2012
DOI: 10.1021/ef300079w
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CO2 Capture Using Phase-Changing Sorbents

Abstract: A novel method for the postcombustion capture of CO 2 from coal-fired power plants has been described utilizing an aminosilicone absorbent. 1,3-Bis(3-aminopropyl)-1,1,3,3-tetramethyldsiloxane (GAP-0) rapidly transforms from a low viscosity liquid to a friable solid upon exposure to CO 2 in simulated flue gas. This material has excellent thermal stability, low vapor pressure, high CO 2 loading capability, and a large dynamic CO 2 capacity between rich and lean solvent loadings. Preliminary plant and process mod… Show more

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Cited by 45 publications
(76 citation statements)
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“…Numerous sorbents have been developed for postcombustion CO 2 capture, which include alkanolamines (Rochelle, 2009;Rodriguez et al, 2011;Bishnoi and Rochelle, 2002;Rainbolt et al, 2011;Faramarzi et al, 2009), diamines (Zhou et al, 2010;Speyer et al, 2010), chilled ammonia (Peltier, 2008;Darde et al, 2010), CO 2 -binding organic liquids Zhang et al, 2013;Mathias et al, 2013), non-amine based solvents (Li et al, 2005;Chang et al, 2013), ionic liquids (Bates et al, 2002;Bara et al, 2009;Shannon et al, 2013), and phase-changing sorbents (Perry et al, 2010(Perry et al, , 2012. Monoethanolamine (MEA) has been the most extensively studied solvent for CO 2 capture applications (Rochelle, 2009;Liu et al, 1999;Freguia and Rochelle, 2003;Fan et al, 2009;Conway et al, 2011;Han et al, 2011;Zhu et al, 2012;Supap et al, 2001).…”
Section: Introductionmentioning
confidence: 99%
“…Numerous sorbents have been developed for postcombustion CO 2 capture, which include alkanolamines (Rochelle, 2009;Rodriguez et al, 2011;Bishnoi and Rochelle, 2002;Rainbolt et al, 2011;Faramarzi et al, 2009), diamines (Zhou et al, 2010;Speyer et al, 2010), chilled ammonia (Peltier, 2008;Darde et al, 2010), CO 2 -binding organic liquids Zhang et al, 2013;Mathias et al, 2013), non-amine based solvents (Li et al, 2005;Chang et al, 2013), ionic liquids (Bates et al, 2002;Bara et al, 2009;Shannon et al, 2013), and phase-changing sorbents (Perry et al, 2010(Perry et al, , 2012. Monoethanolamine (MEA) has been the most extensively studied solvent for CO 2 capture applications (Rochelle, 2009;Liu et al, 1999;Freguia and Rochelle, 2003;Fan et al, 2009;Conway et al, 2011;Han et al, 2011;Zhu et al, 2012;Supap et al, 2001).…”
Section: Introductionmentioning
confidence: 99%
“…(a)13 C and (b) 1 H NMR spectra of CO 2 -loaded SSA solution. Note that the peak at 4.63 ppm in panel b corresponds to the semi-deuterated water (HDO).…”
mentioning
confidence: 99%
“…It is a liquid characterised by a relatively high boiling point (265°C) and low viscosity (4 cP at 25°C). The carbonation product is GAP-0 carbamate which relatively rapidly precipitates [7]. By increasing temperature the GAP-0 carbamate is decomposed into CO 2 and the GAP-0 solvent suitable for reuse.…”
Section: Practical Examplesmentioning
confidence: 99%
“…A non-volatility property simplifies the CO 2 stripping process (there is no need for evaporated solvent separation) thereby decreasing OPEX and CAPEX. The GAP-0 based process is able to reduce energy requirements by up to 50% compared to MEA (with concentration of 30%) [7,8]. Since GAP-0 is less reactive towards CO 2 than MEA, the energy requirements reduction is greater under concentrated CO 2 gas stream conditions, i.e.…”
Section: Practical Examplesmentioning
confidence: 99%