2021
DOI: 10.1016/j.cej.2020.126330
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Metal-oxide stabilized CaO/CuO composites for the integrated Ca/Cu looping process

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Cited by 35 publications
(15 citation statements)
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“…The carbonation reaction proceeds at a slower rate than in the other three cases because of diffusion limitations and CO 2 moving through a network of narrow pores but reaches near completion within a reasonable time. 135 Lastly, Figure 3d shows a case which is most frequently observed with natural CaO-based sorbents. 112,136 A reasonably large amount of CaO is accessible for CO 2 under kinetic control, followed by a gradual decrease in the observed rate of carbonation because of increasing diffusional transport resistance within the pore network.…”
Section: Thermodynamic Properties Of Alkali Metal Oxide Sorbentsmentioning
confidence: 99%
“…The carbonation reaction proceeds at a slower rate than in the other three cases because of diffusion limitations and CO 2 moving through a network of narrow pores but reaches near completion within a reasonable time. 135 Lastly, Figure 3d shows a case which is most frequently observed with natural CaO-based sorbents. 112,136 A reasonably large amount of CaO is accessible for CO 2 under kinetic control, followed by a gradual decrease in the observed rate of carbonation because of increasing diffusional transport resistance within the pore network.…”
Section: Thermodynamic Properties Of Alkali Metal Oxide Sorbentsmentioning
confidence: 99%
“…The most expensive part of the CCS steps CO 2 capture, transport, and storage, is the capture part, and substantial efforts have been devoted to developing effective and economically feasible CO 2 capture technologies. Among these, CO 2 capture using MgO-based sorbents via a reversible carbonation/calcination reaction (MgO + CO 2 ↔ MgCO 3 ) at intermediate temperatures (300–500 °C) has gained increased interest recently. , MgO-based sorbents exhibit promising prospects due to their wide availability, low cost, nontoxicity, and high theoretical CO 2 uptake capacity (∼1.1 g of CO 2 per g of MgO). CO 2 captured by MgO-based sorbents can be released at relatively low temperatures in a less endothermic reaction compared to other solid sorbents that are commonly used, such as CaO-based sorbents; the calcination temperatures range from ∼400–500 °C for MgO-based sorbents compared to 850–950 °C for CaO-based sorbents. However, using bulk MgO as the sorbent for CO 2 capture is challenging owing to its poor sorption kinetics, resulting in a fairly low effective CO 2 uptake capacity (∼ less than 0.01 g CO 2 /g sorbent after 60 min at 400 °C in pure CO 2 ) that limits its potential use in industrial applications.…”
Section: Introductionmentioning
confidence: 99%
“…Figure 2c shows a case where only a small fraction of CaO is converted under kinetic control. The carbonation reaction proceeds at a slower rate than in the other three cases due to diffusion limitations and CO2 moving through a network of narrow pores, but reaches near completion within a reasonable time [122]. Lastly, Figure 2d shows a case which is most frequently observed with natural CaO-based sorbents [99], [123].…”
Section: Cao-caco3 Systemmentioning
confidence: 93%
“…Subsequently, the calcium cobalt oxide phase is regenerated under oxidizing conditions while releasing CO2. Calcium copper oxide is present in CaO/CuO composites that have been investigated for schemes to reduce the energy requirements for sorbent regeneration of the conventional calcium looping process [122], [397]. Here, the exothermic reduction of CuO with a reducing gas such as CH4 is used to provide the heat required for the regeneration of CaCO3 in the same particle.…”
Section: Mgo and Nano3 Interface) This Hypothesis Was Supported Expementioning
confidence: 99%