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A.V. Tarasov, O.G. Yeremin (2003)
Sulfur 2003, Banff, Canada, Conference Preprints
O. Platonov (2007)
Desulfurization of coke-oven gasCoke and Chemistry, 50
P. Clark (2001)
Conversion of CS2 and COS over alumina and titania under Claus process conditions: reaction with H2O and SO2Applied Catalysis B-environmental, 31
The operation of equipment for the hydrolysis of waste gases from the desulfurization of coke-oven gas is analyzed on the basis of chromatographic data. Specifically, the data relate to the operation of such equipment in shop 2 for trapping coking byproducts at OAO Magnitogorskii Metallurgicheskii Kombinat, over a period of four years (2004–2008). The reduced efficiency of the system in the third year of operation is due to sharp deactivation of the CR-31 aluminum-oxide catalyst (La Roche Chemicals) in the R-6301 reactor on account of sulfate formation on opening the reactor. In normal operation, the life of the catalyst in the R-6301 reactor is at least 2–3 years. To restore the efficiency of hydrolysis, the catalyst in the R-6301 reactor must be completely replaced, preferably with a specialized catalyst for hydrolysis and hydrogenation.
Coke and Chemistry – Springer Journals
Published: Feb 4, 2012
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