Benchmarking Electrolytes for the Solid Oxide Electrolyzer Using a Finite Element Model

The demand for green hydrogen is increasing, as it is estimated to reduce ten percent of total global green-house-gas emissions from fossil fuel. The solid oxide electrolysis cell (SOEC) is an electrochemical energy-conversion device (EECD) that produces green hydrogen via steam electrolysis. It is...

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Main Authors: Sriram Srinivas, Shankar Raman Dhanushkodi, Ramesh Kumar Chidambaram, Dorota Skrzyniowska, Anna Korzen, Jan Taler
Format: Article
Language:English
Published: MDPI AG 2023-09-01
Series:Energies
Subjects:
Online Access:https://www.mdpi.com/1996-1073/16/18/6419
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author Sriram Srinivas
Shankar Raman Dhanushkodi
Ramesh Kumar Chidambaram
Dorota Skrzyniowska
Anna Korzen
Jan Taler
author_facet Sriram Srinivas
Shankar Raman Dhanushkodi
Ramesh Kumar Chidambaram
Dorota Skrzyniowska
Anna Korzen
Jan Taler
author_sort Sriram Srinivas
collection DOAJ
description The demand for green hydrogen is increasing, as it is estimated to reduce ten percent of total global green-house-gas emissions from fossil fuel. The solid oxide electrolysis cell (SOEC) is an electrochemical energy-conversion device (EECD) that produces green hydrogen via steam electrolysis. It is preferred to other EECDs for clean hydrogen production owing to its high efficiency, robust kinetics, and lack of precious-metal requirements for cell construction. Herein, we report a Multiphysics model describing the transport phenomena in the SOEC. The governing equations used in the model include a thorough description of the electrode kinetics and of the behavior of the three electrode–electrolyte interfaces in the cell. For the first time, the effect of the scandium-doped zirconia (SCGZ), yttrium-stabilized zirconia (YSZ), and gadolinium-doped ceria (GDC) electrolytes was modeled at different temperatures and pressures. By linking the convection and diffusion equations with the Butler–Volmer at shorter scales, a true representation of the cell operation was simulated. Our models show a <i>R</i><sup>2</sup> value of over 0.996 in predicting the cell-polarization curves and electrochemical properties at the given operating conditions. The impedance of the SCGZ was 0.0240 Ohm.cm<sup>2</sup>. This value was two- and four-fold lower than the values of the YSZ and GDC, respectively. Furthermore, our theoretical findings of both the polarization data and the impedance were in good agreement with the experimental data.
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spelling doaj.art-5ceca29e799b4fd0b29fc7be67c8a7c82023-11-19T10:24:50ZengMDPI AGEnergies1996-10732023-09-011618641910.3390/en16186419Benchmarking Electrolytes for the Solid Oxide Electrolyzer Using a Finite Element ModelSriram Srinivas0Shankar Raman Dhanushkodi1Ramesh Kumar Chidambaram2Dorota Skrzyniowska3Anna Korzen4Jan Taler5SERD Innovation Laboratory, Department of Chemical Engineering, Vellore Institute of Technology, Vellore 632014, IndiaSERD Innovation Laboratory, Department of Chemical Engineering, Vellore Institute of Technology, Vellore 632014, IndiaAutomotive Research Centre, Vellore Institute of Technology, Vellore 632014, IndiaDepartment of Energy, Cracow University of Technology, 31-864 Cracow, PolandDepartment of Energy, Cracow University of Technology, 31-864 Cracow, PolandDepartment of Energy, Cracow University of Technology, 31-864 Cracow, PolandThe demand for green hydrogen is increasing, as it is estimated to reduce ten percent of total global green-house-gas emissions from fossil fuel. The solid oxide electrolysis cell (SOEC) is an electrochemical energy-conversion device (EECD) that produces green hydrogen via steam electrolysis. It is preferred to other EECDs for clean hydrogen production owing to its high efficiency, robust kinetics, and lack of precious-metal requirements for cell construction. Herein, we report a Multiphysics model describing the transport phenomena in the SOEC. The governing equations used in the model include a thorough description of the electrode kinetics and of the behavior of the three electrode–electrolyte interfaces in the cell. For the first time, the effect of the scandium-doped zirconia (SCGZ), yttrium-stabilized zirconia (YSZ), and gadolinium-doped ceria (GDC) electrolytes was modeled at different temperatures and pressures. By linking the convection and diffusion equations with the Butler–Volmer at shorter scales, a true representation of the cell operation was simulated. Our models show a <i>R</i><sup>2</sup> value of over 0.996 in predicting the cell-polarization curves and electrochemical properties at the given operating conditions. The impedance of the SCGZ was 0.0240 Ohm.cm<sup>2</sup>. This value was two- and four-fold lower than the values of the YSZ and GDC, respectively. Furthermore, our theoretical findings of both the polarization data and the impedance were in good agreement with the experimental data.https://www.mdpi.com/1996-1073/16/18/6419multiphysics modelsolid oxide electrolyzerzirconiaceria-based electrolyteshydrogen productionsteam electrolysis
spellingShingle Sriram Srinivas
Shankar Raman Dhanushkodi
Ramesh Kumar Chidambaram
Dorota Skrzyniowska
Anna Korzen
Jan Taler
Benchmarking Electrolytes for the Solid Oxide Electrolyzer Using a Finite Element Model
Energies
multiphysics model
solid oxide electrolyzer
zirconia
ceria-based electrolytes
hydrogen production
steam electrolysis
title Benchmarking Electrolytes for the Solid Oxide Electrolyzer Using a Finite Element Model
title_full Benchmarking Electrolytes for the Solid Oxide Electrolyzer Using a Finite Element Model
title_fullStr Benchmarking Electrolytes for the Solid Oxide Electrolyzer Using a Finite Element Model
title_full_unstemmed Benchmarking Electrolytes for the Solid Oxide Electrolyzer Using a Finite Element Model
title_short Benchmarking Electrolytes for the Solid Oxide Electrolyzer Using a Finite Element Model
title_sort benchmarking electrolytes for the solid oxide electrolyzer using a finite element model
topic multiphysics model
solid oxide electrolyzer
zirconia
ceria-based electrolytes
hydrogen production
steam electrolysis
url https://www.mdpi.com/1996-1073/16/18/6419
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