Thermal partial oxidation of n-butane in a micro-flow reactor and solid oxide fuel cell stability assessment

The direct use of n-butane in solid oxide fuel cell (SOFC) systems has been challenging due to high performance degradation and/or failure due to carbon deposition on the anode. Previous works have explored SOFCs with expensive integrated catalysts to promote the longevity of the SOFC, but few have achieved significant operating hours. In this work, a SOFC with no integrated catalyst is fed n-butane for 288 h utilizing a novel micro fuel reformer. The impact of temperature (800-900 degrees C), total flow rate (10-50 mL.minxfffd; 1), and equivalence ratio (1-5) on the thermal partial oxidation of n-butane in the micro-flow reactor are characterized. A literature review of n-butane fueled SOFC systems confirms that the 288-hour long term stability test achieved in this study is among the longest conducted with a low voltage degradation of 0.00034 V.h-1. Scanning electron microscope (SEM) images of the SOFC anode confirm no carbon deposition occurred on the surface. Microscale partial oxidation with light internal reforming provides an alternative to traditional catalytic oxidation and internal reforming SOFC systems.

Automated summary

In this study, a novel micro fuel reformer was used to supply n-butane to a solid oxide fuel cell (SOFC) system without an integrated catalyst for 288 hours. The results show that the system exhibits good operating stability and low voltage degradation.