2022
DOI: 10.1016/j.apcatb.2022.121294
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Aging study of low Ru loading dual function materials (DFM) for combined power plant effluent CO2 capture and methanation

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Cited by 24 publications
(14 citation statements)
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“…Other authors also reported degradation with the cycle number at 300ºC for physical mixtures of Na sorbent and Ru catalyst [10]. In contrast to our work, aging studies performed with 5%Ru, 6.1%Na 2 O/γ-Al 2 O 3 tablets by other authors [29] showed stable cyclic performance at 300 ºC or slow very deactivation at 320 ºC under industrially relevant conditions [34]. This suggest that the performance is very sensitive to the metal loadings and preparation method and we have to perform further optimisation of the formulation of our catalyst.…”
Section: Testing In Cycles Of Co 2 Capture and Reductioncontrasting
confidence: 95%
“…Other authors also reported degradation with the cycle number at 300ºC for physical mixtures of Na sorbent and Ru catalyst [10]. In contrast to our work, aging studies performed with 5%Ru, 6.1%Na 2 O/γ-Al 2 O 3 tablets by other authors [29] showed stable cyclic performance at 300 ºC or slow very deactivation at 320 ºC under industrially relevant conditions [34]. This suggest that the performance is very sensitive to the metal loadings and preparation method and we have to perform further optimisation of the formulation of our catalyst.…”
Section: Testing In Cycles Of Co 2 Capture and Reductioncontrasting
confidence: 95%
“…56 However, using low loadings of Ru (0.5%Ru) in the absence of Ni has led to diminished performance upon cycling, attributed to deactivation and potentially sintering upon exposure to O 2 and steam in flue gas. 20…”
Section: Effect Of Oxygen Exposure On Recycled Catalyst Performancementioning
confidence: 99%
“…To date, hybrid sorbent/catalyst materials have focused on using metal oxides, metal carbonates and metal bicarbonates as CO 2 capture agents. [8][9][10][11][12][13][14][15][16][17][18][19][20][21][22][23] Once the sorbent reaches saturation through the formation of carbonate or bicarbonate species; the reactor system is heated to an appropriate reaction temperature (300-400 °C), where H 2 is introduced to generate CH 4 . However, due to the strong carbonate/bicarbonate chemical bonds created during carbon uptake, high temperatures are necessary to completely desorb the bound CO 2 so it is available for hydrogenation.…”
Section: Introductionmentioning
confidence: 99%
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