2010
DOI: 10.1016/j.gca.2010.03.022
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Reactive transport of gentisic acid in a hematite-coated sand column: Experimental study and modeling

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Cited by 28 publications
(29 citation statements)
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“…The minute differences in the optimized adsorption constants (logK) among different columns reflect the slight variation in adsorption conditions. This fine-tuning approach is similar to previous studies where the parameters obtained from batch adsorption have to be modified to satisfactorily approximate the column data (Hanna et al 2010;Jing et al 2009). For example, the surface area had to be decreased to simulate a gentisic acid transport process in hematite-coated sand column according to batch experiments due to inaccessibility of the reactive surface sites (Hanna et al 2010).…”
Section: Field Column Resultsmentioning
confidence: 86%
“…The minute differences in the optimized adsorption constants (logK) among different columns reflect the slight variation in adsorption conditions. This fine-tuning approach is similar to previous studies where the parameters obtained from batch adsorption have to be modified to satisfactorily approximate the column data (Hanna et al 2010;Jing et al 2009). For example, the surface area had to be decreased to simulate a gentisic acid transport process in hematite-coated sand column according to batch experiments due to inaccessibility of the reactive surface sites (Hanna et al 2010).…”
Section: Field Column Resultsmentioning
confidence: 86%
“…(3) to be about 7.4, 7.8 and 7.9 mg g À1 for RCS and 77.1, 81.9 and 97.2 mg g À1 for Mg-B for initial lead(II) concentrations of 25, 50 and 100 mg L À1 , respectively. These adsorption capacities were significantly lower than the ones obtained in batch mode (See section 3.2) which could be due to the fact that in batch mode, the adsorbents particles move freely in the aqueous solutions which provides better interactions between active sites of the solid matrixes and lead ions, therefore leading to a higher mass transfer rate and consequently a higher lead retention efficiency (Bulgariu and Bulgariu, 2013;Calero et al, 2013;Hanna et al, 2010). On the other hand, for both RCS and Mg-B, the higher the used initial lead(II) concentration, the faster the appearance of the lead BTCs ( Fig.…”
Section: Lead Btcsmentioning
confidence: 76%
“…Contrary to CXTFIT, Hydrus 1D offers the possibility of BTCs prediction assuming non-linear sorption and even of reactive pollutants in presence of physical and/or chemical non-equilibrium processes. The vertical 1D transport of a non volatile and non biodegradable solute in either saturated or non saturated porous media can be described by the convection-dispersion equation as (Hanna et al, 2010):…”
Section: Hydrus 1d Modelmentioning
confidence: 99%
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“…Mass balance of colloidal particles is between 0.69 and 0.96 (Table 3), attesting to irreversible retention of colloidal particles in porous medium. As conventionally used in transfer modeling [25] [37] [38] and as a first attempt, it was considered that hydrodispersive parameters applied to reactive solutes. The model was then fitted to experimental data by optimizing only the reactive parameters.…”
Section: Transfer and Retention Of Colloidal Particlesmentioning
confidence: 99%