Abstract
The CO-selective methanation process is considered as a promising CO removal process for compact fuel processors producing hydrogen, since the process selectively converts the trace of CO in the hydrogen-rich gas into methane without additional reactants. Two different types of efficient nickel-based catalysts, showing high activity and selectivity to the CO methanation reaction, were developed in our previous works; therefore, the kinetic models of the reactions over these nickel-based catalysts have been investigated adopting the mechanistic kinetic models based on the Langmuir chemisorption theory. In the methanation process, the product species can react with the reactant and also affect the adsorption/desorption of the molecules at the active sites. Thus, the kinetic parameter study should be carried out by global optimization handling all the rate equations for the plausible reactions at once. To estimate the kinetic parameters, an effective optimization algorithm combining both heuristic and deterministic methods is used due to the large solution space and the nonlinearity of the objective function. As a result, 14 kinetic parameters for each catalyst have been determined and the parameter sets for the catalysts have been compared to understand the catalytic characteristics.
Highlights
There has been growing interest in generating electric energy from hydrogen due to serious concerns about climate change brought about by greenhouse gases
We have investigated the kinetics of the reactions in the CO-SELMET process over the two different types of nickel-based catalysts suggested in our previous research studies for comparison: (1) the iridium-doped nickel catalyst [5] and (2) the nickel-zirconium composite catalyst [21]
The CO-SELMET process for deep CO removal from the hydrogen-rich gas produced by fuel processors deals with three competitive reactions: water–gas shift (WGS) or reverse WGS (RWGS), CO and CO2 methanation reactions, as follows: CO methanation reaction: CO + 3H2 → CH4 + H2O CO2 methanation reaction: CO2 + 4H2 → CH4 + 2H2O WGS/RWGS reactions: CO + H2O ↔ CO2 + H2
Summary
There has been growing interest in generating electric energy from hydrogen due to serious concerns about climate change brought about by greenhouse gases. The combination of a methane-steam reformer and polymer electrolyte membrane fuel cells (PEMFCs) has been considered as an effective distributed power source due to the development of compact and low-cost fuel processors and the scalability of the fuel cell system [1,2,3,4]. In this combined system, hydrogen-rich gas fed into the PEMFCs is produced via steam reforming and water–gas shift (WGS) reactions [3,4]. The CO-SELMET process can be a practical and cost-effective solution to the development of the compact fuel processor combined with low-temperature PEMFCs [5,6,7,8]
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