Abstract
The so-called self-sustained electrochemical promotion catalyst or SSEP catalyst is a micro-particulate material with solid-solid interfaces between the active catalyst phase, the oxygen ion conductor, and oxygen reduction phase forming multiple micro-electrochemical cells. We have demonstrated that electrochemical promotion can make the catalyst more effective than conventional transition metal (Ni, Co) based catalysts and precious metal based catalyst for partial oxidation (POX) reforming of hydrocarbons. A computational fluid dynamics (CFD) model will help quantify the effects of the components in the microscopic electrochemical cells and of detailed thermal-chemical processes on electrochemical promotion thereby allowing better understanding and further optimization of the catalyst system.
A multi-physical multi-scale CFD was developed for analyzing POX of methane (CH
4
) over a SSEP catalyst in a fixed-bed reformer. The model incorporates a conventional transport processes, heat transfer, and kinetics for POX of CH
4
over the active components and the electrochemical processes occurring in the unique microstructure. The simulation results show that the temperature in the first reactor with the Ni based conventional catalyst is generally about 30 K lower than that in the second reactor with the Ni-based SSEP catalyst. This temperature difference is impossible to explain the huge difference in the conversion in these two reactors. The simulation results are compared with the experimental results. The good agreement can only be achieved by correctly describing the electrochemical processes and electrochemical promotion in the theoretical system. The validated model was used to predict the performance of the SSEP catalysts as a function of flow rate, O/C ratio, and the microstructure of the catalysts providing guidance for further optimization the SSEP catalyst.