2012
DOI: 10.1016/j.ijggc.2012.01.007
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Improved carbon dioxide capture using metal reinforced hydrotalcite under wet conditions

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Cited by 58 publications
(22 citation statements)
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“…A comparison between a commercial hydrotalcite and two potassium and potassium-sodium containing hydrotalcites allowed to conclude that the last one presented the highest adsorption capacity while the potassium containing hydrotalcite presented no significative deactivation after more than 50 cycles of operation [142]. Kdoped hydrotalcite-based sorbents have been reported elsewhere to present a CO2 capture capacity as high as 9 mol·kg -1 at 300 ºC but under wet conditions (Table 9) [141].…”
Section: Co2 Sorbentsmentioning
confidence: 82%
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“…A comparison between a commercial hydrotalcite and two potassium and potassium-sodium containing hydrotalcites allowed to conclude that the last one presented the highest adsorption capacity while the potassium containing hydrotalcite presented no significative deactivation after more than 50 cycles of operation [142]. Kdoped hydrotalcite-based sorbents have been reported elsewhere to present a CO2 capture capacity as high as 9 mol·kg -1 at 300 ºC but under wet conditions (Table 9) [141].…”
Section: Co2 Sorbentsmentioning
confidence: 82%
“…Different materials like hydrotalcites [140][141][142][143][144], CaO-based materials [145][146][147][148][149], lithium zirconates [150][151][152][153][154] and lithium silicates [155][156][157][158][159], among others, have been reported in the literature as CO2 sorbents for SERs applications. It is expected from a good CO2 sorbent to couple in a GSR process to present high CO2 capture capacity and selectivity at moderated temperatures (300-500 ºC), good regenerability (adequate sorptiondesorption kinetics), good hydrothermal and mechanical stability and low-cost [160][161][162][163].…”
Section: Co2 Sorbentsmentioning
confidence: 99%
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“…However, such water contents are considered to be disadvantageous due to the high vaporization costs involved at industrial scale. Moreover, even if they allow avoiding coke formation, high water contents may lead to catalyst and sorbent deactivation due to pore blocking [18]. On the contrary, lower WGFRs are not so problematic from the economic point of view since the glycerol produced through the biodiesel production process is composed by low amounts of water (3.2% water, 40% fatty matter, 33% glycerol, 23% methanol and 3.8% ash) [19].…”
Section: Effect Of Water-to-glycerol Feed Ratiomentioning
confidence: 99%
“…The charge compensating anion of hydrotalcites also influences the CO 2 capture, due to the promotion of increase of Brunauer, Emmet, and Teller (BET) specific surface (114.3 m 2 ·g −1 ). Experimental evidences also pointed that after more than 50 operative cycles, potassium hydrotalcites showed no significant decay [106]. Adsorbents like CaO-based materials, lithium zirconates and silicates show generally a lessen CO 2 capacity and slowest adsorption kinetics at 300-400 • C, regeneration temperatures above 650 • C and a moderate inactivation due to sintering of the active surfaces [101].…”
Section: General Case Studymentioning
confidence: 93%