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In this program, the values of m,n of hydrocarbons
(CmHn), steam ratio, reaction
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rate constants, the size of catalyst bed and the
size of increment are used to
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establish a set of simultaneous equations among
the following reforming, CO
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conversion and methanation reactions for each
catalyst bed increment by material
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and energy balance.
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A Paper titled "A
SIMULATION PROGRAM FOR A TUBULAR REFORMER TO
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PRODUCE HYDROGEN FROM HYDROCARBONS FOR
FUEL CELL APPLICATION" at
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Regional World Renewable Energy Congress,
April 18, 2005, JAKARTA, INDONESIA
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