Operating behavior and scale-up of an ECPrOx unit for CO removal from reformate for PEM fuel cell application

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  • Max Planck Institute for Dynamics of Complex Technical Systems
  • Otto-von-Guericke University Magdeburg
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Original languageEnglish
Pages (from-to)B1267-B1275
JournalJournal of the Electrochemical Society
Volume2009
Issue number156
Publication statusPublished - 2009
Externally publishedYes

Abstract

Recently, an approach involving electrochemical preferential oxidation (ECPrOx) of CO was suggested as having the potential to replace the PrOx concept for deep CO removal from reformate gas in proton exchange membrane (PEM) fuel cells. The first part of this paper deals with the characterization of such an ECPrOx unit from a reaction engineering point of view. Based on a spatially lumped, isothermal model, the qualitative selectivity-conversion behavior is discussed for varying feed flow rates and CO inlet mole fractions. A simple two-phase mechanism is suggested that explains the findings. The second part of the contribution considers qualitative questions on cascading of two ECPrOx reactors. The crucial importance of the configuration of their electrical connection is demonstrated and explained. While two cells connected electrically in parallel exhibit almost the same selectivity-conversion behavior in comparison with a single cell, an electrical series connection enables a considerable increase in the selectivity at the same CO conversion.

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Sustainable Development Goals

Cite this

Operating behavior and scale-up of an ECPrOx unit for CO removal from reformate for PEM fuel cell application. / Hanke-Rauschenbach, Richard; Weinzierl, Christine; Krasnyk, Mykhaylo et al.
In: Journal of the Electrochemical Society, Vol. 2009, No. 156, 2009, p. B1267-B1275.

Research output: Contribution to journalArticleResearchpeer review

Hanke-Rauschenbach R, Weinzierl C, Krasnyk M, Rihko-Struckmann L, Lu H, Sundmacher K. Operating behavior and scale-up of an ECPrOx unit for CO removal from reformate for PEM fuel cell application. Journal of the Electrochemical Society. 2009;2009(156):B1267-B1275. doi: 10.1149/1.3196244
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title = "Operating behavior and scale-up of an ECPrOx unit for CO removal from reformate for PEM fuel cell application",
abstract = "Recently, an approach involving electrochemical preferential oxidation (ECPrOx) of CO was suggested as having the potential to replace the PrOx concept for deep CO removal from reformate gas in proton exchange membrane (PEM) fuel cells. The first part of this paper deals with the characterization of such an ECPrOx unit from a reaction engineering point of view. Based on a spatially lumped, isothermal model, the qualitative selectivity-conversion behavior is discussed for varying feed flow rates and CO inlet mole fractions. A simple two-phase mechanism is suggested that explains the findings. The second part of the contribution considers qualitative questions on cascading of two ECPrOx reactors. The crucial importance of the configuration of their electrical connection is demonstrated and explained. While two cells connected electrically in parallel exhibit almost the same selectivity-conversion behavior in comparison with a single cell, an electrical series connection enables a considerable increase in the selectivity at the same CO conversion.",
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AU - Hanke-Rauschenbach, Richard

AU - Weinzierl, Christine

AU - Krasnyk, Mykhaylo

AU - Rihko-Struckmann, Liisa

AU - Lu, Hui

AU - Sundmacher, Kai

N1 - Copyright: Copyright 2009 Elsevier B.V., All rights reserved.

PY - 2009

Y1 - 2009

N2 - Recently, an approach involving electrochemical preferential oxidation (ECPrOx) of CO was suggested as having the potential to replace the PrOx concept for deep CO removal from reformate gas in proton exchange membrane (PEM) fuel cells. The first part of this paper deals with the characterization of such an ECPrOx unit from a reaction engineering point of view. Based on a spatially lumped, isothermal model, the qualitative selectivity-conversion behavior is discussed for varying feed flow rates and CO inlet mole fractions. A simple two-phase mechanism is suggested that explains the findings. The second part of the contribution considers qualitative questions on cascading of two ECPrOx reactors. The crucial importance of the configuration of their electrical connection is demonstrated and explained. While two cells connected electrically in parallel exhibit almost the same selectivity-conversion behavior in comparison with a single cell, an electrical series connection enables a considerable increase in the selectivity at the same CO conversion.

AB - Recently, an approach involving electrochemical preferential oxidation (ECPrOx) of CO was suggested as having the potential to replace the PrOx concept for deep CO removal from reformate gas in proton exchange membrane (PEM) fuel cells. The first part of this paper deals with the characterization of such an ECPrOx unit from a reaction engineering point of view. Based on a spatially lumped, isothermal model, the qualitative selectivity-conversion behavior is discussed for varying feed flow rates and CO inlet mole fractions. A simple two-phase mechanism is suggested that explains the findings. The second part of the contribution considers qualitative questions on cascading of two ECPrOx reactors. The crucial importance of the configuration of their electrical connection is demonstrated and explained. While two cells connected electrically in parallel exhibit almost the same selectivity-conversion behavior in comparison with a single cell, an electrical series connection enables a considerable increase in the selectivity at the same CO conversion.

KW - Electric connectors

KW - Fuel cells

KW - CO conversion

KW - CO removal

KW - Electrical connection

KW - Cell membranes

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