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Deactivation of the Pd-Ag-Al2O3 catalyst and Ag-Al2O3 chemisorbent at joint operation in the process of selective acetylene hydrogenation

  • Catalysis in Chemical and Petrochemical Industry
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Abstract

The deactivation of the commercial Al-Pd catalyst promoted with silver and Ag-containing chemisorbent in selective acetylene hydrogenation in an ethane-ethylene mixture was studied. It was found that carbonaceous deposits are formed on dispersed silver particles of the Pd-Ag-Al2O3 catalyst and on large silver crystallites of the Ag-Al2O3 chemisorbent. The lightest rapidly burning hydrocarbons of composition CH2.5m with a low degree of aromaticity are sorbed on the silver particles or in the nearest neighborhood of them. Slowly burning hydrocarbons of composition CH1.5–1.8m with high a degree of aromaticity are fixed on the alumina support. It was suggested to replace the Pd-Ag-Al2O3 catalyst currently used at the Nizhnekamskneftekhim plant in the process of selective acetylene hydrogenation by a system with a lower content of silver or without it.

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Original Russian Text © S.P. Egorova, A.A. Lamberov, L.R. Galimzyanova, M.V. Nazarov, V.M. Shatilov, Kh.Kh. Gil’manov, 2009, published in Kataliz v Promyshlennosti.

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Egorova, S.P., Lamberov, A.A., Galimzyanova, L.R. et al. Deactivation of the Pd-Ag-Al2O3 catalyst and Ag-Al2O3 chemisorbent at joint operation in the process of selective acetylene hydrogenation. Catal. Ind. 1, 102–110 (2009). https://doi.org/10.1134/S2070050409020020

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  • DOI: https://doi.org/10.1134/S2070050409020020

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