in the temperature range, and then heated to 160 to 200 ° C. over 2 to 3 hours. A method of producing a composite material powder composed of a polyamic acid or a polyimide resin having the following formula (2) as a repeating unit and an inorganic material, which is prepared by refluxing for 5 minutes to 6 hours while maintaining a temperature range. [Formula 2]

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