2013
DOI: 10.1016/j.egypro.2013.05.087
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Post-Combustion CO2 Capture Using Solid Sorbents: 1 MWe Pilot Evaluation

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Cited by 49 publications
(33 citation statements)
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“…8 Krutka et al report on a 1 MW pilot scale multistage bubbling bed adsorber with a bubbling bed regenerator. 9 Khongprom et al proposed a circulating fluidized bed adsorber with riser as the adsorber, and a bubbling bed regenerator integrated in the downcomer. 10 Tarka et al evaluated a fluidized bed adsorber as well as novel design consisting of multiple radial flow fixed bed reactors.…”
Section: Introductionmentioning
confidence: 99%
“…8 Krutka et al report on a 1 MW pilot scale multistage bubbling bed adsorber with a bubbling bed regenerator. 9 Khongprom et al proposed a circulating fluidized bed adsorber with riser as the adsorber, and a bubbling bed regenerator integrated in the downcomer. 10 Tarka et al evaluated a fluidized bed adsorber as well as novel design consisting of multiple radial flow fixed bed reactors.…”
Section: Introductionmentioning
confidence: 99%
“…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%
“…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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“…Selection of material for CO 2 capture at different environmental and industrial conditions is still a major challenge for the energy generation sector. Large number of materials such as polymers (Du et al 2011), co-polymers (He et al 2014), organic/inorganic materials (Veselovskaya et al 2013), metal organic composites (Seema et al 2014), solids adsorbents (Krutka et al 2013), liquid absorbents (Munoz et al 2009), ionic liquids (Kumar et al 2014) and various nano-composite structures have been investigated to capture CO 2 from the flue gas. Some of the major challenges that require due attention at the material selection stage are; CO 2 capturing efficiency, reproducibility, selectivity (Seema et al 2014), capability (Markewitz et al 2012), stability at various temperature and pressure conditions (Al-Khabbaz et al 2014), multi-purpose applicability ) and economic practicability (Tzimas and Peteves 2005) of the material.…”
Section: Introductionmentioning
confidence: 99%