Nowadays, most of
the hydrogen is obtained from fossil fuels. At
the same time, the effort and resources dedicated to the development
of sustainable hydrogen manufacturing processes are rapidly increasing
to promote the energy transition toward renewable sources. In this
direction, a potential source of hydrogen could be hydrogen sulfide,
produced as a byproduct in several processes, and in particular in
the oil extraction and refinery operations. Methane reforming using
H2S has recently attracted much interest for its economic
and environmental implications. Its conversion, in fact, provides
a viable way for the elimination of a hazardous molecule, producing
a high-added value product like hydrogen. At the same time, some of
the still open key aspects of this process are the coke deposition
due to thermal pyrolysis of methane and the process endothermicity.
In this work, the methane reforming with H2S by co-feeding
sulfur is investigated through a detailed thermodynamic analysis as
a way to alleviate the critical aspects highlighted for the process.
A parametric analysis was conducted to assess the best thermodynamic
conditions in terms of pressure, temperature, and feed composition.
Changing the sulfur, H2S, and methane feed composition
can enhance the system by improving the hydrogen production yield,
reducing the carbon and sulfur deposition, increasing the H2S removal efficiency, and reducing the necessary thermal duty.