Electrical separators for batteries, especially lithium batteries, having a shutdown mechanism. A process for their production. An electrical separator is used in batteries and other systems in which electrodes have to be separated from each other while maintaining ion conductivity. Safety is very i
Electrical separators for batteries, especially lithium batteries, having a shutdown mechanism. A process for their production. An electrical separator is used in batteries and other systems in which electrodes have to be separated from each other while maintaining ion conductivity. Safety is very important in lithium batteries, since in contrast to other types of battery (Pb, NiCd, NiMeH) the solvent for the electrolyte is not water but a combustible solvent. A separator for lithium cells must possess a shutdown mechanism while not being able to melt down. This is achieved by an electrical separator having a shutdown layer which comprises particles which melt at a desired temperature, close the pores of the separator, and so stop ion flow. Since the separator also comprises a porous inorganic (ceramic) layer on a carrier, the cells cannot melt down as a result of a completely melted separator.
대표청구항▼
What is claimed is: 1. A process for producing a lithium battery separator having a shutdown function, which comprises applying particles having a defined, desired melting temperature to a porous inorganic layer of a separator and fixing said particles on said layer, wherein the porous inorganic la
What is claimed is: 1. A process for producing a lithium battery separator having a shutdown function, which comprises applying particles having a defined, desired melting temperature to a porous inorganic layer of a separator and fixing said particles on said layer, wherein the porous inorganic layer comprises a porous carrier having a porous inorganic nonelectroconductive coating layer on and in said carrier, and wherein said particles form a shutdown layer on said porous inorganic and close the pores of said inorganic layer upon melting. 2. The process according to claim 1, wherein said carrier is flexible and less than 50 μm in thickness. 3. The process according to claim 1, wherein said carrier comprises woven or non-woven polymeric or glass fibers. 4. The process according to claim 3, wherein said carrier is a polymeric nonwoven. 5. The process according to claim 4, wherein said polymeric fibers are selected from fibers of polyacrylonitrile, polyester and/or polyolefin. 6. The process according to claim 1, wherein said carrier is less than 30 μm in thickness. 7. The process according to claim 1, wherein said porous inorganic coating layer present on said carrier comprises oxide particles of the elements Al, Si and/or Zr from 0.5 to 10 μm in size on average. 8. The process according to claim 1, wherein said shutdown particles have an average size (Dw) which is greater than the average pore size (d) of said pores of said porous inorganic layer. 9. The process according to claim 1, wherein the layer of shutdown particles has a thickness (zw) which is approximately in the range from said average size of said shutdown particles (Dw) up to 10 times said particle size Dw. 10. The process according to claim 1, wherein said shutdown particles are selected from the group consisting of polymers, polymer blends, natural waxes and artificial waxes. 11. The process according to claim 1, further comprising said porous inorganic layer being hydrophobicized before said shutdown particles are applied to it. 12. The process according to claim 1, further comprising said porous inorganic layer being treated with an adhesion promoter before said shutdown particles are applied to it. 13. The process according to claim 12, further comprising said porous inorganic layer being produced by using a polymeric sol comprising a silane adhesion promoter for said shutdown particles to be applied later. 14. The process according to claim 1, further comprising said layer of shutdown particles being generated by applying a suspension of shutdown particles having an average size larger than the average pore size of the separator layer in a suspension medium selected from a sol, water or alcohols. 15. The process according to claim 14, wherein said suspension comprises an adhesion promoter. 16. The process according to claim 15, further comprising selecting said adhesion promoter from hydrolyzed or nonhydrolyzed functionalized alkyltrialkoxysilanes. 17. The process according to claim 14, further comprising said suspension being applied to said porous inorganic layer by printing on, pressing, pressing in, rolling on, knifecoating on, brushing on, dipping, squirting, spraying or pouring on. 18. The process according to claim 14, further comprising said layer being obtained by said applied suspension being dried at a temperature in the range from room temperature to 100° C. 19. The process according to claim 1, further comprising following application said particles being fixed on said porous inorganic layer by single heating to a temperature above the glass transition temperature to fuse on said particles without changing the actual shape. 20. The process according to claim 1, wherein said shutdown particles are selected from particles comprising polymers, polymer blends, natural waxes and/or artificial waxes. 21. The process according to claim 20, wherein said shutdown particles are particles composed of polyethylene wax.
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