Industrial effluent (COD = 1800 mg O2/dm3) was purified by the method of catalytic wet air oxidation. Catalysts containing 0.3% wt. of Pt supported on a SiO2-TiO2 and on a carbon black composite were investigated in this process in a fixed bed reactor under T = 393 - 473 K, p = 5.0 and 8.0 Mpa, LHSV = 2 h"1. Effect of the reaction conditions on the COD decrease and catalyst's stability is discussed.
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Industrial effluent (COD = 1800 mg O2/dm3) was purified by the method of catalytic wet air oxidation. Catalysts containing 0.3% wt. of Pt supported on a SiO2-TiO2 and on a carbon black composite were investigated in this process in a fixed bed reactor under T = 393 - 473 K, p = 5.0 and 8.0 Mpa, LHSV = 2 h"1. Effect of the reaction conditions on the COD decrease and catalyst's stability is discussed.
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