Influence of Stoichiometry on the Two-Phase Flow Behavior of Proton Exchange Membrane Electrolyzers

In order for electrolysis cells to operate optimally, mass transport must be improved. The key initial component for optimal operation is the current collector, which is also essential for mass transport. Water as an educt of the reaction must be evenly distributed by the current collector to the me...

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Main Authors: Olha Panchenko, Lennard Giesenberg, Elena Borgardt, Walter Zwaygardt, Nikolay Kardjilov, Henning Markötter, Tobias Arlt, Ingo Manke, Martin Müller, Detlef Stolten, Werner Lehnert
Format: Article
Language:English
Published: MDPI AG 2019-01-01
Series:Energies
Subjects:
Online Access:https://www.mdpi.com/1996-1073/12/3/350
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spelling doaj-a22f698f632d4b69a33e7298a6ea17ea2020-11-25T01:42:58ZengMDPI AGEnergies1996-10732019-01-0112335010.3390/en12030350en12030350Influence of Stoichiometry on the Two-Phase Flow Behavior of Proton Exchange Membrane ElectrolyzersOlha Panchenko0Lennard Giesenberg1Elena Borgardt2Walter Zwaygardt3Nikolay Kardjilov4Henning Markötter5Tobias Arlt6Ingo Manke7Martin Müller8Detlef Stolten9Werner Lehnert10Institute of Energy and Climate Research – Electrochemical Process Engineering (IEK-3) Forschungszentrum Jülich GmbH, Jülich 52428, GermanyInstitute of Energy and Climate Research – Electrochemical Process Engineering (IEK-3) Forschungszentrum Jülich GmbH, Jülich 52428, GermanyInstitute of Energy and Climate Research – Electrochemical Process Engineering (IEK-3) Forschungszentrum Jülich GmbH, Jülich 52428, GermanyInstitute of Energy and Climate Research – Electrochemical Process Engineering (IEK-3) Forschungszentrum Jülich GmbH, Jülich 52428, GermanyInstitute of Applied Materials, Helmholtz Zentrum Berlin, Berlin 14109, GermanyInstitute of Applied Materials, Helmholtz Zentrum Berlin, Berlin 14109, GermanyInstitute of Applied Materials, Technische Universität Berlin, Berlin 10623, GermanyInstitute of Applied Materials, Helmholtz Zentrum Berlin, Berlin 14109, GermanyInstitute of Energy and Climate Research – Electrochemical Process Engineering (IEK-3) Forschungszentrum Jülich GmbH, Jülich 52428, GermanyInstitute of Energy and Climate Research – Electrochemical Process Engineering (IEK-3) Forschungszentrum Jülich GmbH, Jülich 52428, GermanyInstitute of Energy and Climate Research – Electrochemical Process Engineering (IEK-3) Forschungszentrum Jülich GmbH, Jülich 52428, GermanyIn order for electrolysis cells to operate optimally, mass transport must be improved. The key initial component for optimal operation is the current collector, which is also essential for mass transport. Water as an educt of the reaction must be evenly distributed by the current collector to the membrane electrode assembly. As products of the reaction, hydrogen and oxygen must also be directed quickly and efficiently through the current collector into the channel and removed from the cell. The second key component is the stoichiometry, which includes the current density and water volume flow rate and represents the ratio between the water supplied and water consumed. This study presents the correlation of the stoichiometry, two-phase flow in the channel and gas fraction in the porous transport layer for the first time. The gas-water ratio in the channel and porous transport layer during cell operation with various stoichiometries was investigated by means of a model in the form of an ex situ cell without electrochemical processes. Bubble formation in the channel was observed using a transparent cell. The gas-water exchange in the porous transport layer was then investigated using neutron radiography.https://www.mdpi.com/1996-1073/12/3/350proton exchange membrane electrolysisstoichiometryneutron radiographytwo-phase flowflow regime
collection DOAJ
language English
format Article
sources DOAJ
author Olha Panchenko
Lennard Giesenberg
Elena Borgardt
Walter Zwaygardt
Nikolay Kardjilov
Henning Markötter
Tobias Arlt
Ingo Manke
Martin Müller
Detlef Stolten
Werner Lehnert
spellingShingle Olha Panchenko
Lennard Giesenberg
Elena Borgardt
Walter Zwaygardt
Nikolay Kardjilov
Henning Markötter
Tobias Arlt
Ingo Manke
Martin Müller
Detlef Stolten
Werner Lehnert
Influence of Stoichiometry on the Two-Phase Flow Behavior of Proton Exchange Membrane Electrolyzers
Energies
proton exchange membrane electrolysis
stoichiometry
neutron radiography
two-phase flow
flow regime
author_facet Olha Panchenko
Lennard Giesenberg
Elena Borgardt
Walter Zwaygardt
Nikolay Kardjilov
Henning Markötter
Tobias Arlt
Ingo Manke
Martin Müller
Detlef Stolten
Werner Lehnert
author_sort Olha Panchenko
title Influence of Stoichiometry on the Two-Phase Flow Behavior of Proton Exchange Membrane Electrolyzers
title_short Influence of Stoichiometry on the Two-Phase Flow Behavior of Proton Exchange Membrane Electrolyzers
title_full Influence of Stoichiometry on the Two-Phase Flow Behavior of Proton Exchange Membrane Electrolyzers
title_fullStr Influence of Stoichiometry on the Two-Phase Flow Behavior of Proton Exchange Membrane Electrolyzers
title_full_unstemmed Influence of Stoichiometry on the Two-Phase Flow Behavior of Proton Exchange Membrane Electrolyzers
title_sort influence of stoichiometry on the two-phase flow behavior of proton exchange membrane electrolyzers
publisher MDPI AG
series Energies
issn 1996-1073
publishDate 2019-01-01
description In order for electrolysis cells to operate optimally, mass transport must be improved. The key initial component for optimal operation is the current collector, which is also essential for mass transport. Water as an educt of the reaction must be evenly distributed by the current collector to the membrane electrode assembly. As products of the reaction, hydrogen and oxygen must also be directed quickly and efficiently through the current collector into the channel and removed from the cell. The second key component is the stoichiometry, which includes the current density and water volume flow rate and represents the ratio between the water supplied and water consumed. This study presents the correlation of the stoichiometry, two-phase flow in the channel and gas fraction in the porous transport layer for the first time. The gas-water ratio in the channel and porous transport layer during cell operation with various stoichiometries was investigated by means of a model in the form of an ex situ cell without electrochemical processes. Bubble formation in the channel was observed using a transparent cell. The gas-water exchange in the porous transport layer was then investigated using neutron radiography.
topic proton exchange membrane electrolysis
stoichiometry
neutron radiography
two-phase flow
flow regime
url https://www.mdpi.com/1996-1073/12/3/350
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