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Résumé :
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There are many large scale hydrogen production units worldwide. Pure hydrogen is produced for many applications including hydrocracking processes. A comprehensive simulation of an industrial hydrogen production unit is presented with state of the art models. First, all sub-units including reformer reactor, shift converters, and methanator reactor are mathematically modeled and the amine package is simulated by using the HYSYS process simulator; then the effect of some important parameters (reformer feed pressure and temperature, steam to carbon ratio, and carbon dioxide to methane ratio) on hydrogen yield is investigated. Results show that by increasing reformer feed pressure, steam to carbon ratio, and carbon dioxide to methane ratio while decreasing reformer feed temperature, the mole fraction of hydrogen is decreased in the reformer, high temperature water gas shift reactor, low temperature water gas shift reactor, and methanator.
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