JP7392151B2 - 二次電池、当該二次電池を含む電池モジュール、電池パック及び装置 - Google Patents
二次電池、当該二次電池を含む電池モジュール、電池パック及び装置 Download PDFInfo
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- JP7392151B2 JP7392151B2 JP2022532691A JP2022532691A JP7392151B2 JP 7392151 B2 JP7392151 B2 JP 7392151B2 JP 2022532691 A JP2022532691 A JP 2022532691A JP 2022532691 A JP2022532691 A JP 2022532691A JP 7392151 B2 JP7392151 B2 JP 7392151B2
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- negative electrode
- active material
- electrode active
- secondary battery
- artificial graphite
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Description
二次電池であって、正極シート及び負極シートを含み、
前記正極シートは正極集電体及び前記正極集電体の少なくとも一つの表面に設置され且つ正極活性材料を含む正極フィルムシートを含み、前記正極活性材料は層状のリチウム遷移金属酸化物及びその改質化合物のうちの一種又は複数種を含み、
前記負極シートは負極集電体と前記負極集電体の少なくとも一つの表面に設置され且つ負極活性材料を含む負極フィルムシートを含み、前記負極活性材料が第1の材料及び第2の材料を含み、
前記第1の材料は人造黒鉛を含み、前記第2の材料は天然黒鉛を含み、
前記人造黒鉛は一次粒子及び二次粒子を同時に含み、且つ前記負極活性材料における前記二次粒子の数量割合Sは10%≦S≦50%を満たす、二次電池を提供する。
(1)非針状石油コークスを原料とし、原料を粉砕して微粉を除去し、原料を反応釜に入れて加熱し、且つ整形して微粉を除去し、中間品1を得て、中間品1を高温で黒鉛化し、中間品2を得て、中間品2を混合機で混合し、篩分けした後、人造黒鉛Aを得る工程と、
(2)生針状石油コークスを原料とし、原料を粉砕して微粉を除去し、高温で黒鉛化して篩分けし、人造黒鉛Bを得る工程と、
(3)前記人造黒鉛Aと前記人造黒鉛Bを混合して人造黒鉛を得る工程と、
(4)鱗片の黒鉛原料を選択し、原料を破砕し、球状化処理を行い、中間体1を得て、中間体1を化学的に精製し、中間体2を得て、中間体2を乾燥し、アスファルトと混合した後に炭化処理を行い、篩分けした後、天然黒鉛を得る工程と、
(5)前記人造黒鉛と前記天然黒鉛を混合して、負極活性材料を得て、前記負極活性材料が人造黒鉛及び天然黒鉛を含み、前記人造黒鉛が同時に一次粒子及び二次粒子を含み、且つ前記前記負極活性材料における二次粒子の数量割合Sが10%≦S≦50%を満たす工程と、を含む、二次電池の製造方法を提供する。
二次電池
[負極シート]
3.0μmであってもよい。負極活性材料の体積分布粒径Dv90は、以下に記載の数値のうちのいずれか二つを端値として構成される数値範囲内あってもよい。上記数値は、16.0μm、20.0μm、25.0μm、26.0μm、30.0μm、32.0μm、33.0μmである。例えば、負極活性材料の体積分布粒径Dv90は、16.0μm~25.0μm、20.0μm~25.0μm、25.0μm~32.0μm、26.0μm~30.0μmであってもよい。
[正極シート]
一、人造黒鉛の製造
1、人造黒鉛Aの製造
2、人造黒鉛Bの製造
3、人造黒鉛の製造
二、天然黒鉛の製造
三、負極活性材料の調製
[電解質]
[セパレータ]
装置
実施例
実施例1
正極シートの作製
負極シートの作製
セパレータ
電解液の調製
二次電池の作製
実施例2~7、15~27及び比較例1~2
実施例8
正極シートの作製
負極シートの作製
セパレータ
電解液の調製
二次電池の作製
実施例9~14、28~40及び比較例3~4
測定内容
(1)電池の動力学性能測定
(2)電池の高温サイクル性能の測定
(3)電池のサイクル膨張率の測定
Claims (27)
- 正極シート及び負極シートを含み、
前記正極シートは正極集電体及び前記正極集電体の少なくとも一つの表面に設置され且つ正極活性材料を含む正極フィルムシートを含み、
前記正極活性材料は層状のリチウム遷移金属酸化物又はその改質化合物のうちの一種又は複数種を含み、
前記負極シートは負極集電体及び前記負極集電体の少なくとも一つの表面に設置され且つ負極活性材料を含む負極フィルムシートを含む二次電池の製造方法であって、
(1)非針状石油コークスを原料とし、原料を粉砕し且つ微粉を除去し、原料を反応釜に入れて加熱し、且つ整形して微粉を除去し、中間品1を得て、中間品1を高温黒鉛化して、中間品2を得て、中間品2を混合機で混合し、篩分けした後に人造黒鉛Aを得る工程と、
(2)生針状石油コークスを原料とし、原料を粉砕し且つ微粉を除去し、高温黒鉛化して篩分けし、人造黒鉛Bを得る工程と、
(3)前記人造黒鉛Aと前記人造黒鉛Bを混合して人造黒鉛を得る工程と、
(4)鱗片の黒鉛原料を選択し、原料を破砕し、球状化処理を行い、中間体1を得て、中間体1を化学的に精製し、中間体2を得て、中間体2を乾燥し、アスファルトと混合した後に炭化処理を行い、篩分けした後、天然黒鉛を得る工程と、
(5)前記人造黒鉛と前記天然黒鉛を混合して、負極活性材料を得る工程と、を採用して前記負極活性材料を製造し、
前記負極活性材料は人造黒鉛及び天然黒鉛を含み、前記人造黒鉛は同時に一次粒子及び二次粒子を含み、且つ前記負極活性材料における前記二次粒子の数量割合Sは10%≦S≦50%を満たす、二次電池の製造方法。 - 前記Sが、10%≦S≦30%である、請求項1に記載の二次電池の製造方法。
- 前記Sが、15%≦S≦30%である、請求項2に記載の二次電池の製造方法。
- 前記負極活性材料の体積平均粒径Dv50は≦14.0μmである、請求項1~3のいずれか一項に記載の二次電池の製造方法。
- 前記負極活性材料の体積平均粒径D v 50は8.0μm~12.0μmである、請求項4に記載の二次電池の製造方法。
- 前記負極活性材料の体積平均粒径D v 50は12.0μm~14.0μmである、請求項1又は4に記載の二次電池の製造方法。
- 前記人造黒鉛の体積平均粒径Dv50は10.0μm~14.5μmであり、及び/又は、
前記天然黒鉛の体積平均粒径Dv50は7.0μm~14.0μmである、請求項1~6のいずれか一項に記載の二次電池の製造方法。 - 前記人造黒鉛の体積平均粒径D v 50は11.0μm~13.5μmであり、及び/又は、
前記天然黒鉛の体積平均粒径D v 50は7.0μm~13.0μmである、請求項7に記載の二次電池の製造方法。 - 前記負極活性材料の体積分布粒径Dv90は16.0μm~25.0μmであり、及び/又は、
前記人造黒鉛の体積分布粒径Dv90は23.0μm~30.0μmであり、及び/又は、
前記天然黒鉛の体積分布粒径Dv90は15.0μm~23.0μmである、請求項1~8のいずれか一項に記載の二次電池の製造方法。 - 前記負極活性材料の体積分布粒径D v 90は20.0μm~25.0μmであり、及び/又は、
前記人造黒鉛の体積分布粒径D v 90は25.0μm~29.0μmであり、及び/又は、
前記天然黒鉛の体積分布粒径D v 90は18.0μm~21.0μmである、請求項9に記載の二次電池の製造方法。 - 前記負極活性材料の体積分布粒径Dv99は25.0μm~37.0μmであり、及び/又は、
前記人造黒鉛の体積分布粒径Dv99は30.0μm~45.0μmであり、及び/又は、
前記天然黒鉛の体積分布粒径Dv99は21.0μm~35.0μmである、請求項1~10のいずれか一項に記載の二次電池の製造方法。 - 前記負極活性材料の体積分布粒径D v 99は33.0μm~36.5μmであり、及び/又は、
前記人造黒鉛の体積分布粒径D v 99は32.0μm~43.0μmであり、及び/又は、
前記天然黒鉛の体積分布粒径D v 99は25.0μm~30.0μmである、請求項11に記載の二次電池の製造方法。 - 前記負極活性材料の粒度分布(Dv90-Dv10)/Dv50は1.30~1.55であり、及び/又は、
前記人造黒鉛の粒度分布(Dv90-Dv10)/Dv50は1.25~1.95であり、及び/又は、
前記天然黒鉛の粒度分布(Dv90-Dv10)/Dv50は0.88~1.28である、請求項1~12のいずれか一項に記載の二次電池の製造方法。 - 前記負極活性材料の粒度分布(D v 90-D v 10)/D v 50は1.35~1.50であり、及び/又は、
前記人造黒鉛の粒度分布(D v 90-D v 10)/D v 50は1.35~1.80であり、及び/又は、
前記天然黒鉛の粒度分布(D v 90-D v 10)/D v 50は0.98~1.18である、請求項13に記載の二次電池の製造方法。 - 前記二次粒子の前記人造黒鉛における数量割合は、25%~60%である、請求項1~14のいずれか一項に記載の二次電池の製造方法。
- 前記二次粒子の前記人造黒鉛における数量割合は、30%~50%である、請求項15に記載の二次電池の製造方法。
- 前記負極活性材料のタップ密度は1.10g/cm3 以上であり、及び/又は、
前記人造黒鉛のタップ密度は0.90g/cm3~1.20g/cm3であり、及び/又は、
前記天然黒鉛のタップ密度は0.90g/cm3~1.18g/cm3である、請求項1~16のいずれか一項に記載の二次電池の製造方法。 - 前記負極活性材料のタップ密度は1.10g/cm 3 ~1.15g/cm 3 であり、及び/又は、
前記人造黒鉛のタップ密度は1.05g/cm 3 ~1.15g/cm 3 であり、及び/又は、
前記天然黒鉛のタップ密度は0.93g/cm 3 ~1.13g/cm 3 である、請求項17に記載の二次電池の製造方法。 - 前記負極活性材料の黒鉛化度は92%~96%であり、及び/又は、
前記人造黒鉛の黒鉛化度は90%~95%であり、及び/又は、
前記天然黒鉛の黒鉛化度は95%~98%である、請求項1~18のいずれか一項に記載の二次電池の製造方法。 - 前記負極活性材料の黒鉛化度は93%~95%であり、
及び/又は、
前記人造黒鉛の黒鉛化度は93%~95%であり、及び/又は、
前記天然黒鉛の黒鉛化度は95%~97%である、請求項19に記載の二次電池の製造方法。 - 前記天然黒鉛の表面は被覆層を有する、請求項1~20のいずれか一項に記載の二次電池の製造方法。
- 前記負極活性材料における前記天然黒鉛の質量割合は30%以下である、請求項1~21のいずれか一項に記載の二次電池の製造方法。
- 前記負極活性材料における前記天然黒鉛の質量割合は15%~25%である、請求項22に記載の二次電池の製造方法。
- 前記負極フィルムシートの圧縮密度は1.60g/cm3~1.80g/cm3であり、及び/又は、
前記負極フィルムシートの面密度は10.0mg/cm2~13.0mg/cm2であり、及び/又は、
前記負極フィルムシートの凝集力Fは220N/m≦F≦300N/mを満たす、請求項1~23のいずれか一項に記載の二次電池の製造方法。 - 前記負極フィルムシートの圧縮密度は1.65g/cm 3 ~1.75g/cm 3 であり、及び/又は、
前記負極フィルムシートの面密度は10.5mg/cm 2 ~11.5mg/cm 2 であり、及び/又は、
前記負極フィルムシートの凝集力Fは240N/m≦F≦260N/mを満たす、請求項24に記載の二次電池の製造方法。 - 前記正極活性材料は一般式がLiaNibCocMdM’eOfAgである層状のリチウム遷移金属酸化物を含み、0.8≦a≦1.2、0.6≦b<1、0<c<1、0<d<1、0≦e≦0.1、1≦f≦2、0≦g≦1、MはMn及びAlから選択される一種又は複数種であり、M’はZr、Mn、Al、Zn、Cu、Cr、Mg、Fe、V、Ti及びBから選択される一種又は複数種であり、AはN、F、S及びClから選択される一種又は複数種である、請求項1~25のいずれか一項に記載の二次電池の製造方法。
- 0.65≦b<1である、請求項26に記載の二次電池の製造方法。
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