2003
DOI: 10.1080/10473289.2003.10466171
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Modeling Sorbent Injection for Mercury Control in Baghouse Filters: I—Model Development and Sensitivity Analysis

Abstract: A two-stage mathematical model for Hg removal using powdered activated carbon injection upstream of a baghouse filter was developed, with the first stage accounting for removal in the ductwork and the second stage accounting for additional removal caused by the retention of carbon particles on the filter. The model shows that removal in the ductwork is minimal, and the additional carbon detention time from the entrapment of the carbon particles in the fabric filter enhances the Hg removal from the gas phase. A… Show more

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Cited by 35 publications
(33 citation statements)
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“…The rate-based model showed negligible uptake under standard operating conditions. Similar results were obtained by Flora et al (2003) .…”
Section: Rsupporting
confidence: 81%
“…The rate-based model showed negligible uptake under standard operating conditions. Similar results were obtained by Flora et al (2003) .…”
Section: Rsupporting
confidence: 81%
“…A number of kinetic models that describe heavy metal adsorption processes, mainly from liquid phase, have been studied. 15,16 Some of them are based on the diffusion of gas molecules inside the adsorbent porous network, while others take into account the pollutant mass balance inside the column. A very small number of studies have examined simplified models based on a combination of internal particle and external mass transfer theories with isothermal adsorption and powdered injection procedures.…”
Section: Introductionmentioning
confidence: 99%
“…In an ideal plug flow system with no resistance to mass transfer, by neglecting the axial dispersion term and by assuming that the rate of adsorption is given by a first order kinetic expression k c, Equation 13 can be simplified to Equation 14: (15) where k is the kinetic constant, k 0 is the initial value of k and h 0 is the dimensionless variable.…”
mentioning
confidence: 99%
“…Because the diffusion coefficient of Hg in air was determined to be 0.22 cm 2 /s by Chapman-Enskog theory (Meserole et al 1999;Flora et al 2003), the dispersion coefficient was obtained using equation (2). Using equations (1) and (2), the number of layers (N) was determined to be less than 1; therefore, each layer was assumed to behave like a continuous stirred tank reactor (CSTR).…”
Section: Modelling Proceduresmentioning
confidence: 99%
“…The total length of sorbent layers in the filter was calculated based on the amount of sorbent particles accumulated in the filter at a sorbent loading of 15 mg/m 3 . An empirical correlation was used to determine the dispersion coefficient (Flora et al 2003):…”
Section: Modelling Proceduresmentioning
confidence: 99%