Title of Invention

NON-AQUEOUS ELECTROLYTE AND ELECTROCHEMICAL DEVICE WITH AN IMPROVED SAFETY

Abstract The present invention discloses a non-aqueous electrolyte comprising a lithium salt and a solvent, the electrolyte containing, based on the weight of the electrolyte, 1-5 wt% of a compound of Formula 1 or its decomposition product, and 1-3 wt% of an aliphatic di-nitrile compound of Formula 2: [Formula 1] wherein X is fluorine and Y is hydrogen, chlorine or fluorine, [Formula 2] N=C—R—C=N wherein R is (CH2)n (n is an integer of 2-12).
Full Text

NON-AQUEOUS ELECTROLYTE AND ELECTROCHEMICAL DEVICE WITH
AN IMPROVED SAFETY
Technical Field
The present invention relates to a non-aqueous
electrolyte having improved safety and to an
electrochemical device comprising the same.
Background Art
Recently, as electronic instruments have become
wireless and portable, non-aqueous electrolyte-based
secondary batteries with high capacity and high energy
density have been practically used as drive sources for
the electronic instruments. A lithium secondary battery,
which is a typical example of the non-aqueous secondary
batteries, comprises a cathode, an anode and an
electrolyte and is chargeable and dischargeable because
lithium ions coming out from a cathode active material
during a charge process are intercalated into an anode
active material and deintercalated during a discharge
process, so that the lithium ions run between both the
electrodes while serving to transfer energy. Such a
high-capacity lithium secondary battery has an advantage
in that it can be used for a long period of time due to
high energy density. However, the lithium secondary
battery has problems in that when the battery is exposed
to high temperatures for a long period of time due to
internal heat generation during the driving thereof, the
stable structure of the battery, comprising a
cathode(ex. lithium transition metal oxide), an anode
(ex. crystalline or non-crystalline carbon) and a
separator, will be changed due to gas generation caused
by the oxidation of the electrolyte to deteriorate the
performance of the battery or, in severe cases, to cause
the ignition and explosion of the battery due to

internal short circuits in severe cases.
To solve such problems, there have been many-
recent attempts to improve the high-temperature safety
of the battery by (1) using a porous polyolefin-based
separator having a high melting point, which does not
easily melt in the internal/external thermal
environments or (2) adding a non-flammable organic
solvent to a non-aqueous electrolyte comprising a
lithium salt and a flammable organic solvent.
However, the polyolefin-based separator has a
disadvantage in that it should generally have high film
thickness in order to achieve high-melting point and to
prevent internal short circuits. This high film
thickness relatively reduces the loading amount of the
cathode and the anode, thus making it impossible to
realize a high capacity of the battery, or deteriorating
the performance of the battery in severe cases. Also,
the polyolefin-based separator consists of a polymer
such as PE or PP, which has a melting point of about
150 °C, and thus, when the battery is exposed to high
temperatures above 150 oC for a long period of time, the
separator will melt, causing short circuits inside the
battery, thus causing the ignition and explosion of the
battery.
Meanwhile, a lithium secondary battery comprising
a flammable non-aqueous electrolyte containing a lithium
salt, cyclic carbonate and linear carbonate has the
following problems at high temperatures: (1) a large
amount of heat is generated due to the reaction between
lithium transition metal oxide and the carbonate solvent
to cause the short circuit and ignition of the battery,
and (2) a thermally stable battery cannot be realized
due to the flammability of the non-aqueous electrolyte
itself.
Recently, efforts to solve the problems associated

with the flammability of the electrolyte by adding a
phosphorus (P)-based compound having flame retardancy
have been made, but the compound causes a problem of
accelerating irreversible reactions, including Li
corrosion, in a battery, thus significantly reducing the
performance and efficiency of the battery.
Disclosure of the Invention
The present inventors have found that when both a
fluoroethylene carbonate (FEC) compound and an aliphatic
di-nitrile compound are used as electrolyte additive,
these compounds show a synergic effect in terms of the
performance of a battery, as well as in terms of the
safety of the battery, for example in terms of the
prevention of battery ignition at over-charged state
and/or the prevention of ignition/explosion caused by
internal short circuit of a battery at high temperatures
above 150 °C. The present invention is based on this
finding.
The present invention provides a non-aqueous
electrolyte comprising a lithium salt and a solvent, the
electrolyte containing, based on the weight of the
electrolyte, 1-10 wt% of a compound of Formula 1 or its
decomposition product, and 1-10 wt% of an aliphatic di-
nitrile compound, as well as an electrochemical device
comprising the non-aqueous electrolyte:
[Formula 1]

wherein X and Y are each independently hydrogen,
chlorine or fluorine, except that both X and Y are not
hydrogen.
In another aspect, the present invention provides
an electrochemical device comprising: a cathode having a

complex formed between a surface of a cathode active
material and an aliphatic di-nitrile compound; and a
non-aqueous electrolyte containing 1-10 wt% of a
compound of Formula 1 or its decomposition product based
on the weight of the electrolyte.
In the present invention, the aliphatic di-nitrile
compound is preferably succinonitrile.
Moreover, in the present invention, the
decomposition product of the compound of Formula 1 has
an opened-ring structure.
Brief Description of the Accompanying Drawings
FIGS. 1 to 3 are graphic diagrams showing whether
the ignition and explosion of batteries occur after the
batteries are stored in- an oven at 150 °C in a state in
wliich the batteries are charged to 4.2V. Herein, FIG. 1
is for Example 1, FIG. 2 for Comparative Example 1, FIG.
3 for Comparative Example 2.
FIG. 4 is a graphic diagram showing the results of
heat generation analysis conducted using differential
scanning calorimetry (DSC) in order to examine the
thermal safety of each of the batteries manufactured in
Example 1 and Comparative Example 1.
Mode for Carrying Out the Invention
Hereinafter, the present invention will be
described in detail.
The present inventors have found through
experiments that the compound of Formula 1 and a nitrile
compound having a cyano (-CN) functional group show a
synergic effect in terms of securing battery safety
associated with thermal shock and in terms of high-
temperature cycle life (see FIGS. 1 to 3) .
When the compound of Formula 1 or its
decomposition product and the aliphatic di-nitrile

compound are used in combination as additive, they can
show a synergic effect in terms of the safety of a
battery, and the mechanism thereof is as follows.
The ignition and explosion reactions of a lithium
ion battery can occur due to a rapid exothermic reaction
between a charged cathode and an electrolyte, and if the
capacity of the battery increases, only controlling the
exothermic reaction between the cathode and the
electrolyte cannot secure the safety of the battery.
Generally, when the charge voltage of the cathode
is high or the capacity of the battery is increased (an
increase in the number of stacks (pouch type batteries,
etc.) or the number of electrode windings of jelly-rolls
(cylindrical or prismatic batteries, etc.)), the energy
level of the battery will be increased, and thus the
battery will tend to generate heat due to physical shock
(e.g., heat, temperature, pressure, etc.), or in severe
cases, explode, thus reducing the safety of the battery.
The compound of Formula 1 such as a fluoroethylene
carbonate can prevent or delay the battery from being
ignited by the exothermic reaction, compared to ethylene
carbonate. This is because the compound of Formula 1
consists of a halogen-based compound (e.g., one
introduced with at least one of fluorine (F) and
chlorine (CI) ) having a high flame-retardant effect, and
in particular, the compound can form an SEI layer
(protective layer) on the anode surface upon charge to
delay micro- or 'macro-thermal short circuits occurring
inside the battery.
However, the compound of Formula 1 such as a
fluoroethylene carbonate is so thermally fragile to be
easily decomposed at high temperature and to generate a
large amount of gas. The generated gas can vent a pouch-
typed or can-typed battery case, thereby accelerating
the combustion of the electrolyte and causing the

ignition and explosion of the battery due to internal
short circuits
That is, when the compound of Formula 1 or its
decomposition product is used alone, the safety of the
battery, particularly the high-temperature safety of the
battery, cannot be sufficiently secured (see FIG. 2).
Accordingly, the present invention is characterized in
that the aliphatic di-nitrile compound is used in
combination with the compound of Formula 1 or its
decomposition product.
When the aliphatic di-nitrile compound is used in
combination with the compound of Formula 1 or its
decomposition product, the aliphatic di-nitrile compound
can form a complex on the surface of a cathode
consisting of lithium-transition metal oxide so as to
inhibit the reaction between the electrolyte (ex. linear
carbonates or cyclic carbonates) and the cathode, thus
controlling heat generation and controlling an increase
in the temperature of the battery. Also, the complex
formation can prevent the combustion of the electrolyte,
which is accelerated by oxygen liberated due to the
structural collapse of the cathode, prevent thermal
runaway phenomena, and prevent the internal short
circuit of the battery from occurring due to heat
generation (see FIG. 4).
Also, the continuous interaction chemically
between the compound of Formula 1 and the cyano (-CN)
functional group of the nitrile compound prevents a
large amount of gas generation occurred when using the
compound of Formula 1 alone.
In short, 1) the compound of Formula 1 or its
decomposition product and 2) an aliphatic di-nitrile
compound such as succinonitrile can show a synergic
effect, thus improving the safety of the battery.
Furthermore, when the compound of Formula 1 or its

decomposition product and the aliphatic di-nitrile
compound are used in combination, they can show a
synergic effect in terms of the performance of a
battery, and the mechanism thereof is as follows.
The compound of Formula 1 or its decomposition
product forms a dense and close passivation layer on the
anode upon the initial charge cycle (which is generally
referred as formation of a battery). The passivation
layer prevents co-intercalation of the carbonate solvent
into the layered structure of active materials and
decomposition of the carbonate solvent, and thus reduces
irreversible reactions in the battery. Additionally, the
passivation layer allows only Li+ to be
intercalated/deintercalated through the layer, thereby
improving the life characteristics of the battery.
However, the passivation layer {SEI layer) formed
by the compound is easily decomposed at high temperature
(above 60 *C) to generate a large amount of gas (CO2 and
CO) , and particularly in the case of a cylindrical
battery, the generated gas breaks a current interruptive
device (CID), an electrochemical device at a cylindrical
cap region, to interrupt electric current, thus reducing
the function of the battery. In severe cases, the
generated gas opens the cap region, so that the
electrolyte leaks to corrode the appearance of the
battery or to cause a significant reduction in the
performance of the battery.
According to the present invention, gas generation
resulting from the compound of Formula 1 or its
decomposition product can be inhibited through the use
of the aliphatic di-nitrile compound by the chemical
interaction between the compound of Formula 1 or its
decomposition and a cyano (-CN) functional group, thus
improving the high-temperature cycle life
characteristics of the battery(see Table 2).

When considering this effect together with an
improvement in the performance of a high-capacity
battery, succinonitrile is most suitable as aliphatic
di-nitrile.
Among aliphatic di-nitrile compounds, those having
long chain length have no great effect on the
performance and safety of the battery or adversely
affect the performance of the battery, and thus those
having short chain length are preferable. However,
malononitrile (CN-CH2-CN) having an excessively short
chain length causes side reactions such as gas
generation in the battery, and thus it is preferable to
use those having 2-12 aliphatic hydrocarbons (CN-(CH2)n_
CN, n=2-12), including succinonitrile. Among them, it is
more preferable to select nitrile having small carbon
number. Most preferred is succinonitrile.
Meanwhile, among compounds containing a' cyano
functional group, aromatic nitriles and fluorinated
aromatic nitrile compounds are not preferable because
they are electrochemically easily decomposed in the
battery to interfere with the migration of Li ions, thus
deteriorating the performance of the battery.
The content of the compound of Formula 1 or its
decomposition product for use in the inventive
electrolyte is preferably 1-10 wt%, and more preferably
1-5 wt%. The compound of Formula 1 has a high viscosity,
and thus when the compound of Formula 1 is used in an
excessive amount, the ion conductivity of the
electrolyte can be reduced and the mobility of Li ion
can be inhibited, causing to a reduction of the cycle
life and capacity of battery.
The content of the aliphatic di-nitrile compound
is preferably 1-10 wt%, more preferably 1-5 wt%, and
most preferably 1-3 wt%, in view of the performance of
the electrolyte.

The inventive electrolyte may contain as an
additive an aliphatic mono-nitrile compound having one
cyano (-CN) functional group such as R-CN, wherein R is
aliphatic hydrocarbon etc.).
The inventive non-aqueous electrolyte for lithium
secondary batteries contain a general non-aqueous
organic solvents, including cyclic carbonates, linear
carbonates and combinations thereof. Typical examples of
the cyclic carbonates include ethylene carbonate (EC) ,
propylene carbonate (PC), gamma-butyrolactone (GBL) and
the like, and typical examples of the linear carbonates
include diethyl carbonate (DEC), dimethyl carbonate
(DMC), ethylmethyl carbonate (EMC) and the like.
The non-aqueous electrolyte contains a lithium
salt, non-limiting examples of which include LiCIOa,
LiCF3S03, LiPF6, LiBF4, LiAsF6, LiSbF6, LiN (CF3S02) 2,
LiN(C2F5S02)2, L1AIO4, LiAlCl4, LiS03CF3, and
LiN (CxF2x+iS02) (CyF2y+iS02) (x and y = natural numbers).
Meanwhile, the aliphatic di-nitrile compounds can
form a bond with a transition metal, such as cobalt,
contained in the cathode active material through their
cyano functional groups having high dipole moment.
Particularly, the cyano functional groups can form
stronger bonds with the surface of the cathode at high
temperature, thereby forming a complex structure.
In order to simplify a manufacturing process of a
battery, it is preferable that the aliphatic di-nitrile
compound is introduced into an electrolyte, and then a
complex is formed between the surface of a cathode
active material and the aliphatic di-nitrile compound.
However, it is also possible to separately prepare a
cathode having a complex formed on the surface thereof,
before the assemblage of a battery.
Preferably, the complex between the surface of a
cathode active material and the aliphatic di-nitrile

compound is formed by dipping a cathode, comprising a
cathode active material coated on a collector, into an
electrolyte containing the aliphatic di-nitrile compound
added thereto, followed by heat treatment at high
temperature. The high-temperature heat treatment may be
performed in such a temperature range as not to affect
electrode active materials and a binder, generally at a
temperature of 18 0 °C or lower. Otherwise, although the
high-temperature heat treatment depends on the kind of
the aliphatic di-nitrile compound, it may be performed
at such a temperature range as to prevent excessive
evaporation of the aliphatic di-nitrile compound,
generally at a temperature of 100 °C or lower. In
general, the high-temperature treatment is suitably
performed at a temperature between 60 °C and 90 °C. Long-
term treatment at a temperature between 30 °C and 4 0 °C
may provide the same effect.
In addition, in the present invention, a compound
capable of forming a passivation layer on the surface of
an anode may additionally be used to prevent side
reactions where a passivation layer formed on the anode
from the compound of Formula 1, such as fluoroethylene
carbonate, emits a large amount of gas at high
temperature. Non-limiting examples of the compound
include alkylene compounds, such as vinylene carbonate
(VC), sulfur-containing compounds, such as propane
sulfone, ethylene sulfite and 1,3-propane sultone, and
lactam-based compounds, such as N-acetyl lactam.
Furthermore, the electrolyte according to the
present invention may comprise vinylene carbonate,
propane sulfone and ethylene sulfite at the same time,
but only a sulfur-containing compound may also be
selectively added to the electrolyte to improve the
high-temperature cycle life characteristics of the
battery.

A typical example of electrochemical devices,
which can be manufactured according to the present
invention, is a lithium secondary battery, which may
comprise: (1) a cathode capable of intercalating and
deintercalating lithium ions; (2) an anode capable of
intercalating and deintercalating lithium ions; (3) a
porous separator; and (4) a) a lithium salt, and b) an
electrolyte solvent.
In general, as a cathode active material for use
in a lithium secondary battery, lithium-containing
transition metal oxides may be used. The cathode active
material can be at least one material selected from the
group consisting of LiCo02, LiNi02, LiMn204, LiMn02, and
LiNii-xCoxMy02 (wherein 0:2 X metal such as Mg, Al, Sr or La) . Meanwhile, as an anode
active material for use a lithium secondary battery,
carbon, lithium metal or lithium alloy may be used. In
addition, other metal oxides capable of lithium
intercalation/deintercalation and having an electric
potential of less than 2V based on lithium (for example,
Ti02 and Sn02) may be used as the anode active material.
The lithium secondary battery according to the
present invention may have a cylindrical, prismatic or
pouch-like shape.
Hereinafter, the present invention will be
described in further detail with reference to examples.
It is to be understood, however, that these examples are
illustrative only and the present invention is not
limited thereto.
Examples
Example 1
An electrolyte used in this Example was a 1M LiPF6
solution having a composition of EC: EMC = 1: 2. To the
electrolyte, 1 wt % of fluoroethylene carbonate and 2
wt % of succinonitrile were added. Artificial graphite
c ■ •

and LiCoC>2 were used as an anode active material and a
cathode active material, respectively. Then, a 3443 size
of lithium polymer battery was manufactured according to
a conventional method and aluminum laminate was used as
the battery package.
Example 2
A lithium polymer battery was manufactured in the
same manner as in Example 1, except that 3. wt% of
fluoroethylene carbonate was used instead of 1 wt% of
fluoroethylene carbonate.
Example 3
A lithium polymer battery was manufactured in the
same manner as in Example 1, except that 5 wt% of
fluoroethylene carbonate was used instead of 1 wt% of
fluoroethylene carbonate.
Comparative Example 1
A lithium polymer battery was manufactured in the
same manner as in Example 1, except that 1 wt% of
fluoroethylene carbonate was added and succinonitrile
was not added.
Comparative Example 2
A lithium polymer battery was manufactured in the
same manner as in Example 1, except that 2 wt% of
succinonitrile was added and fluoroethylene carbonate
was not added.
Comparative Example 3
A lithium polymer battery was manufactured in the
same manner as in Comparative Example 1, except that 3
wt% of fluoroethylene carbonate was used.
Comparative Example 4
A lithium polymer battery was manufactured in the
same manner as in Example 1, except that fluoroethylene
carbonate and succinonitrile were not added.
Comparative Example 5
A lithium polymer battery was manufactured in the

same manner as in Comparative Example 1, except that 5
wt% of fluoroethylene carbonate was used.
Comparative Example 6
A lithium polymer battery was manufactured in the
same manner as in Comparative Example 2, except that 5
wt% of butyronitrile was used instead of succinonitrile.

1. Test for Safety (1)
Each of the batteries manufactured in Example 1
and. Comparative Examples 1 and 2 was charged to 4.25V
and stored in an oven at 150 °C, and then whether the
ignition and explosion of the batteries occurred was
observed. The observation results are shown in FIGS. 1
to 3.
As can be seen in FIG. 1, only the case of the
battery containing 1 wt% of fluoroethylene carbonate
(FEC) and 2 wt% of the succinonitrile compound (SN)
added to the electrolyte solvent realized a thermally
stable battery at high temperature for 1 hour or longer
without ignition.
On the other hand, in the case of adding
fluoroethylene carbonate alone (FIG. 2) or the case of
"lidding oh'ly succinonitrile (FIG. 3), it could be seen
that the battery was ignited and exploded at a high
temperature above 150 °C without mTiTrifaTnirfg high-
temperature safety for 1 hour. However, the battery
comprising the electrolyte containing only
succinonitrile added thereto had an advantage in that
the time for the battery to explode was long because the
battery was superior to the battery comprising the
electrolyte containing fluoroethylene carbonate alone
with respect to controlling heat generation resulting
from the reaction between the cathode and the
electrolyte and the structural collapse of the cathode.
2. Test for Safety (2)

Each of the batteries manufactured in Example 1
and Comparative Example 4 was charged to 4.2V. A general
thermogravimetric analyzer, DSC (Differential Scanning
Calorimeter), was used, wherein two high-pressure pans
capable of resisting the vapor pressure of the
electrolyte were used as pans for measurement. To one
pan, about 5-10 mg of the cathode sample separated from
each of the batteries charged to 4.2V was introduced,
while the other pan was left empty. The calorific
difference between the two pans was analyzed while the
pans were heated at a rate of 5 "C/min to 400 'Cto
measure temperature peaks corresponding to heat
generation.
As shown in FIG. 4, the battery (Comparative
Example 4) manufactured without the aliphatic di-nitrile
compound shows heat generation peaks at about 200 °C and
about 240 °C. Generally, the peak at about 200 °C
indicates heat generation caused by the reaction between
the electrolyte and the cathode, while the peak at about
240 13 indicates heat generation caused by combined
factors including the reaction between the electrolyte
and the cathode, and the structural collapse of the
cathode. The battery comprising the non-aqueous
electrolyte containing succinonitrile added thereto
showed a remarkable reduction in heat generation without
showing the above two temperature peaks. This indicates
that heat generation caused by the reaction between the
electrolyte and the cathode was controlled due to the
formation of a protective layer through a strong bond
between succinonitrile and the cathode surface.
3. Test for Safety (3)
Each battery obtained from Examples 1 and 2, and
Comparative Examples 1, 2, 3, 4 and 6 was tested under
the overcharge conditions of 12V/1C and 20V/1C in a
CC/CV (Constant Current/Constant Voltage) manner. The

above overcharge test was repeated many times and the
average values for the test results are shown in the
Table 1.
As shown in Table 1, only the case of the battery
containing fluoroethylene carbonate and succinonitrile
compound added to the electrolyte solvent showed a
excellent safety without ignition nor internal short
circuits, by controlling the oxidation of the
electrolyte and the exothermic reaction resulting from
the structural collapse of the cathode.
On the other hand, in the case of adding
fluoroethylene carbonate alone such as Comparative
Example 1 and 3 or the case of adding only aliphatic
mono-nitrile compound or the aliphatic di-nitrile
compound such as Comparative Example 2 and 6, it could
be seen that the frequency of the battery ignition at
over-charged state is not constant and is largely high.
For example, batteries were ignited while a high
temperature above 200 °C was detected inside the battery/
at surface of the battery.
Meanwhile, the case of adding neither aliphatic
mono-nitrile compound nor the aliphatic di-nitrile
compound(Comparative Example 4), all the batteries were
ignited.

4. Test for battery performance

Each battery obtained from Example 3 and
Comparative Examples 4 and 5 was stored at a high
temperature of 80°C for 10 days and tested for battery
performance. The test results are shown in the following
table 2. Exmaple 3 comprising the non-aqueous
electrolyte containing fluoroethylene carbonate and
succinonitrile added thereto according to the present
invention, showed excellent capacity restorability and
battery performance even after a high-temperature
storage.

Industrial Applicability
As can be seen from the foregoing, according to
the present invention, when the compound of Formula 1
and the aliphatic di-nitrile compound are used in
combination, they can show a synergic effect in terms of
securing safety at over-charged condition or in case of
a high-temperature storage, and also can provide
excellent battery performance.
Although the preferred embodiment of the present
invention has been described for illustrative purposes,
those skilled in the art will appreciate that various
modifications, additions and substitutions are possible,
without departing from the scope and spirit of the
invention as disclosed in the accompanying claims.

We Claim:
1. A non-aqueous electrolyte comprising a lithium salt and a solvent, the
electrolyte containing, based on the weight of the electrolyte, 1-5 wt% of a
compound of Formula 1 or its decomposition product, and 1-3 wt% of an aliphatic
di-nitrile compound of Formula 2:
[Formula 1]

wherein X is fluorine and Y is hydrogen, chlorine or fluorine,
[Formula 2]
N=C—R—C=N
wherein R is (CH2)n (n is an integer of 2-12).
2. The non-aqueous electrolyte as claimed in claim 1, wherein the aliphatic
di-nitrile compound is succinonitrile.
3. The non-aqueous electrolyte as claimed in claim 1, wherein the solvent
includes cyclic carbonates or linear carbonates,wherein the cyclic carbonates are
selected from the group consisting of ethylene carbonate(EC), propylene
carbonate(PC) and gamma-butyrolactone(GBL), wherein the linear carbonates are
selected from the group consisting of diethyl carbonate(DEC), dimethyl
carbonate(DMC), ethyl methyl carbonate(EMC) and methyl propyl
carbonate(MPC).

4. The non-aqueous electrolyte as claimed in claim 1, wherein the
electrolyte includes an aliphatic mono-nitrile compound.
5. The non-aqueous electrolyte as claimed in claim 1, wherein the
electrolyte includes a compound selected from alkylene compounds, sulfur-
containing compounds and lactam-based compounds, which can form a passivation
layer on an anode surface.
6. An electrochemical device comprising a cathode, an anode, and a non-
aqueous electrolyte as claimed in any of claims 1 and 2 to 5.
7. The electrochemical device as claimed in claim 6, the cathode has a
complex formed between a surface of a cathode active material and the aliphatic di-
nitrile compound

8. The electrochemical device as claimed in claim 7, the complex between
the cathode active material surface and the aliphatic di-nitrile compound is formed
by high-temperature treating the electrochemical device manufactured from an
electrolyte containing the aliphatic di-nitrile compound added thereto, or by
dipping the cathode, comprising the cathode active material coated on a collector,
into the electrolyte containing the aliphatic di-nitrile compound added thereto,
followed by heat treatment at high temperature.

9. The electrochemical device as claimed in claim 10, wherein the high-
temperature treatment is performed at a temperature of 30 °C or more before or
after assemblage of the electrochemical device.



ABSTRACT


NON-AQUEOUS ELECTROLYTE AND ELECTROCHEMICAL DEVICE WITH AN
IMPROVED SAFETY
The present invention discloses a non-aqueous electrolyte comprising a lithium salt and a
solvent, the electrolyte containing, based on the weight of the electrolyte, 1-5 wt% of a compound of
Formula 1 or its decomposition product, and 1-3 wt% of an aliphatic di-nitrile compound of Formula 2:
[Formula 1]

wherein X is fluorine and Y is hydrogen, chlorine or fluorine,
[Formula 2]
N=C—R—C=N
wherein R is (CH2)n (n is an integer of 2-12).

Documents:

3402-KOLNP-2008-(01-03-2013)-ANNEXURE TO FORM-3.pdf

3402-KOLNP-2008-(01-03-2013)-CORRESPONDENCE.pdf

3402-KOLNP-2008-(02-05-2014)-ABSTRACT.pdf

3402-KOLNP-2008-(02-05-2014)-ANNEXURE TO FORM 3.pdf

3402-KOLNP-2008-(02-05-2014)-CLAIMS.pdf

3402-KOLNP-2008-(02-05-2014)-CORRESPONDENCE.pdf

3402-KOLNP-2008-(02-05-2014)-DRAWINGS.pdf

3402-KOLNP-2008-(02-05-2014)-FORM-1.pdf

3402-KOLNP-2008-(02-05-2014)-FORM-13.pdf

3402-KOLNP-2008-(02-05-2014)-FORM-2.pdf

3402-KOLNP-2008-(02-05-2014)-FORM-3.pdf

3402-KOLNP-2008-(02-05-2014)-FORM-5.pdf

3402-KOLNP-2008-(02-05-2014)-GPA.pdf

3402-KOLNP-2008-(02-05-2014)-OTHERS.pdf

3402-KOLNP-2008-(02-05-2014)-PETITION UNDER RULE 137.pdf

3402-KOLNP-2008-(25-02-2013)-CORRESPONDENCE.pdf

3402-KOLNP-2008-(25-02-2013)-FORM 3.pdf

3402-KOLNP-2008-(31-03-2014)-CORRESPONDENCE.pdf

3402-KOLNP-2008-(31-03-2014)-OTHERS.pdf

3402-kolnp-2008-abstract.pdf

3402-kolnp-2008-ASSIGNMENT-1.1.pdf

3402-kolnp-2008-assignment.pdf

3402-kolnp-2008-CANCELLED PAGES.pdf

3402-kolnp-2008-claims.pdf

3402-kolnp-2008-CORRESPONDENCE-1.1.pdf

3402-kolnp-2008-correspondence.pdf

3402-kolnp-2008-description (complete).pdf

3402-kolnp-2008-drawings.pdf

3402-kolnp-2008-EXAMINATION REPORT.pdf

3402-kolnp-2008-form 1.pdf

3402-kolnp-2008-FORM 13.pdf

3402-kolnp-2008-FORM 18-1.1.pdf

3402-kolnp-2008-form 18.pdf

3402-kolnp-2008-form 3.pdf

3402-kolnp-2008-form 5.pdf

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Patent Number 263787
Indian Patent Application Number 3402/KOLNP/2008
PG Journal Number 48/2014
Publication Date 28-Nov-2014
Grant Date 20-Nov-2014
Date of Filing 21-Aug-2008
Name of Patentee LG CHEM, LTD.
Applicant Address 20, YOIDO-DONG, YOUNGDUNGPO-GU SEOUL
Inventors:
# Inventor's Name Inventor's Address
1 KIM, YOUNG-SOO 202, 122-17 SHINSUNG-DONG, YUSEONG-GU, DAEJEON 305-345
2 HA, SOO-HYUN 1902, YEONSAN SSANGYONG APARTMENT, 603-7, YEONSAN4-DONG, YEONJE-GU, BUSAN 611-820
3 AHN, SOON-HO 108-502, DAELIM DURE APARTMENT, SHINSUNG-DONG, YUSEONG-GU, DAEJEON 305-720
PCT International Classification Number H01M 10/40
PCT International Application Number PCT/KR2007/000809
PCT International Filing date 2007-02-15
PCT Conventions:
# PCT Application Number Date of Convention Priority Country
1 10-2006-0014640 2006-02-15 Republic of Korea