U.S. patent application number 12/400523 was filed with the patent office on 2009-07-09 for secondary cell electrode and fabrication method, and secondary cell, complex cell, and vehicle.
This patent application is currently assigned to NISSAN MOTOR CO., LTD.. Invention is credited to Mori Nagayama, Takamistu Saito, Osamu Shimamura.
Application Number | 20090173632 12/400523 |
Document ID | / |
Family ID | 34117922 |
Filed Date | 2009-07-09 |
United States Patent
Application |
20090173632 |
Kind Code |
A1 |
Nagayama; Mori ; et
al. |
July 9, 2009 |
SECONDARY CELL ELECTRODE AND FABRICATION METHOD, AND SECONDARY
CELL, COMPLEX CELL, AND VEHICLE
Abstract
In a nonaqueous electrolyte cell-oriented electrode (10), an
electrode active material layer (12) formed on a collector (1) has
a density gradient developed with a gradient of a varied
concentration of a solid along a thickness from a surface of the
electrode active material layer (12) toward the collector (1), and
in a gel electrolyte cell-oriented electrode (30), an electrode
active material layer (32) formed on a collector (1) has a density
gradient developed with (a) gradient(s) of (a) varied
concentration(s) of one or both of an electrolyte salt and a film
forming material along a thickness from a surface of the electrode
active material layer (32) toward the collector (1).
Inventors: |
Nagayama; Mori;
(Yokohama-shi, JP) ; Saito; Takamistu;
(Yokohama-shi, JP) ; Shimamura; Osamu;
(Yokohama-shi, JP) |
Correspondence
Address: |
FOLEY AND LARDNER LLP;SUITE 500
3000 K STREET NW
WASHINGTON
DC
20007
US
|
Assignee: |
NISSAN MOTOR CO., LTD.
|
Family ID: |
34117922 |
Appl. No.: |
12/400523 |
Filed: |
March 9, 2009 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
|
|
10565171 |
Jan 19, 2006 |
|
|
|
PCT/JP04/11021 |
Jul 27, 2004 |
|
|
|
12400523 |
|
|
|
|
Current U.S.
Class: |
205/98 ;
427/58 |
Current CPC
Class: |
H01M 4/02 20130101; Y02E
60/10 20130101; H01M 50/543 20210101; H01M 4/366 20130101; H01M
2300/0022 20130101; H01M 10/0525 20130101; H01M 2300/0085 20130101;
H01M 4/0404 20130101 |
Class at
Publication: |
205/98 ;
427/58 |
International
Class: |
C25B 11/00 20060101
C25B011/00; C25D 21/14 20060101 C25D021/14 |
Foreign Application Data
Date |
Code |
Application Number |
Jul 31, 2003 |
JP |
2003-283974 |
Jul 31, 2003 |
JP |
2003-283975 |
Claims
1. A fabrication method comprising fabricating a secondary cell
electrode comprising an electrode active material layer having a
density gradient.
2. The fabrication method as claimed in claim 1, wherein the
secondary cell electrode comprises a nonaqueous electrolyte
cell-oriented electrode, comprising: (a) changing a quantity of a
solid to be added to compose the electrode active material layer,
thereby preparing a plurality of kinds of electrode slurry
different in concentration of the solid; and (b) coating a
collector with the plurality of kinds of electrode slurry so that
the density gradient is developed with a gradient of a
concentration of the solid sequentially increased from a surface of
the electrode active material layer toward the collector, thereby
laminating a plurality of thin film layers different in
concentration of the solid.
3. The fabrication method as claimed in claim 2, wherein a thin
film layer is coated by a thickness within a range of 1-100 .mu.m
in the step (b).
4. The fabrication method as claimed in claim 2, wherein the
electrode slurry is coated onto the collector by an ink jet method
in the step (b).
5. The fabrication method as claimed in claim 4, wherein the ink
jet method employs a piezo system.
6. The fabrication method as claimed in claim 1, wherein the
secondary cell electrode comprises a gel electrolyte cell-oriented
electrode, comprising: (a) changing a quantity of an electrolyte
salt to be added to compose the electrode active material layer,
thereby preparing a plurality of kinds of electrode slurry
different in concentration of the electrolyte salt; and (b) coating
a collector with the plurality of kinds of electrode slurry so that
the density gradient is developed with a gradient of a
concentration of the electrolyte salt from a surface of the
electrode active material layer toward the collector, thereby
laminating a plurality of thin film layers different in
concentration of the electrolyte salt.
7. The fabrication method as claimed in claim 1, wherein the
secondary cell electrode comprises a gel electrolyte cell-oriented
electrode, comprising: (a) changing a quantity of a film forming
raw material to be added to compose the electrode active material
layer, thereby preparing a plurality of kinds of electrode slurry
different in concentration of the film forming raw material; and
(b) coating a collector with the plurality of kinds of electrode
slurry so that the density gradient is developed with a gradient of
a concentration of the film forming raw material from a surface of
the electrode active material layer toward the collector, thereby
laminating a plurality of thin film layers different in
concentration of the film forming raw material.
8. The fabrication method as claimed in claim 1, wherein the
secondary cell electrode comprises a gel electrolyte cell-oriented
electrode, comprising: (a) changing quantities of an electrolyte
salt and a film forming raw material to be added to compose the
electrode active material layer, thereby preparing a plurality of
kinds of electrode slurry different in concentrations of the
electrolyte salt and the film forming raw material; and (b) coating
a collector with the plurality of kinds of electrode slurry so that
the density gradient is developed with gradients of concentrations
of the electrolyte salt and the film forming raw material from a
surface of the electrode active material layer toward the
collector, thereby laminating a plurality of thin film layers
different in concentrations of the electrolyte salt and film
forming raw material.
9. The fabrication method as claimed in claim 6, wherein a thin
film layer is coated by a thickness within a range of 1-100 .mu.m
in the step (b).
10. The fabrication method as claimed in claim 7, wherein a thin
film layer is coated by a thickness within a range of 1-100 .mu.m
in the step (b).
11. The fabrication method as claimed in claim 8, wherein a thin
film layer is coated by a thickness within a range of 1-100 .mu.m
in the step (b).
12. The fabrication method as claimed in claim 6, wherein the
electrode slurry is coated onto the collector by an ink jet method
in the step (b).
13. The fabrication method as claimed in claim 7, wherein the
electrode slurry is coated onto the collector by an ink jet method
in the step (b).
14. The fabrication method as claimed in claim 8, wherein the
electrode slurry is coated onto the collector by an ink jet method
in the step (b).
15. The fabrication method as claimed in claim 12, wherein the ink
jet method employs a piezo system.
16. The fabrication method as claimed in claim 13, wherein the ink
jet method employs a piezo system.
17. The fabrication method as claimed in claim 14, wherein the ink
jet method employs a piezo system.
Description
[0001] The present application is a divisional of U.S. application
Ser. No. 10/565,171, filed Jan. 19, 2006, which is the national
stage entry of PCT/JP2004/011021, filed Jul. 27, 2004, which in
turn claims benefit of priority to Japanese application Nos.
2003-283974 and 2003-283975, both filed Jul. 31, 2003, the entire
contents of which are incorporated herein by reference.
TECHNICAL FIELD
[0002] The present invention relates to a secondary cell electrode,
and particularly, to a nonaqueous electrolyte electrode and a gel
electrolyte electrode, and further to a fabrication method of the
same, as well as to a secondary cell employing the secondary cell
electrode, a complex cell employing the secondary cell, and a
vehicle employing the secondary cell or the complex cell.
BACKGROUND ART
[0003] Recent years have observed, on the background with a rising
trend for environmental protection, demands for a promoted
introduction of an electric vehicle (EV), a hybrid vehicle (HEV),
and a fuel cell powered vehicle (FCV), as well as developments of
cells for their drive motors.
[0004] For objectives needing high output and high energy density
such as for driving a motor of EV, HEV, or FCV, it practically is
difficult to cope with a big-scale simplex cell, and a typical
measure is the use of a complex cell composed of a plurality of
serially connected cells. For use to such a complex cell, Japanese
Patent Application Laid-Open Publication No. 2003-151526 has
proposed a thin laminate cell.
DISCLOSURE OF THE INVENTION
[0005] This laminate cell has a positive or negative polarized
electrode formed with an electrode active material spread over a
collector or foil, by using a coater or the like, thus having a
three-dimensionally uniform concentration of solid material or
electrolyte ingredients.
[0006] As will be discussed later, such a laminate cell suffers an
unfavorable tendency for Li ions to be exhausted in a charge or
discharge at a high current rate, resulting in a reduced cell
performance such as charge or discharge capacity.
[0007] The present invention has been made with such points in
view. It therefore is an object of the invention to provide a
secondary cell electrode that works even at a high current rate,
and a fabrication method therefor, as well as a secondary cell, a
complex cell, and a vehicle employing such a secondary cell.
[0008] The present inventors have found using such an electrode
that has an electrode active material layer low of the resistance
to diffusion of Li ions supplied from an electrolyte layer, with a
changed constitution of electrolyte in a patterning of the
layer.
[0009] To achieve the object, a first aspect of the invention
provides a secondary cell electrode comprising an electrode active
material layer having a density gradient.
[0010] Another aspect of the invention provides a fabrication
method comprising fabricating a secondary cell electrode comprising
an electrode active material layer having a density gradient.
[0011] Another aspect of the invention provides a secondary cell
comprising the secondary cell electrode.
[0012] Another aspect of the invention provides a complex cell
comprising a plurality of secondary cells connected to each
other.
[0013] Another aspect of the invention provides a complex cell
comprising a plurality of secondary cells fabricated by the
fabrication method, connected to each other.
[0014] Another aspect of the invention provides a vehicle including
the secondary cell.
[0015] Another aspect of the invention provides a vehicle including
a secondary cell fabricated by the fabrication method.
[0016] Other and further features, advantages, and benefits of the
present invention will become more apparent from the following
description taken in conjunction with the accompanying
drawings.
BRIEF DESCRIPTION OF THE DRAWINGS
[0017] FIG. 1 is a section of an electrode of a typical nonaqueous
electrolyte secondary cell.
[0018] FIG. 2 is a section of an electrode of a nonaqueous
electrolyte secondary cell according to a first embodiment of the
invention.
[0019] FIG. 3 is a section of an electrode of a nonaqueous
electrolyte secondary cell according to a modification of the first
embodiment.
[0020] FIG. 4 is a section of an electrode of a gel electrolyte
secondary cell according to a second embodiment of the
invention.
[0021] FIG. 5 is a section of an electrode of a gel electrolyte
secondary cell according to a modification of the second
embodiment.
[0022] FIG. 6 is a block diagram of a secondary cell
fabricator.
[0023] FIG. 7 is a flowchart of control of the cell fabricator.
[0024] FIG. 8 is a plan of a secondary cell electrode.
[0025] FIG. 9 is a perspective view of a secondary cell.
[0026] FIG. 10A is a plan view of a complex cell employing the
secondary cell.
[0027] FIG. 10B is a cross sectional view taken along line B-B of
FIG. 10A.
[0028] FIG. 10C is a cross sectional view taken along line C-C of
FIG. 10A.
[0029] FIG. 11 is a perspective view of a battery block employing
the complex cell.
[0030] FIG. 12 is a side view of a vehicle employing the battery
block.
BEST MODE FOR CARRYING OUT THE INVENTION
[0031] There will be detailed below preferred embodiments of the
invention, as the best modes, with reference to the accompanying
drawings. Like elements or members are designated by like reference
characters.
[0032] The description is made by four Parts:
[0033] Part-1 Introduction to Embodiments
[0034] Part-2 Details of Embodiments
[0035] Part-3 Specific Examples
[0036] Part-4 Supplements
[0037] For ensured comprehension, similar comments, notes or pieces
of description are repeated to refer to particular meanings they
have where they are involved.
Part-1 Introduction to Embodiments
[0038] This Part covers:
[0039] 1.1 Typical structure of electrode
[0040] 1.2 Introduction to first embodiment
[0041] 1.3 Introduction to second embodiment
[0042] 1.4 Fabrication and Installation
1.1 Typical Structure of Electrode
[0043] FIG. 1 shows, in schematic section, an electrode of a
typical nonaqueous electrolyte secondary cell SC.
[0044] In the secondary cell SC, a single sheet of electric charge
collector (referred herein to "current collector", or simply to
"collector") 1 has an active material layer 2 coated thereon to
form the electrode, which in turn has a film-shaped electrolyte
layer 3 formed thereon.
[0045] Over an area of the electrode, the active material layer 2
is spread as an electrode-defining system of uniformly distributed
particles of electrochemically active composite (referred herein
collectively to "electrode active material", or simply to "active
material") 4, with a body of electrolytic composite (referred
herein to "electrolyte") 5 filling gaps in between.
[0046] Assuming the secondary cell SC to be a lithium ion cell, the
electrolyte layer 3 contains Li ions 6, which can diffuse to move
as carriers of positive charges.
[0047] The collector 1 has free electrons 7 to be conducted as
carriers of negative charges.
[0048] The velocity of an entire electrode reaction depends on a
resistance of the electrode active material layer 2 to the
diffusion of Li ions 6 supplied from the electrolyte layer 3.
[0049] For instance, in a discharge process of the secondary cell
SC, Li ions 6 in electrolyte 5 of the electrode active material
layer 2 are absorbed into particles of electrode active material 4,
rapidly.
[0050] Resultant reduction in concentration of Li ion 6 in the
electrolyte 5 of electrode active material layer 2 is to be covered
by diffusion of Li ions 6 from the electrolyte layer 3.
[0051] Like this, in accordance with a varying concentration of Li
ion in the electrode active material layer 2, Li ions 6 are
diffused out of or back into the electrolyte layer 3. Concurrently,
electrons 7 of collector 1 are conducted via an electrochemically
conductive material, for promotion of the electrode reaction.
[0052] The diffusion of Li ions 6 is slow relative to the
conduction of electrons 7. At a high rate of charge or discharge,
Li ions 6 tend to be exhausted, with an increased tendency, as they
move into depths, where the ion mobility due to diffusion is
reduced.
[0053] On the other hand, the conductivity by Li ion 6 increases
with an increasing concentration of Li ion 6, but decreases with an
excessively increased Li ion concentration that accompanies an
increase in viscosity of the electrolyte 5, which restricts the
diffusion of Li ion 6.
[0054] Again, at a high rate of charge or discharge, Li ions 6 tend
to be exhausted, with an increased tendency, as they move into
depths, where the ion mobility due to diffusion is reduced.
[0055] In the electrode SC which has a three dimensionally
homogeneous electrode active material layer 2, at a high rate
charge or discharge, the diffusion of Li ion 6 in this layer 2
fails to catch up a variation of Li ion concentration in a
thickness or depth zone vicinal to or near the bottom where the
upside of collector 1 extends, resulting in an occurrence of an
over-voltage, thus failing to provide a sufficient charge or
discharge capacity, as a problem.
[0056] As an effective solution to such an issue, the present
inventors have devised providing a secondary cell electrode with an
electrode active material layer having a continuously or stepwise
changed gradient of ingredient concentration not to be three
dimensionally homogeneous.
1.2 Introduction to First Embodiment
[0057] As a first embodiment of the invention, the secondary cell
electrode preferably comprises a nonaqueous electrolyte
cell-oriented electrode in which the electrode active material
layer on a collector is formed with a gradient of density developed
with an increased solid concentration along a thickness from a
surface of the electrode active material layer toward the
collector.
[0058] FIG. 2 shows, in schematic section, an electrode of a
nonaqueous electrolyte secondary cell 10 according to the first
embodiment.
[0059] In the secondary cell 10, a single sheet of electric charge
collector 1 has an active material layer 12 spread thereon to form
the electrode, which in turn has a film-shaped electrolyte layer 3
formed thereon.
[0060] Over an area of the electrode, the active material layer 12
is spread as an electrode-defining system of
non-"three-dimensionally-uniformly" distributed particles of solid
active material 14, with a liquid body of electrolyte 15 filling
depth-wise varied gaps in between.
[0061] The solid active material 14 has a commensurately changed
concentration providing a density gradient in the active material
layer 12, as follows:
[0062] In a first depth zone 12a near a top surface of electrode
active material layer 12, the concentration of solid active
material 14a in electrolyte 15a is relatively small.
[0063] In a second depth zone 12b beneath the first depth zone 12a,
the concentration of solid active material 14b in electrolyte 15b
is medium.
[0064] In a third depth zone 12c beneath the second depth zone 12b
and near the collector 1, the concentration of solid active
material 14c in electrolyte 15c is relatively large.
[0065] The first depth zone 12a contains a greater volume of
electrolyte 15 in which Li ions 6 can diffuse, and has a reduced
diffusion resistance to Li ion 6.
[0066] The third depth zone 12c contains a greater quantity of
solid material 14 such as electrode active material, electrically
conductive material, and binder, and has a reduced contact
resistance to the collector 1, allowing an increased mobility of
electron 7.
[0067] As a result, Li ions 6 have an increased tendency to diffuse
into the third zone 12c, and electrons 7 have an increased tendency
to move from the collector 1, allowing for the electrode 10 to
withstand a high rate charge or discharge.
[0068] It is noted that the concentration of solid active material
15 may preferably be changed continuously or stepwise, along the
depth of electrode active material layer 12 or even in respective
depth zone or zones 12a, 12b, 12c. At any depth, the concentration
of solid material may well exclude two dimensional gradients
thereof.
[0069] FIG. 3 shows, in schematic section, an electrode of a
nonaqueous electrolyte secondary cell 20 according to a
modification of the first embodiment.
[0070] This cell 20 is different from the first embodiment 10 in
that an electrode active material layer 22 has its first, second,
and third depth zones 22a, 22b, 22c layered as coats and laminated
together, with continuously extending external boundaries 8, 8
against an electrolyte layer 3 and a collector 1, and likewise
extending inter-layer boundaries 9, 9.
[0071] In the first depth zone 22a near a top surface of electrode
active material layer 22, the concentration of solid active
material 24a in electrolyte 25a is relatively small.
[0072] In the second depth zone 22b beneath the first depth zone
22a, the concentration of solid active material 24b in electrolyte
25b is medium.
[0073] In the third depth zone 22c beneath the second depth zone
22b and near the collector 1, the concentration of solid active
material 24c in electrolyte 25c is relatively large.
[0074] The layered depth zones 22a, 22b, 22c may have their
concentrations of solid material 24 in electrolyte 25 prepared
homogeneous within associated coats (22a, 22b, 22c).
[0075] According to the first embodiment, the electrode active
material layer may preferably be provided by laminating a plurality
of thin-film layers having different densities due to different
concentrations of the solid material.
[0076] The solid concentration may preferably be a concentration of
the electrode active material.
[0077] The solid concentration may preferably be a concentration of
the electrode active material, an electrically conductive material,
and a binder.
[0078] The electrode active material may preferably have a
thickness within a range of 1-100 .mu.m.
[0079] As the secondary cell electrode comprises a nonaqueous
electrolyte cell-oriented electrode, its fabrication method may
preferably comprise: (a) changing a quantity of a solid material to
be added to compose an electrode active material layer, thereby
preparing a plurality of kinds of electrode slurry having different
densities due to different concentrations of the solid material;
and (b) coating a collector with a sequence of the plurality of
kinds of electrode slurry so that the concentration of the solid
material is sequentially increased from a surface of the electrode
active material layer toward the collector, thereby laminating a
plurality of thin-film layers different in density, as well as in
concentration of the solid material.
[0080] The thin-film layer may preferably be coated by a thickness
within a range of 1-100 .mu.m in the step (b).
[0081] The electrode slurry may preferably be coated onto the
collector by an ink jet method in the step (b).
[0082] The ink jet method may preferably employ a piezo system.
[0083] A secondary cell according to the first embodiment may
preferably be a bipolar cell.
1.3 Introduction to Second Embodiment
[0084] As a second embodiment of the invention, the secondary cell
electrode preferably comprises a gel electrolyte cell-oriented
electrode in which the electrode active material layer on a
collector has a gradient of density developed with (a) changed
concentration(s) of (an) ingredient(s) (either an electrolyte salt
or a film-forming material, or a combination thereof), along a
thickness from a surface of the electrode active material layer
toward the collector.
[0085] FIG. 4 shows, in schematic section, an electrode of a gel
electrolyte secondary cell 30 according to the second
embodiment.
[0086] In the secondary cell 30, a single sheet of electric charge
collector 1 has an active material layer 32 spread thereon to form
the electrode, which in turn has a film-shaped electrolyte layer 3
formed thereon.
[0087] Over an area of the electrode, the active material layer 32
is spread as an electrode-defining system of three dimensionally
uniformly distributed particles of solid active material 34, with a
non-"three-dimensionally-uniformly" prepared liquid body of
electrolyte 35 filling even gaps in between.
[0088] The electrolyte 35 has a commensurately changed
ingredient-concentration providing a density gradient of the active
material layer 32, as follows:
[0089] A first depth zone 32a, located near a top surface of
electrode active material layer 32, has a relatively small
concentration with respect to an electrolyte salt in an electrolyte
35a filled between particles of solid active material 34a.
[0090] A second depth zone 32b, located beneath the first depth
zone 32a, has a medium concentration with respect to the
above-noted electrolyte salt in an electrolyte 35b filled between
particles of solid active material 34b.
[0091] A third depth zone 32c, located beneath the second depth
zone 32b and near the bottom of electrode active material layer 32
where a top surface of collector 1 extends, has a relatively large
concentration with respect to the electrolyte salt in an
electrolyte 35c filled between particles of solid active material
34c.
[0092] As a result, Li ions 6 have an increased tendency to be
concentrated in the third zone 32c, and kept from being exhausted
even at a high rate charge or discharge.
[0093] Further, along an electrical potential gradient due to a
gradient of concentration of electrolyte salt, Li ions 6 as well as
electrons 7 are accelerated, and have an increased tendency to
diffuse from the electrolyte layer 3.
[0094] On the contrary, the concentration of electrolyte salt may
be decreased along the depth from a top surface of the electrode
active material layer 32 toward the collector 1. In this case, Li
ions are rich in the first depth zone 32a, and tend to be released
therefrom. In addition, due to the concentration gradient, Li ions
have an increased tendency to diffuse.
[0095] The secondary cell 30 is thus adapted to cope with a high
rate charge or discharge.
[0096] It is noted that the concentration gradient of electrolyte
salt may preferably be changed continuously or stepwise, along the
depth of electrode active material layer 32 or even in respective
depth zone or zones 32a, 32b, 32c. At any depth, the concentration
of electrolyte salt may well exclude two dimensional gradients.
[0097] The electrode active material layer may preferably be
provided by laminating a plurality of thin-film layers different in
concentration of the electrolyte salt.
[0098] FIG. 5 shows, in schematic section, an electrode of a gel
electrolyte secondary cell 40 according to a modification of the
second embodiment.
[0099] This cell 40 is different from the second embodiment 30 in
that an electrode active material layer 42 has its first, second,
and third depth zones 42a, 42b, 42c layered as coats and laminated
together, with continuously extending external boundaries 8, 8
against an electrolyte layer 3 and a collector 1, and likewise
extending inter-layer boundaries 9, 9. Designated at reference
character 45 is an entire system of three-dimensionally uniformly
distributed particles of solid active material.
[0100] The first depth zone 42a, located near a top surface of
electrode active material layer 42, has a relatively small
concentration with respect to an electrolyte salt in an electrolyte
45a filled between particles of solid active material 44a.
[0101] The second depth zone 42b, located beneath the first depth
zone 42a, has a medium concentration with respect to the
above-noted electrolyte salt in an electrolyte 45b filled between
particles of solid active material 44b.
[0102] The third depth zone 42c, located beneath the second depth
zone 42b and near the bottom of electrode active material layer 42
where a top surface of collector 1 extends, has a relatively large
concentration with respect to the electrolyte salt in an
electrolyte 44c filled between particles of solid active material
45c.
[0103] The layered depth zones 42a, 42b, 42c may have their
concentrations of electrolyte salt in electrolyte 45 prepared
homogeneous within associated coats (42a, 42b, 42c).
[0104] According to the second embodiment, as the secondary cell
electrode comprises a gel electrolyte cell-oriented electrode, its
fabrication method may preferably comprise: (a) changing a quantity
of an electrolyte salt to be added to compose an electrode active
material layer, thereby preparing a plurality of kinds of electrode
slurry having different densities due to different concentrations
of the electrolyte salt; and (b) coating a collector with a
sequence of the plurality of kinds of electrode slurry, thereby
laminating a plurality of thin-film layers different in density, as
well as in a concentration of the electrolyte salt, such that the
electrode active material layer has a density gradient developed
with a gradient of the concentration of the electrolyte salt from a
surface of the electrode active material layer toward the
collector.
[0105] Or, as the secondary cell electrode comprise a gel
electrolyte cell-oriented electrode, its fabrication method may
preferably comprise: (a) changing a quantity of a film forming raw
material to be added to compose an electrode active material layer,
thereby preparing a plurality of kinds of electrode slurry having
different densities due to different concentrations of the film
forming raw material; and (b) coating a collector with a sequence
of the plurality of kinds of electrode slurry, thereby laminating a
plurality of thin-film layers different in density, as well as in a
concentration of the film forming raw material, such that the
electrode active material layer has a density gradient developed
with a gradient of the concentration of the film forming raw
material from a surface of the electrode active material layer
toward the collector.
[0106] Or, as the secondary cell electrode comprise a gel
electrolyte cell-oriented electrode, its fabrication method may
preferably comprise: (a) changing quantities of an electrolyte salt
and a film forming raw material to be added to compose an electrode
active material layer, thereby preparing a plurality of kinds of
electrode slurry having different densities due to different
concentrations of the electrolyte salt and the film forming raw
material; and (b) coating a collector with a sequence of the
plurality of kinds of electrode slurry, thereby laminating a
plurality of thin-film layers different in density, as well as in
concentrations of the electrolyte salt and the film forming raw
material, such that the electrode active material layer has a
density gradient developed with gradients of the concentration of
the electrolyte salt and the film forming raw material from a
surface of the electrode active material layer toward the
collector.
[0107] The thin-film layer may preferably be coated in a thickness
within a range of 1-100 .mu.m in the step (b).
[0108] The electrode slurry may preferably be coated onto the
collector by an ink jet method in the step (b).
[0109] The ink jet method may preferably employ a piezo system.
[0110] A secondary cell according to the second embodiment may
preferably be a lithium ion secondary cell.
[0111] The secondary cell may preferably be a bipolar cell.
[0112] The secondary cell may preferably comprise: a positive
electrode comprising a first collector, and a positive-electrode
oriented active material layer having a density gradient developed
with a gradient of a concentration of an electrolyte salt increased
along a thickness from a surface of the positive-electrode oriented
active material layer toward the first collector; a negative
electrode comprising a second collector, and a negative-electrode
oriented active material layer having a density gradient developed
with a gradient of a concentration of an electrolyte salt decreased
along a thickness from a surface of the negative-electrode oriented
active material layer toward the second collector; and an
electrolyte layer.
[0113] To the contrary, the secondary cell may preferably comprise:
a positive electrode comprising a first collector, and a
positive-electrode oriented active material layer having a density
gradient developed with a gradient of a concentration of an
electrolyte salt decreased along a thickness from a surface of the
positive-electrode oriented active material layer toward the first
collector; a negative electrode comprising a second collector, and
a negative-electrode oriented active material layer having a
density gradient developed with a gradient of a concentration of an
electrolyte salt increased along a thickness from a surface of the
negative-electrode oriented active material layer toward the second
collector; and an electrolyte layer.
[0114] The negative-electrode oriented active material layer may
preferably have the density gradient developed with a gradient of a
concentration of a film forming material increased along the
thickness from the surface of the negative-electrode oriented
active material layer toward the second collector.
[0115] The secondary cell may preferably comprise a
negative-electrode oriented active material layer having a density
gradient developed with a gradient of a concentration of a film
forming material increased along a thickness from a surface of the
negative-electrode oriented electrolyte layer toward a
collector.
1.4 Fabrication and Installation
[0116] FIG. 6 shows, in block diagram, a cell electrode fabricator
CF for secondary cell electrodes according to an embodiment of the
invention.
[0117] The cell electrode fabricator CF is configured with: a
controller 100 as a computer provided with necessary peripherals
including a multi-purpose interface 102, an interactive display
104, and a memory 106 for storing necessary programs and data; an
ink jet system including a set of injection nozzles 108a, 108b, . .
. (collectively 108), and a set of ink containers 109a, 109b, . . .
(collectively 109); and associated facilities including a drying
heater 112, and a carrier 150 for carrying a collector 110.
[0118] The controller 100 governs an entirety of the fabricator CF,
and has a mapping operator 101 for processing four-dimensional data
to map a temporal sequence of injection patterns of ink P, of which
a selected one is indicated on the display 104, an entirety is
stored in the memory 106, and demanded ones are transmitted
together with commands to local controllers of the ink jet system
and associated facilities to develop a current ink jet pattern on
the collector 110.
[0119] The set of injection nozzles 108 may be one of, but not
limited to, a piezoelectric system, a thermal system, and a bubble
jet (trademark) system.
[0120] In the piezoelectric system, a piezoelectric element
disposed at a bottom of an ink accumulating chamber is electrically
deformed to thereby inject droplets of ink from an associated
injection nozzle 108.
[0121] In the thermal system as well as the bubble jet system, a
heating element heats ink, causing evaporation accompanying steam
explosion, of which energy injects droplets of ink from an
associated injection nozzle 108. The thermal and bubble jet systems
are different in an area to be heated, but identical in
principle.
[0122] The set of ink containers 109 are grouped into subsets (like
109a, 109b, . . . ) by kinds of handling active materials, and
one-to-one connected to injection nozzles 108 (108a, 108b, . . . ).
The set of ink containers 109 may be provided with a stirring
module 109c for stirring ink, and a heater 109d for heating
ink.
[0123] The heater 112 is for drying active materials deposited on
the collector 110. After deposition of ink, the collector 110
travels, as it is carried by the carrier 150, to enter a drying
furnace, where the heater 112 is installed.
[0124] The fabricator CF has a number of different kinds of ink,
and selects a suitable one in accordance with an intended polarity
of a respective electrode, and an intended concentration of solid
material or electrolyte salt at an associated thickness zone of an
active material layer of the electrode.
[0125] For example, in an ink group oriented for fabrication of a
positive-pole electrode, any kind of ink contains ingredients of
the active material layer of that electrode, while the proportions
of ingredients are changed by the kind of ink.
[0126] Likewise, in another ink group oriented for fabrication of a
negative-pole electrode, any kind of ink contains ingredients of an
active material layer of that electrode, while the proportions of
ingredients are changed by the kind of ink.
[0127] FIG. 7 shows a sequence of steps in a fabrication of a
secondary cell electrode.
[0128] At a step S1, a necessary number of deposition patterns are
prepared at the computer 100.
[0129] At a step S2, the deposition patterns are stored in the
memory 106.
[0130] At a step S3, for current use in the fabrication, a
corresponding pattern is read from the memory 106.
[0131] At a step S4, the read pattern is processed by the mapping
operator 101, so that a layer of an active material is deposited in
a mapped pattern on the collector 110.
[0132] At a step S5, the collector 110 is carried into the drying
furnace, where the layer of deposited active material is heated and
dried by the heater 112.
[0133] In the case of a secondary cell electrode to be fabricated
as a bipolar electrode with a positive electrode layer formed on
one side of the collector 110 and a negative electrode layer formed
on the other side, the sequence of steps described are repeated two
times, one for forming the positive electrode layer and the other
for forming the negative electrode layer.
[0134] FIG. 8 shows, in plan, a secondary cell electrode as a
bipolar electrode fabricated by repetition of the sequence of steps
described.
[0135] A hatched planar area, one-size smaller than the collector
110, is an electrode layer 111 formed with a volume of active
material injected on one side of the collector 100.
[0136] The bipolar electrode has positive and negative electrode
layers formed on both sides of the collector 110. Assuming the
electrode layer 111 of FIG. 8 to be a positive, a negative
electrode layer is formed on the opposite side.
[0137] FIG. 9 shows a perspective view of a simplex secondary cell
120.
[0138] The secondary cell 120 internally accommodates a cell
element composed of a plurality of secondary cell electrodes (that
may be bipolar electrodes) fabricated in the described manner and
laminated together with intervening electrolyte layers. The cell
element is sheathed in a planer sheath 122 formed with a pair of
polymer-metal composite laminate films sealed gas-tight. A positive
electrode terminal 124 and a negative electrode terminal 126,
internally connected to the cell element, are extended through an
edge of the sheath 122, to be exposed for external connection.
[0139] Such secondary cells may be connected in series, parallel,
or serial-parallel, and packaged as a complex cell or cell
module.
[0140] FIGS. 10A to 10C illustrate a complex cell 200 packaged in a
rectangular elongate casing 202. This complex cell 200 is
configured with a plurality of secondary cells 120 connected inside
the casing 202 in series, parallel, or serial-parallel, and has a
pair of terminals 204 connected either to a positive electrode
terminal 124 of an outermost secondary cell 120 and the other to a
negative electrode terminal 126 of another outermost secondary cell
120, and extended outside the casing 202 for external connection to
associated devices.
[0141] Such complex cells may be connected in series, parallel, or
serial-parallel, and piled up to be assembled as a battery
block.
[0142] FIG. 11 is a perspective view of a battery block 300.
[0143] This battery block 300 is configured with a plurality of
piled complex cells 200 connected in series, parallel, or
serial-parallel and assembled together with electrical connecting
end plates 302 fixed thereto by screws 304. The battery block 300
is protected against external impacts, by an elastic material
applied in gaps and on outside surfaces including a bottom
surface.
[0144] The number of secondary cells 120 constituting a complex
cell 200 and that of complex cells 200 constituting a battery block
300, as well as their internal connections, are specified in
accordance with a required capacity and power. The secondary cell
is fabricated with an increased stability for use to a complex
cell, and with a yet increased stability for use to a battery
block. In the complex cell, as well as in the battery block,
employed secondary cells are wholly kept stable with an increased
durability to avoid adverse affects arising from deterioration of
any secondary cell.
[0145] Such a complex cell or battery block may well be used in a
vehicle.
[0146] FIG. 12 shows, in side view, a typical vehicle 400 having a
combination of complex cell 200 and battery block 300 installed
therein.
[0147] The complex cell 200 and the battery block 300 installed in
the vehicle 400 have matching electrical characteristics, such as
power supply ratings, to required performances such as for power
distribution and driving of the vehicle 400. The complex cell 200
and the battery block 300 have their secondary cells adapted for a
conforming power supply service even after a long use, with a high
durability. Further, they are configured to exhibit a stable
performance against continued vibrations in the vehicle 400,
without significant deterioration due to resonance.
Part-2 Details of Embodiments
[0148] This part covers details of nonaqueous electrolyte
electrodes according to the first embodiment, and those of gel
electrolyte electrodes according to the second embodiment.
2.1 Details of First Embodiment
Nonaqueous Electrolyte Electrodes
2.1.1 Configuration of Nonaqueous Electrolyte Electrode
2.1.1a Nonaqueous Electrolyte Electrodes
[0149] The electrode active material layer may preferably be
configured with, but not limited to, a number of laminated
thin-film layers different from each other in solid
concentration.
[0150] This configuration allows the electrode active material
layer to be formed with a concentration gradient making the solid
concentration increase along the thickness from the layer surface
toward the collector.
[0151] The number of laminated thin film layers may be two or more,
preferably three or more, or more preferably, five or more.
[0152] "Solid" in terms of solid concentration means a solid
electrode material, such as an electrode active material,
electrically conductive material, or binder, that may be contained
in electrode active material layers.
[0153] Such solids may be adequately selected to form a
concentration gradient with which the solid concentration increases
along the thickness from the surface of electrode active material
layer toward the collector.
[0154] For instance, with such a concentration gradient, the
diffusion resistance of Li ion can be reduced, allowing for an
effective electrode reaction even at high rate charge or discharge,
as an advantage.
[0155] For a more advantageous effect, electrode active material,
electrically conductive material, and binder may be distributed
with such a concentration gradient to thereby reduce the contact
resistance between collector and electrode, as well.
[0156] The electrode, positive or negative in polarity, may
preferably have a thickness of electrode active material layer
within a range of 1-100 .mu.m, more preferably within a range of
5-50 .mu.m.
[0157] The preferable thickness range of electrode active material
layer excludes a thickness range under 1 .mu.m where the formation
of concentration gradient is very difficult, and a thickness range
over 100 .mu.m where the ion diffusion distance may be too great to
ensure high output.
[0158] The collector may be typical or general, and may preferably
be, for example, an aluminum foil, a SUS (stainless steel) foil, a
clad material of nickel and aluminum, a clad material of copper and
aluminum, a clad material of SUS and aluminum, or a combination of
such metals to be plated.
[0159] Further, the collector may be a metal of which surface is
covered with aluminum, or may be a pair of stuck metallic foils as
circumstances require.
[0160] In use of a complex collector, the material of its
positive-pole collector may preferably be an electrically
conductive metal such as aluminum, aluminum alloy, SUS, or
titanium, while aluminum is most preferable.
[0161] The material of negative-pole collector may preferably be an
electrically conductive metal such as copper, nickel, silver, or
SUS, while nickel and SUS are most preferable.
[0162] In the complex collector, the positive-pole and
negative-pole collectors may well be electrically connected
directly to each other, or via an electrically conductive
intermediate layer made of a third material.
[0163] The positive-pole and negative-pole collectors of complex
collector may have their thicknesses within a typical range of, for
example, about 1-100 .mu.m.
[0164] For collectors (with complex collectors inclusive), the
thickness range of about 1-100 .mu.m is preferable from the
viewpoint of making a thin cell.
2.1.1b Electrodes for Positive Pole
[0165] For use to a positive pole, the positive-pole oriented
electrode active material layer (referred herein sometimes simply
to "positive electrode layer") contains a positive electrode active
material, and necessary additives including an electrically
conductive material for enhanced electron conductivity, a binder, a
lithium salt for enhanced ion conductivity, and an electrolyte.
[0166] The positive electrode active material may preferably be a
lithium-transition metal complex oxide that is a complex oxide of a
transition metal and lithium.
[0167] More specifically, the positive electrode active material
may preferably be one of a family of Li--Co complex oxides such as
LiCoO.sub.2, a family of Li--Ni complex oxides such as LiNiO.sub.2,
a family of Li--Mn complex oxides such as spinel LiMn.sub.2O.sub.4,
and a family of Li--Fe complex oxides such as LiFeO.sub.2, or any
of them having elements of its transition metal substituted with
others.
[0168] These lithium transition metal complex oxides are excellent
in reactivity and cycle durability, and relatively low in cost.
[0169] They are thus advantageously used for electrodes to provide
a cell excellent in output characteristics.
[0170] The positive electrode active material may preferably be one
of phosphorates or sulfates of lithium and transition metal, such
as LiFePO.sub.4; transition metal oxides or sulfides, such as
V.sub.2O.sub.5, MnO.sub.2, TiS.sub.2, MoS.sub.2, and MoO.sub.3; and
other applicable compounds such as PbO.sub.2, AgO, and NiOOH.
[0171] The particle size of positive active material may preferably
fall within a range of 0.1-50 .mu.m, or more preferably within a
range of 0.1-20 .mu.m.
[0172] The preferable particle size range excludes a range under
0.1 .mu.m where the difficulty of fabrication may fail to provide a
desirable charge or discharge characteristic, and a range over 50
.mu.m where one may suffer a difficulty in rubbing to the positive
electrode active material.
[0173] The electrically conductive material may preferably be
acetylene black, carbon black, graphite, or the like.
[0174] The particle size of electrically conductive material may
preferably fall within a range of 0.1-50, or more preferably within
a range of 1-30 .mu.m.
[0175] The preferable particle size range of electrically
conductive material excludes a range under 0.1 .mu.m where the
quantity of conductive material needs to be increased for necessary
conduction of electrons, and a range over 50 .mu.m where one may
suffer a difficulty in rubbing to the positive electrode active
material.
[0176] The binder may be, but not limited to, poly vinylidene
fluoride (PVDF), SBR, polyimide, or the like.
[0177] The lithium salt may be one of, but not limited to, BETI
(lithium bis(par fluoro ethylene sulfonyl imide)),
Li(C.sub.2F.sub.5SO.sub.2).sub.2N, LiBF.sub.4, LiPF.sub.6,
LiN(SO.sub.2CF.sub.3).sub.2, LiN(SO.sub.2C.sub.2F.sub.5).sub.2, and
LiBOB (lithium bis oxide borate), or one of their mixtures.
[0178] The electrolyte is nonaqueous to provide a necessary
concentration gradient. The nonaqueous electrolyte may preferably
be a full-solid electrolyte composed of electrolytic high polymer
and support salt such as a lithium salt, or a high polymer gel
electrolyte composed of electrolytic high polymer and an
electrolytic solution held therein.
[0179] As the electrolyte is nonaqueous, the positive electrode
layer may preferably contain nonaqueous electrolyte.
[0180] With the nonaqueous electrolyte filling gaps between
particles of positive electrode active material, the ion transfer
in positive electrode layer is smoothed, allowing for an entire
cell to have an enhanced output.
[0181] If the electrolyte is high polymer gel or has a separator
with soaked electrolytic solution, the positive electrode layer may
contain no electrolyte, subject to a known binder binding particles
of positive electrode active material.
[0182] The full-solid electrolytic high polymer may be, but not
limited to, polyoxyethylene (PEO), polypropylene oxide (PPO), or
their copolymers. Such polyalkylene oxide polymers well dissolve
lithium salts such as BETI, LiBF.sub.4, LiPF.sub.6,
LiN(SO.sub.2CF.sub.3).sub.2, and
LiN(SO.sub.2C.sub.2F.sub.5).sub.2.
[0183] They form a cross-linking structure, thereby exhibiting an
excellent mechanical strength.
[0184] According to the embodiment, high polymer solid electrolyte
is contained in at least either positive or negative electrode
active material layer.
[0185] However, it may preferably be contained in both of them for
an enhanced performance of bipolar cell.
[0186] The high polymer gel electrolyte may be a full-solid
electrolyte-oriented ion-conductive high polymer containing an
electrolytic solution, or a lithium ion-nonconductive host polymer
having a similar electrolytic solution held in its frame.
[0187] The electrolytic solution (electrolyte salt and plasticizer)
to be contained in high polymer gel electrolyte may be a typical
one for lithium ion cells, and may be, but not limited to, such one
that contains at least one kind of lithium salt (electrolyte
support salt) selected from among inorganic acid anion salts such
as LiBOB (lithium bis oxide borate), LiPF.sub.6, LiBF.sub.4,
LiClO.sub.4, LiAsF.sub.6, LiTaF.sub.6, LiAlCl.sub.4, and
Li.sub.2B.sub.10Cl.sub.10, and organic acid anion salts such as
LiCF.sub.3SO.sub.3, Li(CF.sub.3SO.sub.2).sub.2N, and
Li(C.sub.2F.sub.5SO.sub.2).sub.2N, in an organic solvent
(plasticizer) such an as aprotic solvent, using at least one kind,
or having mixed two or more kinds, selected from among cyclic
carbonates such as propylene carbonate (PC), and ethylene carbonate
(EC), chain carbonates such as dimethyl carbonate, methylethyl
carbonate, and diethylcarbonate, ethers such as tetrahydrofuran,
2-methyltetrahydrofuran, 1,4-dioxane, 1,2-dimethoxyethane, and
1,2-dibutoxyethane, lactones such as .gamma.-butyrolactone,
nitriles such as acetonitrile, esters such as methyl propionate,
amides such as dimethyl formamide, methyl acetates, and methyl
formates.
[0188] The lithium ion-nonconductive host polymer to be contained
in high polymer gel electrolyte may be, but not limited to, a
monomer forming a gelled polymer such as poly vinylidene fluoride
(PVDF), polyvinyl chloride (PVC), polyacrylonitrile (PAN), or
polymethyl methacrylates (PMMA).
[0189] It is noted that PAN, PMMA and the like are exemplified as
lithium ion-nonconductive host polymers to be contained in high
polymer gel electrolyte, while they are little ion-conductive and
may belong to a group of ion-conductive high polymers for
electrolyte use.
[0190] The ratio of host polymer and electrolytic solution in high
polymer gel electrolyte may range from 2:98 to 90:10 in mass ratio,
depending on the objective etc.
[0191] Oozing electrolyte from an outer periphery of electrode
active material layer may thus also be effectively sealed by
provision of an insulation layer or insulating part.
[0192] The mass ratio of host polymer and electrolytic solution in
high polymer gel electrolyte may thus be determined, with a higher
priority to cell performance.
[0193] For the positive electrode layer containing positive
electrode active material, electrically conductive material,
binder, nonaqueous electrolyte (host polymer, electrolytic
solution, etc.), lithium salts, and the like, proportions of those
ingredients may be determined in consideration of the objective of
cell (output, energy, etc. to be prioritized) and the conductivity
of Li ion.
[0194] For example, if the proportion of nonaqueous electrolyte is
smaller than required in the positive electrode layer, the
conduction resistance of Li ion as well as the diffusion resistance
becomes great, so that the cell has a reduced performance.
[0195] To the contrary, if the proportion of nonaqueous electrolyte
is greater than necessary in the positive electrode layer, the cell
has a reduced energy density.
[0196] The amount of nonaqueous electrolyte is determined in
consideration of such factors, to meet the objective.
[0197] The description is omitted here as to thickness of the
positive electrode layer as above-mentioned.
[0198] The positive electrode layer has a preferable thickness as
described (see sec. 2.1.1a).
2.1.1c Electrodes for Negative Pole
[0199] For use to a negative pole, the negative-pole oriented
electrode active material layer (referred herein sometimes simply
to "negative electrode layer") contains a negative electrode active
material, and necessary additives including an electrically
conductive material for enhanced electron conductivity, a binder, a
lithium salt for enhanced ion conductivity, and an electrolyte. The
additives are similar to those of positive electrode layer (see
sec. 2.1.1b).
[0200] The negative electrode active material may preferably be one
of various kinds of graphites such as natural or artificial
graphites, for example, fibrous graphite, scale graphite, and
spheroidal graphite, various kinds of lithium alloys, and the
like.
[0201] More specifically, the positive electrode active material
may preferably be one of carbon, graphite, and lithium-transition
metal complex oxide, while carbon and lithium-transition metal
complex oxide are better.
[0202] Lithium transition metal complex oxide and carbon are
excellent in reactivity and cycle durability, and relatively low in
cost.
[0203] They are thus advantageously used for electrodes to provide
a cell excellent in output characteristics.
[0204] The lithium transition metal complex oxide may be a
lithium-titanium complex oxide such as Li.sub.4Ti.sub.5O.sub.12,
for example.
[0205] The carbon may be graphite, hard carbon, or soft carbon, for
example.
[0206] The negative electrode layer has a preferable thickness as
described (see sec. 2.1.1a).
2.1.2 Fabrication of Nonaqueous Electrolyte Electrodes
2.1.2a Method of Fabrication
[0207] According to the first embodiment, a nonaqueous electrolyte
electrode is fabricated by a method including: a step (a) of
changing a quantity of a solid material to be added to compose an
electrode active material layer, thereby preparing a plurality of
kinds of electrode slurry different in density and in a
concentration of the solid material; and a step (b) of coating a
collector with the plurality of kinds of electrode slurry so that
the concentration of the solid material is sequentially increased
from a surface of the electrode active material layer toward the
collector, thereby laminating a plurality of thin-film layers
different in concentration of the solid material.
[0208] This method can provide a nonaqueous electrolyte electrode
according to the first embodiment, in which a plurality of
thin-film layers different in density and in a concentration of a
solid material are laminated to have a concentration gradient with
which the concentration of the solid material is increased from a
surface of an electrode active layer toward a collector.
2.1.2b Fabrication of Electrodes for Positive Pole
[0209] For fabrication of a positive-pole oriented electrode, at
the step (a) of the method described (see sec. 2.1.2a), the
plurality of kinds of electrode slurry are each respectively
prepared as a corresponding solution containing a positive
electrode active material (referred herein simply to "positive
electrode slurry", or sometimes to "positive electrode ink" in this
embodiment).
[0210] This slurry may contain an electrically conductive material,
a binder, an electrolyte-oriented high polymer as a raw material of
nonaqueous electrolyte, an electrolyte support salt, an initiator,
a solvent, and the like, as necessary.
[0211] For instance, the positive electrode slurry may be prepared
by adding additives such as an electrically conductive material, a
binder, and an electrolyte support salt to a solvent containing a
positive electrode active material, and by stirring a resultant
solution for a homogeneous mixing or such.
[0212] Likewise, a plurality of kinds of slurry are prepared,
having solid materials such as a positive electrode active
material, an electrically conductive material, and a binder changed
in quantities of addition, as necessary, to provide a desirable
concentration gradient.
[0213] For the positive electrode active material, electric
conductivity, binder, electrolyte-oriented high polymer, and
electrolyte support salt, refer to the foregoing description.
[0214] For viscosity control of positive electrode slurry, an
adequate solvent such as n-methyl-2-pyrrolidone (NMP) or
n-pyrrolidone may be selected in accordance with the kind of
slurry.
[0215] An identical solvent may preferably be used for the
respective kinds of positive electrode slurry.
[0216] The particle size of positive electrode active material may
be set under 50 .mu.m in consideration of the film thickness of
positive electrode layer, preferably within a range of 0.1-50
.mu.m, or more preferably within a range of 1-20 .mu.m.
[0217] The initiator is properly selected in accordance with the
compounds to be polymerized and an employed method of
polymerization such as for thermal polymerization,
photopolymerization, radiation polymerization, or electron beam
polymerization.
[0218] For instance, the initiator may be, but not limited to,
benzyldimetilketarl as a photoinitiator, or azobis isobutyronitrile
as a thermal initiator.
[0219] For positive electrode active material, electrolyte support
salt, and electric conduction assisting agent, the quantity of
addition may be controlled in accordance with the objective of
cell, etc.
[0220] The addition quantity of initiator depends on the number of
crosslinkable functional groups in an electrolyte-oriented polymer
employed for the nonaqueous electrolyte.
[0221] Typically, it falls within a range of about 0.01-1% in mass
ratio to the electrolyte-oriented polymer.
[0222] At the step (b) in the method of fabrication described (see
sec. 2.1.2a), the "coating a collector with the plurality of kinds
of positive electrode slurry" may preferably be done by one of a
screen printing method, a spray coating method, an electrostatic
spray coating method, and an ink jet method.
[0223] The ink jet method is a method of spreading droplets of
positive electrode slurry from ink jet nozzles on a collector,
enabling target regions on the collector to be coated by a
desirable uniform thin-film thickness of slurry, thus allowing the
positive electrode slurry to be spread in optimum pattern. This is
preferable.
[0224] Spreading positive electrode slurry "in optimum pattern" in
a coating by the ink jet method means spreading the positive
electrode slurry on a collector so that a solid material has a
sequentially increased concentration.
[0225] The ink jet method employs a known drop-on-demand
system.
[0226] The system may preferably be a piezo type in which a ceramic
piezo element deforms with a voltage imposed thereon to deliver
liquid.
[0227] In the piezo type, electrode materials contained in the
positive electrode slurry (i.e. positive electrode ink) are
excellent in thermal stability so that the quantity of ink to be
spread is variable.
[0228] A piezo type ink jet head is adapted to deliver various
kinds of liquid relatively high of viscosity with an ensured
stability and precision better than other types, within an
effective delivery range up to a viscosity of 10 Pas (100 cp).
[0229] A typical piezo type ink jet head is configured with an ink
chamber for storing a positive electrode ink in the head, and an
ink introducing part communicating with the ink chamber via an ink
channel.
[0230] This ink jet head has a multiplicity of nozzles arrayed in a
lower portion thereof, an array of piezoelectric elements disposed
in an upper portion thereof, and a driver for driving piezoelectric
elements to deliver liquid of the ink chamber, to be spread from
associated nozzles.
[0231] Such a structure of ink jet head is a mere illustration, and
not restrictive.
[0232] An ink jet head available on the market may well be
used.
[0233] Metallic foils to be coated with positive electrode ink may
suffer a difficulty in their feed to an ink jet printer. Such foils
may be stuck on sheets of quality paper, to be fed to the ink jet
printer.
[0234] A plastic-make ink introducing part may be partially
dissolved by a solvent of positive electrode ink.
[0235] The ink introducing part may preferably be metallic.
[0236] The viscosity of positive electrode slurry may preferably
fall within a range of 0.1-100 cP at 25.degree. C., more
preferably, within a range of 0.5-10 cP, or yet more preferably,
within a range of 1-3 cP.
[0237] The preferable viscosity range may exclude a range under 0.1
cP where the positive electrode ink may suffer a difficulty in
liquid quantity control in use as an ink for ink jet, and a range
exceeding 100 cP where the positive electrode ink may suffer a
difficulty in passing nozzles in the use as an ink for ink jet.
[0238] The viscosity may well be measured by an L-type
viscosimeter, a rotary viscosimeter, etc.
[0239] In use of a high-viscous positive electrode slurry as an ink
for ink jet, the positive electrode slurry coated on a collector
may have a stroke, plot or thin spot.
[0240] In such a case, the positive electrode slurry may preferably
be heated to an adequate viscosity, with a heater provided of the
ink chamber.
[0241] A low-viscous positive electrode slurry may have a positive
electrode active material deposited in the ink chamber, which may
well be stirred by rotary blades or the like.
[0242] The method of spreading a positive electrode slurry by an
ink jet system may preferably be one of, but not limited to: a
method (1) of providing a single ink jet head, and independently
controlling liquid delivery actions of a plurality of its
minute-diameter nozzles, thereby spreading droplets on a collector
surface in optimum pattern; and a method (2) of providing a
plurality of ink jet heads, and independently controlling their
liquid delivery actions, thereby spreading droplets on a collector
surface in optimum pattern.
[0243] These methods enable forming a desirable optimum pattern in
a short time.
[0244] In the methods (1) and (2) described, the "independently
controlling liquid delivery actions" may include, but may not be
limited to, for instance, connecting an ink jet printer using the
ink jet head(s) to a computer available in the market or the like,
preparing a desirable pattern by software, such as Power Points (by
Microsoft Corporation) or Auto CAD (by AutoDesk Corporation), read
therein, and executing control with electric signals from such
software.
[0245] In the method (1), the "spreading droplets on a collector
surface in optimum pattern" may preferably include steps of
independently controlling respective liquid delivery actions of the
minute-diameter nozzles, thereby spreading a kind of positive
electrode slurry on the collector surface to form a thin-film
layer, and thereafter, repeating spreading a kind of positive
electrode slurry smaller in concentration of solid material, each
time to form a thin-film layer, thus laminating a plurality of
coats of positive electrode slurry different in concentration, to
achieve a desirable concentration gradient.
[0246] In the method (2), the "spreading droplets on a collector
surface in optimum pattern" may preferably include a step of
independently controlling the respective ink jet heads, thereby
spreading mixed droplets of a plurality of kinds of positive
electrode slurry different in concentration of solid material,
thereby laminating a plurality of thin-film layers having a
desirable concentration gradient.
[0247] The particle size of droplets of positive electrode slurry
to be delivered from ink jet head may preferably set within a range
of 1-500 pl, or more preferably within a range of 1-100 pl, in
consideration of the film thickness of positive electrode
layer.
[0248] The thickness of thin film to be spread may preferably fall
within a range of 1-100 .mu.m, or more preferably within a range of
5-50 .mu.m, as the thickness is adjustable to achieve a desirable
thickness of electrode active material layer.
[0249] The preferable thickness range excludes a range under 1
.mu.m where the capacity of cell may be extremely reduced, and a
range over 100 .mu.m where an elongated diffusion distance of Li
ion in the electrode may render the resistance large.
[0250] The plurality of thin-film layers to be laminated in a
positive electrode active material layer may have their thicknesses
respectively determined adequately to achieve a desirable electrode
characteristic, without the need to be even.
[0251] Spread positive electrode slurry may well be dried in a
typical atmosphere, preferably in a vacuum atmosphere within a
temperature range of 20-200.degree. C. for a period within a range
of 1 minute-8 hours, or more preferably, within a temperature range
of 80-150.degree. C. for a period within a range of 3 minutes-1
hour.
[0252] These conditions are not restrictive, so that the drying
condition may be determined in a suitable manner depending on, for
instance, the quantity of solvent in the spread positive electrode
slurry.
[0253] If an employed positive electrode slurry is free of
nonaqueous electrolyte (full-solid electrolyte-oriented high
polymer or high-polymer gel electrolyte), dried positive electrode
slurry may be soaked with later-described electrolyte slurry.
[0254] The soaking may preferably be made by, but not limited to,
an applicator or coater configured for supply of minute
quantity.
[0255] The method of porimerizing electrolyte high polymer
contained in positive electrode slurry may well be properly
determined in accordance with an employed initiator, and in use of
a photoinitiator for example, may be developed even in atmospheric
air, but preferably, in an inactive atmosphere such as argon or
nitrogen, or more preferably, in a vacuum atmosphere, within a
temperature range of 0-150.degree. C., still preferably, within a
temperature range of 20-40.degree. C., for a period within a range
of 1 minute-8 hours, yet preferably, within a range of 5 minutes-1
hour, subject to an irradiation by ultraviolet rays.
[0256] According to the embodiment, the positive-pole electrode may
be fabricated otherwise.
[0257] The positive electrode slurry may be prepared with, for
instance, electrolyte-oriented high polymer and initiator or the
like initially added thereto.
[0258] A plurality of coats of positive electrode slurry may well
be laminated on a substrate such as an electrolyte layer
(electrolyte film) or a separator soaked with electrolyte,
preferably through a step of sequentially spreading a plurality of
kinds of positive electrode slurry, starting from that kind which
is smallest in concentration of solid material, for lamination to
achieve a desirable concentration gradient.
[0259] Thereafter, a collector may be joined on a lamination of
dried and polymerized coats of positive electrode slurry to
fabricate a positive-pole electrode, as another applicable
method.
2.1.2c Fabrication of Electrodes for Negative Pole
[0260] For fabrication of a negative-pole oriented electrode, at
the step (a) of the method described (see sec. 2.1.2a), the
plurality of kinds of electrode slurry are each respectively
prepared as a corresponding solution containing a negative
electrode active material (referred herein simply to "negative
electrode slurry", or sometimes to "negative electrode ink" in this
embodiment).
[0261] This slurry may contain an electrically conductive material,
a binder, an electrolyte-oriented high polymer as a raw material of
nonaqueous electrolyte, an electrolyte support salt, an initiator,
a solvent, and the like, as necessary.
[0262] For negative electrode active material, electrically
conductive material, binder, electrolyte-oriented high polymer,
electrolyte support salt, initiator, solvent, and the like, their
kinds as well as quantities of additions are referred to in the
foregoing description.
[0263] The particle size of negative electrode active material may
preferably be set within a range under 50 .mu.m, or more
preferably, within a range of 0.1-20 .mu.m, as such particles are
spread in the negative electrode active material layer.
[0264] At the step (b) in the method of fabrication described (see
sec. 2.1.2a), the "coating a collector with the plurality of kinds
of negative electrode slurry" may preferably be done in a similar
manner to the positive electrode slurry.
[0265] It is noted that in the first embodiment the negative-pole
electrode as well as the positive-pole electrode may preferably be
fabricated at temperatures under a dew point of -20.degree. C.
inclusive, to avoid inclusion such as of moisture into the
electrode.
2.1.3 Applications of Nonaqueous Electrolyte Electrodes
2.1.3a Nonaqueous Electrolyte Cell
[0266] The first embodiment provides various nonaqueous electrolyte
electrodes that can withstand high rate charge or discharge, which
are employed to obtain a nonaqueous electrolyte cell excellent in
performance.
[0267] For positive-pole and negative-pole electrodes of the
nonaqueous electrolyte cell, refer to the foregoing
description.
[0268] The nonaqueous electrolyte cell has its electrolyte layers,
any of which may be a nonaqueous electrolyte layer configured with
full-solid electrolyte-oriented high polymer or high-polymer gel
electrolyte.
[0269] For formation of such electrolyte layer, an adequate
electrolyte slurry (referred sometimes to "electrolyte ink" in this
embodiment) is prepared, containing electrolyte-oriented high
polymer and lithium salt, as well as initiator, solvent, etc. These
ingredients may be properly prepared to obtain a desirable
nonaqueous electrolyte layer.
[0270] The full-solid electrolyte-oriented high polymer may be
formed as a compound of polymer and lithium salt by, but not
limited to, polymerizing a monomer from a mixture of high polymer
for electrolyte and lithium salt.
[0271] The full-solid electrolyte-oriented high polymer may be
formed by soaking a gel electrolyte or full-solid
electrolyte-oriented high polymer to a separator.
[0272] The electrolyte-oriented high polymer, lithium salt,
initiator, and solvent, are similar to those described.
[0273] The high-polymer gel electrolyte may be formed by, but not
limited to, polymerizing a monomer by using an electrolytic
solution that contains an electrolyte-oriented high polymer to form
a gelled polymer.
[0274] The electrolyte-oriented high polymer and electrolytic
solution, as well as their proportions, are similar to those
described.
[0275] However, the quantity of electrolytic solution contained in
the high-polymer gel electrolyte may preferably be held
substantially even therein, or reduced from the center in an
inclined manner toward the periphery.
[0276] The former allows reaction over a wider region, as an
advantage. The latter has, at the periphery, an enhanced
sealability against electrolytic solution of full-solid
electrolyte-oriented high polymer, as an advantage.
[0277] The smaller in thickness the nonaqueous electrolyte layer
is, the better performance it has in reduction of internal
resistance.
[0278] The thickness of nonaqueous electrolyte layer may fall
within a range of 0.1-100 .mu.m, or preferably within a range of
5-20 .mu.m.
[0279] This thickness refers to the thickness of nonaqueous
electrolyte layer provided between positive-pole and negative-pole
electrodes.
[0280] Therefore, in some electrolyte layer fabrication method, the
nonaqueous electrolyte layer may be formed by joining, such as by
sticking together, a plurality of electrolyte films identical or
different in thickness.
[0281] Even in such a case, the thickness of nonaqueous electrolyte
layer refers to that formed by joining the electrolyte films.
[0282] The nonaqueous electrolyte cell according to this embodiment
may be fabricated by, but not limited to, steps of forming a
positive electrode active material layer on a collector in a
described manner, laminating thereon a nonaqueous electrolyte layer
and a negative electrode electrolyte layer to provide a lamination
by an ink jet system, holding this between collectors or the like,
and sealing a resultant laminate with a cell case so that simply
positive-pole and negative-pole electrode leads extend outside the
cell.
[0283] The nonaqueous electrolyte layer, positive-pole electrode,
and negative-pole electrode have their nonaqueous electrolyte, as
necessary, which may be identical or different.
[0284] Electrolyte slurry may preferably be coated by, but not
limited to, using a piezo type ink jet system, which allows the
nonaqueous electrolyte layer to be formed very thin.
[0285] The viscosity of electrolyte slurry may be similar to that
of positive electrode slurry.
[0286] The size of spread electrolyte layer may preferably be a
little greater than that of an electrode forming portion.
[0287] Spread electrolyte slurry may be dried and polymerized in a
similar manner to the positive electrode slurry.
[0288] Polymerized electrolyte slurry may be used to form a
negative electrode active material layer in a similar manner to the
described manner, to provide a desirable concentration
gradient.
[0289] For a nonaqueous electrolyte layer to be coated with
different kinds of negative electrode slurry spread thereon as
thin-films layers, the lamination may preferably be started from
that kind of negative electrode slurry which has a lower solid
concentration, and after a repeated lamination of a plurality of
thin-film layers, ended with that kind of negative electrode slurry
which has a higher solid concentration.
[0290] A thus prepared laminate may be held between separate
collectors or the like, and sealed with a cell case so that simply
leads of positive-pole and negative-pole electrodes extend outside
the cell.
[0291] The cell case may be configured to prevent external impact
or environmental deterioration in use.
[0292] For example, a sheath made of a laminate material having
laminated high polymer films and metallic foils may be thermally
fusion-bonded to be joined along the periphery, or configured in an
envelope form to be thermally fusion-bonded to be closed tight at
the opening, so that lead terminals of positive-pole and
negative-pole electrodes can be drawn out from the fusion-bonded
part.
[0293] The number of lead draw-out parts may be one or more for
each lead terminal.
[0294] The material of cell case may be else than described, for
instance, plastic, metal, rubber, or the like, or combination of
them. The configuration may also be film-shape, planer, or
box-shape.
[0295] The cell case may be provided with a connector for
connection between a cell inner end thereof connected to a
collector, and a cell outer end thereof connected to a lead
terminal to take out a current therefrom.
[0296] According to this embodiment, the gel electrolyte cell may
be a lithium ion secondary cell, sodium ion secondary cell,
potassium ion secondary cell, magnesium ion secondary cell, or
calcium ion secondary cell.
[0297] The lithium ion secondary cell is preferable from a
practical viewpoint.
[0298] The nonaqueous electrolyte cell using electrodes according
to the embodiment may be categorized by configuration or structure
into, but not limited to, a (planer) laminate cell, a (cylindrical)
rolled cell, or any known form or type else.
[0299] As advantages, the nonaqueous electrolyte cell has no liquid
to leak, and is free from the problem of short-circuit by liquid,
thus having high reliability, simple in structure, and excellent in
output characteristic.
[0300] The nonaqueous electrolyte cell may be improved in output
characteristics, by using a lithium-transition metal complex oxide
as the positive electrode active material, which is a low-cost
material excellent in reactivity and cycle durability, as
advantage.
[0301] The nonaqueous electrolyte cell may have an advantage in
cost and workability, by employing the (planer) laminate structure
which can provide an ensured long reliability by a simple sealing
technique such as a thermal pressure bonding.
2.1.3b Bipolar Cell
[0302] From the viewpoint of internal electrical connection
(electrode structure), the nonaqueous electrolyte cell according to
this embodiment may be categorized into a bipolar cell (an
internally serial-connected type) or non-bipolar cell (an
internally parallel-connected type).
[0303] The bipolar cell has a relatively high voltage as a simplex
cell, and allows fabrication of a cell excellent in capacity and
output characteristics.
[0304] The nonaqueous electrolyte cell according to this embodiment
may preferably be fabricated as an excellent bipolar lithium ion
secondary cell (referred herein sometimes simply to "bipolar
cell").
2.1.3c Complex Cell
[0305] According to this embodiment, a complex cell may be formed
with a plurality of nonaqueous electrolyte cells, or preferably,
with a plurality of bipolar cells.
[0306] In other words, two or more bipolar cells according to the
embodiment may be connected in serial-parallel to provide a complex
cell as a high-capacity, high-output cell or battery module, which
allows objective-dependent various demands for cell capacity and
output to be coped with at relatively low costs.
2.1.3d Vehicle
[0307] According to this embodiment, the nonaqueous electrolyte
cell has various advantages, and is preferable in application to
vehicles, in particular as a driving power supply for vehicles
severe of demand for energy and output density, such as an electric
vehicle or hybrid electric vehicle. It can provide an electric
vehicle or hybrid electric vehicle excellent in fuel consumption
and traveling performance.
[0308] Such an electric vehicle or hybrid electric vehicle may
preferably have a set of complex cells mounted as a driving power
supply under, but not limited to, a central seat of the vehicle,
with an advantageous wide space left for the passenger's room or
trunk room.
[0309] The set of complex cells may be installed under a vehicular
floor, or in a trunk room, engine room, roof space, bonnet hood,
etc.
[0310] The set of cells may preferably comprise complex cells,
bipolar cells, or combination thereof, as suitable for the
objective.
[0311] The cell set of bipolar and/or complex cells may preferably
be mounted in, but not limited to, an electric vehicle or hybrid
electric vehicle.
2.2 Details of Second Embodiment
Gel Electrolyte Electrodes
2.2.1 Configuration of Gel Electrolyte Electrode
2.2.1a Gel Electrolyte Electrode
[0312] The electrode active material layer having such a
concentration gradient may preferably be configured with, but not
limited to, a number of laminated thin-film layers different from
each other in density as well as in electrolyte salt concentration.
The number of laminated thin-film layers may be two or more, and
more preferably three or more. When the number of laminated
thin-film layers is less than two, it becomes possible to perform
rapid discharge at an increased ion concentration, for example, but
the capacity at a normal rate is lowered. On the contrary, when the
ion concentration is decreased, the capacity at a normal rate is
increased, but the rapid discharge is difficult.
[0313] The electrolyte salt to be used in the electrode of this
second embodiment may be, but not limited to, BETI (lithium
bis(perfluoro ethylene sulfonyl imide), i.e.,
Li(C.sub.2F.sub.5SO.sub.2).sub.2N), LiBF.sub.4, LiPF.sub.6,
LiN(SO.sub.2CF.sub.3).sub.2, LiN(SO.sub.2C.sub.2F.sub.5).sub.2, and
LiBOB (lithium bis oxide borate), or mixtures thereof.
[0314] Components of the electrode will be described below.
[0315] The collector may be typical or general, and may preferably
be, for example, an aluminum foil, a SUS (stainless steel) foil, a
clad material of nickel and aluminum, a clad material of copper and
aluminum, a clad material of SUS and aluminum, or a combination of
such metals to be plated.
[0316] Further, the collector may be a metal of which surface is
covered with aluminum, or may be a pair of stuck metallic foils, as
circumstances require.
[0317] In use of a complex collector, the material of its
positive-pole collector may preferably be an electrically
conductive metal such as aluminum, aluminum alloy, SUS, or
titanium, while aluminum is most preferable.
[0318] The material of negative-pole collector may preferably be an
electrically conductive metal such as copper, nickel, silver, or
SUS, while nickel and SUS are most preferable.
[0319] In the complex collector, the positive-pole and
negative-pole collectors may well be electrically connected
directly to each other, or via an electrically conductive
intermediate layer made of a third material.
[0320] The positive-pole and negative-pole collectors of complex
collector may have their thicknesses within a typical range of, for
example, about 1-100 .mu.m.
[0321] For collectors (with complex collectors inclusive), the
thickness range of about 1-100 .mu.m is preferable from the
viewpoint of making a thin cell.
2.2.1b Electrodes for Positive Pole
[0322] For use to a positive pole, the positive-pole oriented
electrode active material layer (referred herein sometimes simply
to "positive electrode layer") contains a positive electrode active
material and an electrolyte salt for enhanced ion conductivity, and
necessary additives including an electrically conductive material
for enhanced electron conductivity, a binder, and an
electrolyte.
[0323] More specifically, the positive electrode active material
may preferably be one of a family of Li--Co complex oxides such as
LiCoO.sub.2, a family of Li--Ni complex oxides such as LiNiO.sub.2,
a family of Li--Mn complex oxides such as spinel LiMn.sub.2O.sub.4,
and a family of Li--Fe complex oxides such as LiFeO.sub.2, or any
of them having elements of its transition metal substituted with
others.
[0324] These lithium transition metal complex oxides are excellent
in reactivity and cycle durability, and relatively low in cost.
[0325] They are thus advantageously used for electrodes to provide
a cell excellent in output characteristics.
[0326] The positive electrode active material may preferably be one
of phosphates or sulfates of lithium and transition metal, such as
LiFePO.sub.4; transition metal oxides or sulfides, such as
V.sub.2O.sub.5, MnO.sub.2, TiS.sub.2, MoS.sub.2, and MoO.sub.3; and
other applicable compounds such as PbO.sub.2, AgO, and NiOOH.
[0327] The particle size of positive active material may preferably
fall within a range of 0.1-50 .mu.m, or more preferably within a
range of 1-20 .mu.m.
[0328] The preferable particle size range excludes a range under
0.1 .mu.m where the difficulty of fabrication may fail to provide a
desirable charge or discharge characteristic, and a range over 50
.mu.m where one may suffer a difficulty in rubbing to the positive
electrode active material.
[0329] The electrically conductive material may preferably be
acetylene black, carbon black, graphite, or the like.
[0330] The binder may be of, but not limited to, poly vinylidene
fluoride (PVDF), SBR, polyimide, or the like.
[0331] For the electrolyte salt, refer to the foregoing
description.
[0332] In case of using, as the electrolyte layer, a separator
impregnated with gel electrolyte or electrolytic solution, the
positive electrode layer needs not to contain electrolyte, but
needs to contain a known binder for mutually binding particles of
the positive electrode active material.
[0333] The electrolyte may preferably be a gel electrolyte for an
enhanced Li-ion conductivity. The gel electrolyte, which typically
contains an electrolytic solution in an ion-conductive full-solid
high polymer electrolyte, may be such one that additionally has a
similar electrolytic solution held in a frame of a lithium
ion-nonconductive electrolytic high polymer (host polymer).
[0334] The electrolytic solution (electrolyte salt and plasticizer)
to be contained in gel electrolyte may be a typical one for lithium
ion cells, and may be, but not limited to, such one that contains
at least one kind of electrolyte salt selected from among inorganic
acid anion salts such as LiBOB (lithium bis oxide borate),
LiPF.sub.6, LiBF.sub.4, LiClO.sub.4, LiAsF.sub.6, LiTaF.sub.6,
LiAlCl.sub.4, and Li.sub.2B.sub.10Cl.sub.10, and organic acid anion
salts such as LiCF.sub.3SO.sub.3, Li(CF.sub.3SO.sub.2).sub.2N, and
Li(C.sub.2F.sub.5SO.sub.2).sub.2N, in an organic solvent
(plasticizer) such an as aprotic solvent, using at least one kind,
or having mixed two or more kinds, selected from among cyclic
carbonates such as propylene carbonate (PC), and ethylene carbonate
(EC), chain carbonates such as dimethyl carbonate, methylethyl
carbonate, and diethylcarbonate, ethers such as tetrahydrofuran,
2-methyltetrahydrofuran, 1,4-dioxane, 1,2-dimethoxyethane, and
1,2-dibutoxyethane, lactones such as .gamma.-butyrolactone,
nitriles such as acetonitrile, esters such as methyl propionate,
amides such as dimethyl formamide, methyl acetates, and methyl
formates.
[0335] The lithium ion-nonconductive host polymer to be contained
in gel electrolyte may be, but not limited to, a monomer forming a
gelled polymer such as poly vinylidene fluoride (PVDF), polyvinyl
chloride (PVC), polyacrylonitrile (PAN), or polymethyl
methacrylates (PMMA).
[0336] It is noted that PAN, PMMA and the like are exemplified as
lithium ion-nonconductive host polymers to be contained in gel
electrolyte, while they are little ion-conductive and may belong to
a group of ion-conductive high polymers.
[0337] The ratio of electrolytic high polymer and electrolytic
solution in gel electrolyte may range from 2:98 to 90:10 in mass
ratio, depending on the objective etc.
[0338] Oozing electrolyte from an outer periphery of electrode
active material layer may thus also be effectively sealed by
provision of an insulation layer or insulating part.
[0339] The mass ratio of electrolytic high polymer and electrolytic
solution in gel electrolyte may thus be determined, with a higher
priority to cell performance.
2.2.1c Electrodes for Negative Poles
[0340] For use to a negative pole, the negative-pole oriented
electrode active material layer (referred herein sometimes simply
to "negative electrode layer") contains a negative electrode active
material and electrolyte salt for enhanced ion conductivity, as
well as necessary additives including an electrically conductive
material for enhanced electron conductivity, a binder, an
electrolyte, and a film forming material for forming a film. Other
additives else than the negative electrode active material and film
forming material may be similar to those of positive electrode
layer (see sec. 2.2.1b).
[0341] The negative electrode active material may preferably be one
of various kinds of graphites such as natural or artificial
graphites, for example, fibrous graphite, scale graphite, and
spherical graphite, various kinds of lithium alloys, and the
like.
[0342] More specifically, the positive electrode active material
may preferably be one of carbon, graphite, and lithium-transition
metal complex oxide, while carbon and lithium-transition metal
complex oxide are better.
[0343] Lithium transition metal complex oxide and carbon are
excellent in reactivity and cycle durability, and relatively low in
cost.
[0344] They are thus advantageously used for electrodes to provide
a cell excellent in output characteristics.
[0345] The lithium transition metal complex oxide may be a
lithium-titanium complex oxide such as Li.sub.4Ti.sub.5O.sub.12,
for example.
[0346] The carbon may be graphite, hard carbon, or soft carbon, for
example.
[0347] The film forming material means a variety of additives for
forming decomposition-product film (solid electrolyte interface:
SEI film) by reductive decomposition of the gel electrolyte, on the
negative electrode surface. The film to be formed is
characteristically required to be thin, to have a higher ion
conductivity, and to restrict infiltration of electrolyte into the
electrode.
[0348] The film forming raw material may thus be any of succinic
anhydride, 1,6-dioxaspiro[4,4]nonane-2,7-dione,
1,4-dioxaspiro[4,5]decane-2-one, and the like; and besides,
carbonates such as vinylene carbonate, trifluoropropylene
carbonate, catechol carbonate; cyclic ethers such as
12-crown-4-ether; acid anhydrides such as glutaric anhydride;
cyclic ketones such as cyclopentanone, cyclohexanone; sultones such
as 1,3-propane sultone, 1,4-butane sultone; sulfur-containing
compounds including thio-carbonate; and nitrogen-containing
compounds including imides.
[0349] The film forming raw material may preferably be one of
sulfur-containing compounds including sultones having an
--OS(.dbd.O).sub.2-- bond, and its concrete examples include
1,3-propane sultone, 1,4-butane sultone, 2,3-dimethyl butene
sultone, 2-ethoxypentafluoro propane-1,2-sultone, dimethyl sulfate,
diethyl sulfate, ethylmethyl sulfonate. Adoption of such a film
forming raw material causes lithium-sulfur compound to intermix
into the film of negative electrode surface, increases ion
conductivity within the film, and smoothens the ion transport.
[0350] The electrode of this embodiment may be such one that has a
density gradient developed with a concentration gradient of the
film forming material from the electrode active material layer
surface toward the collector, in the electrode active material
layer on the collector. Also the film forming material act as a
cause disturbing diffusion of Li ion at high rate charge or
discharge. Thus, when the negative-electrode oriented active
material layer is designed such that the concentration of the film
forming material is increased along the thickness from the
negative-electrode oriented active material layer surface toward
the collector, the concentration of the film forming material at
the negative-electrode oriented active material layer surface can
be decreased to allow Li ion to be smoothly diffused.
[0351] Li ion can be smoothly diffused in the electrode having a
concentration gradient of the film forming material, as compared
with an electrode having a film forming material formed at a
uniformly high concentration. Further, stability of negative
electrode is enhanced in the electrode having a concentration
gradient of the film forming material, as compared with an
electrode having a film forming material formed at a uniform low
concentration.
[0352] The electrode of this embodiment preferably has
concentration gradients of the electrolyte salt and film forming
material along the thickness from the electrode active material
layer surface toward the collector, preferably in the electrode
active material layer on the collector, thereby enabling more
excellent effect to be exhibited at high rate charge or discharge.
The concentration gradients of electrolyte salt and film forming
material may be appropriately determined to obtain a desirable
electrode.
[0353] The electrode, positive or negative in polarity, may
preferably have a thickness of electrode active material layer
within a range of 1-100 .mu.m, more preferably within a range of
5-50 .mu.m.
[0354] The preferable thickness range of electrode active material
layer excludes a thickness range under 1 .mu.m where the formation
of concentration gradient is very difficult, and a thickness range
over 100 .mu.m where the ion diffusion distance may be too great to
ensure high output.
2.2.2 Fabrication of Gel Electrolyte Electrodes
2.2.2a Method of Fabrication
[0355] According to the second embodiment, a gel electrolyte
electrode is fabricated by a method including: a step (a) of
changing a quantity of an electrolyte salt to be added to compose
an electrode active material layer, thereby preparing a plurality
of kinds of electrode slurry different density as well as in a
concentration of the electrolyte salt; and a step (b) of coating a
collector with a sequence of the plurality of kinds of electrode
slurry so that the electrode active material layer has a density
gradient developed with a concentration gradient of the electrolyte
salt from a surface of the electrode active material layer toward
the collector, thereby laminating a plurality of thin-film layers
different density as well as in the concentration of the
electrolyte salt.
[0356] This method can provide the electrode according to the
second embodiment, in which a plurality of thin-film layers
different in concentration of an electrolyte salt are laminated to
have a concentration gradient with which the electrolyte salt has a
concentration gradient from a surface of an electrode active
material layer toward a collector.
2.2.2b Fabrication of Electrodes for Positive Pole
[0357] For fabrication of a positive-pole oriented electrode, at
the step (a) of the method described (see sec. 2.2.2a), the
plurality of kinds of electrode slurry are each respectively
prepared as a corresponding solution containing a positive
electrode active material (referred herein simply to "positive
electrode slurry", or sometimes to "positive electrode ink" in this
embodiment) and an electrolyte salt. This slurry may contain an
electrically conductive material, a binder, an electrolyte-oriented
high polymer as a raw material of gel electrolyte, an initiator,
and the like, as necessary.
[0358] For instance, the positive electrode slurry may be prepared
by adding additives such as an electrically conductive material,
and a binder to a solvent containing a positive electrode active
material and an electrolyte salt, and by stirring a resultant
solution for a homogeneous mixing or such.
[0359] Likewise, a plurality of kinds of slurry are prepared,
having a solvent or an electrolyte salt changed in quantities of
addition, as necessary, to provide a desirable concentration
gradient.
[0360] For the positive electrode active material, electric
conductivity, binder, electrolytic high polymer, and electrolyte
salt, refer to the foregoing description.
[0361] For viscosity control of positive electrode slurry, an
adequate solvent such as n-methyl-2-pyrrolidone (NMP) or
n-pyrrolidone may be selected in accordance with the kind of
slurry.
[0362] The particle size of positive electrode active material may
be set under 50 .mu.m in consideration of rubbing into the
positive-electrode oriented active material layer, preferably
within a range of 0.1-50 .mu.m, or more preferably within a range
of 1-20 .mu.m.
[0363] The initiator is properly selected in accordance with the
compounds to be polymerized and an employed method of
polymerization such as for thermal polymerization,
photopolymerization, radiation polymerization, or electron beam
polymerization.
[0364] For instance, the initiator may be, but not limited to,
benzyldimethylketal as a photoinitiator, or azobis isobutyronitrile
as a thermal initiator.
[0365] For positive electrode active material, electrolyte salt,
electrically conductive material, binder, and electrolytic high
polymer, the quantity of addition may be controlled in accordance
with the objective of cell, etc.
[0366] The addition quantity of initiator depends on the number of
crosslinkable functional groups in an electrolytic high polymer
employed for the gel electrolyte.
[0367] Typically, it falls within a range of about 0.01-1% in mass
ratio to the electrolytic high polymer.
[0368] At the step (b) in the method of fabrication described (see
sec. 2.2.2a), the "coating a collector with the plurality of kinds
of positive electrode slurry" may preferably be done by one of a
screen printing method, a spray coating method, an electrostatic
spray coating method, and an ink jet method.
[0369] The ink jet method is a method of using a positive electrode
slurry as an ink for ink jet and spreading droplets of positive
electrode slurry from ink jet nozzles on a collector, enabling
target regions on the collector to be coated by a desirable uniform
thin-film thickness of slurry, thus allowing the positive electrode
slurry to be spread in an optimum pattern. This is preferable.
[0370] Spreading positive electrode slurry "in an optimum pattern"
in a coating by the ink jet method means spreading the positive
electrode slurry on a collector so that an electrolyte salt has a
desirable concentration gradient.
[0371] The ink jet method employs a known drop-on-demand
system.
[0372] The system may preferably be a piezo type in which a ceramic
piezo element deforms with a voltage imposed thereon to deliver
liquid.
[0373] In the piezo type, electrode materials contained in the
positive electrode slurry (i.e. positive electrode ink) are
excellent in thermal stability so that the quantity of ink to be
spread is variable.
[0374] A piezo type ink jet head is adapted to deliver various
kinds of liquid relatively high of viscosity with an ensured
stability and precision better than other types, within an
effective delivery range up to a viscosity of 10 Pas (100 cp).
[0375] A typical piezo type ink jet head is configured with an ink
chamber for storing a positive electrode ink in the head, and an
ink introducing part communicating with the ink chamber via an ink
channel.
[0376] This ink jet head has a multiplicity of nozzles arrayed in a
lower portion thereof, an array of piezoelectric elements disposed
in an upper portion thereof, and a driver for driving piezoelectric
elements to deliver liquid of the ink chamber, to be spread from
associated nozzles.
[0377] Such a structure of ink jet head is a mere illustration, and
not restrictive.
[0378] An ink jet head available on the market may well be
used.
[0379] Metallic foils to be coated with positive electrode ink may
suffer a difficulty in their feed to an ink jet printer. Such foils
may be stuck on sheets of quality paper, to be fed to the ink jet
printer.
[0380] A plastic-make ink introducing part may be partially
dissolved by a solvent of positive electrode ink.
[0381] The ink introducing part may preferably be metallic.
[0382] The viscosity of positive electrode slurry may preferably
fall within a range of 0.1-100 cP at 25.degree. C., more
preferably, within a range of 0.5-10 cP, or yet more preferably,
within a range of 1-3 cP.
[0383] The preferable viscosity range may exclude a range under 0.1
cP where the positive electrode ink may suffer a difficulty in
liquid quantity control in the use as an ink for ink jet, and a
range exceeding 100 cP where the positive electrode ink may suffer
a difficulty in passing nozzles in the use as an ink for ink
jet.
[0384] The viscosity may well be measured by an L-type
viscosimeter, a rotary viscosimeter, or the like.
[0385] In use of a high-viscous positive electrode slurry as an ink
for ink jet, the positive electrode slurry coated on a collector
may have a stroke, plot or thin spot.
[0386] In such a case, the positive electrode slurry may preferably
be heated to an adequate viscosity, with a heater provided for the
ink chamber.
[0387] A low-viscous positive electrode slurry may have a positive
electrode active material deposited in the ink chamber, which may
well be stirred by rotary blades or the like.
[0388] The method of spreading a positive electrode slurry by an
ink jet system may preferably be one of, but not limited to: a
method (1) of providing a single ink jet head, and independently
controlling liquid delivery actions of a plurality of its
minute-diameter nozzles, thereby spreading droplets on a collector
surface in optimum pattern; and a method (2) of providing a
plurality of ink jet heads, and independently controlling their
liquid delivery actions, thereby spreading droplets on a collector
surface in an optimum pattern.
[0389] These methods enable forming a desirable optimum pattern in
a short time.
[0390] In the methods (1) and (2) described, the "independently
controlling liquid delivery actions" may include, but may not be
limited to, for instance, connecting an ink jet printer using the
ink jet head(s) to a computer available in the market or the like,
preparing a desirable pattern by software, such as Power Points (by
Microsoft Corporation) or Auto CAD (by AutoDesk Corporation), read
therein, and executing control with electric signals from such
software.
[0391] In the method (1), the "spreading droplets on a collector
surface in an optimum pattern" may exemplarily and preferably
include steps of independently controlling respective liquid
delivery actions of the minute-diameter nozzles, thereby spreading
a kind of positive electrode slurry on the collector surface to
form a thin-film layer, and thereafter, repeating spreading a kind
of positive electrode slurry lower in concentration of electrolyte
salt, each time to form a thin-film layer, thus laminating a
plurality of coats of positive electrode slurry different in
concentration, to achieve a desirable concentration gradient.
Droplets of positive electrode slurries different in electrolyte
salt concentration are delivered and mixed to thereby form
thin-film layers. Further, the method may include a step of
laminating a plurality of thin-film layers different in electrolyte
salt concentration in a suitable manner to obtain a desirable
concentration gradient.
[0392] In the method (2), the "spreading droplets on a collector
surface in an optimum pattern" may exemplarily and preferably
include a step of independently controlling the respective ink jet
heads, thereby spreading delivered and mixed droplets of a
plurality of kinds of positive electrode slurry different in
concentration of electrolyte salt, thereby forming thin-film
layers. Further, the method may include a step of laminating a
plurality of thin-film layers different in electrolyte salt
concentration in a suitable manner to obtain a desirable
concentration gradient.
[0393] The particle size of droplets of positive electrode slurry
to be delivered from ink jet head may preferably set within a range
of 1-500 pl, or more preferably within a range of 1-100 pl, in
consideration of the film thickness of thin-film layers.
[0394] The thickness of thin film to be coated and spread may
preferably fall within a range of 1-100 .mu.m, or more preferably
within a range of 5-50 .mu.m, as the thickness is adjustable to
achieve a desirable thickness of electrode active material
layer.
[0395] The preferable thickness range excludes a range under 1
.mu.m where the capacity of cell may be extremely reduced, and a
range over 100 .mu.m where an elongated diffusion distance of ion
in the electrode may render the resistance large.
[0396] The plurality of thin-film layers to be laminated in a
positive electrode active material layer may have their thicknesses
respectively determined adequately to achieve a desirable electrode
characteristic, without the need to be even.
[0397] Spread positive electrode slurry may well be dried in a
typical atmosphere, preferably in a vacuum atmosphere within a
temperature range of 20-200.degree. C. for a period within a range
of 1 minute to 8 hours, or more preferably, within a temperature
range of 80-150.degree. C. for a period within a range of 3 minutes
to 1 hour.
[0398] These conditions are not restrictive, so that the drying
condition may be determined in a suitable manner depending on, for
instance, the quantity of solvent in the spread positive electrode
slurry.
[0399] The method of polymerizing electrolyte high polymer
contained in positive electrode slurry may well be properly
determined in accordance with an employed initiator, and in use of
a photoinitiator for example, may be developed even in atmospheric
air, but preferably, in an inactive atmosphere such as argon or
nitrogen, or more preferably, in a vacuum atmosphere, within a
temperature range of 0-150.degree. C., more preferably, within a
temperature range of 20-40.degree. C., for a period within a range
of 1 minute to 8 hours, yet more preferably, within a range of 5
minutes to 1 hour, subject to an irradiation by ultraviolet
rays.
[0400] According to the embodiment, the positive-pole electrode may
be fabricated otherwise.
[0401] Additionally, a plurality of coats of positive electrode
slurry may well be laminated on a substrate such as an electrolyte
layer or a separator soaked with electrolyte, preferably through a
step of sequentially spreading a plurality of kinds of positive
electrode slurry, starting from that kind which has an electrolyte
salt concentration adjusted to a predetermined value, for
lamination to achieve a desirable concentration gradient.
[0402] Thereafter, a collector may be joined on a lamination of
dried and polymerized coats of positive electrode slurry to
fabricate a positive-pole electrode, as another applicable
method.
2.2.2c Fabrication of Electrodes for Negative Pole
[0403] For fabrication of a negative-pole oriented electrode, at
the step (a) of the method described (see sec. 2.2.2a), the
plurality of kinds of electrode slurry are each respectively
prepared as a corresponding solution containing a negative
electrode active material (referred herein simply to "negative
electrode slurry", or sometimes to "negative electrode ink" in this
embodiment) and an electrolyte salt. This slurry may contain an
electrically conductive material, a binder, an electrolytic high
polymer as a raw material of gel electrolyte, an initiator, a film
forming raw material, and the like, as necessary.
[0404] For the negative electrode active material, electrically
conductive material, binder, electrolytic high polymer, electrolyte
salt, initiator, solvent, film forming raw material and the like,
refer to the foregoing description.
[0405] The particle size of negative electrode active material may
preferably be set within a range under 50 .mu.m, or more
preferably, within a range of 0.1-20 .mu.m, as such particles are
spread in the negative electrode active material layer.
[0406] At the step (b) in the method of fabrication described (see
sec. 2.2.2a), the "coating a collector with the plurality of kinds
of negative electrode slurry" may preferably be done in a similar
manner to the positive electrode slurry.
[0407] The aforementioned manufacturing method is to form an
electrode such that the electrolyte salt has a desirable
concentration gradient. However, this embodiment is not limited
thereto, and the electrode may be formed such that the film forming
material has a desirable concentration gradient. Such a method
comprises: (a) changing an adding amount of a film forming raw
material constituting an electrode active material layer, thereby
preparing a plurality of electrode slurries different from each
other in density as well as in film forming raw material
concentration, and (b) coating the electrode slurries onto the
collector such that the electrode active material layer has a
density gradient developed with a concentration gradient of the
film forming raw material along the thickness from the electrode
active material layer surface toward the collector, thereby
laminating a plurality of thin-film layers different from each
other in density as well as in film forming raw material
concentration.
[0408] As another method, the electrode may be formed such that the
electrolyte salt and film forming material have desirable
concentration gradients, respectively. Namely, such a method
comprises: (a) changing adding amounts of an electrolyte salt and a
film forming raw material constituting an electrode active material
layer, thereby preparing a plurality of electrode slurries
different from each other in density as well as in electrolyte salt
concentration and film forming raw material concentration, and (b)
coating the electrode slurries onto the collector such that the
electrode active material layer has a density gradient developed
with concentration gradients of the electrolyte salt and the film
forming raw material along the thickness from the electrode active
material layer surface toward the collector, thereby laminating a
plurality of thin-film layers different from each other in density
as well as in electrolyte salt concentration and film forming raw
material concentration, respectively.
[0409] It is noted that in the first embodiment the negative-pole
electrode as well as the positive-pole electrode may preferably be
fabricated at temperatures under a dew point of -20.degree. C.
inclusive, to avoid inclusion such as of moisture into the
electrode.
2.2.3 Applications of Gel Electrolyte Electrodes
2.2.3a Gel Electrolyte Cell
[0410] The second embodiment provides various gel electrolyte
electrodes that can withstand high rate charge or discharge, which
are employed to obtain a gel electrolyte cell excellent in
performance.
[0411] For example, there can be provided a cell specialized in
high rate discharge, when the cell comprises: a positive electrode
comprising a collector and a positive-electrode oriented active
material layer such that the positive electrode has an electrolyte
salt concentration gradient increased along the thickness from a
positive-electrode oriented electrolyte layer surface toward the
collector; a negative electrode comprising a collector and a
negative-electrode oriented active material layer such that the
negative electrode has an electrolyte salt concentration gradient
decreased along the thickness from a negative-electrode oriented
electrolyte layer surface toward the collector; and an electrolyte
layer.
[0412] In a conventional cell having a constant concentration of
electrolyte salt in the electrodes, there was a possibility of
depletion of Li ion in the positive electrode at high rate
discharge. Further, when the concentration of an electrolyte salt
is kept uniform in the negative electrode, Li-ion conductivity
might be lowered. However, the negative electrode in the cell of
this embodiment contains the electrolyte salt having the
aforementioned concentration gradient, so that the negative
electrode readily releases Li ion. Further, the positive electrode
contains the electrolyte salt having such a concentration gradient
that the electrolyte salt concentration of the positive-electrode
oriented active material layer is high near the collector. This
facilitates diffusion of Li ion, and the large amount of
electrolyte salt is contained in the positive-electrode oriented
active material layer near the collector to thereby avoid deplete
of Li ion, thereby avoiding occurrences of over-voltage.
[0413] In the cell at high rate charge, it is sufficient to
establish concentration gradients opposite to those of the
electrodes (positive and negative electrodes) at discharge. Namely,
there can be provided a cell specialized in high rate charge such
as regeneration, by configuring the cell with: a positive electrode
comprising a collector and a positive-electrode oriented active
material layer such that the positive electrode has a gradient of
an electrolyte salt concentration decreased along the thickness
from a positive-electrode oriented electrolyte layer surface toward
the collector; a negative electrode comprising a collector and a
negative-electrode oriented active material layer such that the
negative electrode has a gradient of an electrolyte salt
concentration increased along the thickness from a
negative-electrode oriented electrolyte layer surface toward the
collector; and an electrolyte layer. Here, the term "regeneration"
means such a situation where a brake is applied in a hybrid
electric vehicle utilizing the motor for starting and accelerating
the vehicle, so as to rotate the motor by a kinetic energy of the
vehicle in a manner reverse to discharge, to thereby charge a
cell.
[0414] Combination of the aforementioned cells specialized in high
rate discharge and high rate charge enable discharge and charge of
a greater electric current in a short time, and such cells are
suitably utilized in a hybrid electric vehicle, for example.
[0415] Further, in the cell of this embodiment, the
negative-electrode oriented active material layer has such a
concentration gradient that the film forming material concentration
is increased along the thickness from the negative-electrode
oriented electrolyte layer surface toward the collector, thereby
enabling an increased Li-ion conductivity. Since the film forming
material is a cause for lowering the Li-ion conductivity, such a
concentration gradient enables a decreased concentration of the
film forming material, thereby enabling a cell specialized in high
rate discharge and charge. It may be more preferable to include
such a concentration gradient of the film forming material in the
negative electrode of the aforementioned cell specialized in high
rate discharge or high rate charge. This enables provision of a
cell specialized in high rate charge or discharge.
[0416] The cell has its electrolyte layers preferably comprising
gel electrolytes.
[0417] For formation of such electrolyte layer, an adequate
electrolyte slurry (referred sometimes to "electrolyte ink" in this
embodiment) is prepared, containing electrolytic high polymer and
electrolyte salt, as well as initiator, solvent, etc. These
ingredients may be properly prepared to obtain a desirable high
polymer electrolyte layer.
[0418] The electrolytic high polymer and electrolyte salt are
similar to those described.
[0419] The gel electrolyte may be formed by, but not limited to,
polymerizing a monomer by using an electrolytic solution that
contains an electrolytic high polymer.
[0420] The electrolytic high polymer and electrolytic solution, as
well as their proportions, are similar to those described.
[0421] However, the quantity of electrolytic solution contained in
the gel electrolyte may preferably be held substantially even
therein, or reduced from the center in an inclined manner toward
the periphery.
[0422] The former allows reaction over a wider region, as an
advantage. The latter has, at the periphery, an enhanced
sealability against electrolytic solution of full-solid high
polymer electrolyte portion, as an advantage.
[0423] The smaller in thickness the gel electrolyte layer is, the
better performance it has in reduction of internal resistance.
[0424] The thickness of electrolyte layer may fall within a range
of 0.1-100 .mu.m, preferably within a range of 1-20 .mu.m, or more
preferably within a range of 5-20 .mu.m.
[0425] This thickness refers to the thickness of electrolyte layer
provided between positive-pole and negative-pole electrodes.
[0426] Therefore, in some electrolyte layer fabrication method, the
electrolyte layer may be formed by joining, such as by sticking
together, a plurality of electrolyte films identical or different
in thickness, or coating them by an ink jet method. Even in such a
case, the thickness of electrolyte layer refers to that formed by
joining the electrolyte films.
[0427] The gel electrolyte cell according to this embodiment may be
fabricated by, but not limited to, steps of forming a positive
electrode active material layer on a collector in a described
manner, laminating thereon an electrolyte layer and a negative
electrode electrolyte layer to provide a lamination by an ink jet
system, holding this between collectors or the like, and sealing a
resultant laminate with a cell case so that simply positive-pole
and negative-pole electrode leads extend outside the cell.
[0428] The gel electrolyte layer, positive-pole electrode, and
negative-pole electrode have their gel electrolyte, as necessary,
which may be identical or different.
[0429] Electrolyte slurry may preferably be coated by, but not
limited to, using a piezo type ink jet system, which allows the
high polymer electrolyte layer to be formed very thin.
[0430] The viscosity of electrolyte slurry may be similar to that
of above described positive electrode slurry.
[0431] The size of spread electrolyte layer may preferably be a
little greater than that of an electrode forming portion.
[0432] Spread electrolyte slurry may be dried and polymerized in a
similar manner to the above described positive electrode
slurry.
[0433] Polymerized electrolyte slurry may be used to form a
negative electrode active material layer in an ink jet method
similar to the described manner, to provide a desirable
concentration gradient.
[0434] A thus prepared laminate may be held between separate
collectors or the like, and sealed with a cell case so that simply
leads of positive-pole and negative-pole electrodes extend outside
the cell.
[0435] The cell case may be configured to prevent external impact
upon usage or environmental deterioration in use.
[0436] For example, a sheath made of a laminate material having
laminated high polymer films and metallic foils may be thermally
fusion-bonded to be joined along the periphery, or configured in an
envelope form to be thermally fusion-bonded to be closed tight at
the opening, so that lead terminals of positive-pole and
negative-pole electrodes can be drawn out from the fusion-bonded
part.
[0437] The number of lead draw-out parts may be one or more for
each lead terminal.
[0438] The material of cell case may be else than described, for
instance, plastic, metal, rubber, or the like, or combination of
them. The configuration may also be film-shape, planer, or
box-shape.
[0439] The cell case may be provided with a connector for
connection between a cell inner end thereof connected to a
collector, and a cell outer end thereof connected to a lead
terminal to take out a current therefrom.
[0440] According to this embodiment, the gel electrolyte cell may
be a lithium ion secondary cell, sodium ion secondary cell,
potassium ion secondary cell, magnesium ion secondary cell, or
calcium ion secondary cell.
[0441] The lithium ion secondary cell is preferable from a
practical viewpoint.
[0442] The gel electrolyte cell using electrodes according to the
embodiment may be categorized by configuration or structure into,
but not limited to, a (planer) laminate cell, a (cylindrical)
rolled cell, or any known form or type else.
[0443] As advantages, the gel electrolyte cell has no liquid to
leak, and is free from the problem of short-circuit by liquid, thus
having high reliability, simple in structure, and excellent in
output characteristic.
[0444] The gel electrolyte cell may be improved in output
characteristics, by using a lithium-transition metal complex oxide
as the positive electrode active material, which is a low-cost
material excellent in reactivity and cycle durability, as
advantage.
[0445] The gel electrolyte cell may have an advantage in cost and
workability, by employing the (planer) laminate structure which can
provide an ensured long reliability by a simple sealing technique
such as a thermal pressure bonding.
2.2.3b Bipolar Cell
[0446] From the viewpoint of internal electrical connection
(electrode structure), the gel electrolyte cell according to this
embodiment may be categorized into a bipolar cell (an internally
serial-connected type) or non-bipolar cell (an internally
parallel-connected type).
[0447] The bipolar cell has a relatively high voltage as a simplex
cell, and allows fabrication of a cell excellent in capacity and
output characteristics.
[0448] The gel electrolyte cell according to this embodiment may
preferably be fabricated as an excellent bipolar lithium ion
secondary cell (referred herein sometimes simply to "bipolar
cell").
2.2.3c Complex Cell
[0449] According to this embodiment, a complex cell may be formed
with a plurality of gel electrolyte cells, or preferably, with a
plurality of bipolar cells.
[0450] In other words, two or more bipolar cells according to the
embodiment may be connected in serial-parallel to provide a complex
cell as a high-capacity, high-output cell or battery module, which
allows objective-dependent various demands for cell capacity and
output to be coped with at relatively low costs.
2.2.3d Vehicle
[0451] According to this embodiment, the gel electrolyte cell has
various advantages, and is preferable in application to vehicles,
in particular as a driving power supply for vehicles severe of
demand for energy and output density, such as an electric vehicle
or hybrid electric vehicle. For example, it can provide an electric
vehicle or hybrid electric vehicle excellent in fuel consumption
and traveling performance.
[0452] Such an electric vehicle or hybrid electric vehicle may
preferably have a set of complex cells mounted as a driving power
supply under, but not limited to, a central seat of the vehicle,
with an advantageous wide space left for the passenger's room or
trunk room.
[0453] The set of complex cells may be installed under a vehicular
floor, or in a trunk room, engine room, roof space, bonnet hood,
etc.
[0454] The set of cells may preferably comprise complex cells,
bipolar cells, or combination thereof, as suitable for the
objective.
[0455] The cell set of bipolar and/or complex cells may preferably
be mounted in, but not limited to, an electric vehicle or hybrid
electric vehicle.
Part-3 Specific Examples
[0456] This Part covers:
[0457] 3.1 Examples of First Embodiment
[0458] 3.2 Examples of Second Embodiment
3.1 Examples of First Embodiment
[0459] The first embodiment is exemplified below.
3.1.1 Example-1
3.1.1a Preparation of positive electrode ink
[0460] A quantity (90 g in weight) of spinel structure
LiMn.sub.2O.sub.4 (particle size: 0.6 .mu.m in average) as a
positive electrode active material, a quantity (5 g in weight) of
acetylene black as an electrically conductive material, and a
quantity (5 g in weight) of polyvinylidene fluoride as a binder
were mixed, and as a solvent to this mixture a quantity (300 g in
weight) of acetonitrile was admixed, thereby preparing a kind of
slurry as a positive electrode ink-1. The positive electrode ink-1
had a viscosity of 3 cP at a temperature of 25.degree. C.
[0461] Next, the positive electrode active material, electrically
conductive material, and binder were mixed in the same amounts as
those of the positive electrode ink-1, and as a solvent to this
mixture a quantity (500 g in weight) of acetonitrile was admixed,
thereby preparing another kind of slurry as a positive electrode
ink-2 thinner in solid concentration than the positive electrode
ink-1. The positive electrode ink-2 had a viscosity of 2 cP at a
temperature of 25.degree. C.
[0462] Further, the positive electrode active material, conductive
material, and binder were mixed in the same amounts as those of the
positive electrode ink-1, and as a solvent to this mixture a
quantity (900 g in weight) of acetonitrile was admixed, thereby
preparing yet another kind of slurry as a positive electrode ink-3
thinner in solid concentration than the positive electrode ink-2.
The positive electrode ink-3 had a viscosity of 1 cP at a
temperature of 25.degree. C.
3.1.1b Preparation of Negative Electrode Ink
[0463] A quantity (90 g in weight) of pulverized graphite (particle
size: 0.7 .mu.m in average) as a negative electrode active
material, a quantity (5 g in weight) of acetylene black as an
electrically conductive material, and a quantity (5 g in weight) of
polyvinylidene fluoride as a binder were mixed, and as a solvent to
this mixture a quantity (300 g in weight) of acetonitrile was
adimxed, thereby preparing a kind of slurry as a negative electrode
ink-1. The negative electrode ink-1 had a viscosity of 3 cP at a
temperature of 25.degree. C.
[0464] Next, the negative electrode active material, electrically
conductive material, and binder were mixed in the same amounts as
those of the negative electrode ink-1, as a solvent to this mixture
a quantity (500 g in weight) of acetonitrile was admixed, thereby
preparing another kind of slurry as a negative electrode ink-2
thinner in solid concentration than the negative electrode ink-1.
The negative electrode ink-2 had a viscosity of 2 cP at a
temperature of 25.degree. C.
[0465] Further, the negative electrode active material,
electrically conductive material, and binder were mixed in the same
amounts as those of the negative electrode ink-1, and as a solvent
to this mixture a quantity (900 g in weight) of acetonitrile was
admixed, thereby preparing yet another kind of slurry as a negative
electrode ink-3 thinner in solid concentration than the negative
electrode ink-2. The negative electrode ink-3 had a viscosity of 1
cP at a temperature of 25.degree. C.
3.1.1c Preparation of Electrolyte Ink
[0466] A quantity (160 g in weight) of macromer between
polyethylene oxide and polypropylene oxide as an electrolyte
polymer identical to that in the preparation of positive electrode
ink, a quantity (80 g in weight) of LiBETl as an electrolyte salt,
and a quantity (0.1 mass % of the electrolyte polymer) of
benzyldimethyl-ketal as a photochemical polymerization initiator
were prepared, a quantity (760 g in weight) of acetonitrile was
added as a solvent thereto, and the mixture was sufficiently
stirred, thereby preparing a slurry as an electrolyte ink. This ink
had a viscosity of 2 cP.
3.1.1d Fabrication of Secondary Cell
[0467] Positive and negative electrodes (corresponding to electrode
in FIG. 2 or FIG. 3) were fabricated by applying the prepared
positive electrode ink-1 to positive electrode ink-3 and negative
electrode ink-1 to negative electrode ink-3, using a commercially
available ink jet printer in the following manner.
[0468] There had been an issue in use of similar inks, such that a
plastic member forming an ink-introducing part of the ink jet
printer was dissolved by acetonitrile as a solvent. Therefore, the
plastic member was replaced with a metallic member, and ink was
directly supplied from an ink sump to the metallic member.
Additionally, to avoid a precipitation of active material due to a
reduced ink viscosity, the ink sump was stirred using a rotary
blade at all times.
[0469] The ink jet printer was controlled with a commercially
available computer and software. For fabrication of a positive
electrode, the positive electrode ink-1 to positive electrode ink-3
were all used. They were printed by the ink jet printer, in a
pattern mapped from the computer. To avoid the difficulty in a
direct feed of metallic foil and non-aqueous electrolyte film to
the printer, these electrode components were stuck on an A4-size
sheet of high-quality paper, which was supplied to the printer for
printing.
[0470] The positive electrode ink-1 to positive electrode ink-3
were introduced into the ink jet printer improved in the described
manner, whereby they were printed in their print patterns mapped
from the computer on a current collector (corresponding to
collector 1 of FIG. 2 or FIG. 3) of a stainless steel foil 20 .mu.m
thick, to thereby form a positive electrode layer (corresponding to
a combination of 1+12 of FIG. 2 or combination of 1+22 of FIG. 3)
composed of the collector and a positive electrode active material
layer (corresponding to electrode active material layer 12 of FIG.
2 or 22 of FIG. 3) formed thereon.
[0471] More specifically, a positive electrode thin layer-1
(corresponding to zone 12c of FIG. 2 or coat 22c of FIG. 3) was
printed with a thickness of 5 .mu.m on the collector, by applying
the positive electrode ink-1. Then, another positive electrode thin
layer-2 (corresponding to zone 12b of FIG. 2 or coat 22b of FIG. 3)
was printed with a thickness of 5 .mu.m on the positive electrode
thin layer-1, by applying the positive electrode ink-2. Further,
yet another positive electrode thin layer-3 (corresponding to zone
12a of FIG. 2 or coat 22a of FIG. 3) was printed with a thickness
of 5 .mu.m on the positive electrode thin layer-2, by applying the
positive electrode ink-3. In order to dry solvent of each printed
positive electrode thin layer, the thin layer was dried in an
evacuated oven at a temperature of 60.degree. C. for two hours.
[0472] The electrolyte ink was impregnated into the positive
electrode thin layer-1 to positive electrode thin layer-3, which
were irradiated with ultra violet rays for twenty minutes under an
evacuated condition, thereby having nonaqueous electrolyte retained
in the positive electrode thin layer-1 to positive electrode thin
layer-3.
[0473] Through the three times of pattern printing, the active
material layer of the positive electrode layer was formed with a
density gradient developed with a gradient of solid concentration
increased along the thickness from a surface of the positive
electrode active material layer toward the current collector.
[0474] Next, the electrolyte ink was introduced into the improved
ink jet printer, whereby it was printed over the positive electrode
layer, so that it was spread over the active material layer with a
slight overhang at edges thereof. The positive electrode layer
having an electrolyte layer thus printed was dried in an evacuated
oven at a temperature of 60.degree. C. for two hours, thereby
drying solvent, and was irradiated with violet rays under an
evacuated condition for twenty minutes, thereby polymerizing
electrolyte polymer, so that a nonaqueous electrolyte layer
(corresponding to layer 3 of FIG. 2 or FIG. 3) was formed on the
active material layer of the positive electrolyte layer. The
nonaqueous electrolyte layer was uniform without
irregularities.
[0475] Then, the negative electrode ink-1 to negative electrode-3
were introduced into the improved ink jet printer, whereby they
were printed in their print patterns mapped from the computer on
the above-noted nonaqueous electrolyte layer, to form thereon an
active material layer (corresponding to layer 12 of FIG. 2 or 22 of
FIG. 3) of negative electrode.
[0476] More specifically, a negative electrode thin layer-3
(corresponding to zone 12a of FIG. 2 or coat 22a of FIG. 3) was
printed with a thickness of 5 .mu.m on the nonaqueous electrolyte
layer, by applying the negative electrode ink-3. Then, another
negative electrode thin layer-2 (corresponding to zone 12b of FIG.
2 or coat 22b of FIG. 3) was printed with a thickness of 5 .mu.m on
the negative electrode thin layer-3, by applying the negative
electrode ink-2. Further, yet another negative electrode thin
layer-1 (corresponding to zone 12c of FIG. 2 or coat 22c of FIG. 3)
was printed with a thickness of 5 .mu.m on the negative electrode
thin layer-2, by applying the negative electrode ink-1. In order to
dry solvent of each printed negative electrode thin layer, the thin
layer was dried in an evacuated oven at a temperature of 60.degree.
C. for two hours.
[0477] The electrolyte ink was impregnated into the dried negative
electrode thin layer-1 to negative electrode thin layer-3, which
were irradiated with ultra violet rays for twenty minutes under an
evacuated condition, thereby having nonaqueous electrolyte retained
in the negative electrode thin layer-1 to negative electrode thin
layer-3.
[0478] Through the three times of pattern printing, the active
material layer of the negative electrode layer was formed with a
density gradient developed with a gradient of solid concentration
increased along the thickness from a bottom surface of the negative
electrode active material layer toward a top surface thereof.
[0479] The top surface of the negative electrode active material
layer was covered with a current collector. A resultant lamination
of positive electrode layer, nonaqueous electrolyte layer, negative
electrode layer, and collector had a sandwiched structure between
current-collecting stainless steel foils, of which an entirety was
enclosed and sealed with an aluminum laminate material to be
molded, simply having positive-pole and negative-pole lead wires
exposed outside, to provide a nonaqueous electrolyte secondary
cell.
3.1.2 Comparative Example-1
3.1.2a Formation of Positive Electrode Layer
[0480] A quantity (90 g in weight) of spinel structure
LiMn.sub.2O.sub.4 as a positive electrode active material, a
quantity (5 g in weight) of acetylene black as an electrically
conductive material, a quantity (5 g in weight) of polyvinylidene
fluoride as a binder, and a quantity (100 g in weight) of
acetonitrile as a solvent were mixed, thereby preparing a positive
electrode slurry. This slurry was coated on one side of a stainless
steel foil (20 .mu.m thick) as a current collector. Then, the
coated slurry was dried at a temperature of approximately
110.degree. C., so that a 15 .mu.m thick positive electrode layer
was formed.
3.1.2b Formation of Negative Electrode Layer
[0481] A quantity (90 g in weight) of pulverized graphite (particle
size: 0.6 .mu.m in average) as a negative electrode active
material, a quantity (5 g in weight) of acetylene black as an
electrically conductive material, a quantity (5 g in weight) of
polyvinylidene fluoride as a binder, and a quantity (100 g in
weight) of acetonitrile as a solvent were mixed, thereby preparing
a negative electrode slurry. This slurry was coated on the
above-noted stainless steel foil, at the opposite side to the
positive electrode layer. Then, the coated slurry was dried at a
temperature of approximately 110.degree. C., so that that a 15
.mu.m thick negative electrode layer was formed.
3.1.2c Formation of Gel Electrolyte Layer
[0482] A quantity (160 g in weight) of macromer between
polyethylene oxide and polypropylene oxide as an electrolyte
polymer identical to that of example-1, a quantity (240 g in
weight) N-methylpyrolidene as a solvent, a quantity (80 g in
weight) of 0.1M LiBETl as an electrolyte salt, and a quantity (0.1
mass % of the electrolyte polymer) of benzyldimethyl-ketal as a
polymerization initiator were mixed, thereby preparing a pre-gel
solution. This solution was impregnated into a piece of PP-made
unwoven fabric (100 .mu.m thick), which was subjected to a thermal
polymerization under an inactive atmosphere at a temperature of
90.degree. C., thereby forming a separator having gel electrolyte
retained therein.
3.1.2d Fabrication of Secondary Cell
[0483] The above-noted pre-gel solution was impregnated into the
positive and negative electrode layers, which were subjected to a
thermal polymerization under an inactive atmosphere at a
temperature of 90.degree. C., so that the electrode layers had gel
electrolyte retained therein.
[0484] These electrode layers were laminated, with the gel
electrolyte separator sandwiched in between. Then, an entirety of
this lamination was enclosed and sealed with aluminum laminate
films constituting a cell exterior to be molded, simply having
positive-pole and negative-pole lead wires exposed outside, to
provide a gel electrolyte secondary cell.
3.1.2e Evaluation
[0485] The secondary cell fabricated in the example-1 and that in
the comparative example-1 were put in a thermostatic chamber, where
their temperatures were held at 25.degree. C., to enter a discharge
performance test using a charge-discharge device.
[0486] In the discharge performance test, the secondary cells were
charged at a constant current with a constant voltage up to a full
charge state (4.2V), and subjected to a constant-current discharge
at a current rate of 20 CA to a reduced level of 2.5V, before
measurements of their discharge capacities in a high-rate discharge
to determine their discharge rates {(discharge capacity at 10
CA/theoretical capacity).times.100%}, of which results are listed
in Table-1.
[0487] The theoretical capacity of secondary cell was determined on
bases of a theoretical capacity of employed positive electrode
active material and a quantity of coated positive electrode active
material.
TABLE-US-00001 TABLE 1 Example-1 Comparative example-1 Discharge
rate at high-rate 84 53 discharge, %
[0488] As in Table 1, the discharge rate was 84% for example-1, but
53% for comparative example-1, thus proving the secondary cell of
the former to be superior.
3.2 Examples of Second Embodiment
[0489] The second embodiment is exemplified below.
3.2.1 Example-2
3.2.1a Preparation of Positive Electrode Ink
[0490] A quantity (90 g in weight) of spinel structure
LiMn.sub.2O.sub.4 (particle size: 0.6 .mu.m in average) as a
positive electrode active material, a quantity (5 g in weight) of
acetylene black as an electrically conductive material, a quantity
(5 g in weight) of polyvinylidene fluoride as a binder, a quantity
(40 g in weight) of LiBETl as an electrolyte salt, a quantity (40 g
in weight) of macromer of ethylene oxide and propylene oxide as an
electrolyte polymer synthesized in accordance with a method
described in Japanese Patent Application Laid-Open Publication No.
2002-110239, and a quantity (0.1 mass % of the electrolyte polymer)
of benzyldimethyl-ketal as a photochemical polymerization initiator
were mixed, and as a solvent to this mixture a quantity (820 g in
weight) of acetonitrile was admixed, thereby preparing a kind of
slurry as a positive electrode ink-4. The positive electrode ink-4
had a viscosity of 3 cP at a temperature of 25.degree. C.
[0491] Next, the same quantities of positive electrode active
material, electrically conductive material, binder, electrolyte
polymer, and photochemical polymerization initiator as the positive
electrode ink-4 were mixed with a quantity (30 g in weight) of
LiBETl as an electrolyte salt, and as a solvent to this mixture a
quantity (830 g in weight) of acetonitrile was admixed, thereby
preparing another kind of slurry as a positive electrode ink-5
thinner in electrolyte salt concentration than the positive
electrode ink-4. The positive electrode ink-5 had a viscosity of 3
cP at a temperature of 25.degree. C.
[0492] Further, the same quantities of positive electrode active
material, electrically conductive material, binder, electrolyte
polymer, and photochemical polymerization initiator as the positive
electrode ink-4 were mixed with a quantity (20 g in weight) of
LiBETl as an electrolyte salt, and as a solvent to this mixture a
quantity (840 g in weight) of acetonitrile was admixed, thereby
preparing yet another kind of slurry as a positive electrode ink-6
thinner in electrolyte salt concentration than the positive
electrode ink-5. The positive electrode ink-6 had a viscosity of 3
cP at a temperature of 25.degree. C.
3.2.1b Preparation of Negative Electrode Ink
[0493] A quantity (90 g in weight) of pulverized graphite (particle
size: 0.6 .mu.m in average) as a negative electrode active
material, a quantity (5 g in weight) of acetylene black as an
electrically conductive material, a quantity (5 g in weight) of
polyvinylidene fluoride as a binder, a quantity (40 g in weight) of
LiBETl as an electrolyte salt, a quantity (40 g in weight) of
macromer between polyethylene oxide and polypropylene oxide as an
electrolyte polymer similar to that employed in the preparation of
positive electrode ink, and a quantity (0.1 mass % of the
electrolyte polymer) of benzyldimethyl-ketal as a photochemical
polymerization initiator were mixed, and as a solvent to this
mixture a quantity (820 g in weight) of acetonitrile was adimxed,
thereby preparing a kind of slurry as a negative electrode ink-4.
The negative electrode ink-4 had a viscosity of 3 cP at a
temperature of 25.degree. C.
[0494] Next, the same quantities of negative electrode active
material, electrically conductive material, binder, electrolyte
polymer, and photochemical polymerization initiator as the negative
electrode ink-4 were mixed with a quantity (30 g in weight) of
LiBETl as an electrolyte salt, and as a solvent to this mixture a
quantity (830 g in weight) of acetonitrile was admixed, thereby
preparing another kind of slurry as a negative electrode ink-5
thinner in electrolyte salt concentration than the negative
electrode ink-4. The negative electrode ink-5 had a viscosity of 3
cP at a temperature of 25.degree. C.
[0495] Further, the same quantities of negative electrode active
material, electrically conductive material, binder, electrolyte
polymer, and photochemical polymerization initiator as the negative
electrode ink-4 were mixed with a quantity (20 g in weight) of
LiBETl as an electrolyte salt, and as a solvent to this mixture a
quantity (840 g in weight) of acetonitrile was admixed, thereby
preparing yet another kind of slurry as a negative electrode ink-6
thinner in electrolyte salt concentration than the negative
electrode ink-5. The negative electrode ink-6 had a viscosity of 3
cP at a temperature of 25.degree. C.
3.2.1c Preparation of Electrolyte Ink
[0496] A quantity (160 g in weight) of macromer between
polyethylene oxide and polypropylene oxide as an electrolyte
polymer identical to that in the preparation of positive electrode
ink, a quantity (80 g in weight) of LiBETl as an electrolyte salt,
and a quantity (0.1 mass % of the electrolyte polymer) of
benzyldimethyl-ketal as a photochemical polymerization initiator
were prepared, a quantity (760 g in weight) of acetonitrile was
added as a solvent thereto, and the mixture was sufficiently
stirred, thereby preparing a slurry as an electrolyte ink. This ink
had a viscosity of 2 cP.
3.2.1d Fabrication of Secondary Cell
[0497] Positive and negative electrodes (corresponding to electrode
in FIG. 4 or FIG. 5) were fabricated by applying the prepared
positive electrode ink-4 to positive electrode ink-6 and negative
electrode ink-4 to negative electrode ink-6, using a commercially
available ink jet printer in the following manner.
[0498] As described, there had been an issue in use of similar
inks, such that a plastic member forming an ink-introducing part of
the ink jet printer was dissolved by acetonitrile as a solvent.
Therefore, the plastic member was replaced with a metallic member,
and ink was directly supplied from an ink sump to the metallic
member. Additionally, to avoid a precipitation of active material
due to a reduced ink viscosity, the ink sump was stirred using a
rotary blade at all times.
[0499] The ink jet printer was controlled with a commercially
available computer and software. For fabrication of a positive
electrode, the positive electrode ink-4 to positive electrode ink-6
were used. They were printed by the ink jet printer, in a pattern
mapped from the computer. To avoid the difficulty in a direct feed
of metallic foil and gel electrolyte film to the printer, these
electrode components were stuck on an A4-size sheet of high-quality
paper, which was supplied to the printer for printing.
[0500] The positive electrode ink-4 to positive electrode ink-6
were introduced into the ink jet printer improved in the described
manner, whereby they were printed in their print patterns mapped
from the computer on a current collector (corresponding to
collector 1 of FIG. 4 or FIG. 5) of a stainless steel foil 20 .mu.m
thick, to thereby form a positive electrode layer (corresponding to
a combination of 1+32 of FIG. 4 or combination of 1+42 of FIG. 5)
composed of the collector and a positive electrode active material
layer (corresponding to electrode active material layer 32 of FIG.
4 or 42 of FIG. 5) formed thereon.
[0501] More specifically, a positive electrode thin layer-4
(corresponding to zone 32c of FIG. 4 or coat 42c of FIG. 5) was
printed with a thickness of 5 .mu.m on the collector, by applying
the positive electrode ink-4. Then, another positive electrode thin
layer-5 (corresponding to zone 32b of FIG. 4 or coat 42b of FIG. 5)
was printed with a thickness of 5 .mu.m on the positive electrode
thin layer-4, by applying the positive electrode ink-5. Further,
yet another positive electrode thin layer-6 (corresponding to zone
32a of FIG. 4 or coat 42a of FIG. 5) was printed with a thickness
of 5 .mu.m on the positive electrode thin layer-5, by applying the
positive electrode ink-6. In order to dry solvent of each printed
positive electrode thin layer, the thin layer was dried in an
evacuated oven at a temperature of 60.degree. C. for two hours.
[0502] The positive electrode thin layer-4 to positive electrode
thin layer-6 were irradiated with ultra violet rays for twenty
minutes under an evacuated condition, thereby having gel
electrolyte retained in the positive electrode thin layer-4 to
positive electrode thin layer-6. Through the three times of pattern
printing, the active material layer of the positive electrode layer
was formed with a density gradient developed with a gradient of
electrolyte concentration increased along the thickness from a
surface of the positive electrode active material layer toward the
current collector.
[0503] Next, the electrolyte ink was introduced into the improved
ink jet printer, whereby it was printed over the positive electrode
layer, so that it was spread over the active material layer with a
slight overhang at edges thereof. The positive electrode layer
having an electrolyte layer thus printed was dried in an evacuated
oven at a temperature of 60.degree. C. for two hours, thereby
drying solvent, and was irradiated with violet rays under an
evacuated condition for twenty minutes, thereby polymerizing
electrolyte polymer, so that a gel electrolyte layer (corresponding
to layer 3 of FIG. 4 or FIG. 5) was formed on the active material
layer of the positive electrolyte layer. The gel electrolyte layer
was uniform without irregularities.
[0504] Then, the negative electrode ink-4 to negative electrode-6
were introduced into the improved ink jet printer, whereby they
were printed in their print patterns mapped from the computer on
the above-noted gel electrolyte layer, to form thereon an active
material layer of negative electrode.
[0505] More specifically, a negative electrode thin layer-4 was
printed with a thickness of 5 .mu.m on the gel electrolyte layer,
by applying the negative electrode ink-4. Then, another negative
electrode thin layer-5 was printed with a thickness of 5 .mu.m on
the negative electrode thin layer-4, by applying the negative
electrode ink-5. Further, yet another negative electrode thin
layer-6 was printed with a thickness of 5 .mu.m on the negative
electrode thin layer-5, by applying the negative electrode ink-6.
In order to dry solvent of each printed negative electrode thin
layer, the thin layer was dried in an evacuated oven at a
temperature of 60.degree. C. for two hours.
[0506] The negative electrode thin layer-1 to negative electrode
thin layer-3 were irradiated with ultra violet rays for twenty
minutes under an evacuated condition, thereby having gel
electrolyte retained in the negative electrode thin layer-1 to
negative electrode thin layer-3. Through the three times of pattern
printing, the active material layer of the negative electrode layer
was formed with a density gradient developed with a gradient of
electrolyte concentration decreased along the thickness from a
bottom surface of the negative electrode active material layer
toward a top surface thereof.
[0507] The top surface of the negative electrode active material
layer was covered with a current collector. A resultant lamination
of positive electrode layer, gel electrolyte layer, negative
electrode layer, and collector had a sandwiched structure between
current-collecting stainless steel foils, of which an entirety was
enclosed and sealed with an aluminum laminate material to be
molded, simply having positive-pole and negative-pole lead wires
exposed outside, to provide a gel electrolyte secondary cell.
3.2.2 Comparative Example-2
3.2.2a Formation of Positive Electrode Layer
[0508] A quantity (90 g in weight) of spinel structure
LiMn.sub.2O.sub.4 as a positive electrode active material, a
quantity (5 g in weight) of acetylene black as an electrically
conductive material, a quantity (5 g in weight) of polyvinylidene
fluoride as a binder, and a quantity (100 g in weight) of
acetonitrile as a solvent were mixed, thereby preparing a positive
electrode slurry. This slurry was coated on one side of a stainless
steel foil (20 .mu.m thick) as a current collector. Then, the
coated slurry was dried at a temperature of approximately
110.degree. C., so that a 15 .mu.m thick positive electrode layer
was formed.
3.2.2b Formation of Negative Electrode Layer
[0509] A quantity (90 g in weight) of pulverized graphite (particle
size: 0.6 .mu.m in average) as a negative electrode active
material, a quantity (5 g in weight) of acetylene black as an
electrically conductive material, a quantity (5 g in weight) of
polyvinylidene fluoride as a binder, and a quantity (100 g in
weight) of acetonitrile as a solvent were mixed, thereby preparing
a negative electrode slurry. This slurry was coated on the
above-noted stainless steel foil, at the opposite side to the
positive electrode layer. Then, the coated slurry was dried at a
temperature of approximately 110.degree. C., so that that a 15
.mu.m thick negative electrode layer was formed.
3.2.2c Formation of Gel Electrolyte Layer
[0510] A quantity (160 g in weight) of macromer between
polyethylene oxide and polypropylene oxide as an electrolyte
polymer identical to that of example-2, a quantity (240 g in
weight) N-methylpyrolidene as a solvent, a quantity (80 g in
weight) of 0.1M LiBETl as an electrolyte salt, and a quantity (0.1
mass % of the electrolyte polymer) of benzyldimethyl-ketal as a
polymerization initiator were mixed, thereby preparing a pre-gel
solution. This solution was impregnated into a piece of PP-made
unwoven fabric (100 .mu.m thick), which was subjected to a thermal
polymerization under an inactive atmosphere at a temperature of
90.degree. C., thereby forming a separator having gel electrolyte
retained therein.
3.2.2d Fabrication of Secondary Cell
[0511] The above-noted pre-gel solution was impregnated into the
positive and negative electrode layers, which were subjected to a
thermal polymerization under an inactive atmosphere at a
temperature of 90.degree. C., so that the electrode layers had gel
electrolyte retained therein.
[0512] These electrode layers were laminated, with the gel
electrolyte separator sandwiched in between. Then, an entirety of
this lamination was enclosed and sealed with aluminum laminate
films constituting a cell exterior to be molded, simply having
positive-pole and negative-pole lead wires exposed outside, to
provide a gel electrolyte secondary cell.
3.2.2e Evaluation
[0513] The secondary cell fabricated in the example-2 and that in
the comparative example-2 were put in a thermostatic chamber, where
their temperatures were held at 25.degree. C., to enter a discharge
performance test using a charge-discharge device.
[0514] In the discharge performance test, the secondary cells were
charged at a constant current with a constant voltage up to a full
charge state (4.2V), and subjected to a constant-current discharge
at a current rate of 20 CA to a reduced level of 2.5V, before
measurements of their discharge capacities in a high-rate discharge
to determine their discharge rates {(discharge capacity at 20
CA/theoretical capacity).times.100%}, of which results are listed
in Table-2.
[0515] The theoretical capacity of secondary cell was determined on
bases of a theoretical capacity of employed positive electrode
active material and a quantity of coated positive electrode active
material.
TABLE-US-00002 TABLE 2 Example-2 Comparative example-2 Discharge
rate at high-rate 21 12 discharge, %
[0516] As in Table 2, the discharge rate was 21% for example-2, but
12% for comparative-example-2, thus proving the secondary cell of
the former to be superior.
Part-4 Supplements
[0517] It is noted that the "density gradient" of electrode active
material layer is a collective expression of, and includes, an
intended change or gradient of concentration or a plurality of
intended co-existing changes or gradients of concentrations of one
or more constituent elements or ingredients (e.g. solids,
electrolyte salts, and/or film forming raw materials) in that
layer, and the artisan may provide a very critical or substantially
critical configuration in which the density is strictly or
substantially kept constant at least in a thickness direction of
the layer, allowing for intentionally varied proportions of
ingredients to provide a changed ingredient concentration for,
e.g., changing the resistance to diffusion of mobile particles,
such as ions.
[0518] The entire contents of Japanese Patent Application No.
2003-283974 filed Jul. 31, 2003, in Japan, and Japanese Patent
Application No. 2003-283975 filed Jul. 31, 2003, in Japan are
incorporated herein by reference.
[0519] Although the invention has been described above by reference
to some embodiments of the invention, the invention is not limited
to the embodiments described. Modifications and variations of the
embodiments will occur to those skilled in the art, in light of the
teachings. The scope of the invention is defined with reference to
the following claims.
INDUSTRIAL APPLICABILITY
[0520] The present invention has wide applications to the
industrial field of secondary cells, in particular to
configuration, fabrication, and industrial application of
nonaqueous electrolyte electrodes and gel electrolyte electrodes to
be adapted for high rate charge or discharge.
* * * * *