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To study the isothermal behaviour of our catalyst at optimal temperature, we prepared five specimens calcined at different times (1, 2, 3, 4 and 5 h).
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The paper demonstrates that the kinetic behaviour of a catalyst is a key element in developing a plantwide control strategy.
The selectivity and the dynamic behaviour of the catalyst are also affected by electrochemical phenomena.
The behaviour of this catalyst in the total oxidation of n-hexane demonstrates high activity and excellent stability after 70 h on reaction stream.
Thus, neural networks have been used to model the behaviour of one catalyst under different reaction conditions for a specific reaction, i.e. n-octane isomerisation.
The behaviour of fine catalyst particles adhering to gas bubbles in aqueous media is governed by the surface hydrophobicity.
Since, the dynamic behaviour of the catalyst is very complex and the variation of the exhaust gas composition is very limited on an engine test bench, various phenomena can hardly be analysed separately on an engine test bench.
The model is used to investigate the effect of various parameters on the behaviour of the catalyst tubes and the furnace.
The flow behaviour of the catalyst in this entrained flow reactor is investigated in a cold flow model and operating conditions for plug flow were found.
However, the model can also explain the behaviour of the catalyst layer in limiting current conditions which the other two models mentioned above are unable to do.
Special attention was given to the behaviour of the catalyst under conditions changing from net oxidization to net reduction, as this is representative for realistic exhaust gas conditions.
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Justyna Jupowicz-Kozak
CEO of Professional Science Editing for Scientists @ prosciediting.com