laboratory-scale galvanic deoxidation technology developed by earlier worke
rs has been improved, with the aim of developing a prototype pilot-scale de
oxidation unit. Each deoxidation cell consists of a one end-closed yttria-s
tabilized zirconia (YSZ) tube coated with a Ni-YSZ cermet anode on the inne
r walls. The YSZ tube is immersed, with its closed end in the metallic melt
, and an oxygen-chemical-potential gradient across the tube is established
by passing a reducing gas through the tube. The melt is then deoxidized by
short circuiting it with the anode. Through laboratory experimentation, the
nature of the anode/electrolyte interface adhesion was identified to be an
important factor in obtaining enhanced deoxidation kinetics. The kinetics
of oxygen removal from the melt was increased by an order of magnitude with
an improved anode/electrolyte interface. A pilot-scale refining unit consi
sting of 53 cells with the improved anode/electrolyte interface was manufac
tured, and a field evaluation of the galvanic deoxidation of copper was con
ducted. The deoxidation-process model was modified to include multiple deox
idation cells, which were required for the pilot-scale trials, and to analy
ze the effect of electrolyte/electrode adhesion on deoxidation kinetics. Pr
eliminary studies on process component lifetimes were conducted by investig
ating the thermal cycling, corrosion behavior of the electrolyte, and stabi
lity of the cermet anode structure. Based on the results of the field trial
and the analyses of the process component lifetime, future work needed tow
ard commercializing the technology is discussed.