Modeling pattern formation during the electrochemical preferential CO oxidation in CO/H 2 mixtures

Research output: Contribution to conferencePaperResearchpeer review

Authors

External Research Organisations

  • Max Planck Institute for Dynamics of Complex Technical Systems
  • Otto-von-Guericke University Magdeburg
View graph of relations

Details

Original languageEnglish
Publication statusPublished - 2010
Externally publishedYes
Event19th International Congress of Chemical and Process Engineering, CHISA 2010 and 7th European Congress of Chemical Engineering, ECCE-7 - Prague, Czech Republic
Duration: 28 Aug 20101 Sept 2010

Conference

Conference19th International Congress of Chemical and Process Engineering, CHISA 2010 and 7th European Congress of Chemical Engineering, ECCE-7
Country/TerritoryCzech Republic
CityPrague
Period28 Aug 20101 Sept 2010

Abstract

One of the major problems hindering the breakthrough of polymer electrolyte membrane (PEM) fuel cells is their sensitivity to traces of CO within the hydrogen used as fuel. A spatially one dimensional reactor has been investigated with a dynamic modeling approach. The model considers mass balances for the channel and the catalyst surface, as well as charge balances for the electrochemical double layers and the electrolytic membrane. Spatio-temporal patterns are observed. As the CO partial pressure decreases along the channel, the oscillation frequency is expected to fall, too. This case is observed when the electrolytic conductivity is low. With an increase in conductivity, synchronization of the oscillation starts at the reactor outlet until the whole cell oscillates in a synchronous manner. Global coupling leads to the long range spatial coupling. Diffusion coupling links adjacent sites and leads to some minor phenomena. This is an abstract of a paper presented at the 7th European Congress of Chemical Engineering 7 and the 19th International Congress of Chemical and Process Engineering CHISA (Prague, Czech Republic 8/28/2010-9/1/2010).

ASJC Scopus subject areas

Cite this

Modeling pattern formation during the electrochemical preferential CO oxidation in CO/H 2 mixtures. / Kirsch, S.; Hanke-Rauschenbach, R.; Sundmacher, K.
2010. Paper presented at 19th International Congress of Chemical and Process Engineering, CHISA 2010 and 7th European Congress of Chemical Engineering, ECCE-7, Prague, Czech Republic.

Research output: Contribution to conferencePaperResearchpeer review

Kirsch, S, Hanke-Rauschenbach, R & Sundmacher, K 2010, 'Modeling pattern formation during the electrochemical preferential CO oxidation in CO/H 2 mixtures', Paper presented at 19th International Congress of Chemical and Process Engineering, CHISA 2010 and 7th European Congress of Chemical Engineering, ECCE-7, Prague, Czech Republic, 28 Aug 2010 - 1 Sept 2010.
Kirsch, S., Hanke-Rauschenbach, R., & Sundmacher, K. (2010). Modeling pattern formation during the electrochemical preferential CO oxidation in CO/H 2 mixtures. Paper presented at 19th International Congress of Chemical and Process Engineering, CHISA 2010 and 7th European Congress of Chemical Engineering, ECCE-7, Prague, Czech Republic.
Kirsch S, Hanke-Rauschenbach R, Sundmacher K. Modeling pattern formation during the electrochemical preferential CO oxidation in CO/H 2 mixtures. 2010. Paper presented at 19th International Congress of Chemical and Process Engineering, CHISA 2010 and 7th European Congress of Chemical Engineering, ECCE-7, Prague, Czech Republic.
Kirsch, S. ; Hanke-Rauschenbach, R. ; Sundmacher, K. / Modeling pattern formation during the electrochemical preferential CO oxidation in CO/H 2 mixtures. Paper presented at 19th International Congress of Chemical and Process Engineering, CHISA 2010 and 7th European Congress of Chemical Engineering, ECCE-7, Prague, Czech Republic.
Download
@conference{a2c376673db742c496d3a9d2923ff236,
title = "Modeling pattern formation during the electrochemical preferential CO oxidation in CO/H 2 mixtures",
abstract = "One of the major problems hindering the breakthrough of polymer electrolyte membrane (PEM) fuel cells is their sensitivity to traces of CO within the hydrogen used as fuel. A spatially one dimensional reactor has been investigated with a dynamic modeling approach. The model considers mass balances for the channel and the catalyst surface, as well as charge balances for the electrochemical double layers and the electrolytic membrane. Spatio-temporal patterns are observed. As the CO partial pressure decreases along the channel, the oscillation frequency is expected to fall, too. This case is observed when the electrolytic conductivity is low. With an increase in conductivity, synchronization of the oscillation starts at the reactor outlet until the whole cell oscillates in a synchronous manner. Global coupling leads to the long range spatial coupling. Diffusion coupling links adjacent sites and leads to some minor phenomena. This is an abstract of a paper presented at the 7th European Congress of Chemical Engineering 7 and the 19th International Congress of Chemical and Process Engineering CHISA (Prague, Czech Republic 8/28/2010-9/1/2010).",
keywords = "Electrodissolution, Oscillatory, Formic Acid Fuel Cell (FAFC)",
author = "S. Kirsch and R. Hanke-Rauschenbach and K. Sundmacher",
note = "Copyright: Copyright 2012 Elsevier B.V., All rights reserved.; 19th International Congress of Chemical and Process Engineering, CHISA 2010 and 7th European Congress of Chemical Engineering, ECCE-7 ; Conference date: 28-08-2010 Through 01-09-2010",
year = "2010",
language = "English",

}

Download

TY - CONF

T1 - Modeling pattern formation during the electrochemical preferential CO oxidation in CO/H 2 mixtures

AU - Kirsch, S.

AU - Hanke-Rauschenbach, R.

AU - Sundmacher, K.

N1 - Copyright: Copyright 2012 Elsevier B.V., All rights reserved.

PY - 2010

Y1 - 2010

N2 - One of the major problems hindering the breakthrough of polymer electrolyte membrane (PEM) fuel cells is their sensitivity to traces of CO within the hydrogen used as fuel. A spatially one dimensional reactor has been investigated with a dynamic modeling approach. The model considers mass balances for the channel and the catalyst surface, as well as charge balances for the electrochemical double layers and the electrolytic membrane. Spatio-temporal patterns are observed. As the CO partial pressure decreases along the channel, the oscillation frequency is expected to fall, too. This case is observed when the electrolytic conductivity is low. With an increase in conductivity, synchronization of the oscillation starts at the reactor outlet until the whole cell oscillates in a synchronous manner. Global coupling leads to the long range spatial coupling. Diffusion coupling links adjacent sites and leads to some minor phenomena. This is an abstract of a paper presented at the 7th European Congress of Chemical Engineering 7 and the 19th International Congress of Chemical and Process Engineering CHISA (Prague, Czech Republic 8/28/2010-9/1/2010).

AB - One of the major problems hindering the breakthrough of polymer electrolyte membrane (PEM) fuel cells is their sensitivity to traces of CO within the hydrogen used as fuel. A spatially one dimensional reactor has been investigated with a dynamic modeling approach. The model considers mass balances for the channel and the catalyst surface, as well as charge balances for the electrochemical double layers and the electrolytic membrane. Spatio-temporal patterns are observed. As the CO partial pressure decreases along the channel, the oscillation frequency is expected to fall, too. This case is observed when the electrolytic conductivity is low. With an increase in conductivity, synchronization of the oscillation starts at the reactor outlet until the whole cell oscillates in a synchronous manner. Global coupling leads to the long range spatial coupling. Diffusion coupling links adjacent sites and leads to some minor phenomena. This is an abstract of a paper presented at the 7th European Congress of Chemical Engineering 7 and the 19th International Congress of Chemical and Process Engineering CHISA (Prague, Czech Republic 8/28/2010-9/1/2010).

KW - Electrodissolution

KW - Oscillatory

KW - Formic Acid Fuel Cell (FAFC)

UR - http://www.scopus.com/inward/record.url?scp=84864316050&partnerID=8YFLogxK

M3 - Paper

T2 - 19th International Congress of Chemical and Process Engineering, CHISA 2010 and 7th European Congress of Chemical Engineering, ECCE-7

Y2 - 28 August 2010 through 1 September 2010

ER -

By the same author(s)