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Thermal Dehydration of Calcium Hydroxide. 2. Surface Area Evolution

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TLDR
The evolution of the specific surface area associated with the thermal decomposition of calcium hydroxide has been studied experimentally and described by kinetic models utilizing two different solids as discussed by the authors.
Abstract
The evolution of the specific surface area associated with the thermal decomposition of calcium hydroxide has been studied experimentally and described by kinetic models utilizing two different solids: commercial calcium hydroxide (So = 83 m2g-') and calcium hydroxide reagent (So = 187 m2g-') The surface area was observed to vary linearly with the fraction decomposed during the dehydration period Sintering phenomena have been experimentally measured by treating calcium oxide samples (So = 46 m2g-'), obtained after dehydration of calcium hydroxide under constant conditions, at temperatures in the range 500-900 "C for periods of time up to 24 h A previously developed model, German and Munir (1976), fits the experimental results well if the surface area decreases to less than 55% of the initial value An empirical kinetic model, where the surface area is linearly related to the heating time, correlates the experimental data, when AS/So L 55% Simulated curves using the obtained kinetic models and parameters, for the specific surface during dehydration and sintering, agree well within the experimental results

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Conceptual process design of a CaO/Ca(OH)2 thermochemical energy storage system using fluidized bed reactors

TL;DR: In this paper, a thermochemical energy storage process using a CaO/Ca(OH)2 chemical loop is proposed to carry out the hydration-dehydration alternating reactions.
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Kinetics of flue gas desulfurization at low temperatures: nonideal surface adsorption model

TL;DR: In this article, a kinetic model and parameters describing best the desulfurization reaction at low temperature and at conditions prevailing in the exhaust gases of coal-fired plants are reported.
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Effect of pore geometry on the sintering of Ca-based sorbents during calcination at high temperatures

TL;DR: In this article, a mathematical model that describes the calcination and sintering of calcium-based sorbents in furnace sorbent injection (FSI) conditions is presented.
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SNRB catalytic baghouse laboratory pilot testing

TL;DR: The SOx-NOx-Rox Box (SNRB) as mentioned in this paper is an advanced air pollution process that provides for significantly reduced sulfur oxides (SO{sub x}), nitrogen oxides, and particulate emissions from coal-fired boilers.
References
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Sintering of nascent calcium oxide

TL;DR: In this article, the sintering rate of calcium oxide in a nitrogen atmosphere was measured at temperatures from 700 to 1100°C, and the model of German and Munir (J. Am. Ceram. Soc., 59, 379-383, 1976) correlates the kinetics of surface reduction and identifies lattice diffusion as the mechanism of solid transport.
Journal ArticleDOI

Surface area evolution of calcium hydroxide during calcination and sintering

TL;DR: In this paper, a simple one-dimensional mathematical model validated with high-temperature entrained-flow reactor data successfully explained dispersed calcium hydroxide particle surface area evolution resulting from concomitant calcination and sintering.
Journal ArticleDOI

Thermal Dehydration of Calcium Hydroxide. 1. Kinetic Model and Parameters

TL;DR: In this article, a pseudohomogeneous kinetic model was proposed to describe the behavior of the dehydration reaction of calcium hydroxide in the range of temperatures 330-450, which corresponds to a pseudo-ohomogenous kinetic model of the form dx PO* exp(-AH/RT) dt - = kso exp(-E, /RT) RT So(1 - x) with kinetic parameters k, = 181 X lozo cm-s-s, E, = 2804 kJmol-', po* = 1834 X lo8 atm, and
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