Abstract

The furnace is operated in both the manual and automatic regimes. The automatic system makes it possible to predict the temperature of the metal, calculate and add the slag-forming materials and deoxidizers to the furnace and ladle, and control the operation of the furnace transformer. A centrifugal fettling machine and a guniting machine, a device for feeding powdered material into the furnace, and a 3-ton-capacity charging machine are located on the shop working platfor~. The scrap preparation section (SPS), designed to process 780,000 tons of scrap a year, is equipped with a baling press with a minimum pressure of 21 MPa and three scrap shears with a cutting force of 12 MN (1200 ton-f). The capacity of these units in terms of the hourly output of 400  400  500 ~m bales is 25 tons for the shear and 20 tons for the press. A truck transports processed scrap from the section to the furnace bay in 80-m 3 cages. After the ferroalloys and slag-forming materials are crushed in a jaw crusher and screened at the warehouse, they are moved to receiving hoppers in the shop by an inclined conveyor. The materials then travel by chutes into the furnace through a hole in the roof, into the ladle during tapping, or into the degassing unit. Steel is made in the arc furnace by the single-slag method with partial deoxidation of the slag in the furnace with coke. Two steelmaking variants are alternated: with placement of the charge on a "dry" (cleaned Of slag and metal residues) furnace bottom for the first heat; with placement of the charge on a "bog" (on the slag and about I/i0 of the metal of the previous heat) for heats 2 through 12. The metallic charge is placed in the furnace in two loads (base and pile) of 60-65 and 40-55 tons, respectively. The furnace is turned on after inspection and fettling of the bottom and banks during cold-charging of the scrap on the "dry" bottom or, when necessary, guniting of the lining of the walls and panels during cold-charging of scrap onto the "bogf" The melting period is conducted with high voltages and a moderate active power of 50-55 ~# (Fig. i). Melting is speeded up by using wall-mounted oxyacetylene burners. Their operating regime is shown in Fig.

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