A kind of preparation method of multilayer coating pole piece
A multi-layer coating and pole piece technology, applied in battery electrodes, structural parts, secondary battery repair/maintenance, etc., can solve the problem of non-uniform distribution of electrochemical reaction rate, limited electron transfer speed, and capacity failure, etc. problems, to achieve the effect of increasing electron transfer speed, high energy density, and simple and easy preparation process
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Embodiment 1
[0018] Positive sheet production: Lithium iron phosphate (positive electrode active material), conductive carbon black (conductive agent), polyvinylidene fluoride (PVDF) and NMP were respectively (97.5:1.3:1.2:80), (95:2.6:2.4: 80) and (92.5:3.9:3.6:80) were evenly mixed to obtain positive electrode slurry 1, positive electrode slurry 2 and positive electrode slurry 3. In this order, the slurry was uniformly coated on the aluminum foil in turn, and the coating thickness of each slurry was ensured to be the same, and the coating speed was controlled. After drying, winding, and rolling, a positive electrode sheet with a thickness of 180 μm was obtained.
[0019] Negative sheet production: Artificial graphite (negative active material), conductive carbon black (conductive agent), SBR and deionized water were respectively mixed with (97:1:2:90), (96:1.5:2.5:90), (94 : 2.5: 3.5: 90) were evenly mixed to obtain negative electrode slurry 1, negative electrode slurry 2 and negative el...
Embodiment 2
[0021] Positive plate production: different from Example 1, lithium iron phosphate (positive active material), conductive carbon black (conductive agent), polyvinylidene fluoride (PVDF) and NMP were respectively (97.1:1.5:1.4:80), The proportions of (94.2:3:2.8:80) and (92:4.5:3.5:80) were uniformly mixed to obtain positive electrode slurry 1, positive electrode slurry 2 and positive electrode slurry 3.
[0022] The rest are the same as in Embodiment 1, and will not be repeated here.
[0023] Negative sheet production: Different from Example 1, artificial graphite (negative electrode active material), conductive carbon black (conductive agent), SBR and deionized water were prepared in (96:1.6:2.4:90), (94.6:2.4: 3:90), (93.5:3:3.5:90) were evenly mixed to obtain negative electrode slurry 1, negative electrode slurry 2 and negative electrode slurry 3.
[0024] The rest are the same as in Embodiment 1, and will not be repeated here.
Embodiment 3
[0026] Positive plate production: different from Example 1, lithium iron phosphate (positive active material), conductive carbon black (conductive agent), polyvinylidene fluoride (PVDF) and NMP were respectively (96.8:1.6:1.6:80), The proportions of (93.6:3.2:3.2:80) and (92.4:3.8:3.8:80) were uniformly mixed to obtain positive electrode slurry 1, positive electrode slurry 2 and positive electrode slurry 3.
[0027] The rest are the same as in Embodiment 1, and will not be repeated here.
[0028] Negative plate production: different from Example 1, artificial graphite (negative active material), conductive carbon black (conductive agent), SBR and deionized water were prepared in (96.2:1.8:2:90), (94.2:2.8: 3:90), (92.4:3.6:4:90) were evenly mixed to obtain negative electrode slurry 1, negative electrode slurry 2 and negative electrode slurry 3.
[0029] The rest are the same as in Embodiment 1, and will not be repeated here.
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