2013
DOI: 10.1016/j.egypro.2013.06.124
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Techno-economic Evaluation Methodology and Preliminary Comparison of an Amine-based and Advanced Solid Sorbent-based CO2 Capture Process for NGCC Power Plants

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Cited by 18 publications
(8 citation statements)
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“…They present a series of advantages such as competitive sorption capacity at low CO 2 partial pressure, faster kinetics, high CO 2 /N 2 selectivity , and excellent tolerance to moisture. High cost, susceptibility to flue gas impurities, amine degradation at higher temperatures (>100 C), and need for time consuming, energy intensive TSA are major disadvantages (Drage et al, 2009a;Xu et al, 2005;Krutka and Sjostrom, 2010;Nasr et al, 2013;Spigarelli and Kawatra, 2013). Amine-grafted materials show faster kinetics, low diffusion resistance, higher cyclic stability, and better thermal stability compared with amine-impregnated solids.…”
Section: Amine Solid Sorbentsmentioning
confidence: 97%
“…They present a series of advantages such as competitive sorption capacity at low CO 2 partial pressure, faster kinetics, high CO 2 /N 2 selectivity , and excellent tolerance to moisture. High cost, susceptibility to flue gas impurities, amine degradation at higher temperatures (>100 C), and need for time consuming, energy intensive TSA are major disadvantages (Drage et al, 2009a;Xu et al, 2005;Krutka and Sjostrom, 2010;Nasr et al, 2013;Spigarelli and Kawatra, 2013). Amine-grafted materials show faster kinetics, low diffusion resistance, higher cyclic stability, and better thermal stability compared with amine-impregnated solids.…”
Section: Amine Solid Sorbentsmentioning
confidence: 97%
“…Temperature or temperature‐pressure swing processes are the most common techniques applied in the regeneration of the sorbent. Main advantages of the AISS in comparison to aqueous MEA lay on the reduction of energy demand for regeneration due to less evaporation of water, and lower specific heat capacity of the sorbent, which allow to obtain a reduction of overall CO 2 capture costs . The heat required for the CO 2 desorption step in processes making use of AISS is around 1.5 GJ/tCO 2 ,.…”
Section: Introductionmentioning
confidence: 99%
“…Main advantages of the AISS in comparison to aqueous MEA lay on the reduction of energy demand for regeneration due to less evaporation of water, and lower specific heat capacity of the sorbent, which allow to obtain a reduction of overall CO 2 capture costs . The heat required for the CO 2 desorption step in processes making use of AISS is around 1.5 GJ/tCO 2 ,. Moreover, the use of solid sorbents like pore‐expanded mesoporous silica loaded with MEA or DEA,, avoids those energy losses associated to the partial evaporation of liquid solvent in the stripper required in MEA process ,…”
Section: Introductionmentioning
confidence: 99%
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“…Therefore, solid adsorbents have been considered for this purpose, despite most of the current capture infrastructure is based on liquid state amine based absorbents. Regardless of either adsorbents or absorbents, capture materials must include the characteristics of null (or minimum) toxicity, low corrosivity, low regeneration cost and low degradation properties . There is an increasing interest on some new alternative materials that are considered as alternative CO 2 capture solvents such as ionic liquids and deep eutectic solvents …”
Section: Introductionmentioning
confidence: 99%