Method for manufacturing secondary battery

Patent metadata

Field	Value
Publication number	US-9269988-B2
Application number	US-201114127715-A
Country	US
Kind code	B2
Filing date	Jun 20, 2011
Priority date	Jun 20, 2011
Publication date	Feb 23, 2016
Grant date	Feb 23, 2016

Abstract

A method for manufacturing a secondary battery determines the amount of the non-aqueous electrolyte to be injected into the bound cell case on the basis of an amount of air space in a positive electrode active material layer, a swelling rate of the positive electrode active material layer, an amount of air space in a negative electrode active material layer, a swelling rate of the negative electrode active material layer, an amount of air space in a separator sheet, a total surface area of an opposing surface of the positive electrode active material layer and the negative electrode active material layer, and a reference electrolyte amount per unit surface area, which is determined in accordance with a binding rate.

First claim

The invention claimed is:

1. A method for manufacturing a secondary battery, comprising:
preparing an elongated positive electrode sheet in which a positive electrode active material layer is formed on a positive electrode collector;
preparing an elongated negative electrode sheet in which a negative electrode active material layer is formed on a negative electrode collector;
forming a flattened wound electrode assembly by winding the positive electrode sheet and the negative electrode sheet between which an elongated separator sheet is interposed;
housing the wound electrode assembly in an angular cell case having two wide surfaces that correspond respectively to flattened surfaces of the wound electrode assembly;
binding the cell case by applying a load to the two opposing wide surfaces of the cell case from an outside of the cell case such that the wide surfaces approach each other; and
injecting a non-aqueous electrolyte into the bound cell case,
wherein an injection amount X [ml] of the non-aqueous electrolyte is determined on the basis of a following Equation (1):
X =( Ap×Bp )+( An×Bn )+ C +( D×E )  (1)

in Equation (1), Ap is an amount of air space [ml] in the positive electrode active material layer, and Bp is a swelling rate determined from Tp 1 /Tp 0 , where Tp 0 is a thickness of the positive electrode active material layer before the positive electrode active material layer is impregnated with the non-aqueous electrolyte and Tp 1 is a thickness of the positive electrode active material layer after the positive electrode active material layer is impregnated with the non-aqueous electrolyte,
An is an amount of air space [ml] in the negative electrode active material layer, and Bn is a swelling rate determined from Tn 1 /Tn 0 , where Tn 0 is a thickness of the negative electrode active material layer before the negative electrode active material layer is impregnated with the non-aqueous electrolyte and Tn 1 is a thickness of the negative electrode active material layer after the negative electrode active material layer is impregnated with the non-aqueous electrolyte,
C is an amount of air space [ml] in the separator sheet,
D is a total surface area [cm 2 ] of an opposing surface of the positive electrode active material layer and the negative electrode active material layer, and
E is a reference electrolyte amount [ml/cm 2 ] per unit surface area of the opposing surface, which is determined in accordance with a binding rate [%] determined from (L 0 −L 1 )/L 0 ×100, where L 0 is a distance between an inner side of the wide surface of the cell case and the flattened surface of the wound electrode assembly before the cell case is bound and L 1 is a distance between the inner side of the wide surface of the cell case and the flattened surface of the wound electrode assembly after the cell case is bound.

2. The manufacturing method according to claim 1 , wherein when the cell case is bound such that the binding rate is between 90% and 100%, a value of E is determined within a range of 0.9×10 −3 ml/cm 2 to 1.7×10 −3 ml/cm 2 .

3. The manufacturing method according to claim 1 , wherein a positive electrode sheet having a positive electrode active material layer with a active material density set such that a value of Bp is within a range of 1.02 to 1.09 is used.

4. The manufacturing method according to claim 1 , wherein a negative electrode sheet having a negative electrode active material layer with a active material density set such that a value of Bn is within a range of 1.03 to 1.09 is used.

5. The manufacturing method according to claim 1 , wherein a plurality of the cell cases each housing the wound electrode assembly are arranged such that the wide surfaces of the respective cell cases oppose each other, the plurality of cell cases are bound by applying a load to the plurality of cell cases in an arrangement direction thereof, and an amount of the non-aqueous electrolyte to be injected into each of the cell cases is determined on the basis of the binding rate of each of the cell cases.

Assignees

• Tamaki Takumi
• Takeda Kazuhisa
• Shinkai Ryuichirou
• Takenaka Hiroe
• Wakamatsu Naoki
• Sakamoto Shinya
• Toyota Motor Co Ltd

Inventors

• Tamaki Takumi
• Takeda Kazuhisa
• Shinkai Ryuichirou
• Takenaka Hiroe
• Wakamatsu Naoki
• Sakamoto Shinya

Classifications

• H01M50/609

  Arrangements or processes for filling with liquid, e.g. electrolytes · CPC title

• H01M50/209

  adapted for prismatic or rectangular cells (H01M50/216 takes precedence) · CPC title

• H01M50/264

  for cells or batteries, e.g. straps, tie rods or peripheral frames · CPC title

• Y02P70/50

  Manufacturing or production processes characterised by the final manufactured product · CPC title

• Y02E60/10

  Energy storage using batteries · CPC title