Negative electrodes for electrochemical cells
US-2020036002-A1 · Jan 30, 2020 · US
US2024063398A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2024063398-A1 |
| Application number | US-202318451458-A |
| Country | US |
| Kind code | A1 |
| Filing date | Aug 17, 2023 |
| Priority date | Aug 17, 2022 |
| Publication date | Feb 22, 2024 |
| Grant date | — |
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According to one aspect, an additive for an iron negative electrode of an alkaline electrochemical cell may include a powder of discrete granules including agglomerated particles, the agglomerated particles including at least one metal sulfide.
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What is claimed is: 1 . An additive for an iron negative electrode of an alkaline electrochemical cell, the additive comprising: a powder of discrete granules including agglomerated particles, the agglomerated particles including at least one metal sulfide. 2 . The additive of claim 1 , wherein the at least one metal sulfide of the agglomerated particles is greater than 50 wt % of the discrete granules. 3 . The additive of claim 1 , wherein the discrete granules have a mean particle size of greater than about 30 microns and less than about 800 microns on a weight percentage basis. 4 . The additive of claim 1 , wherein the discrete granules of the agglomerated particles of the at least one metal sulfide have a median pore size of greater than about 75 nanometers and less than about 15 microns as determined by mercury intrusion porosimetry. 5 . The additive of claim 1 , wherein the discrete granules have a first average apparent density, the particles including the at least one metal sulfide have a second average apparent density, and the first average apparent density is less than the second average apparent density. 6 . The additive of claim 1 , wherein the discrete granules have a friability of less than about 10% weight loss according to European Pharmacopoeia 2.9.41.-2 (Method B). 7 . The additive of claim 1 , wherein solid-state bonding holds at least some of the agglomerated particles together in the discrete granules possess solid state bonding between the agglomerated particles. 8 . The additive of claim 1 , wherein the discrete granules include a binder, and at least some of the agglomerated particles of the discrete granules are bonded by the binder. 9 . The additive of claim 1 , wherein the at least one metal sulfide includes zinc sulfide (ZnS). 10 . The additive of claim 9 , wherein the powder of the discrete granules is greater than or equal to 90% by weight zinc sulfide (ZnS). 11 . The additive of claim 1 , wherein the agglomerated particles of the discrete granules have surface-connected porosity. 12 . An iron negative electrode for an alkaline electrochemical cell, the iron negative electrode comprising: a first powder including an iron active material; and a second powder including the additive of claim 1 , the first powder and the second powder forming a powder blend in which the second powder is dispersed relative to the first powder. 13 . A method of making an additive for an iron negative electrode of an alkaline electrochemical cell, the method comprising: forming a feedstock including a particulate material having a predetermined composition; and processing the feedstock including the particulate material into a powder of discrete granules including agglomerated particles of the particulate material, the agglomerated particles including at least one metal sulfide. 14 . The method of claim 13 , wherein processing the feedstock of the particulate material includes solid-state bonding of the particulate material. 15 . The method of claim 13 , wherein forming the feedstock includes introducing at least one polymeric binder to the particulate material. 16 . The method of claim 15 , wherein processing the feedstock into the discrete granules includes pyrolyzing the at least one polymeric binder to form a graphitized film on the particulate material. 17 . The method of claim 16 , wherein, with the at least one polymeric binder introduced to the particulate material, the particulate material is thermomechanically bonded in a processing atmosphere including hydrogen gas. 18 . The method of claim 17 , wherein forming the feedstock of the particulate material includes mixing at least two metal sulfides together in a predetermined weight ratio relative to one another. 19 . The method of claim 18 , wherein the at least two metal sulfides include zinc sulfide (ZnS) and iron sulfide (FeS). 20 . The method of claim 13 , wherein the particulate material includes particles of the at least one metal sulfide includes particles of zinc sulfide (ZnS).
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