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The oxidative reforming of methane to synthesis gas on a commercial steam reforming catalyst

The oxidative reforming of methane to predominantly carbon monoxide and hydrogen was studied over a commercial steam reforming catalyst. The said reaction was performed in an integral fixed-bed reactor at temperatures between 575°C and 650°C at a total pressure of 200 kPa(a). The primary objective o...

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Bibliographic Details
Main Author: Theron, Johannes Nicolaas
Other Authors: Fletcher, Jack
Format: Thesis
Language:English
Published: Department of Chemical Engineering 2023
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