SI-BASED ANODES WITH CROSS-LINKED CARBON NANOTUBES
Systems and methods are provided for Si-based anodes with cross-linked carbon nanotubes. A slurry for use in anodes may be mixed, with the slurry including an anode active material and a carbon-based additive, where the slurry may be used in forming an anode. The anode active material may yield a silicon-dominant anode when the slurry is used in forming the anode, and the carbon-based additive forms a mesh-like structure in the silicon-dominant anode. The carbon-based additive includes cross-linked carbon nanotubes (CNT).
1 . An electrochemical cell comprising:
a silicon-dominant anode;
a cathode;
a separator; and
an electrolyte;
wherein the silicon-dominant anode comprises an anode active material and a carbon-based additive that forms a mesh or net structure comprising carbon fibers and/or tubes connected to each other.
2 . The electrochemical cell of claim 1 , wherein the carbon-based additive comprises cross-linked carbon nanotubes (CNTs).
3 . The electrochemical cell of claim 1 , wherein the carbon-based additive percolates and creates in the silicon-dominant anode a conductive network at low concentration, and wherein the low concentration is <1%, <0.5%, or <0.25%.
4 . The electrochemical cell of claim 1 , wherein the silicon-dominant anode has, as a result of forming of the mesh or net structure, an expansion of less than 1%, or less than 0.8%, with density higher than 1 gm/cm 3 , or higher than 1.1 g/cm 3 .
5 . The electrochemical cell of claim 1 , wherein the silicon-dominant anode has, as a result of forming of the mesh or net structure, resistance less than 5 Ω·m, less than 2 Ω·m, or less than 1.64 Ω·m.
6 . The electrochemical cell of claim 1 , wherein the silicon-dominant anode comprises a pyrolyzed carbon-based binder.
7 . The electrochemical cell of claim 6 , wherein the slurry comprises a precursor for the pyrolyzed carbon-based binder.
8 . The electrochemical cell of claim 7 , wherein the precursor for the pyrolyzed carbon-based binder is dispersed in an organic based solvent, an inorganic based solvent, or a mixture of organic and inorganic solvents.
9 . The electrochemical cell of claim 8 , wherein the organic based solvent used in the slurry comprises N-Methyl pyrrolidone (NMP) based solvent.
10 . The electrochemical cell of claim 6 , wherein the pyrolyzed carbon-based binder comprises a pyrolytic carbon derived from polyamide-imide (PAI).
11 . The electrochemical cell of claim 1 , wherein the slurry further comprises polyvinyl alcohol (PVA) solution in water.
12 . The electrochemical cell of claim 1 , wherein the slurry further comprises a surfactant.
13 . The slurry used to make electrodes of claim 1 , wherein a precursor for the carbon-based additive is dispersed in water.
14 . A method comprising:
mixing a slurry for use in anodes, the slurry comprising an anode active material and a carbon-based additive; and
forming an anode using the slurry;
wherein:
the anode active material yields a silicon-dominant anode when the slurry is used in forming the anode; and
the carbon-based additive forms a mesh or net structure in the silicon-dominant anode, the mesh or net structure comprising carbon fibers and/or tubes connected to each other.
15 . The method of claim 14 , wherein the carbon-based additive comprises cross-linked carbon nanotubes (CNT).
16 . The method of claim 14 , wherein the carbon-based additive percolates and creates in the final silicon-dominant anode a conductive network at low concentration, and wherein the low concentration is <1%, <0.5%, or <0.25%.
17 . The method of claim 14 , wherein the silicon-dominant anode has, as a result of forming of the mesh or net structure, an expansion of less than 1%, or less than 0.8%, with density higher than 1 gm/cm 3 , or higher than 1.1 g/cm 3 .
18 . The method of claim 14 , wherein the silicon-dominant anode has, as a result of forming of the mesh or net structure, resistance less than 2 Ω·m, or less than 1.64 Ω·m.
19 . The method of claim 14 , comprising forming the silicon-dominant anode using a direct coating process of the slurry on a current collector to provide a coated anode.
20 . The method of claim 19 , further comprising calendaring the coated anode.
21 . The method of claim 20 , further comprising calendaring the coated anode at 70° C.
22 . The method of claim 21 , further comprising pyrolyzing the coated anode at >500° C., 5° C./min ramp, and 60-120 min dwell time under Argon (Ar) atmosphere.
23 . The method of claim 21 , further comprising pyrolyzing the coated anode at >500° C., 5° C./min ramp, and 60-120 min dwell time under Ar/H 2 forming gas.
24 . The method of claim 21 , further comprising pyrolyzing the coated anode at >500° C., 5° C./min ramp, and 120-180 min dwell time under N 2 nitrogen gas.
25 . The method of claim 21 , further comprising pyrolyzing the coated anode at >500° C., 5° C./min ramp, and 120-180 min dwell time under Argon (Ar) atmosphere.