2005
DOI: 10.1016/j.ces.2004.09.060
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Modeling study on the impaction and humidification process in desulfurization activation reactor

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Cited by 12 publications
(7 citation statements)
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“…Due to the fact that the speed of the reaction in the liquid phase is higher than that of diffusion of the dissolved sorbent and SO 2 [28,29], one can assume that the reaction front occurs where there is zero concentration of both components, i.e., dissolved sorbent and SO 2 . This phase is called constant-rate period.…”
Section: Desulfurization Modelmentioning
confidence: 99%
“…Due to the fact that the speed of the reaction in the liquid phase is higher than that of diffusion of the dissolved sorbent and SO 2 [28,29], one can assume that the reaction front occurs where there is zero concentration of both components, i.e., dissolved sorbent and SO 2 . This phase is called constant-rate period.…”
Section: Desulfurization Modelmentioning
confidence: 99%
“…The water sprayer used a Y-type two-fluid nozzle. The droplet spray characteristics were selected according to the spray characteristics of two-fluid nozzles commonly used in semidry FGD reactors , . The average droplet diameter was about 75 µm and the spray angle was about 20°.…”
Section: Methodsmentioning
confidence: 99%
“…The contact efficiency between the spray droplets and the sorbent particles is an important parameter affecting the desulfurization efficiency in semidry FGD processes (17). The usual water spray method was a downstream water spray with the water sprayer facing upward, which prevented the negative effect of droplet deposition on the operating stability (18).…”
Section: Effect Of Water Spray Methodmentioning
confidence: 99%
“…As measured by a phase Doppler Particle Analyzer, the average diameters of fogging droplets were 50−100 μm, the fogging angles were 15−25°, and the mass flow rate of the sprayed water was 5−10 kg/h (the mass ratio of the spray water to the sorbents was 0.21−0.42 under the condition of Ca/S = 2.0); these measurements are consistent with commonly used values of droplet diameters and fogging angles. 22 The fogging nozzle was located on the centerline of the bed, 2.5 m above the distributor and 1.0 m above the sorbent feed port.…”
Section: ■ Introductionmentioning
confidence: 99%