Stanisław Murgrabia, Robert Cherbański, Eugeniusz Molga, Andrzej Stankiewicz, Tomasz Kotkowski
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引用次数: 0
Abstract
Methane pyrolysis (MP) is an attractive method for producing H2 without emitting CO2. However, the widespread adoption of MP is hindered by catalyst coking, which leads to catalyst deactivation. To extend catalyst lifespan, periodic regeneration is required. Based on thermodynamic calculations, CO2 was selected as the gasifying agent, as gasification with H2O can lead to CO2 emissions through a secondary water-gas shift reaction. The experiments were performed in a thermogravimetric analyser coupled with a micro GC. The chemical reaction was examined within a temperature range of 880–960 °C, and CO2 partial pressures between 851 Pa and 4412 Pa. The volume reaction model was applied to model coke gasification. Based on statistical analysis of the results, a reaction order was found to be n = 1.04±0.102, which aligns with the value reported in the literature. The activation energy was determined to be approximately 183 kJ/mol.
期刊介绍:
Chemical Engineering and Processing: Process Intensification is intended for practicing researchers in industry and academia, working in the field of Process Engineering and related to the subject of Process Intensification.Articles published in the Journal demonstrate how novel discoveries, developments and theories in the field of Process Engineering and in particular Process Intensification may be used for analysis and design of innovative equipment and processing methods with substantially improved sustainability, efficiency and environmental performance.