Papers - Nonferrous Reduction Metallurgy - Direct Production of Metallic Zinc by the Electrothermic Process (Metals Technology, Feb. 1939,) (with discussion)

The American Institute of Mining, Metallurgical, and Petroleum Engineers
George F. Weaton Carleton C. Long
Organization:
The American Institute of Mining, Metallurgical, and Petroleum Engineers
Pages:
12
File Size:
603 KB
Publication Date:
Jan 1, 1943

Abstract

Two years ago the general features of the St. Joseph Lead Company's zine-smelting process were described.' At that time the discussion was limited to a description of the production of high-purity electrothermic zinc oxide. The present paper will describe the commercial production of electrothermic zinc metal. Since a fairly complete description of the plant of the Josephtowlz smelter was given in the earlier paper, the brief recapitulation given here will be limited to mention of additional equip-ment recently installed and a bare outline of the preparatory process. The raw material is zinc sulphide concentrate received from the company's mines in St. Lawrence County, New York. An average dry-weight analysis of this material is: Zn, 58.28 per cent; Pb, 0.56; insoluble, 1.6; SiO², 1.12; Fe, 6.4; CaO, 0.47; MgO, 0.27; S, 31.9; Cd, 0.1; Cu, 0.06; Mn, 0.24. Moisture content is usually about 3 per cent. Three 21-ft. 6-in. diameter, 12-hearth Nichols-Herreshoff furnaces roast the coacentrate to a calcine of average conlposition (first 10 months of 1938): Zn, 67.69 per cent; Pb, 0.06; insoluble, 1.75; SiO², 1.26; Fe, 7.24; CaO, 0.47; MgO, 0.36; S, 1.88; Cd, 0.1; Cu, 0.07'; Mn, 0.27. The sulphur dioxide gas, after passing through a waste-heat boiler, proceeds through a recently redesigned low-resistance gas-purification assembly to the contact sulphuric acid plant, of which the capacity is 200 tons of concentrates per day. The calcine is mixed with a portion of returned furnace residues and sintered on 42-in, by 44-ft. Dwight-Lloyd sintering machines, gas-fired. Wind-box gases pass through air coolers before filtering in a 1440-bag Dracco unit, and thence to stack. The Dracco fume is mixed with Cottrell dust, from roaster gas cleaning, and sent to the leach plant, where it is roasted (SO² to acid plant) and leached with sulphuric acid to recover, as end products, lead sulphate, zinc sulphate and cadmium.
Citation

APA: George F. Weaton Carleton C. Long  (1943)  Papers - Nonferrous Reduction Metallurgy - Direct Production of Metallic Zinc by the Electrothermic Process (Metals Technology, Feb. 1939,) (with discussion)

MLA: George F. Weaton Carleton C. Long Papers - Nonferrous Reduction Metallurgy - Direct Production of Metallic Zinc by the Electrothermic Process (Metals Technology, Feb. 1939,) (with discussion). The American Institute of Mining, Metallurgical, and Petroleum Engineers, 1943.

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