2019
DOI: 10.1016/j.apenergy.2018.10.014
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Exergetic assessment of CO2 methanation processes for the chemical storage of renewable energies

Abstract: One option in the power-togas scenario is the methanation (Sabatier) reaction using carbon dioxide from anaerobic digestion as a carbon source and hydrogen obtained by electrolysis. The exergetic efficiencies of four process configurations for the methanation are assessed in this contribution. The specifications of the German natural gas grid are used as product quality requirement for the produced methane. The configurations are analyzed on the system level, including the acquisition of the reactants, the che… Show more

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Cited by 44 publications
(10 citation statements)
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“…is currently subject of intensive investigations due to its major role for the utilization of renewable energy for synthetic fuels and platform chemicals production. [56][57][58][59][60][61] Some studies also consider the following side-reactions to account for possible CO formation…”
Section: Dynamic Reactor Modelingmentioning
confidence: 99%
“…is currently subject of intensive investigations due to its major role for the utilization of renewable energy for synthetic fuels and platform chemicals production. [56][57][58][59][60][61] Some studies also consider the following side-reactions to account for possible CO formation…”
Section: Dynamic Reactor Modelingmentioning
confidence: 99%
“…Figure 4 illustrates the described process. Chemical heat storage offers several advantages over the other two TCHS processes [90][91][92][93][94][95][96][97][98][99][100][101][102][103][104][105][106][107]:…”
Section: Chemical Reactions Storage Processmentioning
confidence: 99%
“…Among the various reactor types, fixed-bed reactors (FBs) are the most commonly used types for CO 2 methanation. As the CO 2 methanation reaction is thermodynamically favored at low temperatures and high pressures [9], an isothermal fixed-bed reactor (IFB) without a hot spot produces high methane selectivity, exhibits stable operation, and prevents deactivation of catalyst particles through processes such as thermal degradation (i.e., nickel sintering [2]). However, the IFB usually requires high recycling and dilution ratios, and adiabatic reactors to maintain suitable productivity [10][11][12].…”
Section: Introductionmentioning
confidence: 99%