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JP7092536B2 - Endothermic sheet for assembled battery and assembled battery - Google Patents
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JP7092536B2 - Endothermic sheet for assembled battery and assembled battery - Google Patents

Endothermic sheet for assembled battery and assembled battery Download PDF

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JP7092536B2
JP7092536B2 JP2018065759A JP2018065759A JP7092536B2 JP 7092536 B2 JP7092536 B2 JP 7092536B2 JP 2018065759 A JP2018065759 A JP 2018065759A JP 2018065759 A JP2018065759 A JP 2018065759A JP 7092536 B2 JP7092536 B2 JP 7092536B2
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endothermic
sheet
hydrate
assembled battery
hydroxide
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JP2019175806A (en
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直己 高橋
清成 畑中
寿 安藤
栄徳 森永
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Ibiden Co Ltd
Tomoegawa Co Ltd
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/20Mountings; Secondary casings or frames; Racks, modules or packs; Suspension devices; Shock absorbers; Transport or carrying devices; Holders
    • H01M50/249Mountings; Secondary casings or frames; Racks, modules or packs; Suspension devices; Shock absorbers; Transport or carrying devices; Holders specially adapted for aircraft or vehicles, e.g. cars or trains
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/61Types of temperature control
    • H01M10/613Cooling or keeping cold
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/62Heating or cooling; Temperature control specially adapted for specific applications
    • H01M10/625Vehicles
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/64Heating or cooling; Temperature control characterised by the shape of the cells
    • H01M10/647Prismatic or flat cells, e.g. pouch cells
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/65Means for temperature control structurally associated with the cells
    • H01M10/651Means for temperature control structurally associated with the cells characterised by parameters specified by a numeric value or mathematical formula, e.g. ratios, sizes or concentrations
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/65Means for temperature control structurally associated with the cells
    • H01M10/653Means for temperature control structurally associated with the cells characterised by electrically insulating or thermally conductive materials
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/65Means for temperature control structurally associated with the cells
    • H01M10/655Solid structures for heat exchange or heat conduction
    • H01M10/6554Rods or plates
    • H01M10/6555Rods or plates arranged between the cells
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/65Means for temperature control structurally associated with the cells
    • H01M10/658Means for temperature control structurally associated with the cells by thermal insulation or shielding
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/20Mountings; Secondary casings or frames; Racks, modules or packs; Suspension devices; Shock absorbers; Transport or carrying devices; Holders
    • H01M50/204Racks, modules or packs for multiple batteries or multiple cells
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/20Mountings; Secondary casings or frames; Racks, modules or packs; Suspension devices; Shock absorbers; Transport or carrying devices; Holders
    • H01M50/233Mountings; Secondary casings or frames; Racks, modules or packs; Suspension devices; Shock absorbers; Transport or carrying devices; Holders characterised by physical properties of casings or racks, e.g. dimensions
    • H01M50/24Mountings; Secondary casings or frames; Racks, modules or packs; Suspension devices; Shock absorbers; Transport or carrying devices; Holders characterised by physical properties of casings or racks, e.g. dimensions adapted for protecting batteries from their environment, e.g. from corrosion
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

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  • General Chemical & Material Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
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Description

本発明は、例えば、電気自動車またはハイブリッド車などを駆動する電動モータの電源となる組電池に好適に用いられる組電池用吸熱シートに関する。 The present invention relates to, for example, a heat absorbing sheet for an assembled battery that is suitably used for an assembled battery that is a power source for an electric motor that drives an electric vehicle or a hybrid vehicle.

近年、環境保護の観点から電動モータで駆動する電気自動車またはハイブリッド車などの開発が盛んに進められている。この電気自動車またはハイブリッド車などには、駆動用電動モータの電源となるための、複数の電池セルが直列または並列に接続された組電池が搭載されている。 In recent years, from the viewpoint of environmental protection, the development of electric vehicles or hybrid vehicles driven by electric motors has been actively promoted. This electric vehicle or hybrid vehicle is equipped with an assembled battery in which a plurality of battery cells are connected in series or in parallel to serve as a power source for a driving electric motor.

この電池セルには、鉛蓄電池やニッケル水素電池などに比べて、高容量かつ高出力が可能なリチウムイオン二次電池が主に用いられているが、電池の内部短絡や過充電などが原因で1つの電池セルに熱暴走が生じた場合(すなわち、異常時)、隣接する他の電池セルへ熱の伝播が起こることで、他の電池セルの熱暴走を引き起こすおそれがある。 Lithium-ion secondary batteries, which have higher capacity and higher output than lead storage batteries and nickel-hydrogen batteries, are mainly used for these battery cells, but due to internal short circuits and overcharging of the batteries, etc. When a thermal runaway occurs in one battery cell (that is, in an abnormal situation), heat propagation to another adjacent battery cell may cause a thermal runaway of another battery cell.

上記のような熱暴走の伝播を抑制するための技術として、特許文献1には、1以上の蓄電素子を備える蓄電装置であって、前記1以上の蓄電素子のうちの1つである第一蓄電素子の側方に配置された第一板材および第二板材であって、互いの面が対向するように配置された第一板材および第二板材を備え、前記第一板材と前記第二板材との間には、前記第一板材および前記第二板材よりも熱伝導率の低い物質の層である低熱伝導層(例えば、空気層)が形成されていることにより、第一蓄電素子からの輻射熱、または、第一蓄電素子に向かう輻射熱は2枚の板材によって遮断され、かつ、これら2枚の板材の一方から他方への熱の移動は低熱伝導層によって抑制されるため、蓄電素子と他の物体との間の効果的な断熱を実現することができることが開示されている。 As a technique for suppressing the propagation of thermal runaway as described above, Patent Document 1 describes a power storage device including one or more power storage elements, which is one of the one or more power storage elements. The first plate material and the second plate material arranged on the side of the power storage element, the first plate material and the second plate material arranged so that the surfaces face each other are provided, and the first plate material and the second plate material are provided. A low thermal conductive layer (for example, an air layer), which is a layer of a substance having a lower thermal conductivity than the first plate material and the second plate material, is formed between the first plate material and the first plate material. Since the radiant heat or the radiant heat toward the first storage element is blocked by the two plates, and the heat transfer from one of the two plates to the other is suppressed by the low thermal conductive layer, the storage element and the other It is disclosed that effective insulation between the object and the object can be realized.

また、熱暴走の伝播を抑制するための他の技術として、特許文献2には、電解液を収容する電池筐体と、前記電池筐体の中に設けられた、熱暴走抑制物質をその内部に収容する熱暴走抑制物質収容構造体とを備える二次電池であって、前記熱暴走抑制物質として、水酸化アルミニウム水和物などの各種材料が例として開示されている。 Further, as another technique for suppressing the propagation of thermal runaway, Patent Document 2 describes a battery housing containing an electrolytic solution and a thermal runaway suppressing substance provided in the battery housing. A secondary battery including a thermal runaway inhibitor accommodating structure accommodating the thermal runaway inhibitor, and various materials such as aluminum hydroxide hydrate are disclosed as examples of the thermal runaway inhibitor.

特開2015-211013号公報JP-A-2015-210113 特開2009-301798号公報Japanese Unexamined Patent Publication No. 2009-301798

一方、組電池化した電池セルに対し充放電サイクルを行う場合(すなわち、通常使用時)において、電池セルの充放電性能を十分に発揮させるためには、電池セル表面の温度を所定値以下(例えば、150℃以下)に維持する必要がある。
しかしながら、上記特許文献1においては、熱暴走時の熱の伝播抑制のため、複数の電池セル間に断熱層を設けることから、充放電サイクル時に発熱する電池セルを効果的に冷却することができるものではなかった。
また、上記特許文献2においては、異常事態が発生したときに速やかにリチウムイオン二次電池を安全な状態にすることのみを目的としていることから、その解決方法として、水酸化アルミニウム水和物のような、高温(例えば、200℃以上)条件下で水分を放出して周囲の冷却を行うような熱暴走抑制物質を電池内部に収容することしか想定されていない。よって、充放電サイクル時に発熱する電池セルを効果的に冷却するには必ずしも十分であるとは言えなかった。
On the other hand, in the case of performing a charge / discharge cycle on a battery cell made into an assembled battery (that is, during normal use), in order to fully exhibit the charge / discharge performance of the battery cell, the temperature of the battery cell surface should be kept below a predetermined value (that is, during normal use). For example, it is necessary to maintain the temperature below 150 ° C.
However, in Patent Document 1, since a heat insulating layer is provided between a plurality of battery cells in order to suppress heat propagation during thermal runaway, it is possible to effectively cool the battery cells that generate heat during the charge / discharge cycle. It wasn't a thing.
Further, since the purpose of Patent Document 2 is only to promptly put the lithium ion secondary battery into a safe state when an abnormal situation occurs, as a solution to the problem, aluminum hydroxide hydrate is used. It is only assumed that a thermal runaway inhibitor that releases water to cool the surroundings under high temperature (for example, 200 ° C. or higher) conditions is contained in the battery. Therefore, it cannot be said that it is always sufficient to effectively cool the battery cell that generates heat during the charge / discharge cycle.

本発明は、このような事情に着目してなされたものであり、複数の電池セルが直列または並列に接続された組電池を構成するに当たり、異常時における各電池セル間の熱の伝播を抑制しつつ、通常使用時における各電池セルを冷却することのできる、組電池用吸熱シートを提供することを目的とする。 The present invention has been made by paying attention to such a situation, and suppresses heat propagation between each battery cell at the time of abnormality in constructing an assembled battery in which a plurality of battery cells are connected in series or in parallel. However, it is an object of the present invention to provide an endothermic sheet for an assembled battery capable of cooling each battery cell during normal use.

上記目的を達成するため、本発明の一態様に係る組電池用吸熱シートの要旨は、複数の電池セルが吸熱シートを介して配置され、該複数の電池セルが直接または並列に接続された組電池に用いられる吸熱シートであって、脱水温度が異なる物質を2種以上含有するとともに、該物質のうち少なくとも1種は、前記電池セルの通常使用時において脱水可能であり、該物質のうち少なくとも1種は、前記電池セルの異常時において脱水可能であることを特徴とする。 In order to achieve the above object, the gist of the heat absorbing sheet for an assembled battery according to one aspect of the present invention is a set in which a plurality of battery cells are arranged via the heat absorbing sheet and the plurality of battery cells are directly or in parallel connected. A heat absorbing sheet used for a battery, which contains two or more substances having different dehydration temperatures, and at least one of the substances can be dehydrated during normal use of the battery cell, and at least one of the substances. One is characterized in that it can be dehydrated in the event of an abnormality in the battery cell.

上記組電池用吸熱シートにおける好ましい実施形態において、前記通常使用時において脱水可能な物質は、150℃以下の温度で脱水可能な脱水剤であり、前記異常時において脱水可能な物質は、熱分解開始温度が200℃以上の無機水和物である。
上記組電池用吸熱シートにおける好ましい実施形態において、前記脱水剤は、シリカゲル、活性アルミナ、活性炭、ゼオライト、イオン交換樹脂、硫酸塩水和物、亜硫酸塩水和物、リン酸塩水和物、硝酸塩水和物、酢酸塩水和物、金属水和塩からなる群のうち少なくとも1つである。
上記組電池用吸熱シートにおける好ましい実施形態において、前記脱水剤がゼオライトである。
上記組電池用吸熱シートにおける好ましい実施形態において、前記無機水和物は、水酸化アルミニウム、水酸化マグネシウム、水酸化カルシウム、水酸化亜鉛、水酸化鉄、水酸化マンガン、水酸化ジルコニウムおよび水酸化ガリウムからなる群のうち少なくとも1つである。
上記組電池用吸熱シートにおける好ましい実施形態において、前記無機水和物が水酸化アルミニウムである。
上記組電池用吸熱シートにおける好ましい実施形態において、前記吸熱シートにおける厚み方向中心部から両端部に向かうほど、前記通常使用時において脱水可能な物質の含有量が大きく、かつ、前記吸熱シートにおける厚み方向両端部から中心部に向かうほど、前記異常時において脱水可能な物質の含有量が大きい。
上記組電池用吸熱シートにおける好ましい実施形態において、前記異常時において脱水可能な物質を主成分とする第1の吸熱層と、該第1の吸熱層の両面に形成され、前記通常使用時において脱水可能な物質を主成分とする第2の吸熱層を有する。
In a preferred embodiment of the heat-absorbing sheet for an assembled battery, the substance that can be dehydrated during normal use is a dehydrating agent that can be dehydrated at a temperature of 150 ° C. or lower, and the substance that can be dehydrated at the abnormal time starts thermal decomposition. It is an inorganic hydrate having a temperature of 200 ° C. or higher.
In a preferred embodiment of the heat absorbing sheet for an assembled battery, the dehydrating agent is silica gel, active alumina, activated charcoal, zeolite, ion exchange resin, sulfate hydrate, sulfite hydrate, phosphate hydrate, nitrate hydrate. , Acetate hydrate, metal hydrate, at least one of the group.
In a preferred embodiment of the endothermic sheet for assembled batteries, the dehydrating agent is zeolite.
In a preferred embodiment of the heat absorbing sheet for an assembled battery, the inorganic hydrate is aluminum hydroxide, magnesium hydroxide, calcium hydroxide, zinc hydroxide, iron hydroxide, manganese hydroxide, zirconium hydroxide and gallium hydroxide. At least one of the group consisting of.
In a preferred embodiment of the endothermic sheet for assembled batteries, the inorganic hydrate is aluminum hydroxide.
In a preferred embodiment of the endothermic sheet for an endothermic battery, the more the endothermic sheet is from the center in the thickness direction to both ends, the larger the content of the substance that can be dehydrated during normal use is, and the more the endothermic sheet is in the thickness direction. The more from both ends to the center, the greater the content of the substance that can be dehydrated at the time of the abnormality.
In a preferred embodiment of the endothermic sheet for an assembled battery, it is formed on both sides of a first endothermic layer containing a substance that can be dehydrated at the time of abnormality as a main component and the first endothermic layer, and is dehydrated at the time of normal use. It has a second endothermic layer whose main component is a possible substance.

また、本発明の一態様に係る組電池の要旨は、複数の電池セルが、上記の組電池用吸熱シートを介して配置され、該複数の電池セルが直列または並列に接続されたことを特徴とする。 Further, the gist of the assembled battery according to one aspect of the present invention is characterized in that a plurality of battery cells are arranged via the above-mentioned endothermic sheet for assembled batteries, and the plurality of battery cells are connected in series or in parallel. And.

本発明に係る組電池用吸熱シートによれば、複数の電池セルが直列または並列に接続された組電池を構成するに当たり、異常時における各電池セル間の熱の伝播を抑制しつつ、通常使用時における各電池セルを冷却することのできる、組電池用吸熱シートを提供することができる。 According to the endothermic sheet for an assembled battery according to the present invention, when constituting an assembled battery in which a plurality of battery cells are connected in series or in parallel, it is normally used while suppressing heat propagation between the battery cells in an abnormal situation. It is possible to provide an endothermic sheet for an assembled battery capable of cooling each battery cell at the time.

図1は、本発明の第1の実施形態に係る組電池用吸熱シートの構成例を模式的に示す断面図である。FIG. 1 is a cross-sectional view schematically showing a configuration example of an endothermic sheet for an assembled battery according to the first embodiment of the present invention. 図2は、本発明の第1の実施形態に係る組電池用吸熱シートの他の構成例を模式的に示す断面図である。FIG. 2 is a cross-sectional view schematically showing another configuration example of the endothermic sheet for an assembled battery according to the first embodiment of the present invention. 図3は、本発明の第2の実施形態に係る組電池用吸熱シートの構成例を模式的に示す断面図である。FIG. 3 is a cross-sectional view schematically showing a configuration example of an endothermic sheet for an assembled battery according to a second embodiment of the present invention. 図4は、本発明の第2の実施形態に係る組電池用吸熱シートの他の構成例を模式的に示す断面図である。FIG. 4 is a cross-sectional view schematically showing another configuration example of the endothermic sheet for an assembled battery according to the second embodiment of the present invention. 図5は、本発明の第1の実施形態に係る組電池用吸熱シートを適用した組電池の構成例を模式的に示す断面図である。FIG. 5 is a cross-sectional view schematically showing a configuration example of an assembled battery to which the endothermic sheet for an assembled battery according to the first embodiment of the present invention is applied. 図6は、実施例1および比較例1および比較例2の吸熱シートをヒーターで加熱した場合(ヒーター温度:150℃)の、経過時間に対する熱源となる電池セル表面の温度変化をプロットしたグラフである。FIG. 6 is a graph plotting the temperature change on the surface of the battery cell, which is a heat source, with respect to the elapsed time when the endothermic sheets of Example 1, Comparative Example 1 and Comparative Example 2 are heated by a heater (heater temperature: 150 ° C.). be. 図7は、実施例1、比較例1、比較例2および参考例1の吸熱シートをヒーターで加熱した場合(ヒーター温度:700℃)の、経過時間に対する隣接する電池セル表面の温度変化をプロットしたグラフである。FIG. 7 plots the temperature change of the surface of the adjacent battery cell with respect to the elapsed time when the endothermic sheets of Example 1, Comparative Example 1, Comparative Example 2 and Reference Example 1 are heated by a heater (heater temperature: 700 ° C.). It is a graph.

本発明者らは、高温の熱が発生する異常時における各電池セル間の熱の伝播を抑制しつつ、比較的低温の熱が発生する通常使用時における各電池セルを冷却することのできる、組電池用吸熱シートを提供するため、鋭意検討を行ってきた。 The present inventors can cool each battery cell in normal use in which relatively low temperature heat is generated, while suppressing heat propagation between the battery cells in an abnormal state in which high temperature heat is generated. We have been diligently studying to provide heat-absorbing sheets for assembled batteries.

その結果、脱水温度が異なる物質を2種以上含有するとともに、該物質のうち少なくとも1種は、前記電池セルの通常使用時において脱水可能であり、該物質のうち少なくとも1種は、前記電池セルの異常時において脱水可能である吸熱シートを、組電池に配置された各電池セル間に介在させることにより、上記課題を解決できることを見出した。 As a result, two or more substances having different dehydration temperatures are contained, and at least one of the substances can be dehydrated during normal use of the battery cell, and at least one of the substances is the battery cell. It has been found that the above-mentioned problems can be solved by interposing a heat-absorbing sheet that can be dehydrated in the event of an abnormality between the battery cells arranged in the assembled battery.

すなわち、電池セルの温度が比較的低い通常使用時において脱水可能な物質を含有することにより、電池セルの温度が比較的低温で上昇した場合に、当該物質が水分を放出するため、通常使用時における電池セルを効果的に冷却することができる。 That is, by containing a substance that can be dehydrated during normal use when the temperature of the battery cell is relatively low, the substance releases water when the temperature of the battery cell rises at a relatively low temperature, so that during normal use The battery cell in the above can be effectively cooled.

また、通常使用時における電池セルの温度範囲は、一般的に、常温(20℃程度)から最大150℃程度までであるため、通常使用時において脱水可能な物質として、150℃以下の温度で脱水可能な脱水剤を用いることが好ましいことも見出した。 Further, since the temperature range of the battery cell during normal use is generally from room temperature (about 20 ° C) to a maximum of about 150 ° C, dehydration is performed at a temperature of 150 ° C or lower as a substance that can be dehydrated during normal use. It has also been found that it is preferable to use a possible dehydrating agent.

一方、電池セルの温度が高温となる異常時において脱水可能な物質を含有することにより、電池セルの温度が異常に上昇した場合に、当該物質が水分を放出するため、異常時における各電池セル間の熱の伝播を抑制することができる。 On the other hand, by containing a substance that can be dehydrated when the temperature of the battery cell becomes high abnormally, when the temperature of the battery cell rises abnormally, the substance releases water, so that each battery cell at the time of abnormality is released. The heat transfer between them can be suppressed.

また、異常時における電池セルの温度範囲は、一般的に200℃以上であるため、異常時において脱水可能な物質として、熱分解開始温度が200℃以上の無機水和物を用いることが好ましいことも見出した。 Further, since the temperature range of the battery cell at the time of abnormality is generally 200 ° C. or higher, it is preferable to use an inorganic hydrate having a thermal decomposition start temperature of 200 ° C. or higher as a substance that can be dehydrated at the time of abnormality. I also found.

なお、通常使用時における電池セルの冷却を行うために、発生した熱を外部に逃がすための空間を電池セル間に設けたり、また、異常時における各電池セル間の熱の伝播を抑制するための空間を電池セル間に設けたりするものではないため、電池セル間の距離を極端に大きく取る必要がない。このため、吸熱シート全体の厚さを薄くすること(例えば、5mm以下)も可能となり、結果として、組電池の安全性や電池セルの十分な充放電性能を確保しつつ、組電池の体積エネルギー密度の向上を図ることも可能となる。 In addition, in order to cool the battery cells during normal use, a space for releasing the generated heat to the outside is provided between the battery cells, and in order to suppress heat propagation between the battery cells in an abnormal situation. Since the space is not provided between the battery cells, it is not necessary to take an extremely large distance between the battery cells. Therefore, it is possible to reduce the thickness of the entire heat absorbing sheet (for example, 5 mm or less), and as a result, the volume energy of the assembled battery is ensured while ensuring the safety of the assembled battery and sufficient charge / discharge performance of the battery cell. It is also possible to improve the density.

以下、本発明の実施形態(本実施形態)について、図面を参照しつつ詳細に説明する。なお、以下において「~」とは、その下限の値以上、その上限の値以下であることを意味する。 Hereinafter, embodiments of the present invention (the present embodiment) will be described in detail with reference to the drawings. In the following, "to" means that the value is equal to or more than the lower limit value and is equal to or less than the upper limit value.

(第1の実施形態)
まず、本発明の第1の実施形態に係る組電池用吸熱シートについて説明する。第1の実施形態は、当該吸熱シートが単層の場合である。
<組電池用吸熱シートの基本構成>
図1は、第1の実施形態に係る組電池用吸熱シート10の構成例を模式的に示す断面図である。本実施形態に係る組電池用吸熱シート10は、150℃以下の温度で脱水可能な脱水剤22、および熱分解開始温度が200℃以上の無機水和物24を含有する。
(First Embodiment)
First, the endothermic sheet for an assembled battery according to the first embodiment of the present invention will be described. The first embodiment is a case where the endothermic sheet is a single layer.
<Basic configuration of endothermic sheet for assembled batteries>
FIG. 1 is a cross-sectional view schematically showing a configuration example of the endothermic sheet 10 for an assembled battery according to the first embodiment. The endothermic sheet 10 for an assembled battery according to the present embodiment contains a dehydrating agent 22 that can be dehydrated at a temperature of 150 ° C. or lower, and an inorganic hydrate 24 having a thermal decomposition start temperature of 200 ° C. or higher.

本実施形態に係る組電池用吸熱シートは、通常使用時における電池セル20の温度範囲である、常温(20℃程度)から最大150℃程度までの温度範囲内で脱水可能な脱水剤22を有する。そして、電池セル20としての通常使用時である充放電サイクルを行うに際し、電池セル20の温度が比較的低温で上昇した場合に、脱水剤22が水分を放出するため、通常使用時における電池セル20を効果的に冷却することができる。 The endothermic sheet for an assembled battery according to the present embodiment has a dehydrating agent 22 that can be dehydrated within a temperature range from normal temperature (about 20 ° C.) to a maximum of about 150 ° C., which is the temperature range of the battery cell 20 during normal use. .. Then, when the charge / discharge cycle during normal use as the battery cell 20 is performed, when the temperature of the battery cell 20 rises at a relatively low temperature, the dehydrating agent 22 releases water, so that the battery cell during normal use 20 can be effectively cooled.

また、本実施形態に係る組電池用吸熱シートは、異常時における電池セル20の温度範囲である200℃以上の温度範囲内において、熱分解開始温度を有する無機水和物24を有する。そして、電池セル20としての異常時である熱暴走が生じ、電池セル20の温度が異常に上昇した場合において、無機水和物24の分解による吸熱反応が生ずるため、異常時における各電池セル20間の熱の伝播を効果的に抑制することができる。 Further, the endothermic sheet for an assembled battery according to the present embodiment has an inorganic hydrate 24 having a thermal decomposition start temperature within a temperature range of 200 ° C. or higher, which is the temperature range of the battery cell 20 at the time of abnormality. Then, when thermal runaway occurs as the battery cell 20 abnormally and the temperature of the battery cell 20 rises abnormally, an endothermic reaction occurs due to the decomposition of the inorganic hydrate 24, so that each battery cell 20 at the time of abnormality occurs. The heat transfer between them can be effectively suppressed.

この組電池用吸熱シート10の具体的な使用形態としては、図5に示すように、複数の電池セル20が、組電池用吸熱シート10を介して配置され、複数の電池セル20同士が直接または並列に接続された状態(接続された状態は図示を省略)で、電池ケース30に格納されて組電池100が構成される。なお、電池セル20は、例えば、リチウムイオン二次電池が好適に用いられるが、特にこれに限定されず、その他の二次電池にも適用され得る。 As a specific usage pattern of the endothermic sheet 10 for assembled batteries, as shown in FIG. 5, a plurality of battery cells 20 are arranged via the endothermic sheet 10 for assembled batteries, and the plurality of battery cells 20 are directly connected to each other. Alternatively, the assembled battery 100 is configured by being stored in the battery case 30 in a state of being connected in parallel (the connected state is not shown). As the battery cell 20, for example, a lithium ion secondary battery is preferably used, but the battery cell 20 is not particularly limited to this, and can be applied to other secondary batteries.

<組電池用吸熱シートの詳細>
次に、組電池用吸熱シート10における各構成要素につき詳細に説明する。
<Details of endothermic sheet for assembled battery>
Next, each component of the endothermic sheet 10 for an assembled battery will be described in detail.

まず、組電池用吸熱シート10を構成する脱水剤22について説明する。脱水剤22は、150℃以下の温度で脱水可能である。上記脱水剤22としては、例えば、シリカゲル、活性アルミナ、活性炭、ゼオライト、イオン交換樹脂などのような水分吸着剤、あるいは、硫酸塩水和物、亜硫酸塩水和物、リン酸塩水和物、硝酸塩水和物、酢酸塩水和物、金属水和塩などが挙げられる。これらの脱水剤22は、単独で使用してもよいし、2種以上組み合わせて使用してもよい。 First, the dehydrating agent 22 constituting the endothermic sheet 10 for an assembled battery will be described. The dehydrating agent 22 can be dehydrated at a temperature of 150 ° C. or lower. Examples of the dehydrating agent 22 include water adsorbents such as silica gel, active alumina, activated charcoal, zeolite, and ion exchange resin, or sulfate hydrate, sulfite hydrate, phosphate hydrate, and nitrate hydrate. Substances, acetate hydrates, metal hydrates and the like can be mentioned. These dehydrating agents 22 may be used alone or in combination of two or more.

ここで、上記硫酸塩水和物としては、例えば、硫酸アンモニウムアルミニウム12水和物、硫酸ナトリウムアルミニウム12水和物、硫酸アルミニウム27水和物、硫酸アルミニウム18水和物、硫酸アルミニウム16水和物、硫酸アルミニウム10水和物、硫酸アルミニウム6水和物、硫酸カリウムアルミニウム12水和物、硫酸鉄7水和物、硫酸鉄9水和物、硫酸カリウム鉄12水和物、硫酸マグネシウム7水和物、硫酸ナトリウム10水和物、硫酸ニッケル6水和物、硫酸亜鉛7水和物、硫酸ベリリウム4水和物、硫酸ジルコニウム4水和物等が挙げられる。
上記亜硫酸塩水和物としては、例えば、亜硫酸亜鉛2水和物、亜硫酸ナトリウム7水和物等が挙げられる。
上記リン酸塩水和物としては、例えば、リン酸アルミニウム2水和物、リン酸コバルト8水和物、リン酸マグネシウム8水和物、リン酸マグネシウムアンモニウム6水和物、リン酸水素マグネシウム3水和物、リン酸水素マグネシウム7水和物、リン酸亜鉛4水和物、リン酸二水素亜鉛2水和物等が挙げられる。
上記硝酸塩水和物としては、例えば、硝酸アルミニウム9水和物、硝酸亜鉛6水和物、硝酸カルシウム4水和物、硝酸コバルト6水和物、硝酸ビスマス5水和物、硝酸ジルコニウム5水和物、硝酸セリウム6水和物、硝酸鉄6水和物、硝酸鉄9水和物、硝酸ニッケル6水和物、硝酸マグネシウム6水和物等が挙げられる。
上記酢酸塩水和物としては、例えば、酢酸亜鉛2水和物、酢酸コバルト4水和物等が挙げられる。
上記金属水和塩としては、例えば、塩化コバルト6水和物、塩化鉄4水和物等の塩化物塩、ホウ砂(四ホウ酸ナトリウム5水和物、四ホウ酸ナトリウム10水和物)、八ホウ酸二ナトリウム四水物、ホウ酸亜鉛3.5水和物等のホウ酸塩等が挙げられる。
Here, examples of the sulfate hydrate include ammonium aluminum sulfate dodecahydrate, sodium aluminum sulfate dodecahydrate, aluminum sulfate 27 hydrate, aluminum sulfate 18 hydrate, aluminum sulfate hexahydrate, and sulfuric acid. Aluminum decahydrate, aluminum sulfate hexahydrate, potassium aluminum sulfate dodecahydrate, iron sulfate heptahydrate, iron sulfate 9 hydrate, potassium iron sulfate dodecahydrate, magnesium sulfate heptahydrate, Examples thereof include sodium sulfate decahydrate, nickel sulfate hexahydrate, zinc sulfate heptahydrate, beryllium sulfate tetrahydrate, zirconium sulfate tetrahydrate and the like.
Examples of the sulfite hydrate include zinc sulfite dihydrate, sodium sulfite heptahydrate and the like.
Examples of the phosphate hydrate include aluminum phosphate dihydrate, cobalt phosphate octahydrate, magnesium phosphate octahydrate, magnesium ammonium phosphate hexahydrate, and magnesium hydrogen phosphate trihydrate. Examples thereof include Japanese products, magnesium hydrogen phosphate heptahydrate, zinc phosphate tetrahydrate, zinc dihydrogen phosphate dihydrate and the like.
Examples of the nitrate hydrate include aluminum nitrate hexahydrate, zinc nitrate hexahydrate, calcium nitrate tetrahydrate, cobalt nitrate hexahydrate, bismuth nitrate pentahydrate, and zirconium nitrate pentahydrate. Examples thereof include cerium nitrate hexahydrate, iron nitrate hexahydrate, iron nitrate 9 hydrate, nickel nitrate hexahydrate, magnesium nitrate hexahydrate and the like.
Examples of the acetate hydrate include zinc acetate dihydrate, cobalt acetate tetrahydrate and the like.
Examples of the metal hydrate include chloride salts such as cobalt chloride hexahydrate and iron chloride tetrahydrate, and hosand (sodium tetraborate pentahydrate, sodium tetraborate decahydrate). , Disodium octaborate tetrahydrate, zinc borate 3.5 hydrate and other borates and the like.

なお、例えば、150℃以下の温度範囲内における高温側(75℃~150℃)での水分吸着量が大きいゼオライトと、上記高温側での水分吸着量が小さいシリカゲルを併用すれば、温度上昇した電池セル20を広い温度領域で冷却することが可能となるため、好ましい。 For example, if zeolite having a large amount of water adsorbed on the high temperature side (75 ° C. to 150 ° C.) in the temperature range of 150 ° C. or lower and silica gel having a small amount of water adsorbed on the high temperature side are used in combination, the temperature rises. This is preferable because the battery cell 20 can be cooled in a wide temperature range.

上記脱水剤22のうち、より多くの水分を放出することができ、かつ、脱水温度範囲が広いという特性を有する観点から、特にゼオライトを用いることが好ましい。ゼオライトとしては、特に種類に限定されるものではなく、例えば、β型ゼオライト、Y型ゼオライト、フェリエライト、ZSM-5型ゼオライト、モルデナイト、フォージサイト、ゼオライトAおよびゼオライトL等が挙げられる。 Among the dehydrating agents 22, zeolite is particularly preferable from the viewpoint of being able to release more water and having a wide dehydration temperature range. The zeolite is not particularly limited in type, and examples thereof include β-type zeolite, Y-type zeolite, ferrierite, ZSM-5 type zeolite, mordenite, forgesite, zeolite A, and zeolite L.

ゼオライトは、3次元網目構造を有するアルミノケイ酸塩である。水分を吸着するゼオライトは安定的に存在するため、通常、常温条件下で3次元網目構造の隙間に水分などを吸着している。しかし、ある温度以上の熱が与えられることにより、ゼオライトに吸着されていた水分がゼオライトから脱着する。
しかし、水分を吸着していないゼオライトは不安定であるため、脱水したゼオライトは高い吸着作用を有するため、温度が低下した後は再び水分を吸着する。
Zeolites are aluminosilicates with a three-dimensional network structure. Since zeolite that adsorbs water is stably present, it usually adsorbs water or the like in the gaps of the three-dimensional network structure under normal temperature conditions. However, when heat above a certain temperature is applied, the water adsorbed on the zeolite is desorbed from the zeolite.
However, since zeolite that does not adsorb water is unstable, dehydrated zeolite has a high adsorption action, so that it adsorbs water again after the temperature drops.

例えばゼオライトのように、150℃以下の温度で脱水可能な脱水剤22は、充放電サイクルを行う場合の電池セル20表面の上昇温度と温度範囲が大きく重複しているため、通常使用時における電池セル20の温度上昇に伴い、水分を放出することで効果的に電池セル20を冷却することができる。 For example, the dehydrating agent 22 that can be dehydrated at a temperature of 150 ° C. or lower, such as zeolite, has a temperature range that greatly overlaps with the rising temperature of the surface of the battery cell 20 when the charge / discharge cycle is performed. As the temperature of the cell 20 rises, the battery cell 20 can be effectively cooled by releasing water.

また、特にゼオライトの場合には、電池セル20が冷却され、組電池用吸熱シート10内の脱水剤22の温度が低下した後は、組電池用吸熱シート10周囲の水分を再び吸着することとなるため、繰り返し行われる充放電サイクルに対して何度でも再利用することができる。 Further, particularly in the case of zeolite, after the battery cell 20 is cooled and the temperature of the dehydrating agent 22 in the endothermic sheet 10 for the assembled battery drops, the moisture around the endothermic sheet 10 for the assembled battery is adsorbed again. Therefore, it can be reused as many times as necessary for repeated charge / discharge cycles.

上記脱水剤22の配合量としては、組電池用吸熱シート10を構成する材料の合計質量に対して、好ましい上限が90質量%であり、より好ましい上限は65質量%である。
これに対し、上記脱水剤22の配合量の好ましい下限は10質量%であり、より好ましい下限は35質量%である。この配合量が10質量%未満では、十分な脱水効果が得られないおそれがある。また、この配合量が90質量%を超えると、吸熱シート10としての十分な強度を保つことができないおそれがある。
As for the blending amount of the dehydrating agent 22, the preferable upper limit is 90% by mass, and the more preferable upper limit is 65% by mass with respect to the total mass of the materials constituting the endothermic sheet 10 for assembled batteries.
On the other hand, the preferable lower limit of the blending amount of the dehydrating agent 22 is 10% by mass, and the more preferable lower limit is 35% by mass. If this blending amount is less than 10% by mass, a sufficient dehydration effect may not be obtained. Further, if this compounding amount exceeds 90% by mass, it may not be possible to maintain sufficient strength as the endothermic sheet 10.

続いて、組電池用吸熱シート10を構成する無機水和物24について説明する。無機水和物24は、熱分解開始温度が200℃以上である。
上記無機水和物24として、例えば、水酸化アルミニウム(Al(OH))、水酸化マグネシウム(Mg(OH))、水酸化カルシウム(Ca(OH))、水酸化亜鉛(Zn(OH))、水酸化鉄(Fe(OH))、水酸化マンガン(Mn(OH))、水酸化ジルコニウム(Zr(OH))、水酸化ガリウム(Ga(OH))などが挙げられる。
これらの無機水和物24は、単独で使用してもよいし、2種以上組み合わせて使用してもよい。
Subsequently, the inorganic hydrate 24 constituting the endothermic sheet 10 for the assembled battery will be described. The inorganic hydrate 24 has a thermal decomposition start temperature of 200 ° C. or higher.
Examples of the inorganic hydrate 24 include aluminum hydroxide (Al (OH) 3 ), magnesium hydroxide (Mg (OH) 2 ), calcium hydroxide (Ca (OH) 2 ), and zinc hydroxide (Zn (OH)). ) 2 ), iron hydroxide (Fe (OH) 2 ), manganese hydroxide (Mn (OH) 2 ), zinc hydroxide (Zr (OH) 2 ), gallium hydroxide (Ga (OH) 3 ), etc. Be done.
These inorganic hydrates 24 may be used alone or in combination of two or more.

なお、水酸化アルミニウムの熱分解開始温度は約200℃であり、水酸化マグネシウムの熱分解開始温度は約330℃であり、水酸化カルシウムの熱分解開始温度は約580℃であり、水酸化亜鉛の熱分解開始温度は約200℃であり、水酸化鉄の熱分解開始温度は約350℃であり、水酸化マンガンの熱分解開始温度は約300℃であり、水酸化ジルコニウムの熱分解開始温度は約300℃であり、水酸化ガリウムの熱分解開始温度は約300℃である。
このような熱分解開始温度が異なる2種以上の無機水和物24を併用すれば、温度上昇した電池セル20を広い温度領域で冷却することができ、熱暴走時の各電池セル間の熱の伝播を効果的に抑制することが可能となるため、好ましい。
The thermal decomposition start temperature of aluminum hydroxide is about 200 ° C., the thermal decomposition start temperature of magnesium hydroxide is about 330 ° C., the thermal decomposition start temperature of calcium hydroxide is about 580 ° C., and zinc hydroxide The thermal decomposition start temperature of iron hydroxide is about 200 ° C, the thermal decomposition start temperature of iron hydroxide is about 350 ° C, the thermal decomposition start temperature of manganese hydroxide is about 300 ° C, and the thermal decomposition start temperature of zirconium hydroxide. Is about 300 ° C., and the thermal decomposition start temperature of gallium hydroxide is about 300 ° C.
By using two or more kinds of inorganic hydrates 24 having different thermal decomposition start temperatures in combination, the battery cell 20 whose temperature has risen can be cooled in a wide temperature range, and the heat between the battery cells during thermal runaway can be cooled. It is preferable because it can effectively suppress the propagation of.

例えば水酸化アルミニウムの場合、水酸化アルミニウム中には約35%の結晶水を有しており、下記式に示すように、熱分解時に結晶水を放出することで、消炎機能(吸熱反応)を発揮することができる。
2Al(OH)→Al+3H
この機能により、電池セル20で発生した高温の熱を吸収することができ、電池セル20の発熱量を低減することができる。
For example, in the case of aluminum hydroxide, about 35% of water of crystallization is contained in aluminum hydroxide, and as shown in the following formula, the water of crystallization is released during thermal decomposition to provide a flame-extinguishing function (endothermic reaction). Can be demonstrated.
2Al (OH) 3 → Al 2 O 3 + 3H 2 O
With this function, the high-temperature heat generated in the battery cell 20 can be absorbed, and the calorific value of the battery cell 20 can be reduced.

例えば水酸化アルミニウムのような、熱分解温度が200℃以上である無機水和物24は、電池セル20の熱暴走が生じた場合の電池セル20表面の上昇温度と温度範囲が大きく重複しているため、異常時における電池セル20の温度上昇に伴い、熱分解により脱水反応(吸熱反応)を生ずることで、効果的に各電池セル間の熱の伝播を抑制することができる。 For example, the inorganic hydrate 24 having a thermal decomposition temperature of 200 ° C. or higher, such as aluminum hydroxide, has a large overlap in temperature range with the temperature rise on the surface of the battery cell 20 when the battery cell 20 undergoes thermal runaway. Therefore, as the temperature of the battery cell 20 rises at the time of abnormality, a dehydration reaction (heat absorption reaction) occurs due to thermal decomposition, so that heat propagation between the battery cells can be effectively suppressed.

特に水酸化アルミニウムの場合には、上記無機水和物24の中で熱分解開始温度が低め(熱分解開始温度:約200℃)であるため、電池セルの異常時の初期段階(比較的低めの温度)から、電池セル20の冷却を行うことができるため、好ましい。 In particular, in the case of aluminum hydroxide, the thermal decomposition start temperature is lower (thermal decomposition start temperature: about 200 ° C.) in the inorganic hydrate 24, so that it is in the initial stage (relatively lower) when the battery cell is abnormal. The battery cell 20 can be cooled from the above temperature), which is preferable.

上記無機水和物24の配合量としては、組電池用吸熱シート10を構成する材料の合計質量に対して、好ましい上限が90質量%であり、より好ましい上限は65質量%である。
これに対し、上記脱水剤22の配合量の好ましい下限は10質量%であり、より好ましい下限は35質量%である。この配合量が10質量%未満では、十分な脱水効果が得られないおそれがある。また、この配合量が90質量%を超えると、吸熱シート10としての十分な強度を保つことができないおそれがある。
As for the blending amount of the inorganic hydrate 24, a preferable upper limit is 90% by mass, and a more preferable upper limit is 65% by mass with respect to the total mass of the materials constituting the endothermic sheet 10 for assembled batteries.
On the other hand, the preferable lower limit of the blending amount of the dehydrating agent 22 is 10% by mass, and the more preferable lower limit is 35% by mass. If this blending amount is less than 10% by mass, a sufficient dehydration effect may not be obtained. Further, if this compounding amount exceeds 90% by mass, it may not be possible to maintain sufficient strength as the endothermic sheet 10.

なお、上記組電池用吸熱シート10は、成形時の強度向上を目的として、無機繊維やパルプ繊維を含んでいてもよい。 The endothermic sheet 10 for an assembled battery may contain inorganic fibers or pulp fibers for the purpose of improving the strength at the time of molding.

上記無機繊維としては、例えば、シリカ-アルミナ繊維、アルミナ繊維、シリカ繊維、ロックウール、アルカリアースシリケート繊維、ガラス繊維、ジルコニア繊維およびチタン酸カリウムウィスカ繊維などが挙げられる。これらの無機繊維は、耐熱性、強度、入手容易性などの点で好ましい。上記無機繊維は、単独で使用してもよいし2種以上組み合わせて使用してもよい。上記無機繊維のうち、取り扱い性の観点から、特にシリカ-アルミナ繊維、アルミナ繊維、シリカ繊維、ロックウール、アルカリアースシリケート繊維、ガラス繊維が好ましい。 Examples of the inorganic fiber include silica-alumina fiber, alumina fiber, silica fiber, rock wool, alkaline earth silicate fiber, glass fiber, zirconia fiber and potassium titanate whisker fiber. These inorganic fibers are preferable in terms of heat resistance, strength, availability, and the like. The above-mentioned inorganic fibers may be used alone or in combination of two or more. Among the above-mentioned inorganic fibers, silica-alumina fiber, alumina fiber, silica fiber, rock wool, alkaline earth silicate fiber, and glass fiber are particularly preferable from the viewpoint of handleability.

上記無機繊維の断面形状は、特に限定されず、円形断面、扁平断面、中空断面、多角断面、芯鞘断面などが挙げられる。中でも、中空断面、扁平断面または多角断面を有する異形断面繊維は、断熱性が若干向上されるため好適に使用することができる。 The cross-sectional shape of the inorganic fiber is not particularly limited, and examples thereof include a circular cross section, a flat cross section, a hollow cross section, a polygonal cross section, and a core sheath cross section. Among them, the modified cross-section fiber having a hollow cross-section, a flat cross-section or a polygonal cross-section can be preferably used because the heat insulating property is slightly improved.

上記無機繊維の平均繊維長の好ましい下限は0.1mmであり、より好ましい下限は0.5mmである。一方、上記無機繊維の平均繊維長の好ましい上限は50mmであり、より好ましい上限は10mmである。上記無機繊維の平均繊維長が0.1mm未満であると、無機繊維同士の絡み合いが生じにくく、得られる吸熱シート10の機械的強度が低下するおそれがある。一方、50mmを超えると、補強効果は得られるものの無機繊維同士が緊密に絡み合うことができなったり、単一の無機繊維だけで丸まったりし、それにより連続した空隙が生じやすくなるので断熱性の低下を招くおそれがある。 The preferable lower limit of the average fiber length of the inorganic fiber is 0.1 mm, and the more preferable lower limit is 0.5 mm. On the other hand, the preferable upper limit of the average fiber length of the inorganic fiber is 50 mm, and the more preferable upper limit is 10 mm. If the average fiber length of the inorganic fibers is less than 0.1 mm, the inorganic fibers are less likely to be entangled with each other, and the mechanical strength of the obtained endothermic sheet 10 may decrease. On the other hand, if it exceeds 50 mm, although the reinforcing effect can be obtained, the inorganic fibers cannot be closely entangled with each other, or the inorganic fibers are curled up by only a single inorganic fiber, which tends to generate continuous voids, so that the heat insulating property is improved. May cause deterioration.

上記無機繊維の平均繊維径の好ましい下限は1μmであり、より好ましい下限は2μmであり、更に好ましい下限は3μmである。一方、上記無機繊維の平均繊維径の好ましい上限は10μmであり、より好ましい上限は7μmである。上記無機繊維の平均繊維径が1μm未満であると、無機繊維自体の機械的強度が低下するおそれがある。また、人体の健康に対する影響の観点より、上記無機繊維の平均繊維径が3μm以上であるが好ましい。一方、上記無機繊維の平均繊維径が10μmより大きいと、無機繊維を媒体とする固体伝熱が増加して断熱性の低下を招くおそれがあり、また、吸熱シート10の成形性が悪化するおそれがある。 The preferable lower limit of the average fiber diameter of the inorganic fiber is 1 μm, the more preferable lower limit is 2 μm, and the further preferable lower limit is 3 μm. On the other hand, the preferable upper limit of the average fiber diameter of the inorganic fiber is 10 μm, and the more preferable upper limit is 7 μm. If the average fiber diameter of the inorganic fiber is less than 1 μm, the mechanical strength of the inorganic fiber itself may decrease. Further, from the viewpoint of the influence on the health of the human body, the average fiber diameter of the inorganic fibers is preferably 3 μm or more. On the other hand, if the average fiber diameter of the inorganic fiber is larger than 10 μm, solid heat transfer using the inorganic fiber as a medium may increase and the heat insulating property may be deteriorated, and the moldability of the heat absorbing sheet 10 may be deteriorated. There is.

この無機繊維やパルプ繊維は、吸熱シート10を構成する材料の合計重量に対して、10~70質量%の範囲で必要に応じて使用することができる。 The inorganic fiber or pulp fiber can be used as needed in the range of 10 to 70% by mass with respect to the total weight of the materials constituting the endothermic sheet 10.

吸熱シート10を構成する材料として、有機バインダーを必要に応じて使用してもよい。この有機バインダーは、成形時の強度向上を目的とする上で有用であり、例えば高分子凝集剤やアクリルエマルジョンなどを好適に使用することができる。
上記有機バインダーの配合量としては、吸熱シート10を構成する材料の合計重量に対して0.5~5.0質量%の範囲で必要に応じて使用することができる。
As a material constituting the endothermic sheet 10, an organic binder may be used as needed. This organic binder is useful for the purpose of improving the strength at the time of molding, and for example, a polymer flocculant, an acrylic emulsion, or the like can be preferably used.
As the blending amount of the organic binder, it can be used as needed in the range of 0.5 to 5.0% by mass with respect to the total weight of the materials constituting the endothermic sheet 10.

上記吸熱シート10の厚さとしては特に限定されないが、0.05~5mmの範囲にあることが好ましい。吸熱シート10の厚さが0.05mm未満であると、充分な機械的強度を吸熱シート10に付与することができない。一方、吸熱シート10の厚さが5mmを超えると、吸熱シート10の成形自体が困難となるおそれがある。 The thickness of the endothermic sheet 10 is not particularly limited, but is preferably in the range of 0.05 to 5 mm. If the thickness of the endothermic sheet 10 is less than 0.05 mm, sufficient mechanical strength cannot be imparted to the endothermic sheet 10. On the other hand, if the thickness of the endothermic sheet 10 exceeds 5 mm, the molding of the endothermic sheet 10 itself may become difficult.

なお、吸熱シート10に用いられる脱水剤22と無機水和物24の具体的な組み合わせとしては、上記脱水剤22の中で比較的高温(100℃~150℃程度)においても水分吸着量が高めのゼオライトと、上記無機水和物24の中で熱分解開始温度が低めの水酸化アルミニウム(熱分解開始温度:約200℃)の組み合わせが好ましい。
これは、電池セル20における通常使用時の温度範囲と、異常時の温度範囲との境界温度域(150℃~200℃程度)においても、有効に電池セル20の冷却を行うことができるため、好ましい。
As a specific combination of the dehydrating agent 22 and the inorganic hydrate 24 used in the heat absorbing sheet 10, the amount of water adsorbed is high even at a relatively high temperature (about 100 ° C. to 150 ° C.) in the dehydrating agent 22. The above zeolite and aluminum hydroxide (thermal decomposition start temperature: about 200 ° C.) having a lower thermal decomposition start temperature among the inorganic hydrates 24 are preferable.
This is because the battery cell 20 can be effectively cooled even in the boundary temperature range (about 150 ° C. to 200 ° C.) between the temperature range during normal use and the temperature range at the time of abnormality in the battery cell 20. preferable.

ところで、図1においては、脱水剤22と無機水和物24とが均一に分散している例を示しているが、図2に示すように、吸熱シート10における厚み方向(図中の上下方向)中心部から両端部に向かうほど、通常使用時において脱水可能な物質、すなわち脱水剤22の含有量が大きく、かつ、吸熱シート10における厚み方向両端部から中心部に向かうほど、異常時において脱水可能な物質、すなわち無機水和物24の含有量が大きいことが好ましい。
その理由として、図5に示すように、吸熱シート10の両端部はそれぞれ電池セル20に近接しているため、電池セル20の通常使用時において効率よく電池セル20を冷却する必要がある。このため、通常使用時に効果を十分に発揮することのできる脱水剤22は、吸熱シート10内においてより多く両端部側に存在していることが好ましい。
By the way, in FIG. 1, an example in which the dehydrating agent 22 and the inorganic hydrate 24 are uniformly dispersed is shown, but as shown in FIG. 2, the thickness direction of the heat absorbing sheet 10 (the vertical direction in the figure). ) The more from the center to both ends, the larger the content of the substance that can be dehydrated in normal use, that is, the dehydrating agent 22, and the more toward the center from both ends in the thickness direction of the heat absorbing sheet 10, the more dehydrated in an abnormal situation. It is preferable that the content of a possible substance, that is, the inorganic hydrate 24 is large.
The reason is that, as shown in FIG. 5, since both ends of the endothermic sheet 10 are close to the battery cell 20, it is necessary to efficiently cool the battery cell 20 during normal use of the battery cell 20. Therefore, it is preferable that more dehydrating agents 22 that can sufficiently exert their effects during normal use are present on both ends in the endothermic sheet 10.

一方、図5に示すように、吸熱シート10の厚み方向両端側にはそれぞれ電池セル20が存在しており、電池セル20の異常時においては、いずれの電池セル20からも熱暴走が生ずる可能性がある。よって、電池セル20から生ずる熱暴走による、各電池セル20間の熱の伝播を効果的に抑制するためには、異常時に効果を発揮することのできる無機水和物24は、吸熱シート10内の中心部側に多く存在していることが好ましい。 On the other hand, as shown in FIG. 5, battery cells 20 are present on both ends of the endothermic sheet 10 in the thickness direction, and in the event of an abnormality in the battery cells 20, thermal runaway may occur from any of the battery cells 20. There is sex. Therefore, in order to effectively suppress the heat propagation between the battery cells 20 due to the thermal runaway generated from the battery cells 20, the inorganic hydrate 24 capable of exerting an effect at the time of abnormality is contained in the endothermic sheet 10. It is preferable that a large amount of the battery is present on the central side of the battery.

(第2の実施形態)
続いて、本発明の第2の実施形態に係る組電池用吸熱シートについて説明する。第2の実施形態は、当該吸熱シートが複層(積層体)の場合である。
(Second embodiment)
Subsequently, the endothermic sheet for an assembled battery according to the second embodiment of the present invention will be described. The second embodiment is a case where the endothermic sheet is a multi-layer (laminated body).

図3は、第2の実施形態に係る組電池用吸熱シート10の構成例を模式的に示す断面図である。本実施形態に係る組電池用吸熱シート10は、中間層として、異常時において脱水可能な物質、すなわち無機水和物24を主成分とする第1の吸熱層14と、その両面に形成され、通常使用時において脱水可能な物質、すなわち脱水剤22を主成分とする第2の吸熱層12とを有する、3層から構成される。
なお、主成分とは最も多い成分をいい、通常は含有量として50質量%超であり、70質量%超が好ましく、90質量%超がさらに好ましい。
FIG. 3 is a cross-sectional view schematically showing a configuration example of the endothermic sheet 10 for an assembled battery according to the second embodiment. The endothermic sheet 10 for an assembled battery according to the present embodiment is formed as an intermediate layer on both sides of a first endothermic layer 14 containing a substance that can be dehydrated in an abnormal state, that is, an inorganic hydrate 24 as a main component. It is composed of three layers having a substance that can be dehydrated during normal use, that is, a second endothermic layer 12 containing a dehydrating agent 22 as a main component.
The main component means the most abundant component, and the content is usually more than 50% by mass, preferably more than 70% by mass, and more preferably more than 90% by mass.

本実施形態によれば、上述したように、吸熱シート10における厚み方向中心部から両端部に向かうほど、脱水剤22の含有量が大きく、かつ、吸熱シート10における厚み方向両端部から中心部に向かうほど、無機水和物24の含有量が大きくなる構成を容易に実現することができるため、好ましい。 According to the present embodiment, as described above, the content of the dehydrating agent 22 is larger toward both ends from the center in the thickness direction of the endothermic sheet 10, and the endothermic sheet 10 is from both ends in the thickness direction to the center. It is preferable because it is possible to easily realize a structure in which the content of the inorganic hydrate 24 increases toward the distance.

また、図3においては、第1の吸熱層14として無機水和物24のみからなり、また、第2の吸熱層12として脱水剤22のみからなる例を示しているが、例えば、図4に示すように、第1の吸熱層14および第2の吸熱層12のいずれにおいても、脱水剤22および無機水和物24が含まれるものの、第1の吸熱層14には無機水和物24が主成分として含まれ、第2の吸熱層12には脱水剤22が主成分として含まれるような形態であっても良い。 Further, FIG. 3 shows an example in which the first endothermic layer 14 is composed of only the inorganic hydrate 24 and the second endothermic layer 12 is composed of only the dehydrating agent 22. For example, FIG. 4 shows an example. As shown, although both the first endothermic layer 14 and the second endothermic layer 12 contain the dehydrating agent 22 and the inorganic hydrate 24, the first endothermic layer 14 contains the inorganic hydrate 24. It may be contained as a main component, and the second heat absorbing layer 12 may contain the dehydrating agent 22 as the main component.

(組電池用吸熱シートの製造方法)
続いて、組電池用吸熱シート10の製造方法について詳細に説明する。
(Manufacturing method of endothermic sheet for assembled battery)
Subsequently, a method for manufacturing the endothermic sheet 10 for an assembled battery will be described in detail.

本実施形態に係る吸熱シート10は、少なくとも上記脱水剤22および上記無機水和物24から構成される材料を、乾式成形法または湿式成形法により型成形して製造される。以下に、吸熱シート10をそれぞれの成形法により得る場合の製造方法について説明する。 The endothermic sheet 10 according to the present embodiment is manufactured by molding a material composed of at least the dehydrating agent 22 and the inorganic hydrate 24 by a dry molding method or a wet molding method. Hereinafter, a manufacturing method when the endothermic sheet 10 is obtained by each molding method will be described.

[乾式成形法を用いて製造する場合]
まず、乾式成形法では、脱水剤22および上記無機水和物24、更に必要に応じて無機繊維やパルプ繊維、あるいは有機バインダーを所定の割合でV型混合機などの混合機に投入する。混合機に投入された材料を充分に混合した後、所定の型内に混合物を投入し、プレスすることにより吸熱シート10を得る。プレス時には、必要に応じて加熱してもよい。
[When manufacturing using drywall]
First, in the dry molding method, the dehydrating agent 22 and the above-mentioned inorganic hydrate 24, and if necessary, inorganic fibers, pulp fibers, or organic binders are charged into a mixer such as a V-type mixer at a predetermined ratio. After the materials charged in the mixer are sufficiently mixed, the mixture is charged into a predetermined mold and pressed to obtain an endothermic sheet 10. At the time of pressing, it may be heated if necessary.

上記プレス圧は、0.98~9.80MPaの範囲であることが好ましい。プレス圧が0.98MPa未満であると、得られる吸熱シート10において、強度を保つことができずに崩れてしまうおそれがある。一方、プレス圧が9.80MPaを超えると、過度の圧縮によって加工性が低下したり、更に、かさ密度が高くなるため固体伝熱が増加し、断熱性が低下するおそれがある。 The press pressure is preferably in the range of 0.98 to 9.80 MPa. If the press pressure is less than 0.98 MPa, the obtained endothermic sheet 10 may not be able to maintain its strength and may collapse. On the other hand, if the press pressure exceeds 9.80 MPa, the workability may be lowered due to excessive compression, and the bulk density may be increased, so that the solid heat transfer may be increased and the heat insulating property may be lowered.

[湿式成形法を用いて製造する場合]
続いて、湿式成形法では、脱水剤22および上記無機水和物24、更に必要に応じて無機繊維やパルプ繊維、あるいは有機バインダーを水中で混合撹拌して充分に分散させ、その後、凝集剤を添加して、一次凝集体を得る。次に、必要に応じて有機弾性物質のエマルジョンなどを所定の範囲内で上記水中に添加した後、高分子凝集剤を添加することにより凝集体を含むスラリーを得る。
[When manufacturing using the wet molding method]
Subsequently, in the wet molding method, the dehydrating agent 22 and the above-mentioned inorganic hydrate 24, and if necessary, inorganic fibers, pulp fibers, or an organic binder are mixed and stirred in water to sufficiently disperse them, and then the flocculant is applied. Add to obtain primary agglomerates. Next, if necessary, an emulsion of an organic elastic substance or the like is added to the water within a predetermined range, and then a polymer flocculant is added to obtain a slurry containing aggregates.

次に、上記凝集体を含むスラリーを所定の型内へ投入して湿潤した吸熱シート10を得る。得られた吸熱シート10を乾燥することにより、目的の吸熱シート10が得られる。 Next, the slurry containing the agglomerates is put into a predetermined mold to obtain a wet endothermic sheet 10. By drying the obtained endothermic sheet 10, the desired endothermic sheet 10 can be obtained.

上述のように、吸熱シート10は、乾式成形法または湿式成形法のいずれによっても得られるが、一体成形の容易性や機械的強度の点から湿式成形法を用いることが好ましい。 As described above, the endothermic sheet 10 can be obtained by either a dry molding method or a wet molding method, but it is preferable to use the wet molding method from the viewpoint of ease of integral molding and mechanical strength.

なお、図2に示すような、吸熱シート10における厚み方向(図中の上下方向)中心部から両端部に向かうほど、脱水剤22の含有量が大きく、かつ、吸熱シート10における厚み方向両端部から中心部に向かうほど、無機水和物24の含有量が大きくなる吸熱シート10は、例えば、図3で示したように、無機水和物24を主成分とする第1の吸熱層14と、脱水剤22を主成分とする第2の吸熱層12を各々作製し、第1の吸熱層14の両面に第2の吸熱層12を積層することによって得ることができる。 As shown in FIG. 2, the content of the dehydrating agent 22 is larger toward both ends from the center in the endothermic sheet 10 in the thickness direction (upper and lower directions in the figure), and both ends in the endothermic sheet 10 in the thickness direction. The endothermic sheet 10 in which the content of the inorganic hydrate 24 increases toward the center is, for example, with the first endothermic layer 14 containing the inorganic hydrate 24 as a main component, as shown in FIG. It can be obtained by preparing each of the second endothermic layers 12 containing the dehydrating agent 22 as a main component and laminating the second endothermic layer 12 on both surfaces of the first endothermic layer 14.

また、図3や図4に示すような、中間層として無機水和物24を主成分とする第1の吸熱層14と、その両面に形成され、脱水剤22を主成分とする第2の吸熱層12とを有する、3層から構成される吸熱シート10は、第1の吸熱層14および第2の吸熱層12をそれぞれ上記製造方法に基づき作製した後、これらの層がウェット状態での加圧プレスや、これら部材の乾燥後に接着剤を用いて接着する方法などにより得ることができる。 Further, as shown in FIGS. 3 and 4, a first endothermic layer 14 having an inorganic hydrate 24 as a main component as an intermediate layer and a second endothermic layer 14 formed on both sides thereof and having a dehydrating agent 22 as a main component are formed. In the endothermic sheet 10 composed of three layers having the endothermic layer 12, after the first endothermic layer 14 and the second endothermic layer 12 are produced according to the above manufacturing methods, these layers are in a wet state. It can be obtained by a pressure press or a method of adhering these members with an adhesive after drying.

以下に、本実施形態に係る組電池用吸熱シートの実施例を説明するが、本発明はこれらの実施例に限定されるものではない。 Hereinafter, examples of the endothermic sheet for an assembled battery according to the present embodiment will be described, but the present invention is not limited to these examples.

<実施例1>
水酸化アルミニウム(Al(OH))粉末(平均粒径:1μm)を40質量%、ゼオライト粉末(平均粒径:7μm)を40質量%、無機繊維としてロックウールを10質量%、パルプ繊維を9質量%、高分子凝集材を1質量%加え、十分に撹拌混合してスラリーを調整した。上記スラリーを抄造して厚さ2mmの組電池用吸熱シートを得た。
なお、用いた水酸化アルミニウムの熱分解開始温度が200℃であり、ゼオライトは150℃以下の温度で脱水可能であることを確認した。
<Example 1>
Aluminum hydroxide (Al (OH) 3 ) powder (average particle size: 1 μm) is 40% by mass, zeolite powder (average particle size: 7 μm) is 40% by mass, rock wool is 10% by mass as inorganic fiber, and pulp fiber is used. 9% by mass and 1% by mass of the polymer flocculant were added, and the mixture was sufficiently stirred and mixed to prepare a slurry. The above slurry was machined to obtain an endothermic sheet for assembled batteries having a thickness of 2 mm.
It was confirmed that the thermal decomposition start temperature of the aluminum hydroxide used was 200 ° C., and the zeolite was dehydratable at a temperature of 150 ° C. or lower.

<比較例1>
アルカリアースシリケート(AES)ファイバーにより構成される厚み2mのシートを準備し、組電池用吸熱シートとした。
<Comparative Example 1>
A sheet having a thickness of 2 m composed of alkaline earth silicate (AES) fiber was prepared and used as an endothermic sheet for an assembled battery.

<比較例2>
実施例1で使用したものと同一のゼオライト粉末(平均粒径:7μm)を80質量%、無機繊維としてロックウールを10質量%、パルプ繊維を9質量%、高分子凝集材を1質量%加え、十分に撹拌混合してスラリーを調整した。上記スラリーを抄造して厚さ2mmの組電池用吸熱シートを得た。
<Comparative Example 2>
80% by mass of the same zeolite powder (average particle size: 7 μm) used in Example 1, 10% by mass of rock wool as inorganic fibers, 9% by mass of pulp fibers, and 1% by mass of polymer flocculants were added. , Sufficient stirring and mixing was performed to prepare the slurry. The above slurry was machined to obtain an endothermic sheet for assembled batteries having a thickness of 2 mm.

<参考例1>
実施例1で使用したものと同一の水酸化アルミニウム(Al(OH))粉末(平均粒径:1μm)を80質量%、無機繊維としてロックウールを10質量%、パルプ繊維を9質量%、高分子凝集材を1質量%加え、十分に撹拌混合してスラリーを調整した。上記スラリーを抄造して厚さ2mmの組電池用吸熱シートを得た。
<Reference example 1>
80% by mass of the same aluminum hydroxide (Al (OH) 3 ) powder (average particle size: 1 μm) used in Example 1, 10% by mass of rock wool as inorganic fibers, 9% by mass of pulp fibers, 1% by mass of the polymer flocculant was added, and the mixture was sufficiently stirred and mixed to prepare a slurry. The above slurry was machined to obtain an endothermic sheet for assembled batteries having a thickness of 2 mm.

実施例1、比較例1および比較例2で得られた組電池用吸熱シートの一方の面に接するように、熱源となる電池セルを模擬した金属板を配置し、更にその金属板に隣接するようにヒーターを配置した。また、金属板に熱電対を取り付けて、ヒーター温度が150℃になるように加熱し、経過時間に対する熱源となる電池セル(金属板)表面の温度変化を測定した。
実施例1、比較例1および比較例2における、経過時間に対する熱源となる電池セル表面の温度変化をプロットしたグラフを図6に示す。
A metal plate simulating a battery cell as a heat source is arranged so as to be in contact with one surface of the endothermic sheet for assembled batteries obtained in Example 1, Comparative Example 1 and Comparative Example 2, and further adjacent to the metal plate. The heater was arranged so as to. Further, a thermocouple was attached to the metal plate and heated so that the heater temperature became 150 ° C., and the temperature change on the surface of the battery cell (metal plate) serving as a heat source with respect to the elapsed time was measured.
FIG. 6 shows a graph plotting the temperature change on the surface of the battery cell as a heat source with respect to the elapsed time in Example 1, Comparative Example 1 and Comparative Example 2.

また、実施例1、比較例1、比較例2および参考例1で得られた組電池用吸熱シートの一方の面に隣接するようにヒーターを配置し、他方の面に隣接する電池セルを模擬した金属板を配置した。更に、金属板に熱電対を配して、ヒーター温度が700℃になるように加熱し、経過時間に対する隣接する電池セル(金属板)表面の温度変化を測定した。
実施例1、比較例1、比較例2および参考例1における、経過時間に対する隣接する電池セル表面の温度変化をプロットしたグラフを図7に示す。
Further, a heater is arranged so as to be adjacent to one surface of the endothermic sheet for assembled batteries obtained in Example 1, Comparative Example 1, Comparative Example 2 and Reference Example 1, and a battery cell adjacent to the other surface is simulated. The metal plate was placed. Further, a thermocouple was arranged on the metal plate and heated so that the heater temperature became 700 ° C., and the temperature change on the surface of the adjacent battery cell (metal plate) with respect to the elapsed time was measured.
FIG. 7 shows a graph plotting the temperature change of the surface of the adjacent battery cell with respect to the elapsed time in Example 1, Comparative Example 1, Comparative Example 2 and Reference Example 1.

図6の結果に示されるように、ゼオライトと水酸化アルミニウムを併用した実施例1の組電池用吸熱シートは、ゼオライトのみを使用した比較例2の吸熱シートほどは、熱源となるセル表面の最大温度を低く抑えることができなかったものの、AESを使用した比較例1の吸熱シートよりも熱源となるセル表面の最大温度を低く抑えることができた。 As shown in the results of FIG. 6, the endothermic sheet for the assembled battery of Example 1 in which zeolite and aluminum hydroxide are used in combination has the maximum endothermic surface of the cell surface as a heat source as in the endothermic sheet of Comparative Example 2 in which only zeolite is used. Although the temperature could not be kept low, the maximum temperature of the cell surface as a heat source could be kept lower than that of the endothermic sheet of Comparative Example 1 using AES.

また、図7の結果に示されるように、実施例1の吸熱シートは、比較例1や比較例2の吸熱シートに比べ、隣接するセル表面の最大温度を大幅に低く抑えることができた。なお、実施例1の吸熱シートと、水酸化アルミニウムのみを使用した参考例1の吸熱シートとを比べた場合、隣接するセル表面の最大温度はほぼ同等であった。 Further, as shown in the results of FIG. 7, the endothermic sheet of Example 1 was able to significantly reduce the maximum temperature of the adjacent cell surface as compared with the endothermic sheets of Comparative Example 1 and Comparative Example 2. When the endothermic sheet of Example 1 and the endothermic sheet of Reference Example 1 using only aluminum hydroxide were compared, the maximum temperature of the adjacent cell surface was almost the same.

以上のことから、実施例1の吸熱シートは、電池セルとしての通常使用時における電池セルの冷却を効果的に行いつつも、電池セルとしての異常時における各電池セル間の熱の伝播を効果的に抑制できることが実験的に示された。 From the above, the endothermic sheet of Example 1 effectively cools the battery cells during normal use as a battery cell, and at the same time, effectively propagates heat between the battery cells during an abnormality as a battery cell. It was experimentally shown that it can be suppressed.

10 組電池用吸熱シート
12 第2の吸熱層
14 第1の吸熱層
20 電池セル
22 脱水剤(水分吸着剤)
24 無機水和物
30 電池ケース
100 組電池
10 Endothermic sheet for batteries 12 Second heat absorbing layer 14 First heat absorbing layer 20 Battery cell 22 Dehydrating agent (moisture adsorbent)
24 Inorganic hydrate 30 Battery case 100 sets Battery

Claims (8)

複数の電池セルが吸熱シートを介して配置され、該複数の電池セルが直接または並列に接続された組電池に用いられる吸熱シートであって、
脱水温度が異なる物質を2種以上含有するとともに、該物質のうち少なくとも1種は、前記電池セルの通常使用時において脱水可能であり、該物質のうち少なくとも1種は、前記電池セルの異常時において脱水可能であり、
前記吸熱シートにおける厚み方向中心部から両端部に向かうほど、前記通常使用時において脱水可能な物質の含有量が大きく、かつ、
前記吸熱シートにおける厚み方向両端部から中心部に向かうほど、前記異常時において脱水可能な物質の含有量が大きい、組電池用吸熱シート。
A heat absorbing sheet used for an assembled battery in which a plurality of battery cells are arranged via a heat absorbing sheet and the plurality of battery cells are directly or in parallel connected.
It contains two or more substances with different dehydration temperatures, and at least one of the substances can be dehydrated during normal use of the battery cell, and at least one of the substances is at the time of abnormality of the battery cell. Can be dehydrated in
The more from the center in the thickness direction to both ends of the endothermic sheet, the greater the content of the substance that can be dehydrated during normal use, and the more
An endothermic sheet for an assembled battery in which the content of a substance that can be dehydrated in the event of an abnormality increases from both ends in the thickness direction toward the center of the endothermic sheet.
前記異常時において脱水可能な物質を主成分とする第1の吸熱層と、該第1の吸熱層の両面に形成され、前記通常使用時において脱水可能な物質を主成分とする第2の吸熱層を有する、請求項に記載の組電池用吸熱シート。 A second endothermic layer whose main component is a substance that can be dehydrated at the time of abnormality and which is formed on both sides of the first endothermic layer and whose main component is a substance that can be dehydrated during normal use. The endothermic sheet for an assembled battery according to claim 1 , which has a layer. 前記通常使用時において脱水可能な物質は、150℃以下の温度で脱水可能な脱水剤であり、前記異常時において脱水可能な物質は、熱分解開始温度が200℃以上の無機水和物である、請求項1又は2に記載の組電池用吸熱シート。 The substance that can be dehydrated during normal use is a dehydrating agent that can be dehydrated at a temperature of 150 ° C. or lower, and the substance that can be dehydrated during abnormal conditions is an inorganic hydrate having a thermal decomposition start temperature of 200 ° C. or higher. , The heat absorbing sheet for an assembled battery according to claim 1 or 2 . 前記脱水剤は、シリカゲル、活性アルミナ、活性炭、ゼオライト、イオン交換樹脂、硫酸塩水和物、亜硫酸塩水和物、リン酸塩水和物、硝酸塩水和物、酢酸塩水和物、金属水和塩からなる群のうち少なくとも1つである、請求項に記載の組電池用吸熱シート。 The dehydrating agent comprises silica gel, active alumina, activated charcoal, zeolite, ion exchange resin, sulfate hydrate, sulfite hydrate, phosphate hydrate, nitrate hydrate, acetate hydrate, and metal hydrate. The heat absorbing sheet for an assembled battery according to claim 3 , which is at least one of the groups. 前記脱水剤がゼオライトである、請求項に記載の組電池用吸熱シート。 The endothermic sheet for an assembled battery according to claim 4 , wherein the dehydrating agent is zeolite. 前記無機水和物は、水酸化アルミニウム、水酸化マグネシウム、水酸化カルシウム、水酸化亜鉛、水酸化鉄、水酸化マンガン、水酸化ジルコニウムおよび水酸化ガリウムからなる群のうち少なくとも1つである、請求項のいずれか1項に記載の組電池用吸熱シート。 The inorganic hydrate is at least one of the group consisting of aluminum hydroxide, magnesium hydroxide, calcium hydroxide, zinc hydroxide, iron hydroxide, manganese hydroxide, zirconium hydroxide and gallium hydroxide. Item 5. The heat absorbing sheet for an assembled battery according to any one of Items 3 to 5 . 前記無機水和物が水酸化アルミニウムである、請求項に記載の組電池用吸熱シート。 The endothermic sheet for an assembled battery according to claim 6 , wherein the inorganic hydrate is aluminum hydroxide. 前記複数の電池セルが、請求項1~のいずれか1項に記載の組電池用吸熱シートを介して配置され、該複数の電池セルが直列または並列に接続された組電池。 An assembled battery in which the plurality of battery cells are arranged via the endothermic sheet for assembled batteries according to any one of claims 1 to 7 , and the plurality of battery cells are connected in series or in parallel.
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