2007
DOI: 10.1016/j.ssi.2007.09.007
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Transport model for a high temperature, mixed conducting CO2 separation membrane

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Cited by 74 publications
(53 citation statements)
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“…These authors used either a DC-powered system with a carbonate electrolyte or directly an MCFC system. Other authors used a composite membrane constituted by a solid oxide phase in contact with a carbonate phase [7]. By one face of the membrane, CO 2 combines with an oxide ion to become CO 3 2À and, at the opposite face, the partial pressure of CO 2 is lower causing a CO 3 2À to drop back into the solid oxide phase:…”
Section: 2mentioning
confidence: 99%
“…These authors used either a DC-powered system with a carbonate electrolyte or directly an MCFC system. Other authors used a composite membrane constituted by a solid oxide phase in contact with a carbonate phase [7]. By one face of the membrane, CO 2 combines with an oxide ion to become CO 3 2À and, at the opposite face, the partial pressure of CO 2 is lower causing a CO 3 2À to drop back into the solid oxide phase:…”
Section: 2mentioning
confidence: 99%
“…The state-of-the-art technologies for carbon capture at power/chemical plants are primarily based on the principles of physiochemical adsorption/ absorption. However, these technologies are expensive, cumbersome and energy intensive [1][2][3][4][5][6][7], making their implementation into the existing plants very difficult. Development of the next-generation cost-effective, energy-efficient and robust carbon capture technologies needs to be urgently pursued.…”
Section: Introductionmentioning
confidence: 99%
“…1(a) at 650 C, [22][23][24] significantly lower than the target value of 1 sccm cm À2 for any potential commercial use. One of the reasons for the low permeance can be ascribed to the ''inefficient'' microstructure containing poorly intra-and interconnected phases that impede ionic transport.…”
mentioning
confidence: 99%