Article ID Journal Published Year Pages File Type
1281659 International Journal of Hydrogen Energy 2013 10 Pages PDF
Abstract

•Proper electrolyte thermodynamic model for H2SO4–H2O system is tailored.•Experiments of H2SO4 decomposition process to produce 200 L/h H2 are completed.•Simulation of H2SO4 concentration is validated with experimental data.•Rigorous simulation for H2SO4 decomposer is validated with experimental data.

This work is concerned with customization of the existing electrolyte thermodynamic model for process simulation and experimental studies on the sulfuric acid decomposition process of the SI cycle, using a commercial steady state simulator. An electrolyte thermodynamic model for the sulfuric acid–water system was tailored with four candidates available in commercial software, utilizing data from Perry's Handbook. Simulation of the sulfuric acid decomposition process comprising a flash separator, distillation column and decomposer was validated with the experimental results. To facilitate the lumped-parameter steady-state model-based simulation of sulfuric acid decomposition, the decomposer was conceptually decoupled into three sections: evaporation, H2SO4 dissociation, and SO3 catalytic reduction to SO2. The process simulation results exhibited good agreement with experimental data. This work contributes to future work on simulation and experimental study of a scaled-up process system and exergy analysis for an optimal energy-efficient sulfuric acid decomposition process in the SI cycle.

Related Topics
Physical Sciences and Engineering Chemistry Electrochemistry
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