2020
DOI: 10.1002/ente.202000746
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Dual Pressure Level Methanation of Co‐SOEC Syngas

Abstract: The objective of this article is to demonstrate significant efficiency and performance improvements by simple process modifications of a power to gas plant consisting of high‐temperature coelectrolysis and catalytic methanation. For the advanced process design dual step methanation with two different pressure levels including intermediate compression is proposed, leading to several advantages. By experimental investigations on a lab‐scale methanation test plant higher turnovers (increase of up to 7.1 percentag… Show more

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Cited by 4 publications
(3 citation statements)
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“…The methanation subsystem is considered as a two-stage and dual pressure level methanation process. This configuration was investigated by Krammer et al (2021) with relation to integration with co-electrolysis as part of the HydroMetha project. Their analyses revealed that a two-stage process with intermediate compression to up to 10 bar resulted in the highest methane concentrations in the product gas.…”
Section: System Boundary and Process Definitionmentioning
confidence: 99%
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“…The methanation subsystem is considered as a two-stage and dual pressure level methanation process. This configuration was investigated by Krammer et al (2021) with relation to integration with co-electrolysis as part of the HydroMetha project. Their analyses revealed that a two-stage process with intermediate compression to up to 10 bar resulted in the highest methane concentrations in the product gas.…”
Section: System Boundary and Process Definitionmentioning
confidence: 99%
“…For the calculations herein, a product gas composition with a methane content of 89.0% and a hydrogen content of 9.5% was assumed, resulting in an LHV of the product gas of 9.13 kWh/m 3 . Although a hydrogen content of >4 vol% does not allow for a direct feed-in to Austrian public gas grids without further processing, the product gas is presumed to be suitable for industrial combustion processes as a natural gas substitute (Krammer et al, 2021). The substitution of conventional fuels is considered equivalent to the LHV.…”
Section: System Boundary and Process Definitionmentioning
confidence: 99%
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