Abstract
Hydrophobic Pt CWAO-catalysts can achieve complete removal of bisphenol A from a flow of contaminated water in a trickle-bed reactor at an operating temperature of 120°C, total air pressure of 8 bar and a liquid-hourly space velocity of 26.6 h−1. Although increasing the throughput of contaminated water while lowering the operating temperature results in bisphenol A conversions below 100%, these more demanding conditions allow structurally similar catalyst formulations to be differentiated from one another. At 60°C and 8 bar total pressure of air, 2%Pt supported on a SiC-TiC composite material has the highest initial activity from a group of three hydrophobic catalysts with similar surface areas and Pt particle diameters, but it begins to deactivate progressively after 15 hours on stream. This catalyst contains some localised hydrophilicity arising from the presence of surface TiO2, which forms when the exposed TiC component of the support material oxidises during catalyst preparation. At 80 °C and ambient air pressure, the activity is lower but there are no signs of deactivation during 24 hours on stream. The results are consistent with metallic platinum providing the active sites for CWAO of bisphenol A, with oxygen being directly activated from the gas phase at elevated pressures, but with dissolved oxygen also contributing to the reaction particularly at ambient air pressure. Continuous and irreversible deactivation, which occurs at air pressures ≥4 bar, appears to be associated with high occupancy of the active sites by adsorbed oxygen, resulting in leaching of platinum into the aqueous phase.
Original language | English |
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Article number | 119637 |
Journal | Applied Catalysis A: General |
Volume | 676 |
Early online date | 23 Feb 2024 |
DOIs | |
Publication status | Published - 25 Apr 2024 |
Data Availability Statement
Data will be made available on request.Funding
Catalysts were evaluated using a CWAO trickle-bed test facility at the National Institute of Chemistry in Ljubljana, Slovenia, while catalyst preparation and characterisation were carried out at the Cardiff Catalysis Institute in Wales. Financial support was provided by the UK EPSRC (Grant No EP/L016443/1), together with Cardiff University and the Universities of Bath and Bristol, through their funding of the EPSRC Centre for Doctoral Training in Catalysis. Albin Pintar and Gregor Žerjav gratefully acknowledge financial support from the Slovenian Research and Innovation Agency (research core funding no. P2–0150).
Keywords
- Bisphenol A
- Catalytic wet air oxidation
- Hydrophobic catalyst
- Platinum on SiC supports
- Wastewater treatment
ASJC Scopus subject areas
- Catalysis
- Process Chemistry and Technology