converting operations. If excessive amounts of solids form, skimming problems or poor slag-metal separation may become problematic.During the past few decades, regulations for SO 2 and CO 2 emissions from nonferrous smelters have become more stringent. As a result, more advanced smelting technologies have been developed. Continuous copper converters are more energy efficient and more process intensive than conventional Peirce-Smith converters. In order to minimize the operating costs and down time of these units, certain operational parameters require further study. For example, copper penetration into a vessel's refractory bricks can lead to excessive erosion and increased costs. It is often desirable to operate the vessel with a small layer of frozen slag in order to protect the bricks. Excessive solid formation, however, can lead to poor slag-metal separation and a decrease in the effective volume of the unit. It is therefore important to identify which phases are present in the bath and the operating conditions that could lead to their formation/ dissolution.Currently, several continuous converters operate with a calcium ferrite slag system. Although the CaO-FeO-Fe 2 O 3 phase diagram is reasonably well known, industrial slags typically contain Cu 2 O, SO 2 , Al 2 O 3 , As 2 O 3 , As 2 O 5 , and Sb 3 O 3 as well as other impurities that can significantly affect the slag chemistry and alter the precipitation mechanisms. In the copper industry, concentrates with low levels of impurity elements are becoming increasingly difficult to locate. This has forced many smelters to treat materials with ever increasing levels of deleterious impurities. The formation of solid phases with these impurity elements (stoichiometric or solid solutions) must now be considered.