CA2755597C - High temperature lithium battery, having initial low temperature use capability - Google Patents
High temperature lithium battery, having initial low temperature use capability Download PDFInfo
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- CA2755597C CA2755597C CA2755597A CA2755597A CA2755597C CA 2755597 C CA2755597 C CA 2755597C CA 2755597 A CA2755597 A CA 2755597A CA 2755597 A CA2755597 A CA 2755597A CA 2755597 C CA2755597 C CA 2755597C
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/362—Composites
- H01M4/366—Composites as layered products
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/38—Selection of substances as active materials, active masses, active liquids of elements or alloys
- H01M4/40—Alloys based on alkali metals
- H01M4/405—Alloys based on lithium
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M6/00—Primary cells; Manufacture thereof
- H01M6/14—Cells with non-aqueous electrolyte
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/056—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
- H01M10/0561—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of inorganic materials only
- H01M10/0563—Liquid materials, e.g. for Li-SOCl2 cells
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/10—Primary casings; Jackets or wrappings
- H01M50/138—Primary casings; Jackets or wrappings adapted for specific cells, e.g. electrochemical cells operating at high temperature
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M6/00—Primary cells; Manufacture thereof
- H01M6/14—Cells with non-aqueous electrolyte
- H01M6/18—Cells with non-aqueous electrolyte with solid electrolyte
- H01M6/20—Cells with non-aqueous electrolyte with solid electrolyte working at high temperature
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
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- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Composite Materials (AREA)
- Materials Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Primary Cells (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
Description
TEMPERATURE USE CAPABILITY
FIELD OF THE INVENTION
[0001] The present invention relates to batteries.
Substantially pure lithium may be used as the anode, and in certain types of lithium batteries liquid thionyl chloride [SOC12 ] may be used as the cathode, to produce a flow of electrons. The electrochemical oxidation-reduction reaction which occurs to produce such flow of electrons may be as follows:
at the anode: Li,u+ + e-at the cathode: 4Li+ + 4e- + 2S0C12 ¨> 4LiC1 + SO2 + S
overall reaction: 4Li + 2S0C12 ¨> 4LiC1 + SO2 + S
CALLAW\ 1744731\1 - 1 -
magnesium in order to raise the melting point of the resulting 90%Li-10%Mg alloy, thereby raising the maximum temperature to which such a lithium battery may be exposed to up to 200 C, thus rendering lithium-mg alloy batteries usable in downhole applications where temperatures may regularly approach such temperature. (Battery manufactures typically stipulate such batteries are temperature- limited to 180 C, to thereby provide a small "safety buffer")
magnesium in order to raise the melting point of the resulting Li-Mg alloy anode up to 220 C, thereby raising the maximum temperature to which such a lithium battery may be exposed, thus rendering lithium-mg alloy batteries usable in downhole applications where temperatures may regularly approach such temperature. (Battery manufactures typically presently stipulate such batteries are temperature limited to 200 C to thereby similarly stipulate a small "safety buffer"
of approximately 20 C)..
CAL_LAW\ 1744731\1 - 2 -and typically at ambient room temperature of approximately 23 C) to ensure such equipment is properly operating at surface before inserting such equipment downhole for use in drilling operations. This is due to the fact that the power and voltage available from such a lithium metal alloy anode battery at ambient temperatures, for example 23 C, is relatively low, and not sufficient to allow adequate and proper testing of the electrical equipment in the tools powered by such battery at well surface due to insufficient power/voltage supplied by such battery at such ambient temperatures.
and will continue to reliably operate when such battery and associated downhole tool is located downhole.
CAL_LAW\ 1744731\1 - 3 -SUMMARY OF THE INVENTION
(i) an anode comprising a first metal which is a strong reducing agent, and at least one further substance adapted to increase a melting point of said first metal, and (ii) said anode having applied to a surface thereof a thin, substantially uniform layer of said first metal in substantially pure form.
(wt) magnesium with a remainder substantially comprised of lithium, which base anode with a magnesium content of 25% and a thin coating of approximately 0.002 inches of pure lithium CAL_LAW\ 1744731\1 - 4 -allows for operating initially at temperatures less than 160 C and later operating at higher temperatures of up to 200 C. The cathode is in a preferred embodiment thionyl chloride, but may be any other suitable cathodic material, including sulfuryl chloride, which will provide sufficient emf voltage 'V' in the redox reaction to power the desired electrical equipment, provided such cathode and anode are of sufficient surface area to provide sufficient current i (and thus electrical power, where power P=ixV) to power the electrical equipment.
preparing a metallic alloy anode, substantially comprised of a first metal which acts as a strong reducing agent and containing a further substance to raise the melting point of said alloy anode above the melting point of said first metal in substantially pure form; and applying, to an exterior surface of said anode, a thin substantially uniform layer of said first metal, in substantially pure form.
CAL_LAW\ 1744731\1 - 5 -
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. la is a schematic top sectional view through a bobbin- type battery made in accordance with the present invention, taken along plane A-A of FIG. lb;
FIG. lb is a schematic side sectional view of the bobbin-type battery of the present invention shown in FIG. lb;
FIG. 2a is a schematic sectional view through a dual-anode type battery made in accordance with the present invention, taken along plane B-B of FIG. 2b;
FIG. 2b is a schematic side sectional view of the dual-anode type battery shown in FIG.
2a of the present invention;
FIG. 3a is a schematic view of a spiral-wind ("jelly roll") type battery made in accordance with the present invention;
FIG. 3b is a perspective partially-exploded sectional view of the spiral wind ("jelly roll") type battery shown in FIG. 3a of the present invention, taken along plane C-C
of FIG. 3a;
FIG. 4 is a graph of voltage versus time with respect to a control lithium battery and a test lithium battery, each of "DD size", wherein said test lithium battery is made in accordance with the CAL_LAW\ 1744731\1 - 6 -present method, immediately after manufacture of both the control and test batteries, with an initial 250mA start-up current being drawn from the batteries, at 20 C;
FIG. 5 is a graph of voltage versus time with respect to a control lithium battery and a test lithium battery, each of "DD size", wherein said test lithium battery is made in accordance with the present method, said graph obtained after 3 days storage of said batteries at 20 C;
FIG. 6 is a graph of voltage versus time with respect to a control lithium battery and a test lithium battery, each of "DD size" wherein said test lithium battery is made in accordance with the present method, said graph obtained after 15 days storage of said batteries at 20 C;
FIG. 7 is a graph of voltage versus time with respect to a control lithium battery and a test lithium battery, each of "DD size", wherein said test lithium battery is made in accordance with the present method, said graph obtained after 40 days storage of said batteries at 20 C;
FIG. 8 is a graph of voltage versus time with respect to a control lithium battery and a test lithium battery, each of "DD size", wherein said test lithium battery is made in accordance with the present method, said graph obtained after 90 days storage of said batteries at 20 C;
FIG. 9 is a graph of voltage versus time with respect to a control lithium battery and a test lithium battery, each of "DD size", wherein said test lithium battery is made in accordance with the present method, said graph obtained after 3 days storage of said batteries at 50 C;
FIG. 10 is a graph of voltage versus time with respect to a control lithium battery and a test lithium battery, each of "DD size", wherein said test lithium battery is made in accordance with the present method, said graph obtained after 6 days storage of said batteries at 50 C;
FIG. 11 is a graph of voltage versus time with respect to a control lithium battery and a test lithium battery, each of "DD size", wherein said test lithium battery is made in accordance with the present method, said graph obtained after 10 days storage of said batteries at 50 C;
FIG. 12 is a graph of voltage versus time with respect to a control lithium battery and a test lithium battery, each of "DD size", wherein said test lithium battery is made in accordance with the present method, said graph obtained after 14 days storage of said batteries at 50 C;
CAL_LAW\ 1744731\1 - 7 -FIG. 13 is a graph of voltage versus time with respect to a control lithium battery and a test lithium battery, each of "DD size", wherein said test lithium battery is made in accordance with the present method, said graph obtained after 24 days storage of said batteries at 50 C;
FIG. 14 is a graph of voltage versus time with respect to a control lithium battery and a test lithium battery, each of "DD size", wherein said test lithium battery is made in accordance with the present method, said graph obtained after 40 days storage of said batteries at 50 C; and FIG. 15 is a graph of voltage versus time, at room temperature of 24 C, with respect to a dual-anode size DD lithium battery of the present invention, showing the relatively high voltage of approximately 3.5 volts which is thus obtainable for a 4.2 hour period, with a .002 nominal thickness 100% pure lithium layer overlying a lithium-magnesium alloy anode.
DETAILED DESCRIPTION OF SOME PREFERRED EMBODIMENTS
In all embodiments of the battery 10, 12, and 14 of the present invention shown in FIG.'s la, lb, FIGs. 2a, 2b, and FIGs. 3a, 3b respectively, such battery comprises a metallic alloy anode 20 formed of a first metal that is a strong reducing agent, and at least one further compound adapted to increase a melting point of said first metal in said anode 20. In one embodiment, the first metal in said metallic alloy anode 20 is lithium, which is the lightest known metal and a strong reducing agent, and the alloying compound is magnesium. The lithium-magnesium alloy may be formed by direct-alloying by the melting of mole percent specific mixtures of Li and Mg metal under vacuum, or alternatively via kinetically-controlled vapour formation and deposition (KCVD) of a Li¨Mg alloy on a substrate.
CALLAW\ 1744731\1 - 8 -
Such pure form may be 99.8% pure lithium, lithium being a metal that is a strong reducing agent , and may be sourced from such suppliers as FMC Corporation or Chemetall Foote Corp., each of North Carolina, U.S.A. The application/bonding of the thin layer 22 to the metallic alloy anode 20 may be accomplished, where the first metal is lithium, by pressure rolling a thin sheet of such first metal onto the thicker metallic alloy anode 20 containing such first metal in alloy form. One such pressure roller device particularly suitable for bonding a thin layer 22 of lithium to a lithium magnesium alloy anode 20 is a Model No. ECR001 Pressure Roller manufactured by Noremac Industrial Automation Ltd.
magnesium and 75% lithium has bonded thereto by pressure rolling (in the method described above) a thin [0.002 inch (.0508mm) nominal thickness] layer 22 of 99.8% pure lithium. The resulting anode 20 is wound into a cylindrical shape and inserted in canister 25, which may serve as the negative terminal of battery 10. A non-electrically conductive separator 30 comprising a thin sheet of nonwoven fibreglass physically and electrically isolates the anode 20 and negative terminal 50 of battery 10 from a carbon element 32 which serves as the cell cathode and is connected to the cell positive terminal 42. A catholyte 40, preferably thionyl chloride [SOC12] or alternatively sulfuryl chloride [S02C12] , is inserted in battery 10. Catholyte 40, when in the form of thionyl chloride, has dissolved therein an electrolyte salt in the form of lithium tetrachloroaluminate [LiA1C14] and/or lithium tetrachlorogallate [LiGaC14] to increase ion conductivity of the thionyl chloride catholyte and increase current rates, wherein the thionyl chloride catholyte acts as the cathode for the battery 10. An end cap 45 is welded to canister 25, and a glass-metal seal member 44 is used to retain the catholyte 40 within battery canister 25.
Battery 10 via its positive CAL_LAW\ 1744731\1 - 10 -terminal 42 and negative terminal 50 is used to provide electrical current to an electrical device, symbolized by resistance "R" in FIG. lb.
type, having a pair of anodes 20a, 20b, which together result in increased surface area to thereby allow such dual-anode battery 12 to provide higher current than the bobbin-type battery 10. In such configuration a first (outer) metallic alloy anode 20a, rolled from a substantially flat substrate into a cylindrical shape, is provided. In one embodiment metallic alloy anode 20a comprises a flat strip of Li-Mg alloy onto which is pressed a thin (.002 inch nominal thickness) sheet 22a of 99.8% pure Li, and the so-formed anode 20a wound into a cylinder and inserted in cylindrical battery canister 25, with sheet 22 forming the inner periphery of cylindrical anode 20a.
A second (inner) anode 20b is similarly formed, likewise comprised of a Li-Mg metallic alloy and similarly having a thin sheet 22b of substantially pure Li applied to an outer surface thereof, and wound in a cylinder and inserted in battery canister 25 in spaced-apart position from outer anode 20a, as shown in FIG. 2b. The thickness of the thin layer 22b on anode 20b may be different than the thickness of thin layer 22a on anode 20a, or may be approximately the same .
Intermediate thin layer 22a and 22b is a carbon element 32, which has on either side thereof respective fibreglass insulating layers 30a, 30b.
pair of non-electrically conductive separators 30a, 30b each comprising a thin sheet of nonwoven fibreglass, physically and electrically isolate the anodes 20a, 20b from each other.
Electrically conductive leads 70 connected to anode 20a to 20b may be used to provide negative anode 70 for battery 12. Carbon element 32 is electrically coupled to battery positive terminal 42 as shown in FIG.'s 2a,b. An end cap 45 is welded to canister 25, and a glass-metal seal member 44 is used to retain the catholyte 40 within battery canister 25. Catholyte 40 in the form of thionyl chloride having dissolved therein an electrolyte salt in the form of lithium tetrachloroaluminate [LiA1C14] and/or lithium tetrachlorogallate [LiGaC14] is injected into battery 12, to act as the cathode for the battery 12. Battery 12 via its positive terminal 42 and negative terminal is used to provide electrical current to an electrical device, symbolized by resistance "R" in FIG. 2b.
or "jelly-roll" configuration, which as a result of the increased surface area of the anode 20a arising from CAL_LAW\ 1744731\1 - 12 -spiral winding of the anode 20a within canister 25, can provide higher current than either the bobbin-type battery 10 or "dual anode" battery 12.
and/or lithium gallium chloride [LiGaC14] is injected into battery 14, to act as the cathode for the battery 14 . Alternatively sulfuryl chloride may be used as the catholyte. A
liquid-retaining seal 56 is provided immediately above upwardly facing ends of layers 22a, 20a, 22b, 30a, 32, and 30b as shown in FIG. 3b, and an electrically insulating material 56 applied to a top surface of seal 56. A metallic end cap 60 is welded to a top end of canister 25, and a glass-metal seal member 44 is used to retain the catholyte 40 within battery canister 25.
Positive electrode 42, electrically coupled to carbon element 32, and negative electrode 70 electrically coupled to anodes 20a, 20b, protrude from a top end of battery 14..
CAL_LAW\ 1744731\1 - 13 -Example t
with various pre-storage times for each of the respective batteries tested, namely 0 days, 3 days, 15 days, 40 days, and 90 days. Voltage output continued to be monitored after removal of the 250mA load, for a further 300 seconds, for a total voltage monitoring time of 1200 seconds.
batteries tested, for each of the pre-storage times of 0, 3, 15, 40, and 90 days, are set out respectively in FIG.s 4-8, as compared to voltage output over a similar time period from a "control" battery not having any thin layer of pure Li.
Example 2
save that the pre-storage for each of the respective batteries tested, namely 3 days, 6 days, 10 CAL_LAW\ 1744731\1 - 14 -days, 14 days, 24 days, and 40 days, occurred at temperatures of 50 C, instead of at 20 C as in Example 1.
batteries tested, for each of the pre-storage times of 3, 6, 10, 14, 24, and 40 days respectively, are set out respectively in FIG.s 9-14, as compared to voltage output versus time from a "control" battery not having any thin layer of pure Li.
Example 3
being drawn from such cell, voltage from such battery was measured over a time period of approximately 13 hours.
The scope of the claims should not be limited by the preferred embodiments set forth in the foregoing examples, but should be given the broadest interpretation consistent with the description as a whole, and the claims are not to be limited to the preferred or exemplified embodiments of the invention.
CAL_LAW\ 1744731\1 - 16 -
Claims (18)
(i) an anode comprising a first metal of at least 75% by weight lithium that acts as a reducing agent and which has a melting point which does not exceed 160°C, and at least one further substance adapted to increase said melting point of said first metal ;
and (ii) said anode having applied to a surface thereof, in comparison to a thickness of said anode, a thin, substantially uniform layer of said first metal in substantially pure form without said further substance added, which thin layer allows generation of emf by said battery for said initial finite period at temperatures below 160°C.
(i) a lithium alloy anode comprising approximately 25% magnesium and a balance of approximately 75% lithium;
(ii) said anode having applied thereto a thin, substantially uniform layer of substantially pure lithium, which thin layer in said battery generates emf for an intitial finite time period at temperatures less than 160°C.
preparing a metallic alloy anode comprised of said first metal of at least 75%
by weight lithium which acts as said reducing agent and containing a further substance to raise the melting point of said alloy anode above the melting point of said first metal ; and said anode having applied to a surface thereof, in comparison to a thickness of said anode, a thin, substantially uniform layer of said first metal, in substantially pure form, said uniform layer adapted to allow said battery to produce emf for an initial discrete time interval at temperatures less than 160°C .
lithium.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA2755597A CA2755597C (en) | 2011-10-20 | 2011-10-20 | High temperature lithium battery, having initial low temperature use capability |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA2755597A CA2755597C (en) | 2011-10-20 | 2011-10-20 | High temperature lithium battery, having initial low temperature use capability |
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| Publication Number | Publication Date |
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| CA2755597A1 CA2755597A1 (en) | 2013-04-20 |
| CA2755597C true CA2755597C (en) | 2015-01-20 |
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| CA2755597A Active CA2755597C (en) | 2011-10-20 | 2011-10-20 | High temperature lithium battery, having initial low temperature use capability |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11417926B2 (en) | 2018-11-29 | 2022-08-16 | Apple Inc. | Feedthroughs for thin battery cells |
| US11431047B2 (en) | 2018-05-07 | 2022-08-30 | Apple Inc. | Feedthrough with integrated insulator |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102014213693A1 (en) * | 2014-07-15 | 2016-01-21 | Robert Bosch Gmbh | Galvanic cell and method for producing a galvanic cell |
| US11145925B2 (en) | 2018-09-06 | 2021-10-12 | Apple Inc. | Cylindrical battery cell with overmolded glass feedthrough |
| US12191511B2 (en) | 2019-06-20 | 2025-01-07 | Apple Inc. | Battery cell with serpentine tab |
-
2011
- 2011-10-20 CA CA2755597A patent/CA2755597C/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11431047B2 (en) | 2018-05-07 | 2022-08-30 | Apple Inc. | Feedthrough with integrated insulator |
| US11417926B2 (en) | 2018-11-29 | 2022-08-16 | Apple Inc. | Feedthroughs for thin battery cells |
| US11936053B2 (en) | 2018-11-29 | 2024-03-19 | Apple Inc. | Feedthroughs for thin battery cells |
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| Publication number | Publication date |
|---|---|
| CA2755597A1 (en) | 2013-04-20 |
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