U.S. patent application number 09/773908 was filed with the patent office on 2001-08-16 for nickel powder and conductive paste.
This patent application is currently assigned to Mitsui Mining and Smelting Co., Ltd.. Invention is credited to Hayashi, Takao, Yamaguchi, Yasuhide.
Application Number | 20010013263 09/773908 |
Document ID | / |
Family ID | 18552070 |
Filed Date | 2001-08-16 |
United States Patent
Application |
20010013263 |
Kind Code |
A1 |
Yamaguchi, Yasuhide ; et
al. |
August 16, 2001 |
Nickel powder and conductive paste
Abstract
Nickel powder herein disclosed has an average particle size, as
determined by the observation with SEM, of not more than 1 .mu.m, a
particle density of not less than 8.0 g/cm.sup.3, and an average
diameter of crystallites present in the nickel particles of not
more than 550 .ANG.. Moreover, a conductive paste for a multilayer
ceramic capacitor comprises the foregoing nickel powder. The nickel
powder and the conductive paste containing the same can control
heat shrinkage while inhibiting any rapid oxidation and permit the
production of a thin, uniform internal electrode for a multilayer
ceramic capacitor without being accompanied by any crack formation
and delamination during firing.
Inventors: |
Yamaguchi, Yasuhide;
(Yamaguchi, JP) ; Hayashi, Takao; (Yamaguchi,
JP) |
Correspondence
Address: |
YOUNG & THOMPSON
745 SOUTH 23RD STREET 2ND FLOOR
ARLINGTON
VA
22202
|
Assignee: |
Mitsui Mining and Smelting Co.,
Ltd.
|
Family ID: |
18552070 |
Appl. No.: |
09/773908 |
Filed: |
February 2, 2001 |
Current U.S.
Class: |
75/255 |
Current CPC
Class: |
B22F 1/07 20220101; H01G
4/0085 20130101; B22F 9/24 20130101; B22F 1/0007 20130101 |
Class at
Publication: |
75/255 |
International
Class: |
B22F 001/00 |
Foreign Application Data
Date |
Code |
Application Number |
Feb 3, 2000 |
JP |
2000-026319 |
Claims
What is claimed is:
1. Nickel powder having an average particle size, as determined by
the observation with SEM, of not more than 1 .mu.m, a particle
density of not less than 8.0 g/cm.sup.3, and an average diameter of
crystallites present in the nickel particles of not more than 550
.ANG..
2. The nickel powder as set forth in claim 1 wherein it has an
average particle size, as determined by the observation with SEM,
ranging from 0.1 to 1 .mu.m, a particle density of not less than
8.3 g/cm.sup.3, and an average diameter of crystallites present in
the nickel particles of not more than 500 .ANG..
3. The nickel powder as set forth in claim 2 wherein the average
diameter of crystallites present in the nickel particles is not
more than 300 .ANG..
4. The nickel powder as set forth in claim 1 wherein it is prepared
according to a wet method.
5. The nickel powder as set forth in claim 2 wherein it is prepared
according to a wet method.
6. The nickel powder as set forth in claim 3 wherein it is prepared
according to a wet method.
7. A conductive paste for a multilayer ceramic capacitor comprising
nickel powder as set forth in claim 1.
8. A conductive paste for a multilayer ceramic capacitor comprising
nickel powder as set forth in claim 2.
9. A conductive paste for a multilayer ceramic capacitor comprising
nickel powder as set forth in claim 3.
10. A conductive paste for a multilayer ceramic capacitor
comprising nickel powder as set forth in claim 4.
11. A conductive paste for a multilayer ceramic capacitor
comprising nickel powder as set forth in claim 5.
12. A conductive paste for a multilayer ceramic capacitor
comprising nickel powder as set forth in claim 6.
Description
BACKGROUND OF THE INVENTION
[0001] (a) Field of the Invention
[0002] The present invention relates to nickel powder and a
conductive paste containing the same and more particularly to
nickel powder and a conductive paste containing the same, which can
control heat shrinkage while inhibiting the occurrence of any rapid
oxidation and which permit the production of a thin, uniform
internal electrode for a multilayer ceramic capacitor without being
accompanied by any crack formation and delamination during
firing.
[0003] (b) Description of the Prior Art
[0004] A multilayer ceramic capacitor comprises a plurality of
ceramic dielectric layers and internal electrode layers, which are
alternately laminated and united. In the production of the internal
electrode for such a multilayer ceramic capacitor, it is common
that metal fine powder as a material for internal electrodes is
first formed into a paste thereof to give a conductive paste,
followed by printing a green sheet of a ceramic dielectric with the
resulting conductive paste, alternately putting, in layers, a
plurality of these green sheets of the ceramic dielectric and the
conductive paste layers, attaching the latter to the former using
pressure to thus unify them, and then firing the resulting
laminated assembly in a reducing atmosphere at a high temperature
to thus firmly unify the ceramic dielectric layers and the internal
electrodes.
[0005] As materials for such an internal electrode, there have
conventionally been used, for instance, precious metals such as
platinum, palladium and silver-palladium. However, there have
recently been developed techniques in which base metals such as
nickel are substituted for these precious metals and such
techniques have gradually been advanced, for the purpose of
reducing the production cost. When forming a conductive paste layer
using a paste containing nickel powder and then firing the
resulting paste layer to produce a thin and uniform internal
electrode, however, problems such as crack formation and
delamination arise. The occurrence of such crack formation and
delamination would be caused due to, for instance, heat shrinkage
of the conductive paste layer during firing.
[0006] Accordingly, there have conventionally been proposed a
variety of powdery nickel products, which can solve the problem of
heat shrinkage during firing.
SUMMARY OF THE INVENTION
[0007] Similarly, it is an object of the present invention to
provide nickel powder as well as a conductive paste containing the
nickel powder, which can control heat shrinkage while inhibiting
the occurrence of any rapid oxidation and which accordingly, permit
the production of a thin, uniform internal electrode for a
multilayer ceramic capacitor without being accompanied by any crack
formation and delamination during firing.
[0008] The inventors of this invention have conducted various
studies to solve the foregoing problems associated with the
conventional techniques, have found that the foregoing problems of
rapid increase in the oxidation of the conductive paste layer and
the heat shrinkage thereof during firing are solved by increasing
the average particle density of the nickel powder to a level
greater than a desired value and reducing the average diameter of
the crystallites present in the particles to a level smaller than a
predetermined value and that the resulting conductive paste permits
gentle sintering, can ensure a uniform sintering speed and
accordingly, permits the formation of a thin and uniform internal
electrode for a multilayer ceramic capacitor without being
accompanied by any crack formation and delamination, and have thus
completed the present invention based on the foregoing
findings.
[0009] According to an aspect of the present invention, there is
provided nickel powder having an average particle size, as
determined by the observation under a scanning electron microscope
(SEM), of not more than 1 .mu.m, a particle density of not less
than 8.0 g/cm.sup.3, and an average diameter of crystallites
present in the nickel particles of not more than 550 .ANG..
[0010] According to a second aspect of the present invention, there
is provided a conductive paste, which comprises nickel powder
having characteristic properties defined above.
DETAILED DESCRIPTION OF THE INVENTION
[0011] The nickel powder of the present invention is particularly
suitable for use in making an internal electrode for a multilayer
ceramic capacitor or in the preparation of a conductive paste for a
multilayer ceramic capacitor. Accordingly, the average particle
size of the nickel powder of the present invention, as determined
by the observation thereof with an SEM with a magnification of
about .times.10000, is limited to a level of not more than 1 .mu.m,
preferably 0.1 to 1 .mu.m and more preferably 0.2 to 0.8 .mu.m,
while taking into consideration the foregoing applications of the
nickel powder.
[0012] The meaning of the term "particle density", used in this
specification, is identical to that defined in JIS R 1600 (1993).
More specifically, the term "particle density" is the density of
particles, in which the closed spaces included in the particles are
likewise regarded as parts of particles. If the particle density is
reduced, the amount of void spaces present within particles
correspondingly increases, while if the particle density increases,
the amount of void spaces present within particles are
correspondingly reduced. These void spaces expand when exposed to a
high temperature during the high temperature firing step in the
production of a multilayer ceramic capacitor and at least part
thereof is destroyed to cause shrinkage of the particle. Thus, the
presence of such void spaces would greatly affect the thermal
properties, in particular, heat shrinkage of the conductive paste
layer containing nickel powder. In the present invention, the
particle density of the nickel powder is controlled to not less
than 8.0 g/cm.sup.3, preferably not less than 8.3 g/cm.sup.3 and
more preferably not less than 8.5 g/cm.sup.3. Increasing the
particle density of the nickel powder can thus eliminate the
problems of any crack formation and delamination.
[0013] Moreover, the average diameter of crystallites present in
the nickel particles of nickel powder of the present invention is
controlled to a level of not more than 550 .ANG., preferably not
more than 500 .ANG. and more preferably not more than 300 .ANG.. A
product obtained using a paste containing such nickel powder, for
instance, a multilayer ceramic capacitor, is composed of a tidy
sintered film and the sintering of the paste proceeds gently
because the average diameter of the crystallites present in the
nickel particles is small. In other words, the sintering of such a
paste rapidly proceeds if the crystallites present in the nickel
particles have a large diameter, but if the average diameter
thereof is small, the crystallites present in the nickel particles
are first sintered and then the sintering between the nickel
particles gradually proceeds. Accordingly, the nickel
powder-containing paste is gradually sintered at a uniform speed to
thus form a tidy film and the paste hardly causes any crack
formation and delamination.
[0014] As has been discussed above in detail, the nickel powder of
the present invention has an average particle size as determined by
the SEM observation thereof of not more than 1 .mu.m, a particle
density of not less than 8.0 g/cm.sup.3, and an average diameter of
crystallites present in the nickel particle of not more than 550
.ANG.. Accordingly, the conductive paste obtained using such nickel
powder would permit the formation of a thin and uniform internal
electrode for a product such as a multilayer ceramic capacitor,
without causing any crack formation and delamination during
firing.
[0015] The nickel powder of the present invention, which satisfies
various requirements discussed above, is suitably used for
preparing a conductive paste, in particular, a conductive paste for
making a multilayer ceramic capacitor.
[0016] Therefore, the conductive paste according to the present
invention comprises the foregoing nickel powder having excellent
characteristic properties described above and is thus particularly
suitable for use in making a thin and uniform internal electrode
for a multilayer ceramic capacitor.
[0017] Now, we will hereunder explain a preferred method for
preparing the nickel powder of the present invention.
[0018] The nickel powder of the present invention can be prepared
by either a wet method or a dry method, but it is preferably
prepared by a wet method. In such a wet method for preparing the
nickel powder of the present invention, for example, nickel
hydroxide prepared by reacting a nickel salt with an alkali or
commercially available nickel hydroxide per se is reduced by
bringing it into contact with a hydrazine type reducing agent at a
temperature condition of not less than 55.degree. C., while the
rate of nucleation and the rate of growth of fine nickel particles
are stepwise controlled. Examples of such nickel salts are nickel
sulfate, nickel nitrate and nickel halides such as nickel chloride.
On the other hand, examples of such alkalis are sodium hydroxide,
potassium hydroxide and calcium hydroxide. Examples of the
foregoing hydrazine type reducing agents are hydrazine, hydrazine
hydrate, hydrazine sulfate, hydrazine carbonate and hydrazine
hydrochloride.
[0019] Regarding the temperature conditions for the reducing
reaction of the nickel hydroxide, it is preferable to add a
reducing agent to the reactant at a temperature of less than
50.degree. C. and then gradually raise the temperature to a
temperature of not less than 55.degree. C. to proceed the reaction
slowly. By using this process, a nickel powder can be obtained,
which has a small average diameter of crystallites, a high particle
density and a uniform average particle size.
[0020] In particular, the nickel powder having a particle density
of not less than 8.0 g/cm.sup.3 and a uniform particle size as
determined by the SEM observation can be prepared by adding an
aqueous solution of hydrazine to nickel hydroxide obtained through
a reaction of a nickel salt with sodium hydroxide or commercially
available nickel hydroxide per se at a temperature of less than
50.degree. C. and then gradually raising the temperature at a
heating speed of not more than 5.degree. C./min to a temperature of
not less than 55.degree. C., preferably not less than 60.degree. C.
to proceed the reduction slowly and the resulting nickel powder has
a quite low content of the whole impurities derived from the
starting materials.
[0021] The nickel powder of the present invention can be obtained
in the form of monodispersed nickel powder, which is obtained by
bringing nickel hydroxide into contact with a hydrazine type
reducing agent at a temperature of not less than 55.degree. C. to
thus reduce the hydroxide and then the resulting powdery product is
subjected to a pulverization treatment. Such pulverization
treatment usable herein are, for instance, high speed rotary
collision-pulverization treatment in which nickel powder is
pulverized by leading a rotary part, rotating at a high speed, of a
pulverizer to collide with the powder; a medium-stirring
pulverization treatment in which nickel powder is stirred with, for
instance, beads to thus pulverize the same; a high hydraulic
pressure pulverization treatment, which comprises colliding two
streams of aqueous nickel powder slurries injected from different
directions at a high hydraulic pressure to thus pulverize the
nickel powder; and a jet-impact treatment and one can use, for
instance, a high speed moving body-collision type air pulverizer,
an impact type pulverizer, a cage mill, a medium-stirring type
mill, axial-flow mill and a jet-colliding device.
[0022] Next, we will explain a preferred method for preparing a
conductive paste according to the present invention, below in
detail.
[0023] The conductive paste of the present invention is constituted
by, for instance, the foregoing nickel powder of the present
invention, a resin and a solvent. Optionally, it may further
comprise a dispersant, a sintering-inhibitory agent or the like.
More specifically, examples of such resins usable herein are
cellulose derivatives such as ethyl cellulose, vinylic non-curable
resins such as acrylic resins, polyvinyl butyral resins and
polyvinyl alcohol, and thermosetting resins preferably used in
combination with peroxides, such as epoxy resins and acrylic
resins. Resins usable herein further include, for instance, UV
curable resins, electron beam-curable resins such as epoxy acrylate
resins, polybutadiene acrylate resins and urethane acrylate resins
modified with acrylic acid or methacrylic acid, and unsaturated
polyesters. In this connection, in case where the resin used is a
UV curable resin, an optical initiator should be used and examples
thereof include benzoin, acetophenone, benzyl, benzophenone and
benzoin butyl ether. In addition, examples of such solvents usable
herein are terpineol, tetralin, butyl carbitol and carbitol
acetate, which may be used alone or in any combination. Moreover,
this paste may if necessary comprise glass frits. The conductive
paste of the present invention can be prepared by mixing and
stirring the foregoing raw materials in a mixing device such as a
ball mill or a three-roll mill.
[0024] The nickel powder of the present invention permits the
control of any thermal shrinkage of the resulting sheet or film
while inhibiting any rapid oxidation and as a result, the powder
permits the formation of a thin and uniform internal electrode for
a multilayer ceramic capacitor without causing any crack formation
and delamination. Thus, the nickel powder of the present invention
is suitably used for preparing a conductive paste, in particular, a
conductive paste for a multilayer ceramic capacitor.
[0025] In addition, the conductive paste according to the present
invention comprises nickel powder having the foregoing excellent
characteristic properties and therefore, the paste is particularly
suitably used in making a thin and uniform internal electrode for a
multilayer ceramic capacitor.
[0026] The present invention will now be described below in detail
with reference to the following working Examples and Comparative
Examples.
EXAMPLE 1 (WORKING EXAMPLE)
[0027] To one liter of an aqueous solution of sodium hydroxide
having a concentration of 200 g/L, there was gradually dropwise
added an aqueous solution prepared by dissolving 448 g of nickel
sulfate hexahydrate (nickel content: 22.2% by mass) in 800 mL of
pure water, while maintaining the temperature of the mixture to
60.degree. C. to thus precipitate nickel hydroxide. The resulting
suspension was cooled to 40.degree. C. and then 300 g of hydrazine
monohydrate was added slowly over 30 minutes to control temperature
rise. After the addition was finished, the suspension was gradually
heated at a heating speed of 1.degree. C./min to a temperature of
60.degree. C. As the temperature raised, the nickel hydroxide was
reduced into elemental nickel slowly. The resulting nickel
particles was pulverized. The nickel powder thus prepared was
washed with pure water till the pH of the wash liquid reached a
level of not more than 9, followed by filtration thereof and drying
to give a final nickel powder.
[0028] The resulting nickel powder was observed under an SEM with a
magnification of .times.10000 and particle sizes of 1500 particles
present in randomly selected 5 visual fields were determined. As a
result, the average particle size of the nickel powder was found to
be 0.58 .mu.m. Moreover, the particle density of this nickel powder
was determined at room temperature using Multivolume Pycnometer
1305 (available from Micrometrics Co., Ltd. In the United States)
and it was found to be 8.71 g/cm.sup.3. In addition, the average
diameter of crystallites present in the nickel particles was
likewise determined and was found to be 168 .ANG..
[0029] Further, a pressure of 1 t/cm.sup.3 was applied to 0.5 g of
the nickel powder to thus convert the powder into a pellet having a
diameter of 5 mm and a height of about 6 mm. This pellet was
inspected for the heat shrinkage using a thermomechanical analysis
device (TMA/SS6000 available from Seiko Instruments Inc.) in a
nitrogen gas atmosphere at a heating speed of 10.degree. C./min. As
a result, results shown in the following Table 1 were obtained. In
this connection, each heat shrinkage value was one relative to that
observed for the pellet prior to heating.
[0030] Separately, there was added, to 100 part by mass of the
nickel powder, a vehicle, which consisted of 8 parts by mass of
ethyl cellulose, 100 parts by mass of terpineol and 12 parts by
mass of butyl carbitol, followed by admixing these ingredients,
then kneading them in a roll mill to form a conductive paste and
preparation of a multilayer ceramic capacitor of
2.0.times.1.25.times.1.25 mm by firing an assembly comprising 350
laminated layers of dielectric layers (each having a thickness of 2
.mu.m) and internal electrode layers prepared from the conductive
paste (each having a thickness of 1.5 .mu.m). Then the number of
rejected products was determined by randomly selecting 200
multilayer ceramic capacitors among these capacitors thus prepared
and inspection of them for the crack formation and delamination. As
a result, the number of rejected products was found to be 4 and
accordingly, the reject rate was calculated to be only 2%.
[0031] The results obtained in the foregoing determination and
evaluation are summarized and listed in the following Table 1.
EXAMPLE 2 (WORKING EXAMPLE)
[0032] To one liter of an aqueous solution of sodium hydroxide
having a concentration of 200 g/L, there was gradually dropwise
added an aqueous solution prepared by dissolving 448 g of nickel
sulfate hexahydrate (nickel content: 22.2% by mass) in 800 mL of
pure water, while maintaining the temperature of the mixture to
60.degree. C. to thus precipitate nickel hydroxide. The resulting
suspension was cooled to 40.degree. C. and then 420 g of hydrazine
monohydrate was added slowly over 40 minutes to control temperature
rise. After the addition was finished, the suspension was gradually
heated at a heating speed of 4.degree. C./min to a temperature of
65.degree. C. As the temperature raised, the nickel hydroxide was
reduced into elemental nickel slowly. The resulting nickel
particles was pulverized. The nickel powder thus prepared was
washed with pure water till the pH of the wash liquid reached a
level of not more than 9, followed by filtration thereof and drying
to give a final nickel powder.
[0033] The resulting nickel powder was subjected to the
determination of various characteristic properties according to the
same methods used in Example 1. Moreover, a conductive paste and
multilayer ceramic capacitors were prepared by repeating the same
procedures used in Example 1 to thus determine the number of
products rejected due to crack formation and delamination according
to the same method used in Example 1. The results thus obtained in
the foregoing determination and evaluation are likewise summarized
and listed in the following Table 1.
EXAMPLE 3 (COMPARATIVE EXAMPLE)
[0034] To one liter of an aqueous solution of sodium hydroxide
having a concentration of 140 g/L, there was gradually dropwise
added an aqueous solution prepared by dissolving 448 g of nickel
sulfate hexahydrate (nickel content: 22.2% by mass) in 1 L of pure
water, while maintaining the temperature of the mixture to
45.degree. C. to thus precipitate nickel hydroxide. To the
resulting suspension, there was added 260 g of hydrazine
monohydrate over 20 minutes to thus reduce the nickel hydroxide
into elemental nickel and then pulverization of the resulting
nickel particles. The nickel powder thus prepared was washed with
pure water till the pH of the wash liquid reached a level of not
more than 9, followed by filtration thereof and drying to give a
final nickel powder.
[0035] The resulting nickel powder was subjected to the
determination of various characteristic properties according to the
same methods used in Example 1. Moreover, a conductive paste and
multilayer ceramic capacitors were prepared by repeating the same
procedures used in Example 1 to thus determine the number of
products rejected due to crack formation and delamination according
to the same method used in Example 1. The results thus obtained in
the foregoing determination and evaluation are likewise summarized
and listed in the following Table 1.
EXAMPLE 4 (COMPARATIVE EXAMPLE)
[0036] Sufficiently dried anhydrous nickel chloride (22.0 kg)
having a sulfur content of 500 ppm was allowed to stand in a quartz
container and then heated in an argon gas stream as a carrier
having a flow rate of 10 L/min while maintaining the temperature
within the container to 900.degree. C. to thus evaporate nickel
chloride. Hydrogen gas for reduction was passed through the
vaporized nickel chloride gas, at a flow rate of 3.5 L/min, while
controlling the reduction temperature to 1000.degree. C. to thus
convert the nickel chloride gas into nickel powder. The resulting
nickel powder was washed with pure water till the pH of the wash
liquid was not more than 9, followed by filtration thereof, then
drying and introduction of the nickel powder thus washed with water
into a pulverizer Model AP-1SH (available from Hosokawa Micron Co.,
Ltd.) equipped with a knife-like hammer to thus pulverize the
nickel powder at a rotational speed of 2500 rpm. The pulverized
nickel powder was treated using an air separator, i.e., SF Sharp
Cut Separator Model KSC-02 (available from Kurimoto, Ltd.) at a
rotational speed of a rotor of 6000 rpm and a flow rate of the air
of 7.2 m.sup.3/min to thus remove coarse particles and to give
final nickel powder.
[0037] The resulting nickel powder was subjected to the
determination of various characteristic properties according to the
same methods used in Example 1. Moreover, a conductive paste and
multilayer ceramic capacitors were prepared by repeating the same
procedures used in Example 1 to thus determine the number of
products rejected due to crack formation and delamination according
to the same method used in Example 1. The results thus obtained in
the foregoing determination and evaluation are likewise summarized
and listed in the following Table 1.
1 TABLE 1 Example Number 1 2 3* 4* Average Particle Size (.mu.m)
0.58 0.22 0.71 0.62 Particle Density (g/cm.sup.3) 8.71 8.31 7.68
8.68 Average Diameter of Crystallite 168 142 152 560 (.ANG.) Heat
Shrinkage (%) 500.degree. C. -0.2 -0.4 -0.6 -0.4 700.degree. C.
-0.6 -0.5 -1.9 -0.8 900.degree. C. -2.8 -2.2 -7.8 -4.8 1100.degree.
C. -8.6 -7.7 -14.3 -12.7 Evaluation of Ceramic Capacitor Number of
Rejected Products 4 2 24 20 (number) Reject Rate (%) 2 1 12 10 *:
Comparative Example
* * * * *