869 Slags obtained in ferrous metallurgy may poten� tially be used as catalysts in the deep oxidation of poly� cyclic aromatic hydrocarbons from metallurgical pro� duction (1). Accordingly, it is of interest to study the catalytic properties of ferroalloy slags. In the present work, we investigate the catalytic properties of ferroalloy slags in the deep oxidation of polycyclic aromatic hydrocarbons. The output of ferroalloy slags in the Common� wealth of Independent States is more than 5 million t/yr. Slags obtained in the production of ferrochrome alloys differ in chemical and mineralogical composi� tion and in physicochemical properties. The following ferrochrome slags are formed: regular carbon slags, lowcarbon and carbonfree refining slags, and mod� eratecarbon converter slags (2, 3). Structurally, the slags consist of highrefractory spinels, forsterite, and glass saturated with spinel inclusions. The slags con� tain 2-4% chromospinelide (Mg, Fe)O ⋅ (Cr, Al)2O3; 10-15% spinel MgO ⋅ Al2O3; 15-20% forsterite 2MgO ⋅ Si 2 O 3 ; 50-55% glass; up to 1% metallic beads (Cr, Fe); and 0.7-1.0% sulfide phase FeS-CrS. The slags from silicochrome production contain a small quantity (0.3-0.5%) of chromium oxides; its basic components are oxides of silicon, aluminum, and cal� cium. Analysis of the chemical composition and physico� chemical properties of ferroalloy slags suggests that converter slags from the production of moderateand lowcarbon ferrochrome are the best for the catalysis of deep oxidation. Such slags contain the greatest quantity of catalytically active oxides: up to 70% chro� mium oxides and 2% iron oxides. In the present work, we investigate moderatecarbon ferrochrome slag from Aktyubinsk ferroalloy plant. In smelting manganese alloys, slag that is rich in manganese oxide (14.0-52.5%) is formed, as we see in the table (2, 4). Slag from the production of lowphos� phorus manganese corresponds to Technical Specifi� cations TU 14�11�85-73, and contains at least 65% manganese. Manganese slag is formed from the reduc� tion products of higher manganese oxides and fluxing additives (quartzite). The basic components of this slag are manganese oxide MnO (up to 60%), silica SiO 2 (up to 30%), alumina Al2O3 (up to 3%), calcium oxide CaO (up to 4%), and magnesium oxide MgO (up to 3%). Up to 3% K2O and Na2O are present. The melting point of the slag is around 1208°C. In smelting silicomanganese, slag containing 14-17% MnO is formed. The slag mainly consists of silicate of close� packed manganese-calciumsilicate glass of busta� mite type (CaO ⋅ MnO ⋅ 2SiO2); metal beads are present. The slag from the production of carbon and moderatecarbon ferromanganese consists mainly of oxides of manganese (40-50%), silicon (25-35%), alu� minum (0.9-3.0%), and calcium (7-23%). In mineral� ogical composition, the slags consist mainly of tephroite (2MnO ⋅ SiO 2 ) and forsterite (2MgO ⋅ SiO 2 ), with small quantities of bustamite (CaO ⋅ MnO ⋅ 2SiO 2 ). Analysis of the chemical and mineralogical com� position indicates that all the manganese slags consid� ered contain catalytically active oxides; their content is greatest in lowphosphorus manganese slag. All the slags are tested in deep catalytic oxidation.