KR20050104042A - A method for preparing metal inner electrode paste having high dispersibility for multi layer ceramic capacitor having high capacity - Google Patents

Abstract

The present invention relates to a method of manufacturing a metal paste for an internal electrode having excellent surface roughness and dispersibility used in manufacturing a high capacity multilayer ceramic capacitor. Per 100 parts by weight of metal powder, 0-1.5 parts by weight of dispersant, 3-7 parts by weight of ethyl cellulose resin and 30-70 parts by weight of terpineol solvent, after pre-caneteri mixing with high viscosity; Premix the ceramic additive, dispersant, and terpineol solvent, and add low viscosity by adding ethylcellulose resin binder to the premix, wherein the ceramic additive, dispersant, ethylcellulose resin and terpineol solvent are 100 wt% Dispersing low viscosity such that 0-1.5 parts by weight of dispersant, 1-5 parts by weight of ethyl cellulose resin, and 30-150 parts by weight of terpineol solvent; Mixing and dispersing the metal dispersion and the ceramic formulation dispersion to 10-30 parts by weight of the ceramic formulation per 100 parts by weight of the metal powder; Viscosity control and vacuum defoaming; And it provides a method of manufacturing a metal paste for the internal electrode comprising the step of filtering the cartridge.

Metal pastes prepared by this method have improved dispersibility and thus exhibit improved surface roughness, dry film density and plastic shrinkage.

Description

A Method for Preparing Metal Inner Electrode Paste Having High Dispersibility for Multi Layer Ceramic Capacitor Having High Capacity

The present invention relates to a method for producing a highly dispersed metal paste for internal electrodes used in the manufacture of high capacity multilayer ceramic capacitors. More specifically, the present invention relates to a method of manufacturing a metal paste for internal electrodes having excellent surface roughness and dispersibility used in manufacturing a high capacity multilayer ceramic capacitor.

In recent years, due to the high performance and light weight of the electric and electronic equipment industries, the miniaturization, high performance, and low cost of electronic components are also required remarkably. In particular, with the advancement of CPU speed, miniaturization, digitization, and high functionalization, multilayer ceramic capacitors (hereinafter referred to as 'MLCC') also meet these demands in terms of miniaturization, thinning, high capacity, and high frequency. Research and development to implement characteristics such as low impedance in the field is active.

Internal paste metal paste, which is a key raw material of high capacity MLCC, is applied to thin dielectric sheet, and when paste is not evenly distributed, aggregates are generated due to poor dispersion, resulting in short and reliability. Degrades. Therefore, a highly dispersed metal paste is required.

In addition, due to the high capacity of MLCC, thinning of the dielectric layer and double layer internal electrode are required, but the internal electrode metal paste manufactured by the conventional paste manufacturing method has poor surface roughness and dispersibility, so that the internal electrode agglomerates after firing. Since this is severe and the electrode thickness is not uniform, the internal electrode thinning is difficult.

The most important thing to consider when manufacturing the internal electrode paste for MLCC is to minimize the internal structural defects such as cracks by reducing the difference in shrinkage between dielectric material with high firing temperature of 1200 ℃ or higher and metal paste, internal electrode. It is to prevent clustering or breaking due to sex.

Since the metal component and the ceramic dielectric in the metal paste are fundamentally different dissimilar materials, there is a big difference in sinterability. The greater the difference in shrinkage between the dielectric layer and the internal electrode layer made of metal paste according to the firing temperature, the greater the rate of internal defects such as cracks. As a method of reducing the shrinkage of the dielectric layer and the metal paste layer, firstly, the ceramic paste is added to the metal paste to suppress sintering of the metal, or second, the plastic film shrinkage ratio is increased by optimizing the dispersion of the metal powder and the additive to increase the dry film density. Minimize.

When nickel powder is used as the metal powder, the sintering shrinkage of Ni is started by delaying the start of sintering shrinkage of Ni, which starts sintering at a relatively low temperature of 400 to 500 ° C, that is, to start the sintering shrinkage at a higher temperature. In order to minimize the difference in shrinkage with the dielectric by delaying the temperature point as much as possible, a ceramic material having a composition similar to that of the dielectric is added as the sintering retardant.

The ceramic material plays a role in delaying the sintering of the metal, which is an internal electrode, during the firing process of MLCC. After the firing of the metal is completed, the ceramic material exits the dielectric layer and affects the electrical properties of the dielectric. Used as In addition, when the size of the ceramic material is larger than the metal powder, the filling rate decreases and the plastic shrinkage rate increases, and since the sintering of the metal powder is not effectively controlled, the ceramic material having a particle size of 0.2 μm or less than the metal powder is generally used as a sintering delay material. do.

For example, as the MLCC for X7 (5) R characteristics, BaTiO ₃ is used as the dielectric, and BT01 (0.1 μm, BaTiO ₃ ), which is manufactured by hydrothermal method and is excellent in morphology, is used as a ceramic material for nickel paste. As the MLCC for Y5V characteristics, (BaCa) (TiZr) O ₃ is used as the dielectric, BTZ01 (0.1 μm, Ba (TiZr) O ₃ ) is used as the ceramic material for the nickel paste.

The preparation of the metal paste for internal electrodes is generally performed in the order of premixing and dispersing the metal powder and the ceramic blank, mixing and dispersing the metal powder dispersion and the blank dispersion, adjusting and defoaming the viscosity, and filtering.

In the manufacture of the metal paste for internal electrodes, how well the paste is dispersed is most important, and particularly in high capacity internal electrode pastes, high dispersibility is required.

On the other hand, even if the internal electrode paste of the same composition, the dispersibility and uniformity of the metal powder and the ceramic co-working material varies according to the manufacturing method, showing a large quality difference.

That is, when the ceramic powder is mixed with the uniformly dispersed metal powder in a state where the ceramic powder is uniformly dispersed, the filling rate of the paste is increased to increase the dry film density. As a result, the ceramic material effectively delays the sintering of the metal paste and thus the Sintering shrinkage also becomes small. Therefore, the difference in shrinkage with the dielectric is minimized, thereby reducing the internal stress caused by the difference in shrinkage, thereby reducing internal structural defects such as cracks.

On the other hand, in the case of paste having poor dispersibility, agglomerates of metal powder or common powder are formed, and these agglomerates cause short defects and lower the breakdown voltage (BDV). It may cause deterioration.

1 illustrates a conventional metal paste dispersion process for internal electrodes. As shown in FIG. 1, conventionally, the metal powder and the common powder are separately mixed and dispersed by high viscosity using a 3-roll mill, then mixed and dispersed in a paste. In the case of metal powder, dispersibility is secured when dispersing high viscosity using 3-roll mill. However, ceramic coarse powder has high hardness, small particle size of less than 0.2㎛, and large specific surface area, so it is hard to disperse evenly in 3-roll mill. . The paste prepared by such a conventional high viscosity manufacturing method is poor in dispersibility and frequently generates aggregates, and the surface roughness is very rough.

As described above, when chips are manufactured using a metal paste for internal electrodes in which aggregates are formed and dispersion is poor, short defects occur, and internal electrode thicknesses become uneven after firing, and electrode connectivity is poor.

Therefore, in order to obtain excellent internal electrode characteristics, a metal paste including a ceramic material having excellent surface roughness and dispersibility is required. By using a metal paste having excellent dispersibility, the dry film density of the metal inner layer is increased and the plastic shrinkage rate is minimized. do.

As the thinning accelerates due to the high capacity of X7 (5) R, the deterioration of paste due to undispersion is directly related to the deterioration of chip characteristics. Paste development is required.

Accordingly, an object of the present invention is to provide a method of manufacturing a metal paste for internal electrodes having excellent surface roughness and dispersibility used in manufacturing a high capacity multilayer ceramic capacitor.

Another object of the present invention is to provide a method for producing a metal paste for internal electrodes having excellent surface roughness and dispersibility, which can form internal electrodes of a thin film having a high dry film density with a uniform thickness without electrode aggregation. .

According to the invention,

Per 100 parts by weight of the metal powder and the metal powder, 0-1.5 parts by weight of dispersant, 3-7 parts by weight of ethyl cellulose resin and 30-70 parts by weight of terpineol solvent, after pre cataneri mixing with high viscosity;

Premix the ceramic additive, dispersant, and terpineol solvent, and add low viscosity by adding ethylcellulose resin binder to the premix, wherein the ceramic filler, dispersant, ethylcellulose resin and terpineol solvent are 100 wt% of ceramic filler. Dispersing low viscosity such that 0-1.5 parts by weight of dispersant, 1-5 parts by weight of ethyl cellulose resin, and 30-150 parts by weight of terpineol solvent;

Mixing and dispersing the metal dispersion and the ceramic formulation dispersion to 10-30 parts by weight of the ceramic formulation per 100 parts by weight of the metal powder;

Viscosity control and vacuum defoaming; And

Cartridge filtering;

There is provided a metal paste manufacturing method for an internal electrode comprising a.

EMBODIMENT OF THE INVENTION Hereinafter, this invention is demonstrated in detail.

When manufacturing high capacity MLCCs, the metal paste used to form the internal electrode layers requires excellent surface roughness and high dispersibility.

When the internal electrode is formed using a metal paste having excellent surface roughness and dispersibility, there is no aggregation of the electrodes and a thin film internal electrode having a uniform thickness is formed. Internal electrodes formed of highly dispersed metal pastes exhibit excellent dry film densities and thus do not generate short circuits and exhibit excellent electrical properties.

2 shows a method for producing a highly dispersed metal paste of the present invention.

According to the method of the present invention, by dispersing the metal powder and the ceramic blank separately and then mixing and dispersing them separately, the ceramic blank may be evenly distributed in the metal powder while uniformly surrounding the respective metal powder to prepare a metal paste for internal electrodes. have.

Dispersibility is ensured when the metal powder is dispersed at a high viscosity, but the ceramic powder has a high hardness, a small particle diameter of 0.2 μm or less, and a large specific surface area.

Therefore, in the present invention, the metal powder is dispersed in high viscosity, the ceramic powder is separately dispersed in low viscosity, and then the metal paste and the metal powder are evenly dispersed by mixing and dispersing the metal dispersion and the ceramic powder. Lose.

The metal powder first premixes the metal powder, optional dispersant, binder resin and solvent so that the binder uniformly wets the metal powder, and then disperses the premix high viscosity.

Caterary premixing refers to a process of uniformly wetting the binder in the metal powder by sequentially adding a small amount of the binder using a high viscosity mixer.

If the binder is not evenly soaked in the metal powder during premixing, the metal powder mass passes through the gap of the 3-roll mill as it is during high viscosity dispersion, which causes metal flakes and the like to reduce the surface roughness of the paste. It will lower and cause a short.

Nickel powder or copper powder may be used as the metal powder, and the average particle size may be 0.2-0.4 μm as the metal powder. High-capacity MLCC has a thin dielectric layer, which is undesirable because the surface roughness of the metal powder exceeds 0.4 μm, resulting in an electrical short. If the particle size is less than 0.2 μm, the plastic shrinkage control is difficult. It is not preferable because it becomes stronger and the surface roughness worsens and an electrical short occurs.

In preparing the metal dispersion, the metal powder, the binder resin, the solvent and the dispersant are premixed and dispersed so that 3-7 parts by weight of the binder resin, 30-70 parts by weight of the solvent and 0-1.5 parts by weight of the dispersant, if necessary, per 100 parts by weight of the metal powder. do.

As an organic binder resin for imparting thixotropy, adhesiveness, and phase stability, ethyl cellulose resin may be dissolved in a solvent and used as a binder. As the ethyl cellulose resin, an ethyl cellulose resin having a high molecular weight and a high viscosity of 180,000-300,000 may be used, and examples thereof include, but are not limited to, STD200 or STD300 manufactured by Dow Chemical.

In preparing the metal dispersion, the binder resin may be used at 3-7 parts by weight per 100 parts by weight of the metal powder. If the content of the binder resin is less than 3 parts by weight, a precipitate is formed. If the content of the binder resin is more than 7 parts by weight, the viscosity exceeds the regulation value, which is not preferable.

As a solvent, terpineol solvent having excellent compatibility with ethyl cellulose resin and high boiling point and having a low drying rate may be used in an amount of 30 to 70 parts by weight per 100 parts by weight of the metal powder. If the solvent content is less than 30 parts by weight, it is not preferable because the viscosity increases to the extent that exceeds the regulation value, and if it exceeds 70 parts by weight, it is not preferable because the content of the metal powder is relatively small.

Terpineol solvents include terpineol, dihydro terpineol, dihydro terpineol acetate and the like.

If necessary, a dispersant may be used at 0-1.5 parts by weight per 100 parts by weight of the metal powder. As the dispersant, an acidic or amine dispersant may be generally used. Although not limited to this, glycine N-methyl-N-[(9Z) -1-oxo-9-octadecynyl etc. can be used as an acidic dispersing agent, and oleylpropylene diamine etc. can be used as an amine dispersing agent. If the content of the dispersant exceeds 1.5 parts by weight, it is not preferable because it is difficult to control the physical properties in the post-treatment such as heat treatment and firing process.

The functional groups of the dispersant adsorb on the surface of the particles to impede the adsorption between the particles and thus the dispersibility is improved, which is related to the particle surface and the type of dispersant functional group, which the person skilled in the art will appreciate depending on the surface polarity of the metal powder. An acidic or acidic dispersant may be appropriately selected and used.

The caterary premix of the metal powder, binder resin, solvent and dispersant is dispersed at high viscosity of 100,000 to 300,000 cps, for example using a 3-roll mill. At this time, if the viscosity is less than 100,000cps, the shear stress is not applied when the high viscosity dispersion, the work is not desired if it exceeds 300,000cps.

In high viscosity dispersion using a three-roll mill, the metal premix is subjected to strong shear stress as it passes between the gaps between the rolls and is highly dispersed. At this time, the shear stress applied to the viscosity of the metal premix increases.

On the other hand, the ceramic composite material is a fine powder having a hardness of 0.2 µm or less having a smaller particle size than the metal powder, and has a low cohesion because of its strong cohesiveness. That is, after pre-mixing a ceramic common material, a solvent, and a dispersing agent, a binder is added to it and low viscosity is disperse | distributed. Low Viscosity Dispersion is dispersion at low viscosities of 100 to 2,000 cps with strong impact and stress. If the viscosity is less than 100 cps, there is a storage problem due to precipitation, and if it exceeds 2000 cps, stirring is impossible in the bead mill, and workability is bad. Low viscosity dispersion can be carried out in a beads mill or a high pressure jet.

BaTiO 3, Ba (TiZr) O 3, CaZrO 3, or SrZrO 3 may be generally used as the ceramic material.

In preparing the common dispersion, the binder resin may be used in an amount of 1-5 parts by weight based on 100 parts by weight of the common material. Precipitation is formed when the content of the binder resin is less than 1 part by weight, and when the content is more than 5 parts by weight, the viscosity is increased beyond the regulation value, which is not preferable.

In the case of co-dispersion, the binder resin can be used by dissolving ethyl cellulose resin in a solvent. As the ethyl cellulose resin, an ethyl cellulose resin having a molecular weight of 180,000-300,000 and a high viscosity or an ethyl cellulose resin having a low molecular weight and a low viscosity of 44,000-140,000 having a molecular weight of 44,000-140,000 can be used. Examples of the ethyl cellulose resin having a low molecular weight and a low viscosity include, but are not limited to, STD45 or STD4 available from Dow Chemical. These resins may be adjusted in consideration of the viscosity depending on the molecular weight, which can be adjusted as needed by those skilled in the art.

As a solvent, terpineol solvent having excellent compatibility with ethyl cellulose resin and high boiling point and having a low drying rate may be used in an amount of 30 to 150 parts by weight based on 100 parts by weight of the common material. If the solvent content is less than 30 parts by weight, it is not preferable because the viscosity increases beyond the regulation value, and if the solvent content is more than 150 parts by weight, the content of the common material is relatively low. The solvent may be added separately in the premixing of the common material and the dispersant, and may also be used as a solvent for the binder resin and added to the common premix.

As terpineol solvent, terpineol, dihydro terpineol, dihetero terpineol acetate and the like can be used.

In one embodiment, at the time of co-mixing, the pre-mixing of the common material, the solvent and the dispersant may be performed, followed by addition of a binder in which the binder resin is dissolved in the solvent, followed by dispersion.

In another embodiment, the common material, solvent, and dispersant may be premixed, firstly dispersed, and then the binder may be added and secondly dispersed.

By separately adding the binder after premixing or primary dispersion, the dispersant may be first adsorbed onto the ceramic blank to further improve the dispersibility of the blank.

In addition, a dispersant may be used in an amount of 0 to 1.5 parts by weight per 100 parts by weight of the common material, if necessary. If the dispersant is used in an amount exceeding 1.5 parts by weight, it is not preferable because it is difficult to control the physical properties in the post-treatment process such as heat treatment and firing process. Phosphate ester dispersants may be used as the dispersant.

The high viscosity dispersion of the metal powder and the low viscosity dispersion of the ceramic blank are combined and mixed in a general mixer and then dispersed in a three-roll mill to obtain a metal paste in which the metal powder and the ceramic blank are evenly dispersed with each other.

At this time, the metal dispersion and the common dispersion are mixed and dispersed so that the common material is 10-30 parts by weight per 100 parts by weight of the metal powder. If the content of vacancy is less than 10 parts by weight, the content of vacancy is not sufficient, which does not effectively delay the contraction of metal components, thus causing cracking and electrode breakage due to mis-matching with the dielectric. This happens. If the content of the common material exceeds 30 parts by weight, the common material is present in a large amount compared to the same metal content. Therefore, the common material is unsuitable because the electrode layer is uneven and the electrical properties deteriorate after the common material diffuses into the dielectric layer.

The dispersed metal paste has a viscosity of 18000 ± 3000 cps using a solvent and diluent. That is, the viscosity is adjusted by diluting to a viscosity suitable for printing. If the viscosity is less than the lower limit, the bleeding point is increased during printing, and if the viscosity is higher than the upper limit, plate separation is difficult and a saddle-shaped printing shape is generated, which adversely affects electrical characteristics.

The viscosity of the metal paste can be adjusted using petroleum solvent diluents such as terpineol solvent and / or mineral spirits.

After adjusting the viscosity, defoaming in vacuum to remove microbubbles and stress trapped inside the paste to stabilize the viscosity. Viscosity control and vacuum defoaming can be carried out, for example, in a high performance planetary mixer.

Thereafter, the remaining aggregates are filtered out using a fine cartridge filter. As the fine cartridge filter, a fine cartridge filter of about 3 μm or less can be used. Accordingly, all aggregates of 3 μm or more in the paste are removed to prevent the occurrence of an electrical short.

The metal paste prepared by the method of the present invention is advantageously used as a metal paste for internal electrodes of high capacity multilayer ceramic capacitors having a dielectric layer thickness of 1.5-6.0 mu m.

Hereinafter, the present invention will be described in detail through examples. However, the following Examples do not limit the present invention.

Example 1

(Conventional example)

64.85 wt% nickel having an average particle diameter of 0.2 μm, 33.83 wt% of a binder, and 1.32 wt% of a cocoyl glutamic acid dispersant were premixed in a Planetary Mixer.

As a binder, the terpineol solvent was heated to 60-90 ° C., stirred, and then added with an ethyl cellulose resin having a molecular weight of about 200,000 and dissolved for at least 5 hours. The undissolved resin was filtered and removed to obtain 8.5wt% ethyl cellulose. A resin solution was prepared and used.

The nickel metal powder premix with a viscosity of 150,000 cps was dispersed five times at a pressure of 7-10 bar in a three roll-mill.

Meanwhile, 54.42 wt% of BaTiO3 ceramic co-material, 38.33 wt% of 8.5% binder, and 7.46 wt% of phosphate ester dispersant were premixed in a Planetary Mixer. The viscosity of the ceramic co-premix was 100,000 cps, which was dispersed five times at a pressure of 7-10 bar in a three roll-mill. As a binder, an ethyl cellulose resin binder prepared in the same manner as used for preparing the metal dispersion was used.

72 wt% of each dispersed nickel metal dispersion and 28 wt% of the ceramic co-dispersion were mixed at 1000 rpm in a planetary mixer and then dispersed at 1000 rpm in a 3 roll-mill.

The dispersed paste was then adjusted to a viscosity of 18000 cps using terpineol solvent and mineral spirit, and the remaining aggregate was removed using a mesh filter (# 1000, SUS) to obtain a nickel paste.

(Invention example)

68.4 wt% nickel, 10. binder 30.58 wt%, and glycine N-methyl-N-[(9Z) -1-oxo-9-octadecynyl 1.02 wt% with an average particle diameter of 0.2 μm. Caterary premixed at Mixer, Inoue, Japan).

As a binder, a terpineol solvent was heated to 60-90 DEG C, and while stirring, an ethyl cellulose resin having a molecular weight of 200,000 was added thereto, dissolved for at least 5 hours, and the undissolved resin was filtered and removed to obtain a 10 wt% ethyl cellulose resin solution. Was prepared and used.

The nickel metal powder premix with a viscosity of 300,000 cps was dispersed five times at a pressure of 7-10 bar in a three roll-mill.

Meanwhile, 33.89wt% of BaTiO3 ceramic co-material, 54.22wt% of terpineol solvent, and 0.68wt% of phosphate ester dispersant were premixed with an impeller in a tank and firstly mixed in a bead mill for 12 hours. Dispersed. Thereafter, 11.21 wt% of a binder binder was added thereto, followed by secondary dispersion in a bead mill. As the binder binder, the same binder as that used for the production of the metal dispersion was used.

72 wt% of each dispersed nickel metal dispersion and 28 wt% of the ceramic co-dispersion dispersion were mixed at 1000 rpm in a planetary mixer, and then dispersed at 1000 rpm in a 3 roll-mill.

The viscosity of the paste was adjusted to about 18000 cps with a terpineol solvent and a mineral spirit diluent in a planetary mixer, and degassed in vacuo to remove microbubbles inside the paste.

Thereafter, the remaining aggregates were filtered out using a 3 μm fine cartridge filter to obtain a final internal electrode paste in which nickel metal powder and common materials were highly dispersed.

The viscosity, surface roughness, dry film density and plastic shrinkage of the nickel paste prepared in the prior art and the invention example were evaluated and the results are shown in Table 1 below.

(Viscosity measurement)

The viscosity of the metal paste for internal electrodes was measured at 14 or 21 spindles after installing a small sample adapter and a thermostat in a viscometer (HBDVII +, Brookfield, USA).

(Surface roughness)

After applying the internal electrode paste on the slide glass using an applicator with a spacing of 10 μm, and drying at a temperature of 100 ° C., a paste dried film having a thickness of about 1.5 μm was manufactured, and then the surface roughness measuring device was contacted (Kosaka, Japan). ), And then the average value of Ra, Rz, Rmax after 10 measurements.

(Dry film density)

The internal electrode paste was applied on the PET film using an applicator with a spacing of 1 mm, dried at a temperature of 100 ° C., cut into a certain size, and the average value of the dry film density was determined after 10 measurements using the Archimedes method. .

(Plastic shrinkage)

After cutting the prepared paste dried film in a circle, the shrinkage rate for each temperature was measured in the same conditions as the MLCC minor component in the experimental furnace and are shown in Table 1 and FIG.

Meanwhile, the microstructure of the paste prepared in Inventive Example 1 was measured at 20,000 magnification using FE-SEM and is shown in FIG. 4, from which it can be seen that the Ni powder and the common material were evenly dispersed in the mixture.

 TABLE 1

Inventive Example Conventional example Viscosity (22 ℃, cps) 18,000 18,000 Surface Roughness (㎛) Ra 0.0383 0.0876 Rz 0.3480 0.7483 Rmax 0.4088 0.9125 Film density (g / cm 3) 5.83 5.5 Plastic Shrinkage (%) 1000 ℃ -5.0 -5.79 1100 ℃ -8.35 -8.00 1200 ℃ -9.92 -11.85 1290 ℃ -10.2 -12.38

As can be seen in Table 1, the surface roughness, dry film density and shrinkage of the paste prepared in the invention example showed excellent results compared to the waste yeast prepared by the conventional method.

On the other hand, the dry film density is high from the graph comparing the firing shrinkage rate by temperature of the X7 (5) R dielectric for MLCC based on BaTiO3 of FIG. 3 and MgO added, the paste according to the invention example and the paste according to the prior art It can be seen that the paste of the invention example has a smaller shrinkage rate depending on the firing temperature than the paste of the prior art.

Example 2: Application and Properties Evaluation for MLCC

(1) Apply 31A106KQN model

Each paste prepared in Examples and Conventional Examples was applied to an internal electrode layer of an X5R characteristic 31A106KQN type (size 3.2 x 1.6 mm, capacity 10 kPa) having a dielectric sheet thickness of 5.5 µm. As pastes for the internal electrodes, the pastes prepared in Examples and Comparative Examples were applied at a lay down of 0.70 mg / cm 2, respectively, and 280 layers were laminated.

MLCC was manufactured by printing, laminating, pressing, calcination, firing, reoxidation, termination, and plating on a dielectric dielectric sheet for mass production.

After lamination, compression was performed at 1200 kgf / cm 2, and calcining was first calcined in air at 250 ° C. for 43 hours, and then calcined at 850 ° C. for 2 hours in nitrogen atmosphere. Firing was carried out at 1290 ° C. in a reducing atmosphere of PO ₂ = ˜10 ⁻¹¹ atm, and reoxidation was performed at 1000 ° C. for 2 hours in an oxygen atmosphere of 25 ppm. The external electrode was terminated using Cu paste, fired at 855 ° C., and plated with Ni.

The capacity, dielectric loss, insulation resistance, insulation breakdown voltage, short, crack and acceleration life of the prepared MLCC are measured and shown in Table 2 below.

Dose and dielectric loss (DF) were measured at 1 kHz and 1 Vrms using a capacitance meter (Agilent, 4284A).

Insulation resistance was measured using a high resistance meter (Agilent, 4339B), and breakdown voltage (BDV) was measured using an HV BDV tester (PR12PF).

Chips whose capacitance was not measured due to an electrical short were counted as shorts, and cracks were counted by observing the cross section with an optical microscope by molding 100 chips. Accelerated life was calculated by measuring the insulation resistance at a temperature of 150 ° C for three hours at three times the rated voltage (6.3V).

[Table 2] Comparison of MLCC (31A106KON) characteristics evaluation results by paste type

Inventive Example Conventional example Capacity 9.90 9.13 DF (%) 3.00 3.12 IR (x 102Ω) 2.1 1.78 BDV (V) 344 300 short(%) 0 10 crack(%) 0 5 Accelerated Life (FIT) (150 ℃, 18.9V, 72hr) 5 80

As can be seen from Table 2, when the paste of the invention example was applied, no short or crack failure rate occurred. In addition, dielectric breakdown voltage (BDV), capacitance value, and accelerated life characteristics were improved over the paste prepared by the conventional dispersion method.

5A and 5B show optical micrographs showing internal electrode connectivity of each paste after polishing of 31A106KQN. Internal electrode connectivity was observed by optical microscopy after etching the internal electrode with Ni etching solution.

In the case of applying the paste prepared by the manufacturing method of the invention example of FIG. 5A, the surface roughness and the electrode shrinkage ratio are small, so that the electrode connection is excellent and the thickness is uniform (1 500 times, 2 times 1000 times). In the case of applying the prepared paste, the surface roughness was poor and the electrode shrinkage rate was large, resulting in severe breakage of the electrode and uneven thickness (① 500 times and ② 1000 times). . As the Ni etching solution, a mixture of 10 ml of water, 38 ml of nitric acid and 100 ml of glacial acetic acid was used.

(2) 31B106KQN model application

The pastes prepared in Examples and Conventional Examples were applied to the X7R characteristic 31B106KQN model having a dielectric sheet thickness of 4.06 μm in the same manner as those applied to the 31A106KQN model, respectively, and are shown in Table 3 below.

[Table 3] MLCC (31B106KON) characteristics according to the paste type

Inventive Example Conventional example Capacity 10.2 9.40 DF (%) 2.25 2.30 BDV (V) 230 210 short(%) 0 12 crack(%) 0 7 Accelerated Life (FIT) (150 ℃, 18.9V, 72hr) 4 80

The short and crack failure rate of the paste prepared by the method of the invention did not occur at all, and the dielectric breakdown voltage (BDV), the capacity value, and the accelerated lifetime were increased compared to the paste prepared by the conventional dispersion method.

The paste prepared by the dispersing method of the present invention is excellent in surface roughness and dispersibility, and exhibits high capacity even when the internal electrode thinning due to the reduction of printing coating amount due to a small shrinkage rate and an increase in internal electrode connectivity after firing. In addition, it is also effective in reducing short and crack defect rates due to thinning of dielectrics.

6A and 6B show SEM photographs (3000x magnification) showing internal electrode connectivity of each paste after polishing of 31B106KQN. The internal electrode connectivity was observed by SEM after the internal electrode was etched with Ni etching solution. In the case of the paste prepared by the manufacturing method of the invention example of FIG. 6A, the electrode was superior to the paste prepared by the conventional manufacturing method of FIG. 6B. Connectivity and thickness uniformity are shown. As the Ni etching solution, a mixture of 10 ml of water, 38 ml of nitric acid and 100 ml of glacial acetic acid was used.

The metal paste for internal electrodes produced by the method of the present invention has improved dispersibility and thus exhibits improved surface roughness, dry film density and plastic shrinkage. Furthermore, when the paste is applied to the MLCC, due to the improved dispersibility of the paste, a uniform internal electrode is formed, and the acceleration life and the internal electrode connectivity are improved, and it is very effective for the thinning of the internal electrode and the high capacity of the MLCC.

1 is a view showing a conventional metal paste manufacturing process step,

2 is a view showing a metal paste manufacturing process step of the present invention,

Figure 3 is a graph showing the plastic shrinkage rate for each temperature of the nickel paste prepared according to the invention examples and conventional examples,

Figure 4 is a photograph showing the microstructure of the nickel paste prepared in the invention example,

Figure 5a is an optical micrograph showing the internal electrode connectivity when applying the paste of the invention to MLCC,

Figure 5b is an optical micrograph showing the internal electrode connectivity when applying the conventional paste to MLCC,

6A is a SEM photograph showing internal electrode connectivity when the paste of the invention is applied to an MLCC.

6B is a SEM photograph showing internal electrode connectivity when a conventional paste is applied to an MLCC.

Claims (10)

Per 100 parts by weight of the metal powder and the metal powder, 0-1.5 parts by weight of dispersant, 3-7 parts by weight of ethyl cellulose resin and 30-70 parts by weight of terpineol solvent, after pre cataneri mixing with high viscosity; Premix the ceramic additive, dispersant, and terpineol solvent, and add low viscosity by adding ethylcellulose resin binder to the premix, wherein the ceramic filler, dispersant, ethylcellulose resin and terpineol solvent are 100 wt% of ceramic filler. Dispersing low viscosity such that 0-1.5 parts by weight of dispersant, 1-5 parts by weight of ethyl cellulose resin, and 30-150 parts by weight of terpineol solvent; Mixing and dispersing the high-viscosity dispersed metal dispersion and the low-viscosity dispersed ceramic formulation dispersion to 10-30 parts by weight of the ceramic formulation per 100 parts by weight of the metal powder; Viscosity control and vacuum defoaming; And Cartridge filtering; Metal paste manufacturing method for an internal electrode comprising a. The method of claim 1, wherein the high viscosity is 100,000-300,000 cps when manufacturing the metal powder dispersion. The method of claim 1, wherein the low viscosity is 100-2,000 cps in the manufacturing method of the common dispersion. The method of claim 1, wherein the metal powder is nickel powder or copper powder. The method of claim 1, wherein the dispersant is an acidic or amine based dispersant. The method of claim 1, wherein the ceramic material is selected from the group consisting of BaTiO 3, Ba (TiZr) O 3, CaZrO 3, and SrZrO 3. The method of claim 1, wherein the dispersant used in dispersing the ceramic co-process is a phosphate ester. The internal electrode dispersion according to claim 1, wherein the common material dispersion is performed by premixing the ceramic material, the dispersant, and the terpineol solvent, dispersing in one step, adding an ethyl cellulose resin binder, and dispersing in two steps. Metal paste manufacturing method. The method of claim 1, wherein the viscosity control is performed using a terpineol solvent and a petroleum solvent diluent. The method of claim 1, wherein the viscosity is controlled to 18000 ± 3000 cps in the viscosity control.