Development of a Butanol Fuel Processor for Person-Portable Fuel Cell Power Systems
- Type: Conference Presentation
- Conference Type: AIChE Annual Meeting
- Presentation Date: October 31, 2012
- Duration: 15 minutes
- Skill Level: Intermediate
- PDHs: 0.50
An integrated system design approach was undertaken to optimize the fuel processing system configuration and operating conditions. Among the available fuel processing options, systems based on both partial oxidation and auto-thermal reforming (ATR) of isobutanol fuel were investigated. The former, i.e. partial oxidation reforming, results in a simpler but less efficient design to implement. The latter, i.e. autothermal reforming, is a more efficient approach for conversion of isobutanol to hydrogen for the fuel cell anode. A systematic design study has determined the optimal operating conditions for the partial oxidation and autothermal-based systems.
Energy density, in terms of W-h/kg and W-h/L, is a critical parameter for person-portable power systems. These systems must be lightweight and compact, especially for military applications to avoid hindering a soldier’s movements in the field. The butanol-fueled system under development has an inherent advantage due to the increased energy density of the fuel, as compared to methanol-fueled systems. A complete, integrated sub-system was designed using 3-D CAD modeling software to minimize the size and weight of the reformer. 3-D CAD renderings were created for both the partial oxidation and autothermal-based butanol fuel processor systems. The POX-based butanol reforming system is estimated to achieve an energy density of 810 W-h/L and 850 W-h/kg, while the ATR-based system is estimated to achieve an energy density of 1,000 W-h/L and 2,000 W-h/kg.
The concept feasibility of reforming isobutanol to a hydrogen-rich stream via partial oxidation was experimentally demonstrated. Novel catalyst formulations and catalyst support structures have been developed and tested. A Rh/Ce-based reforming catalyst effectively converted isobutanol to an H2-rich stream with no coke formation under the desired system operating conditions. The catalyst was also demonstrated to be regenerable, should carbon deposition occur. In summary, the concept feasibility of both a novel butanol reforming catalyst and fuel processor sub-system design to effectively convert isobutanol to hydrogen with the potential to be packaged into a compact, high energy density system has been demonstrated.
|AIChE Member Credits||0.5|
|AIChE Graduate Student Members||Free|
|AIChE Undergraduate Student Members||Free|