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Product Layer Diffusion during the Reaction of Calcium Oxide with Carbon Dioxide

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TLDR
In this article, the carbonation rate of 15−20 μm, nonporous, calcium oxide crystals has been studied over a temperature range of 550−1100 °C and a CO2 pressure range of 1−11.7 atm.
Abstract
The carbonation rate of 15−20 μm, nonporous, calcium oxide crystals has been studied over a temperature range of 550−1100 °C and a CO2 pressure range of 1−11.7 atm. At temperatures greater than 600 °C, the carbonation rate decreases more rapidly with time than would be expected from diffusion through a uniform product layer and the activation energy is initially low but increases with conversion. The product layer consists of crystalline grains, and these product layer grains grow by coalescence from less than one μm diameter to the approximate dimension of the particle. The carbonation rate can be described by a model where CO2 pressure-independent grain boundary diffusion and diffusion through the carbonate crystals act in parallel. The relative importance of bulk diffusion through the product layer crystals increases with time relative to transport through the grain boundaries and has an effective activation energy of 57 kcal/mol. Diffusion through the crystal boundaries has low activation energy and l...

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Journal ArticleDOI

Adsorbent Materials for Carbon Dioxide Capture from Large Anthropogenic Point Sources

TL;DR: The CO(2) adsorption behavior of several different classes of solid carbon dioxide adsorbents, including zeolites, activated carbons, calcium oxides, hydrotalcites, organic-inorganic hybrids, and metal-organic frameworks are described.
Journal ArticleDOI

The calcium looping cycle for large-scale CO2 capture

TL;DR: The reversible reaction between CaO and CO2 is an extremely promising method of removing CO2 from the exhaust of a power station, generating a pure stream of CO2 ready for geological sequestration.
Journal ArticleDOI

Conversion Limits in the Reaction of CO2 with Lime

TL;DR: The use of calcines of natural limestones as CO2 regenerable sorbents is investigated in this paper by studying the decay of the maximum carbonation conversion during many carbonation/calcination cycles.
Journal ArticleDOI

Carbonation−Calcination Cycle Using High Reactivity Calcium Oxide for Carbon Dioxide Separation from Flue Gas

TL;DR: In this paper, a CaO sorbent obtained from precipitated calcium carbonate (PCC) was used in a reaction-based process for the separation of carbon dioxide (CO2) from flue gas.
Journal ArticleDOI

Review—calcination and carbonation of limestone during thermal cycling for CO2 sequestration

TL;DR: In this paper, a review of the literature on using lime from limestone to sequester CO 2 from combustion systems is presented, and the physical properties of calcined products after sintering and reaction are reviewed.
References
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Journal ArticleDOI

Effect of the product layer on the kinetics of the CO2‐lime reaction

TL;DR: In this paper, the kinetics of reaction between CO2 and lime are investigated in the range of 673 to 998 K with a view to examining the effects of product layer deposition and variations in the limestone calcination atmosphere.
Journal ArticleDOI

Carbon and oxygen diffusion in calcite: Effects of Mn content and PH2O

TL;DR: The diffusion rates of carbon and oxygen in two calcite crystals of different Mn contents have been studied between 500° and 800° C in a CO2-H2O atmosphere (PCO2=1−5 bars, PH2O=0.02−24 bars) labeled with 13C and 18O as discussed by the authors.
Journal ArticleDOI

Effect of CO 2 Pressure on the Reaction with CaO

TL;DR: The effect of temperature and CO2 pressure on the kinetics of the reaction CaO + CO2°CaCO3 was studied in this paper, where the reaction rapidly becomes diffusion-controlled as CaCO3 builds up on the surface of CaO.
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