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•<br />

U.S. STEEL DUQUESNE WORKS<br />

HAER No. PA-115<br />

(Page 177)<br />

first stage or oxidizing period, a charge of cold scrap steel was<br />

melted down and impurities were subseguently eliminated from the<br />

bath. The second stage, or reducing period, involved creating<br />

the required alloy composition in the steel.<br />

The process began with the loading of scrap boxes on the<br />

ground floor of the stockhouse aisle. After each box was loaded<br />

and weighed, it was lifted up by an E.O.T. crane and set on one<br />

of several flat cars located on the scrap makeup floor. The line<br />

of cars were subsequently moved by a Diesel locomotive over<br />

crossover tracks to the charging floor where they were set<br />

alongside the furnaces to be charged. Each box was picked off of<br />

its respective car by the peel of the charging machine and<br />

overturned inside of the furnace through its water cooled<br />

charging door. A thin layer of light scrap was charged first,<br />

followed by heavy scrap, which was placed within or adjacent to<br />

the triangle or "delta" formed by the electrodes. Finally, light<br />

scrap was piled high around the sides of the furnace in order to<br />

protect the roof and side walls from the arc during the high<br />

power melt down period.<br />

When the charging operation was complete, the electrodes<br />

were adjusted into place and the current was turned on. Melt<br />

down usually lasted for three and one-half or four hours, after<br />

which the silicon, manganese, phosphorus, and carbon contained in<br />

the scrap was oxidized, forming a slag which floated on top of<br />

the molten metal. This part of the process lasted for about one<br />

hour. As soon as the oxidizing period was complete, the<br />

electrodes were raised and the current was shut off while the<br />

slag was manually raked off the bath by the manipulation of long<br />

stemmed wooden "rabbles" put through the charging door. During<br />

this period, the furnace was tilted backward to permit the slag<br />

to drain into a cinder pot located on the transfer car running<br />

between the splasher walls. Completion of slag removal made the<br />

heat ready for the reducing stage of the process.<br />

The reducing period began with the addition of a new slag<br />

mixture, composed of burnt lime, fluorspar, silica sand, and<br />

powered coke, to the bath. Before adding the components of the<br />

new slag mixture into the furnace, the charging machine placed<br />

their individual charging boxes into a gas fired drying oven<br />

located on the charging floor, in line with the furnaces.<br />

Powdered coke, which was added to the slag after it became fluid,<br />

supplied the carbon for the formation of calcium carbide. The<br />

presence of calcium carbide in the slag facilitated the removal<br />

of sulphur from the bath and allowed for the addition of alloys<br />

such as manganese, nickel, chromium, vanadium, and tungsten to<br />

the molten metal because it returned their reducible oxides from<br />

the slag to the bath. After a period of approximately two hours

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