0
Research Papers

A Theoretical Study of the Carbon/Carbonate/Hydroxide (Electro-) Chemical System in a Direct Carbon Fuel Cell

[+] Author and Article Information
Kas Hemmes1

Technology Dynamics and Sustainable Development, Delft University of Technology, Jaffalaan 5, 2628 BX, Delft, Netherlandsk.hemmes@tbm.tudelft.nl

Michel Cassir

 École Nationale Supérieure de Chimie, de Paris, Chimie ParisTech, 11, rue Pierre et Marie Curie, 75231 Paris Cedex 05, Francecassir@ext.jussieu.fr

1

Corresponding author.

J. Fuel Cell Sci. Technol 8(5), 051005 (Jun 16, 2011) (5 pages) doi:10.1115/1.4003750 History: Received May 26, 2009; Revised March 03, 2010; Published June 16, 2011; Online June 16, 2011

Both the hydroxide and the carbonate melt are proposed and tested by researchers trying to develop a DCFC (Direct Carbon Fuel Cell). It is well known that the hydroxide melt is not stable due to the carbon dioxide formed in the fuel cell reaction. The hydroxide ion reacts with CO2 to form carbonate ions and water. From this reaction it is clear that in either approach the melt is a mixture of carbonate and hydroxide depending on the partial pressures of water and CO2 above the melt. Therefore a good insight in the equilibria present in the melts is essential for understanding and optimizing the DCFC. Following the method introduced by Smith and Missen a complete and independent set of equilibria describing the chemical equilibrium in the melt can be obtained using linear algebra. Using the modification proposed by Coleman and White also electrochemical equilibria are included. This is done for the cathode as well as the anode environment of a DCFC with a carbonate and/or hydroxide melt as electrolyte. Hereby the open cell voltage for a DCFC including the Boudouard equilibrium could be calculated. It was found that the OCV increases as a function of temperature even more rapidly than the standard potential for the electrochemical oxidation of carbon to CO, which also has a positive slope due to a positive entropy change of the overall reaction. This extra high OCV is an additional argument for developing the DCFC in particular a DCFC at high temperatures in which predominantly CO is produced. Since CO can easily be shifted to hydrogen in a water gas shift reaction with steam, coproduction of hydrogen and power can be obtained using carbon and high temperature heat as energy inputs.

FIGURES IN THIS ARTICLE
<>
Copyright © 2011 by American Society of Mechanical Engineers
Your Session has timed out. Please sign back in to continue.

References

Figures

Grahic Jump Location
Figure 1

Standard potentials for the oxidation of carbon to CO and CO2 and the Open Cell Voltage of a carbonate DCFC assuming pCO + pCO2  = 1 atm. at the anode and pO2  = pCO2  = 1 atm. at the cathode calculated using Eqs. (26) and (27).

Tables

Errata

Discussions

Some tools below are only available to our subscribers or users with an online account.

Related Content

Customize your page view by dragging and repositioning the boxes below.

Related Journal Articles
Related eBook Content
Topic Collections

Sorry! You do not have access to this content. For assistance or to subscribe, please contact us:

  • TELEPHONE: 1-800-843-2763 (Toll-free in the USA)
  • EMAIL: asmedigitalcollection@asme.org
Sign In