Metallurgical plants are a significant source of atmospheric pollution, these facilities being responsible for 12-15% of the quantity of harmful substances introduced into the air. The production of steel in open-hearth (OH) furnaces, moreover, is one of the "dirtiest" metallurgical operations from an enviromnental standpoint. While the current level of OH steelmaking has maximized the productivity of OH furnaces, it has also brought an increase in the discharge of hazardous substances: dust and oxides of sulfur and nitrogen. Open-hearth shop No. 1 at the Karaganda Metallurgical Combine evaluated the dust content of the outgoing gases and their concentration of harmful substances. The study revealed the process factors responsible for the deterioration in pollution control in the shop. It turned out that the escape of gases through the charging doors and leaks in the furnace superstructure account for 5-20% of the emissions registered. Moreover, while the concentration of nitric oxide is not above the MPC (maximum permissible concentration) in every section of the shop, the concentration of sulfur dioxide ranges from 0 to25.4 mg/m 3 -- with the MPC being 10 mg/m 3. The concentration of sulfur dioxide at work stations in the shop is 13.1 mg/m 3. The highest concentration of dust (45 mg/m 3) was found in the area of the tap hole during tapping. The MPC is 4 mg/ m 3. Dust concentration on the working platform of the furnace during cold-charging reaches 13.2 mg/m 3. Uncontrolled emissions could be reduced by increasing the draft, but this would require more powerful ventilating equipment. Also, increasing the amount of cold air brought into the system increases heat losses, disturbs the slag regime, and entails the consumption of additional heat carrier. An alternative solution is to install an aerodynamic screen, hoods, and other devices to control gaseous emissions. The total amount of dust generated by OH steelmaking is reduced 7% when two-level lances are used to blow the metal. The reduced dust formation is accompanied by improved operation of the regnerators, flues, and waste-heat boiler. The level of cleaning of the flue gases (controlled emissions) depends on the efficiency of the electrostatic precipitators in the gas-cleaning system. Their efficiency ranges within 85-99%. The efficiency of the gas-cleaning system as a whole is adversely affected by an increase in the quantity of gas (gas velocity) and an increase in gas temperature at the system inlet. Factors which tend to increase dust generation are: a reduction in the bulk weight of the scrap charge; overheating of the charge before the hot-metal addition; oxygen-blowing of the metal when its carbon content is below 0.15%. These findings suggest that, from an environmental standpoint, it would be helpful to change the OH shop over to the production of killed and low-alloy steels. Unfortunately, the existing gas-cleaning systems do not ensure the removal of oxides of sulfur and nitrogen from the flue gases. Since sulfur in the charge and the fuel is one factor contributing to the formation of sulfur dioxide in the steelmaking process, emissions of SiO 2 could be reduced by using pig iron and fuel oil that are low in sulfur. The concentration of oxides of nitrogen in flue gases depends on the method used to reduce fuel consumption and the extent to which the steelmaking operation is being forced.