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Aluminum for apparatus for ammoniacal H/sub 2/S and HCN removal

Journal Article · · Coke Chem. USSR (Engl. Transl.); (United States)
OSTI ID:5571497
In recent years, the Soviet coking industry has been turning, in the Eastern plants, towards the ammoniacal method of removing H/sub 2/S and HCN from coke-oven gas, which is already widely used in Western Europe. The ammonia-cycle method comprises H/sub 2/S and HCN absorption from the gas with ammoniacal solution, which is regenerated by distillation. One of the most important stages in the process is the regeneration of a solution containing corrosive components such as ammonia, H/sub 2/S and HCN, among others. Dependable apparatus must be fabricated in materials of the necessary corrosion resistance. When the ammonia-cycle process was first developed in the FRG during the 1950s, difficulties arose from corrosion in the distillation apparatus, which was made from cast iron. To develop the process in the USSR and select materials for the apparatus, VUKhIN issued plans for a pilot ammonia-process unit to remove H/sub 2/S and HCN from coke-oven gas at a throughput of 150 m/sup 3//h. The regeneration equipment, comprising a still, an acidification-regeneration column and a heat exchanger for incoming and stripped solutions, was fabricated in grade AMts aluminum, which is much superior in corrosion resistance and mechanical properties to pure aluminum. Corrosion tests in the equipment took place over two summer periods of 3 months each. The most corrosion resistant material for the conditions are titanium alloys VT1-1 and VT1-0, with corrosion rates measured in thousandths of 1 mm/year, followed by steels 08Kh18N10T and 10Kh17N13M2T at around 0.1 mm/year. Aluminum grades AMgo, AMts and AD-1 corrode at rates of about 0.2 to 0.4 mm/year.
OSTI ID:
5571497
Journal Information:
Coke Chem. USSR (Engl. Transl.); (United States), Journal Name: Coke Chem. USSR (Engl. Transl.); (United States) Vol. 9; ISSN COKCA
Country of Publication:
United States
Language:
English