A diesel fuel processor for fuel-cell-based auxiliary power unit applications

Abstract Producing a hydrogen-rich gas from diesel fuel enables the efficient generation of electricity in a fuel-cell-based auxiliary power unit. In recent years, significant progress has been achieved in diesel reforming. One issue encountered is the stable operation of water-gas shift reactors with real reformates. A new fuel processor is developed using a commercial shift catalyst. The system is operated using optimized start-up and shut-down strategies. Experiments with diesel and kerosene fuels show slight performance drops in the shift reactor during continuous operation for 100 h. CO concentrations much lower than the target value are achieved during system operation in auxiliary power unit mode at partial loads of up to 60%. The regeneration leads to full recovery of the shift activity. Finally, a new operation strategy is developed whereby the gas hourly space velocity of the shift stages is re-designed. This strategy is validated using different diesel and kerosene fuels, showing a maximum CO concentration of 1.5% at the fuel processor outlet under extreme conditions, which can be tolerated by a high-temperature PEFC. The proposed operation strategy solves the issue of strong performance drop in the shift reactor and makes this technology available for reducing emissions in the transportation sector.

[1]  Antje Wörner,et al.  Direct steam reforming of diesel and diesel–biodiesel blends for distributed hydrogen generation , 2015 .

[2]  M. Nilsson,et al.  Characterization and optimization of an autothermal diesel and jet fuel reformer for 5 kWe mobile fuel cell applications , 2010 .

[3]  Zoran Filipi,et al.  Simulation Study of a Series Hydraulic Hybrid Propulsion System for a Light Truck , 2007 .

[4]  Detlef Stolten,et al.  A novel reactor type for autothermal reforming of diesel fuel and kerosene , 2015 .

[5]  Detlef Stolten,et al.  Fuel cell systems with reforming of petroleum-based and synthetic-based diesel and kerosene fuels for APU applications , 2015 .

[6]  Levi T. Thompson,et al.  Deactivation of Au/CeOx water gas shift catalysts , 2005 .

[7]  Detlef Stolten,et al.  Electrical start-up for diesel fuel processing in a fuel-cell-based auxiliary power unit , 2016 .

[8]  Michael G. Waller,et al.  Diesel auto-thermal reforming for solid oxide fuel cell systems: Anode off-gas recycle simulation , 2014 .

[9]  Roland Peters,et al.  Enhancing the Efficiency of SOFC‐Based Auxiliary Power Units by Intermediate Methanation , 2012 .

[10]  Werner Lehnert,et al.  Design and test of a 5kWe high-temperature polymer electrolyte fuel cell system operated with diesel and kerosene , 2014 .

[11]  Detlef Stolten,et al.  Elimination of by-products of autothermal diesel reforming , 2016 .

[12]  R. J. Behm,et al.  Activity, stability and deactivation behavior of Au/CeO2 catalysts in the water gas shift reaction at increased reaction temperature (300 °C) , 2009 .

[13]  R. J. Behm,et al.  Influence of H2, CO2 and H2O on the activity and deactivation behavior of Au/CeO2 catalysts in the water gas shift reaction at 300 °C , 2010 .

[14]  Lukas Lüke Analyse des Betriebsverhaltens von Hochtemperatur-Polymerelektrolyt-Brennstoffzellen , 2013 .

[15]  Rolf Jürgen Behm,et al.  Influence of CO2 and H2 on the low-temperature water–gas shift reaction on Au/CeO2 catalysts in idealized and realistic reformate , 2007 .

[16]  Philip Engelhardt,et al.  Integrated fuel cell APU based on a compact steam reformer for diesel and a PEMFC , 2012 .

[17]  Christie-Joy Brodrick,et al.  Analysis of potential fuel consumption and emissions reductions from fuel cell auxiliary power units (APUs) in long-haul trucks , 2007 .

[18]  J. Bae,et al.  Liquid fuel processing for hydrogen production: A review , 2016 .

[19]  Peiwen Li,et al.  Small-scale reforming of diesel and jet fuels to make hydrogen and syngas for fuel cells: A review , 2013 .

[20]  Detlef Stolten,et al.  Long-term stability at fuel processing of diesel and kerosene , 2014 .

[21]  Roland Peters,et al.  Analysis and optimization of solid oxide fuel cell-based auxiliary power units using a generic zero-dimensional fuel cell model , 2011 .

[22]  Detlef Stolten,et al.  Operating strategies for fuel processing systems with a focus on water–gas shift reactor stability , 2016 .

[23]  Janko Petrovčič,et al.  A model-based approach to battery selection for truck onboard fuel cell-based APU in an anti-idling application , 2015 .

[24]  S. Specchia Fuel processing activities at European level: A panoramic overview , 2014 .

[25]  Gunther Kolb,et al.  Microchannel Fuel Processors as a Hydrogen Source for Fuel Cells in Distributed Energy Supply Systems , 2013 .

[26]  V. Recupero,et al.  Hydrogen-rich gas production by steam reforming of n-dodecane: Part I: Catalytic activity of Pt/CeO2 catalysts in optimized bed configuration , 2016 .

[27]  J. Bae,et al.  Diesel autothermal reforming with hydrogen peroxide for low-oxygen environments , 2015 .

[28]  Marius Maximini,et al.  Coupled operation of a diesel steam reformer and an LT- and HT-PEFC , 2014 .

[29]  R. Behm,et al.  Influence of the catalyst surface area on the activity and stability of Au/CeO2 catalysts for the low-temperature water gas shift reaction , 2007 .

[30]  Zhen Ma,et al.  Water-gas shift on gold catalysts: catalyst systems and fundamental studies. , 2013, Physical chemistry chemical physics : PCCP.