Polymer separators generally are made from microporous polymer membranes. Such membranes are typically fabricated from a variety of inorganic, organic and naturally occurring materials. Pore sizes are typically larger than 50–100 Å. Dry and wet processes are the most common separation production methods for polymeric membranes. The extrusion and stretching portions of these processes induce porosity and can serve as a means of mechanical strengthening. Membranes synthesized by dry processes are more suitable for higher power density, given their open and uniform pore structure, while those made by wet processes are offer more charge/discharge cycles because of their tortuous and interconnected pore structure. This helps to suppress the conversion of charge carriers into crystals on anodes during fast or low temperature charging.
Dry process The dry process involves extruding, annealing and stretching steps. The final porosity depends on the morphology of the precursor film and the specifics of each step. The extruding step is generally carried out at a temperature higher than the
melting point of the
polymer resin. This is because the resins are melted to shape them into a uniaxially-oriented tubular film, called a precursor film. The structure and orientation of the precursor film depends on the processing conditions and the resin's characteristics. In the
annealing process, the precursor is annealed at a temperature slightly lower than the polymer's melting point. The purpose of this step is to improve the crystalline structure. During stretching, the annealed film is deformed along the machine direction by a cold stretch followed by a hot stretch followed by relaxation. The cold stretch creates the
pore structure by stretching the film at a lower temperature with a faster strain rate. The hot stretch increases pore sizes using a higher temperature and a slower strain rate. The relaxation step reduces internal stress within the film. The dry process is only suitable for polymers with high
crystallinity. These include but are not limited to: semi-crystalline
polyolefins,
polyoxymethylene, and
isotactic poly (4-methyl-1-pentene). One can also use blends of immiscible polymers, in which at least one polymer has a crystalline structure, such as polyethylene-
polypropylene, polystyrene-polypropylene, and poly (
ethylene terephthalate) - polypropylene blends.
Dry Microstructure After processing, separators formed from the dry process possess a porous microstructure. While specific processing parameters (such as temperature and rolling speed) influence the final microstructure, generally, these separators have elongated, slit-like pores and thin fibrils that run parallel to the machine direction. These fibrils connect larger regions of semi-crystalline polymer, which run perpendicular to the machine direction.
Wet Microstructure When subjected to biaxial stretching, separators formed from the wet process have rounded pores. These pores are dispersed throughout an interconnected polymer matrix. and
siloxane grafted polyethylene separators, which show favorable surface morphology and electrochemical properties compared to conventional polyethylene separators. In addition,
polyvinylidene fluoride (PVDF)
nanofiber webs can be synthesized as a separator to improve both ion conductivity and dimensional stability. ==Placement==