A method and apparatus for producing a purified liquid argon product in which liquid argon having oxygen impurities is produced in a cryogenic air separation plant by separating argon from oxygen within an argon column. An impure liquid argon stream, composed of part of the liquid argon, is purified in an adsorbent bed by adsorbing the oxygen impurities in an adsorbent to produce a purified liquid argon stream that constitutes the purified liquid argon product. During adsorption, the adsorbent bed is maintained at a reduced temperature with a coolant to prevent vaporization of the liquid argon. The bed is then regenerated by draining residual liquid argon from the adsorbent bed, introducing the residual liquid argon back into the air separation plant and then desorbing the oxygen impurities with a regeneration gas. After regeneration, the adsorbent bed is refilled with purified liquid argon prior to being brought back on-line.

A method and apparatus for argon recovery in which an impure argon stream is separated from air within a cryogenic air separation unit having a divided wall argon rejection/rectification column. The resulting argon stream is subsequently recovered and purified within an integrated pressure swing adsorption system to produce product grade argon.

A system and method of optimizing the production of argon in a cryogenic air separation unit using a temperature profile of a distillation column or distillation column section obtained via fiber optic temperature measurements on the exterior surface of the distillation column or the distillation column section is provided. The temperature profiles are used to determine the vertical location and/or spatial movement of the maximum argon concentration in the distillation column or the distillation column section. Distillation column operation is then adjusted such that the vertical location or spatial movement of the maximum argon concentration is aligned proximate with the location of an argon-rich draw from the distillation column.