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U.S. STEEL DUQUESNE WORKS<br />

HAER NO. PA-115<br />

(Page 71)<br />

number six, were also rebuilt during this period. Conforming to<br />

new ideas about the relationship between productive capacity and<br />

the design of furnace lines, the rebuild resulted in furnaces<br />

with larger hearth diameters (17'-0" for all rebuilt furnaces but<br />

number two which was lS'-O") and shorter bosh heights. When,<br />

however, it was found that the furnace rebuilding project<br />

increased annual capacity for the entire plant by only 6,600 tons<br />

over the pre-reconstruction figure of 1,035,000 tons, each of the<br />

six furnaces were relined in 1928 and 1929. The relining, which<br />

slightly increased the bosh diameter of each furnace, expanded<br />

annual capacity to 1,319,200 tons. 4<br />

Although furnace linings normally wore out every four or<br />

five years, the slack demand for iron and steel products during<br />

the depression years meant that the furnaces were hardly in use<br />

until the first half of the 1940s. Consequently, no further<br />

additions or modifications were made to the iron production and<br />

delivery facilities until after World War II when all of the<br />

furnaces were relined and ferromanganese was added to the plant's<br />

product mix at blast furnace number two in 1949. The relining<br />

resulted in larger hearth diameters for each furnace, thereby<br />

increasing annual plant capacity to 1,451,400 tons, of which<br />

105,200 tons were devoted to the production of ferromanganese.<br />

The steps involved in the production and delivery of<br />

ferromanganese necessitated significant changes to the blast<br />

furnace plant between 1949 and 1956. In the process of making<br />

these changes, many of which began as on site improvisations<br />

seeking ways to upgrade old methods, the Duquesne Works became<br />

the most modern ferromanganese production and delivery facility<br />

of the time.<br />

A common alloy of steel, ferromanganese was produced by<br />

charging four parts manganese ore to one part iron ore into the<br />

top of the blast furnace along with coke and limestone.<br />

Moreover, because of the high melting point of the manganese ore,<br />

the production of ferromanganese required twice as much coke as<br />

the production of basic iron which, in turn, considerably<br />

increased temperatures inside of the furnace. As a result, it<br />

was normal practice to put a furnace on ferromanganese production<br />

during the last year of its scheduled campaign (i.e. when its<br />

lining was about ready to give out). When the decision to<br />

produce ferromanganese at Duquesne was made, however, it was<br />

decided to abandon normal practice by adding special features to<br />

the furnaces used for this purpose. Consequently, blast furnace<br />

number two, and, in 1953, blast furnace number three, were fitted<br />

with nine extra rows of cooling plates and new water sprays<br />

inside the furnace before they were put on "ferro".

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