Methanation of CO/CO2 mixtures

Research output: ThesisDoctoral Thesis

Standard

Methanation of CO/CO2 mixtures. / Krammer, Andreas.
2024.

Research output: ThesisDoctoral Thesis

Harvard

Krammer, A 2024, 'Methanation of CO/CO2 mixtures', Dr.mont., Montanuniversitaet Leoben (000). https://doi.org/10.34901/mul.pub.2024.206

APA

Krammer, A. (2024). Methanation of CO/CO2 mixtures. [Doctoral Thesis, Montanuniversitaet Leoben (000)]. https://doi.org/10.34901/mul.pub.2024.206

Vancouver

Krammer A. Methanation of CO/CO2 mixtures. 2024. doi: 10.34901/mul.pub.2024.206

Bibtex - Download

@phdthesis{b0beb9d8f09441eebd7a78683c59e391,
title = "Methanation of CO/CO2 mixtures",
abstract = "Methanation of CO/CO2 can be used to store renewable electric energy in the form of the well-known transportable gaseous energy carrier methane, which makes it a crucial technology to transform our existing fossil-based energy infrastructure. Methanation plants suitable for industrial-scale capacity at low complexity are necessary to produce cheap renewable synthetic natural gas (SNG) from fossil or biogenic carbon sources. To achieve highly optimized methanation reactors for CO/CO2 feed, such as from high temperature Co-electrolysis (Co-SOEC), the limiting mechanisms of existing reactor systems were identified. Several reactors with different dimensions, natural air-cooling or thermal-oil cooling and under variation of process conditions including pressure and catalyst load were experimentally investigated. A 1D plug-flow reactor model in MATLAB and a 2D CFD reactor model in COMSOL Multiphysics were developed and used to verify experimental findings and deepen the understanding of the methanation process. Based on a combined modelling and experimental approach tuning parameters were derived to overcome process limitations and a strategy to design high performance methanation reactors was elaborated. Thermodynamic and kinetic limitations along the reactor axis could be identified and significantly reduced by optimizing the axial temperature curve based on appropriate reactor dimensions and operation parameters. The 1D model works as a reactor optimization and design tool for CO/CO2 mixtures and other feed gases, such as biogas or CO2. Reactor and process design examples for single-stage Co-SOEC syngas methanation, high-capacity methanation at 100.000 h-1 GHSV (gas hourly space velocity) and energy efficient dual-pressure stage methanation are presented. The findings and proposals formulated in this thesis significantly improved the process of CO/CO2 methanation with the aim to contribute to a liveable future for upcoming generations on our planet.",
keywords = "Synthesegasmethanisierung, Festbett-Methanisierung, Einstufige Methanisierung, {\"O}l-gek{\"u}hlte Methanisierung, Co-SOEC-Syngas Methanisierung, Power-to-Gas, syngas methanation, fixed bed methanation, single-stage methanation, oil-cooled methanation, Co-SOEC syngas methanation, power-to-gas",
author = "Andreas Krammer",
note = "no embargo",
year = "2024",
doi = "10.34901/mul.pub.2024.206",
language = "English",
school = "Montanuniversitaet Leoben (000)",

}

RIS (suitable for import to EndNote) - Download

TY - BOOK

T1 - Methanation of CO/CO2 mixtures

AU - Krammer, Andreas

N1 - no embargo

PY - 2024

Y1 - 2024

N2 - Methanation of CO/CO2 can be used to store renewable electric energy in the form of the well-known transportable gaseous energy carrier methane, which makes it a crucial technology to transform our existing fossil-based energy infrastructure. Methanation plants suitable for industrial-scale capacity at low complexity are necessary to produce cheap renewable synthetic natural gas (SNG) from fossil or biogenic carbon sources. To achieve highly optimized methanation reactors for CO/CO2 feed, such as from high temperature Co-electrolysis (Co-SOEC), the limiting mechanisms of existing reactor systems were identified. Several reactors with different dimensions, natural air-cooling or thermal-oil cooling and under variation of process conditions including pressure and catalyst load were experimentally investigated. A 1D plug-flow reactor model in MATLAB and a 2D CFD reactor model in COMSOL Multiphysics were developed and used to verify experimental findings and deepen the understanding of the methanation process. Based on a combined modelling and experimental approach tuning parameters were derived to overcome process limitations and a strategy to design high performance methanation reactors was elaborated. Thermodynamic and kinetic limitations along the reactor axis could be identified and significantly reduced by optimizing the axial temperature curve based on appropriate reactor dimensions and operation parameters. The 1D model works as a reactor optimization and design tool for CO/CO2 mixtures and other feed gases, such as biogas or CO2. Reactor and process design examples for single-stage Co-SOEC syngas methanation, high-capacity methanation at 100.000 h-1 GHSV (gas hourly space velocity) and energy efficient dual-pressure stage methanation are presented. The findings and proposals formulated in this thesis significantly improved the process of CO/CO2 methanation with the aim to contribute to a liveable future for upcoming generations on our planet.

AB - Methanation of CO/CO2 can be used to store renewable electric energy in the form of the well-known transportable gaseous energy carrier methane, which makes it a crucial technology to transform our existing fossil-based energy infrastructure. Methanation plants suitable for industrial-scale capacity at low complexity are necessary to produce cheap renewable synthetic natural gas (SNG) from fossil or biogenic carbon sources. To achieve highly optimized methanation reactors for CO/CO2 feed, such as from high temperature Co-electrolysis (Co-SOEC), the limiting mechanisms of existing reactor systems were identified. Several reactors with different dimensions, natural air-cooling or thermal-oil cooling and under variation of process conditions including pressure and catalyst load were experimentally investigated. A 1D plug-flow reactor model in MATLAB and a 2D CFD reactor model in COMSOL Multiphysics were developed and used to verify experimental findings and deepen the understanding of the methanation process. Based on a combined modelling and experimental approach tuning parameters were derived to overcome process limitations and a strategy to design high performance methanation reactors was elaborated. Thermodynamic and kinetic limitations along the reactor axis could be identified and significantly reduced by optimizing the axial temperature curve based on appropriate reactor dimensions and operation parameters. The 1D model works as a reactor optimization and design tool for CO/CO2 mixtures and other feed gases, such as biogas or CO2. Reactor and process design examples for single-stage Co-SOEC syngas methanation, high-capacity methanation at 100.000 h-1 GHSV (gas hourly space velocity) and energy efficient dual-pressure stage methanation are presented. The findings and proposals formulated in this thesis significantly improved the process of CO/CO2 methanation with the aim to contribute to a liveable future for upcoming generations on our planet.

KW - Synthesegasmethanisierung

KW - Festbett-Methanisierung

KW - Einstufige Methanisierung

KW - Öl-gekühlte Methanisierung

KW - Co-SOEC-Syngas Methanisierung

KW - Power-to-Gas

KW - syngas methanation

KW - fixed bed methanation

KW - single-stage methanation

KW - oil-cooled methanation

KW - Co-SOEC syngas methanation

KW - power-to-gas

U2 - 10.34901/mul.pub.2024.206

DO - 10.34901/mul.pub.2024.206

M3 - Doctoral Thesis

ER -