Stability of Sn-Pd-Kaolinite catalyst during heat treatment and nitrate reduction in continuous flow reaction.

Chemosphere

Department of Civil and Environmental Engineering, National Laboratory Astana, Nazarbayev University, 53 Kabanbay Batyr Ave., Astana, 010000, Kazakhstan. Electronic address:

Published: February 2020


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Article Abstract

In this study, a novel and highly reactive Sn-Pd catalyst supported by environmentally benign kaolinite (Sn-Pd-kaolinite) was developed and evaluated for stability for effective nitrate (NO) reduction in batch and continuous mode. Complete NO removal with fast reduction kinetics (k = 18.16 × 10 min) and 71% selectivity toward N were achieved by the Sn-Pd-kaolinite catalyst during batch reactions. During continuous tests, 100% NO removal and 80% N was achieved for 60 h. However, NO removal efficiency gradually decreased to 80% in170 h. The catalyst was then successfully regenerated in the system by increasing H flow which achieved a complete NO removal again. The metal leaching from catalyst surface was negligible (Sn 0.01% and Pd 0.006%) and the structure was stable during the continuous test, confirming that the Sn-Pd-Kaolinite catalyst had a superior reaction kinetics and operational durability.

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http://dx.doi.org/10.1016/j.chemosphere.2019.125115DOI Listing

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Stability of Sn-Pd-Kaolinite catalyst during heat treatment and nitrate reduction in continuous flow reaction.

Chemosphere

February 2020

Department of Civil and Environmental Engineering, National Laboratory Astana, Nazarbayev University, 53 Kabanbay Batyr Ave., Astana, 010000, Kazakhstan. Electronic address:

In this study, a novel and highly reactive Sn-Pd catalyst supported by environmentally benign kaolinite (Sn-Pd-kaolinite) was developed and evaluated for stability for effective nitrate (NO) reduction in batch and continuous mode. Complete NO removal with fast reduction kinetics (k = 18.16 × 10 min) and 71% selectivity toward N were achieved by the Sn-Pd-kaolinite catalyst during batch reactions.

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