2011
DOI: 10.1016/j.cej.2011.01.008
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From MEA to demixing solvents and future steps, a roadmap for lowering the cost of post-combustion carbon capture

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Cited by 227 publications
(97 citation statements)
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“…The specificity of aqueous solutions is a partial miscibility. These so called "thermomorphic" biphasic amine solvents are potential absorbent for breakthrough technologies of CO 2 capture [7]. The phase separation will be induced at the output of the absorber.…”
Section: Resultsmentioning
confidence: 99%
“…The specificity of aqueous solutions is a partial miscibility. These so called "thermomorphic" biphasic amine solvents are potential absorbent for breakthrough technologies of CO 2 capture [7]. The phase separation will be induced at the output of the absorber.…”
Section: Resultsmentioning
confidence: 99%
“…It has been described with further details in [11,12] and only a quick description is given hereafter. The main objective being to present the techno-economic comparison with the MEA process.…”
Section: Dmx Tm Process Descriptionmentioning
confidence: 99%
“…The use of amines to remove CO 2 from a gas stream is well established but current interest is focused on identifying suitable blended amines to minimise cost. Monoethanolamine (MEA), the most common in use, is giving way to other amine species having improved capacity and, importantly, low regeneration energy cost (Rochelle et al [3], Raynal et al [4]). Puxty et al [5] tested a large number of amines using equilibrium capacity for CO 2 and initial absorption rate into a liquid sample exposed to a stream of 15% CO 2 as indicators of performance.…”
Section: Introductionmentioning
confidence: 99%