2017 Annual Meeting
(582ct) Integration of Random Pore Model & Langmuir-Hinshelwood Kinetics to Study High Temperature Coal Gasification
There have been attempts to combine random pore model with LH kinetics for competing CO2 and H2O gasification reactions (Umemoto et. al., 2013). But these efforts are restricted to the low temperature kinetically controlled regime. There is a need to extend the combined model to systems at higher temperature that are pore diffusion controlled to better understand the industrial systems of coal gasification.
In this study, we extend the random pore model with transport and diffusion effects to incorporate LH kinetics first to CO2 gasification systems with varying amounts of CO using multi-species reaction diffusion modeling. We then study the H2O gasification systems in presence of H2O, CO and H2. Finally we combine both these efforts to study the complete industrial gasification systems that involve both CO2 and H2O in the presence of all four gases: CO2, CO, H2O and H2. Using this model we gain important insights into optimizing the feed compositions to obtain the final product: syngas, with the desired specifications.
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