1. Date of download: 9/17/2016 Copyright © ASME. All rights reserved. From: Computational Fluid Dynamics Modeling of a Catalytic Flat Plate Fuel Reformer for On-Board Hydrogen Generation J. Fuel Cell Sci. Technol. 2013;10(6):061005-061005-6. doi:10.1115/1.4025056 Computational simulation domain geometry Figure Legend:

2. Date of download: 9/17/2016 Copyright © ASME. All rights reserved. From: Computational Fluid Dynamics Modeling of a Catalytic Flat Plate Fuel Reformer for On-Board Hydrogen Generation J. Fuel Cell Sci. Technol. 2013;10(6):061005-061005-6. doi:10.1115/1.4025056 Production of dry H 2 at different inlet velocities along the reformer channel without the water gas shift (WGS) reaction Figure Legend:

3. Date of download: 9/17/2016 Copyright © ASME. All rights reserved. From: Computational Fluid Dynamics Modeling of a Catalytic Flat Plate Fuel Reformer for On-Board Hydrogen Generation J. Fuel Cell Sci. Technol. 2013;10(6):061005-061005-6. doi:10.1115/1.4025056 Production of dry CO at different inlet velocities along the reformer channel without the water gas shift (WGS) reaction Figure Legend:

4. Date of download: 9/17/2016 Copyright © ASME. All rights reserved. From: Computational Fluid Dynamics Modeling of a Catalytic Flat Plate Fuel Reformer for On-Board Hydrogen Generation J. Fuel Cell Sci. Technol. 2013;10(6):061005-061005-6. doi:10.1115/1.4025056 Production of dry H 2 at different channel heights at 4 m/s inlet mixture velocity without the WGS Figure Legend:

5. Date of download: 9/17/2016 Copyright © ASME. All rights reserved. From: Computational Fluid Dynamics Modeling of a Catalytic Flat Plate Fuel Reformer for On-Board Hydrogen Generation J. Fuel Cell Sci. Technol. 2013;10(6):061005-061005-6. doi:10.1115/1.4025056 Production of CO at different channel heights at 4 m/s inlet mixture velocity without the WGS Figure Legend:

6. Date of download: 9/17/2016 Copyright © ASME. All rights reserved. From: Computational Fluid Dynamics Modeling of a Catalytic Flat Plate Fuel Reformer for On-Board Hydrogen Generation J. Fuel Cell Sci. Technol. 2013;10(6):061005-061005-6. doi:10.1115/1.4025056 Production of dry H 2 with the WGS reaction as a function of channel length Figure Legend:

7. Date of download: 9/17/2016 Copyright © ASME. All rights reserved. From: Computational Fluid Dynamics Modeling of a Catalytic Flat Plate Fuel Reformer for On-Board Hydrogen Generation J. Fuel Cell Sci. Technol. 2013;10(6):061005-061005-6. doi:10.1115/1.4025056 Reduction of CO in the WGS reaction as a function of channel length Figure Legend:

8. Date of download: 9/17/2016 Copyright © ASME. All rights reserved. From: Computational Fluid Dynamics Modeling of a Catalytic Flat Plate Fuel Reformer for On-Board Hydrogen Generation J. Fuel Cell Sci. Technol. 2013;10(6):061005-061005-6. doi:10.1115/1.4025056 Reduction of CO at different catalyst layer thicknesses in the WGS reaction zone as a function of channel length Figure Legend:

9. Date of download: 9/17/2016 Copyright © ASME. All rights reserved. From: Computational Fluid Dynamics Modeling of a Catalytic Flat Plate Fuel Reformer for On-Board Hydrogen Generation J. Fuel Cell Sci. Technol. 2013;10(6):061005-061005-6. doi:10.1115/1.4025056 Production of dry H 2 during the WGS with optimized reformer geometry Figure Legend:

10. Date of download: 9/17/2016 Copyright © ASME. All rights reserved. From: Computational Fluid Dynamics Modeling of a Catalytic Flat Plate Fuel Reformer for On-Board Hydrogen Generation J. Fuel Cell Sci. Technol. 2013;10(6):061005-061005-6. doi:10.1115/1.4025056 Reduction of dry CO during the WGS with optimized reformer geometry Figure Legend: