Abstract
Decomposition of ammonia over silica-supported cobalt catalysts for Fischer–Tropsch synthesis has been studied at a pressure of 0.1 MPa, a gas hourly space velocity in the range of 1000–6000 h–1, and a temperature in the range of 400–650°C in a tubular fixed bed reactor in a flow-through mode. It was found that silica-supported cobalt catalysts for hydrocarbons synthesis via the Fischer–Tropsch protocol also exhibit high activity in ammonia decomposition. Both the activity and hydrogen performance decrease in the series: Co-Ru/SiO2 > Co-Al2O3/SiO2 > Ru/SiO2 > Co-Al2O3/SiO2(35%)/ZSM-5(30%)/Al2O3(35%). The relatively low values of effective activation energies estimated for all catalysts indicate that the reaction can proceed with high conversion at moderate temperatures.
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This study was performed within the framework of the strategic project “Scientific Innovation Cluster “Contract R&D Center”” of the Development Program at Platov South-Russian State Polytechnic University (NPI), in implementation of the program of strategic academic leadership “Priority-2030.”
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Abbreviations and notation: FTS, Fischer–Tropsch synthesis; TPR, temperature-programmed reduction; SEM, scanning electron microscopy; EDA, energy dispersive microanalysis; XRD, X-ray diffraction analysis; CSR, coherent scattering region; GSV, gas space velocity.
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Yakovenko, R.E., Krasnyakova, T.V., Saliev, A.N. et al. Ammonia Decomposition over Cobalt-Based Silica-Supported Fischer-Tropsch Synthesis Catalysts. Kinet Catal 64, 180–190 (2023). https://doi.org/10.1134/S002315842302009X
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DOI: https://doi.org/10.1134/S002315842302009X