Abstract: A system and method for mitigating the impact of ingested lithium coin cell batteries is described. A coating is provided on an exterior facing of the cell, preferably within the crimp region, which releases acid and/or other additives. These acids and/or additives are selected to neutralize hydroxide that may evolve from hydrolysis of saliva that occurs if/when the coin cell becomes lodged in the digestive tract.

Abstract: A system and method for mitigating the impact of ingested lithium coin cell batteries is described. A coating is provided on an exterior facing of the cell, preferably within the crimp region, which releases acid and/or other additives. These acids and/or additives are selected to neutralize hydroxide that may evolve from hydrolysis of saliva that occurs if/when the coin cell becomes lodged in the digestive tract.

Abstract: Electrochemical battery cells, and more particularly, to cells comprising a lithium negative electrode and an iron disulfide positive electrode. Before use in the cell, the iron disulfide has an inherent pH, or a mixture of iron disulfide and an pH raising additive compound have a calculated pH, of at least a predetermined minimum pH value. In a preferred embodiment, the pH raising additive compound comprises a Group IIA element of the Periodic Table of the Elements, or an acid scavenger or pH control agent such as an organic amine, cycloaliphatic epoxy, amino alcohol or overbased calcium sulfonate. In one embodiment, the iron disulfide particles utilized in the cell have a specific reduced average particle size range.

Abstract: A lithium/iron disulfide electrochemical battery cell with a high discharge capacity. The cell has a lithium negative electrode, an iron disulfide positive electrode and a nonaqueous electrolyte. The iron disulfide of the positive electrode has a controlled average particle size range which allows the electrochemical cells to exhibit desired properties in both low and high rate applications. In various embodiments, the iron disulfide particles are wet milled, preferably utilizing a media mill or milled utilizing a non-mechanical mill such as a jet mill, which reduces the iron disulfide particles to a desired average particle size range for incorporation into the positive electrode.