Recycling method for electrolyte in waste power lithium ion battery
A technology of lithium ion battery and recovery method, which is applied to the field of electrolyte recovery in waste power lithium ion battery, can solve the problems of small collection amount, difficult collection, inaccurate analysis and research, etc., and achieves the effect of high recovery efficiency and simple process
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Embodiment 1
[0019] In order to achieve the above object, the technical scheme adopted in the present invention is as follows:
[0020] A method for recovering electrolyte in a waste power lithium-ion battery, comprising the steps of:
[0021] (1) Cut the waste power lithium-ion battery under the protection of nitrogen, remove the casing, take out the battery cell, and cut the battery cell. The cutting size of the battery cell is 5-15mm;
[0022] (2) adding dichloroethane to the cell fragments obtained after cutting for leaching, adding dichloroethane: cell fragments according to the ratio of 100ml:50g, soaking and stirring for 3 hours, and then negative pressure suction filtration to obtain the leachate;
[0023] (3) Atmospheric distillation of the leaching solution at 50° C., cooling and reflux to obtain dichloromethane;
[0024] (4) Carry out vacuum distillation and separation of the remaining liquid after reflux at 1000 Pa and 80° C. to obtain the organic solvent of the electrolyte an...
Embodiment 2
[0026] In order to achieve the above object, the technical scheme adopted in the present invention is as follows:
[0027] A method for recovering electrolyte in a waste power lithium-ion battery, comprising the steps of:
[0028] (1) Cut the waste power lithium-ion battery under the protection of nitrogen, remove the casing, take out the battery cell, and cut the battery cell. The cutting size of the battery cell is 5-15mm;
[0029] (2) adding dichloroethane to the cell fragments obtained after cutting for leaching, adding dichloroethane: cell fragments according to the ratio of 80ml:45g, soaking and stirring for 3 hours, and then negative pressure suction filtration to obtain the leachate;
[0030] (3) Distill the leaching solution under normal pressure at 35° C., cool and reflux to obtain dichloromethane;
[0031] (4) Carry out vacuum distillation and separation of the remaining liquid after reflux at 1000 Pa and 80° C. to obtain the organic solvent of the electrolyte and ...
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Abstract
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