2020
DOI: 10.1039/c9re00351g
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Catalytic methanation of CO2 in biogas: experimental results from a reactor at full scale

Abstract: Methanation technology for direct catalytic upgrading of CO2 in biogas is proven ready for full scale implementation.

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Cited by 69 publications
(34 citation statements)
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“…Recent demonstration projects with integration of SOEC systems with downstream synthesis processes are promising, e.g. for upgrading of biogas to pipeline quality biomethane in a pilot plant providing 10 Nm 3 /h (75). Here, a constant production was maintained for more than 2000 hours with electric power consumption for the SOEC of 3.07 kWh/Nm 3 H2 and the overall exergy efficiency from DC power to extra methane was close to 80 % (76).…”
Section: Synergies and Integration Of Soec With Chemical Synthesismentioning
confidence: 93%
“…Recent demonstration projects with integration of SOEC systems with downstream synthesis processes are promising, e.g. for upgrading of biogas to pipeline quality biomethane in a pilot plant providing 10 Nm 3 /h (75). Here, a constant production was maintained for more than 2000 hours with electric power consumption for the SOEC of 3.07 kWh/Nm 3 H2 and the overall exergy efficiency from DC power to extra methane was close to 80 % (76).…”
Section: Synergies and Integration Of Soec With Chemical Synthesismentioning
confidence: 93%
“…16 It can also be applied to convert biogas to biomethane. 17 In our previous studies, we characterized Ni/γ− Al 2 O 3 catalysts and their activity in CO 2 methanation under atmospheric pressure, 18 also in comparison with Ru/γ-Al 2 O 3 catalysts. 19 Moreover, we reported efforts to improve Ni/γ− Al 2 O 3 catalysts' activity and selectivity by adding silica and lanthana to catalyst formulation.…”
Section: ■ Introductionmentioning
confidence: 99%
“… 19 In these conditions, the Ni catalysts show low deactivation, so that the catalyst replacement can be planned for every 2 years. 20 H 2 and CO 2 were preheated to the inlet temperature by using a small fraction of the waste heat from the reactor, avoiding the need for external heating. The excess H 2 in the product stream was removed through a membrane to reach the grid-injection requirement of 2 mol per mol%.…”
Section: Methodsmentioning
confidence: 99%