Battery Research Group Secondary Li Battery Technology for Next Generation Nov. 30, 2006 Hyun-Soo Kim Battery Research Group Korea Electrotechonology Research Institute - 4th CEPRI-CRIEPI-KERI Technical Meeting-
Battery Research Group Merits of Lithium-Ion Battery High energy density No memory effect High operation voltage Environment-friendly
Battery Research Group Application of Lithium-Ion Battery motor scooter Electric wheel chair HEV Electric bicycle Golf cart Mobile IT appliance
Battery Research Group Market of Secondary Battery Growth rate (%) Ni/MH ▽ 0.4 LIB8861,0841,2241,4571,7302,0512,4352, LIPB * Yano Report 2004 Lithium-Ion battery Lithium-ion polymer battery Ni/MH battery ,000 2,000 1, Million Cell
Battery Research Group R&D Trends of Secondary Battery ,400 Spec. Power Density (W/kg) Spec. Energy Density (Wh/kg) Lead Acid Ni/Cd Ni/MH Lithium-Ion Battery High Power LIB High Energy LIB Mobile IT HEV Next Generation Battery ?
Battery Research Group Cathode Materials for Lithium-Ion Battery LiCoO2LiNiO2LiMn2O4 Li[Co⅓Ni⅓ Mn⅓]O 2 LiNi½Mn½ O 2 LiFePO4LiMnO2 StructureLayered SpinelLayered OlivineLayered Theoretical Capacity 274mAh/g275mAh/g148mAh/g285mAh/g 170mAh/g344mAh/g Practical Capacity 140mAh/g180mAh/g120mAh/g170mAh/g 150mAh/g 180mAh/g 4.4-3V: V:90 Operation Voltage 3.6V3.5V3.8V3.6V 3.45V3.4V Merits High electric conductivity, easy preparation High capacity Low cost, nontoxic High capacity & thermal stability, low cost High capacity Low cost, thermal stability Low cost, nontoxic Demerits High cost, toxicity Hard preparation, Low thermal stability Mn dissolution Low tap density Low electric conductivity Hard preparation, Mn dissolution
Battery Research Group Synthesis of Li[Ni 1/3 Mn 1/3 Co 1/3 ] (1-x) Zr x O 2 Li, Ni, Mn, Co Nitrates in Ethanol (stoichiometric) ZrOCl 2 hydrate (Zirconyl Chloride) Drying (80 ℃ ) ‘Mud’ of Chemical Compounds ㆍ 450 ℃, 3hr : Calcination ㆍ Grinding ㆍ 650 ℃, 5hr : Melt Li salts ㆍ 950 ℃, 5hr : Oxide Structure Stirring for 0.5 hr Heat Treatment
Battery Research Group XRD Patterns of Li[Ni 1/3 Mn 1/3 Co 1/3 ] (1-x) Zr x O 2 No impurity phase up to about 4.0 at% Zr doping Zirconia-like impurity was formed over than about 5.0 at% Zr doping
Battery Research Group Morphologies of Li[Ni 1/3 Mn 1/3 Co 1/3 ] (1-x) Zr x O 2 Primary particle : ~ 300 nm After heat-treatment, the particles agglomerated to form a secondary particle with ~5 ㎛.
Battery Research Group Rate Capability of Li[Ni 1/3 Mn 1/3 Co 1/3 ] (1-x) Zr x O 2 Current Rate Un-dopedZr-doped Capacity (mAh/g) Ratio (%) Capacity (mAh/g) Ratio (%) 0.2C C C C
Battery Research Group Cycle Performance of Li[Ni 1/3 Mn 1/3 Co 1/3 ] (1-x) Zr x O 2 Un-dopied material; (84.2%) Zr-doped material; (97.6%) Cycle performance of the Zr-doped material : 13% up (after 50 th cycle).
Battery Research Group Lattice Parameter of Li[Ni 1/3 Mn 1/3 Co 1/3 ] (1-x) Zr x O 2 A-axis decreased slightly with Zr-doping. C-axis increased remarkably with Zr-doping and it caused to enhanced rate-capability.
Battery Research Group Inter-slab Space Model In the LiNiO2 system the dramatic deterioration of electrochemical performances is strongly related to the change in oxidation state of the extra nickel ions, which induces local collapses of the structure and hinders not only lithium diffusion in the inter-slab space but also lithium reintercalation in the six sites around each extra nickel ion. In the LiNiMgO2 system, the magnesium ions, with a size very close to that of lithium, remain in the divalent state during cell charge. Therefore, their presence in the inter-slab space does not strongly affect lithium reintercalation because no shrinkage of the structure appears upon cycling. The size of Mg2+ and Zr4+ is similar to Li+ ion and this result explains why the Zr-substituted phases have good cycling properties. Li x Ni 1+z O 2 systemLi x Ni 1-y Mg y O 2 system (Source; C. Delmas et al., J. Electrochem. Soc., 147 (2000) p. 2061)
Battery Research Group LiNi 1/3 Mn 1/3 Co 1/3 O 2 C 9 H 21 AlO 3 Heat treatments Preheating at 130 ℃ for 10h O 2 Sintering at 700 ℃ for 5h in O 2 Measurement of Electrochemical Properties Cell : Al 2 O 3 -coated LiNi 1/3 Mn 1/3 Co 1/3 O 2 /Li cell. Separator : Polypropylene (15 ㎛ ). Electrolyte : 1.15M LiPF 6 EC/EMC/DEC=3/5/2. Cycle-life : 1C rate, 4.5~2.8V, 50cycle. Rate capability : 0.2C, 0.5C, 1C, 2C. Temperature : room temperature. Cell : Al 2 O 3 -coated LiNi 1/3 Mn 1/3 Co 1/3 O 2 /Li cell. Separator : Polypropylene (15 ㎛ ). Electrolyte : 1.15M LiPF 6 EC/EMC/DEC=3/5/2. Cycle-life : 1C rate, 4.5~2.8V, 50cycle. Rate capability : 0.2C, 0.5C, 1C, 2C. Temperature : room temperature. Al 2 O 3 coating by a Sol-gel method Surface Treatments of LiNi 1/3 Mn1/3Co1/3O 2 High purity ethanol-stirred for 1h at 50 ℃
Battery Research Group XRD Patterns of Al 2 O 3 -coated LiNi 1/3 Co 1/3 Mn 1/3 O Intensity (A.U.) Al 2 O 3 coated (003) (113) (110) (018) (107) (015) (104) (012) (006) (101) LiNi 1/3 Co 1/3 Mn 1/3 O 2
Battery Research Group (b) Al 2 O 3 coated(a) LiNi 1/3 Co 1/3 Mn 1/3 O 2 Morphologies of Al 2 O 3 -coated LiNi 1/3 Co 1/3 Mn 1/3 O 2
Battery Research Group Rate Capability of Al 2 O 3 -coated LiNi 1/3 Co 1/3 Mn 1/3 O 2
Battery Research Group Cycle Performances of Al 2 O 3 -coated LiNi 1/3 Co 1/3 Mn 1/3 O 2 Al 3+ diffuse and formed for a thin layer of Li-Al-O solid solution phase during the heat treatment and the charging/discharging process. This reaction layer has not only high Li-ion conductivity but also stabilize the layered structure. The lattice parameters might be slightly changed during the charging/discharging process. [1] A. Bibby and L. Mercier, Chem. Mater., 14, 1594 (2002).[2] J. Cho, Y.J. Kim, and B. Park, Chem. Mater., 12, 3788 (2000).
Battery Research Group Nyquist plot of Al 2 O 3 -coated LiNi 1/3 Co 1/3 Mn 1/3 O 2
Battery Research Group DSC Profiles of Al 2 O 3 -coated LiNi 1/3 Co 1/3 Mn 1/3 O 2
Battery Research Group Crosslink-Type Gel Polymer Electrolyte Separator Electrode Heat Cure Filling of Precursor Whole Gelation Precursor Heat Cure(Gelation) Electrolyte Filling Core Cell
Battery Research Group Manufacturing Process of Polymer Battery CathodePE/PP SeparatorAnode (+)/(-) tab Al Pouch Electrolyte + Monomer + Initiator Winding/Stacking Vacuum Sealing Formation Aging Precursor Filling Vacuum Drying Core cell Insertion Ultrasonic Welding Curing ALB 25 ℃, 3days 80 ℃, 1hr
Battery Research Group Electrode Coating Process Mixer Press Slitter Coater Mixer Press Slitter Coater Mixing Coating Pressing Slitting Mixing Coating Pressing Slitting
Battery Research Group Winding & Precursor Filling Process Winding J/R Pressing Pouch Forming Precursor Filling
Battery Research Group Sealing & Formation Process Sealing Pouch Folding Formation & Grading
Battery Research Group Manufacture of Gel Polymer Electrolyte Battery (GPB) Electrode Formulation ; Cathode : LiCoO 2 + ECP-04 + PVDF (95.65 : 1.5 : 2.85 wt%) Anode : Graphite + ECP-04 + PVDF (90 : 2 : 8 wt%) Separator ; Polypropylene (Asahi) Thick. 20 ㎛, Porosity 40%, permeability 85~92 sec/100cc Electrolyte, Monomer & Initiator ; Electrolyte : 1.1M LiPF 6 /EC+PC+DMC+EMC+DEC (30/10/10/30/20 wt%) Monomer : Polyurethane acrylate (PUA), Polyoxyalkylene glycol acrylate (POGA, Elexcel TA-140, Daiichi Kogyo Seiyaku 사 ) Initiator : Bis-(4-tert-butylcyclohexyl)peroxy-dicarbonate (BBP)
Battery Research Group Cell Design of GPEB Design of GPEB Design Capacity ; 800 mAh Electrode Size ; 4.6x5.05 mm (Cathode), 4.6x5.2 mm (Anode) Electrolyte ; 3ml/Cell (3.4g per 1000mAh) Aging ; 40 ℃, 2days Specification of Electrode CathodeAnode Thick Thickness 134 ㎛ 163 ㎛ Loading density 3.22 g/cm g/cm mg/cm mg/cm 2 Thin Thickness 127 ㎛ 143 ㎛ Loading density 3.07 g/cm g/cm 3 35 mg/cm 2 18 mg/cm 2
Battery Research Group Rate Capability of PUA-based GPEB Polymerization condition 60 ℃, 90min Charge/discharge 0.2C, 0.5C, 1.0C and 2.0C Discharge capacity 0.2C ; 1969 mAh 0.5C ; 1952 mAh (99.1%) 1.0C ; 1928 mAh (98.0%) 2.0C ; 1896 mAh (96.3%) Polymerization condition 60 ℃, 90min Charge/discharge 0.2C, 0.5C, 1.0C and 2.0C Discharge capacity 0.2C ; 1969 mAh 0.5C ; 1952 mAh (99.1%) 1.0C ; 1928 mAh (98.0%) 2.0C ; 1896 mAh (96.3%)
Battery Research Group Temper. Dependences of PUA-based GPEB Polymerization ; 60 ℃, 90min Charge/discharge 20, 0, -10, -20 ℃ 0.5C/0.5C 유지시간 ; 20 h Discharge capacity 20 ℃ ; 1969 mAh (100%) 0 ℃ ; 1952 mAh (98.9%) -10 ℃ ; 1928 mAh (95.6%) -20 ℃ ; 1775 mAh (91.2%) Polymerization ; 60 ℃, 90min Charge/discharge 20, 0, -10, -20 ℃ 0.5C/0.5C 유지시간 ; 20 h Discharge capacity 20 ℃ ; 1969 mAh (100%) 0 ℃ ; 1952 mAh (98.9%) -10 ℃ ; 1928 mAh (95.6%) -20 ℃ ; 1775 mAh (91.2%)
Battery Research Group Cycle Performances of PUA-based GPEB Polymerization Conditon 60 ℃, 90min Charge/discharge 0.5C/0.5C, 4.2/3.0V, 20 ℃ Discharge capacity 1st; 1960 mAh 200th; 1753 mAh (90.5%) Polymerization Conditon 60 ℃, 90min Charge/discharge 0.5C/0.5C, 4.2/3.0V, 20 ℃ Discharge capacity 1st; 1960 mAh 200th; 1753 mAh (90.5%)
Battery Research Group Overcharge Test for PUA-based GPEB Volt. & Tem. Profile After test Test procedure Charge 2.5 times of the capacity at a constant current of 1C rate for the full-charged cell Charge at a CV over 12V. Requirements No fire and no explosion Test Result PASS
Battery Research Group Crush Test for PUA-based GPEB Test procedure (IEC ) Apply force approximately 13 kN for 1 min on the cell. Both the wide and narrow sides are tested. (20±5 ℃ ) Requirements No fire and no explosion Test Result PASS Before test After side crush test After crush test
Battery Research Group Nail Penetration Test for PUA-based GPEB Test procedure Penetrate on the center of the full-charged cell using nail with a diameter of 5 mm. Requirements No fire and no explosion Max Temp. <100 ℃ Test Result PASS After test
Battery Research Group Thermal Exposure Test for PUA-based GPEB Test procedure The full-charged cell was kept at a oven maintained at 130±2 ℃ for 30 min. Requirements No fire and no explosion Test Result PASS After test
Battery Research Group Thank you for your attention !