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Paras Trivedi

Publications and source records attributed to Paras Trivedi.

6 recordsLinked to original sources

Treatment of zinc-contaminated water using a multistage ferrihydrite sorption system.

Previous studies demonstrated the environmental and economic benefits of treating lead(II)-contaminated water streams with ferrihydrite in multiple equilibrium sorption stages. In this work, multistage ferrihydrite sorption systems were evaluated for their effectiveness in reducing single-solute zinc(II) (Zn(II)) concentrations in contaminated water streams to very low levels. As for lead(II) (Pb(II)), experimental data and modeling results indicate that a multistage sorption system can significantly reduce Zn(II) effluent concentrations for the same total amount of sorbent or, alternatively, dramatically lower total sorbent consumption for the same effluent Zn(II) concentration. Compared to Pb(II), however, Zn(II) removal requires on the order of 10 times more sorbent to achieve the same target effluent concentration for the same pH and number of stages. Model predictions were made using a steady-state, multistage, equilibrium adsorber model that was previously developed for and integrated into OLI Systems' Environmental Simulation Program (ESP). The modified triple-layer model was used to simulate Zn(II) surface-liquid equilibria within the adsorber model. Engineering screening evaluations again indicate that a 2- to 3-stage sorption process can provide significant economic savings when compared to a 1-stage process operating with the same target effluent Zn(II) concentration. Additional equilibrium stages beyond 2 or 3 provide diminishing economic returns. The major economic driver for multiple contacting stages is reduced capital investment and operating costs for sludge handling, dewatering, and disposal.

Journal Article↗

Mechanistic and thermodynamic interpretations of zinc sorption onto ferrihydrite.

Elucidating the reaction mechanisms and estimating the associated transport and thermodynamic parameters are important for an accurate description of the fate of toxic metal pollutants, such as Zn(II), in soils and aquatic ecosystems rich in iron oxides. Consequently, sorption of Zn(II) ions onto ferrihydrite was investigated with macroscopic and spectroscopic studies as a function of pH (4.0-8.0), ionic strength (10(-3)-10(-1) M NaNO(3)), aqueous Zn(II) concentration (10(-8)-10(-2) M), and temperature (4-25 degrees C). Present findings suggest that, for a given set of pH and temperature conditions, Zn sorption onto ferrihydrite can best be described by one average reaction mechanism below the saturation limits. Thermodynamic analyses reveal that the Zn(II) ions sorb onto the ferrihydrite surfaces via strong endothermic chemical reactions. Consistently, X-ray absorption spectroscopic (XAS) analyses confirm that, at pH < 6.5, for all Zn loadings, Zn(II) ions form corner-sharing, mononuclear, bidentate inner-sphere complexes with ferrihydrite, where R(Zn-O) approximately 1.97 A and R(Zn-Fe) approximately 3.48 A. For pH >/=6.5, similar sorption complexes were observed at lower sorption densities. Then again, for pH >/=6.5 and at higher sorption densities, Zn(II) ions may begin to form zinc-hydroxide-like polynuclear sorption complexes on the surfaces of the ferrihydrite, where R(Zn-Zn) approximately 3.53 A. Surprisingly, small changes in temperature had a significant impact on the affinity of zinc for the ferrihydrite surface; equilibrium sorption capacity decreased by 3-4 orders of magnitude as temperature fell from 25 to 4 degrees C for all pH. Zinc sorption onto ferrihydrite, therefore, is governed by pH as well as by temperature and sorbate/sorbent ratio.

Journal Article↗

Surface complexation modeling of zinc sorption onto ferrihydrite.

A previous study involving lead(II) [Pb(II)] sorption onto ferrihydrite over a wide range of conditions highlighted the advantages of combining molecular- and macroscopic-scale investigations with surface complexation modeling to predict Pb(II) speciation and partitioning in aqueous systems. In this work, an extensive collection of new macroscopic and spectroscopic data was used to assess the ability of the modified triple-layer model (TLM) to predict single-solute zinc(II) [Zn(II)] sorption onto 2-line ferrihydrite in NaNO(3) solutions as a function of pH, ionic strength, and concentration. Regression of constant-pH isotherm data, together with potentiometric titration and pH edge data, was a much more rigorous test of the modified TLM than fitting pH edge data alone. When coupled with valuable input from spectroscopic analyses, good fits of the isotherm data were obtained with a one-species, one-Zn-sorption-site model using the bidentate-mononuclear surface complex, (triple bond FeO)(2)Zn; however, surprisingly, both the density of Zn(II) sorption sites and the value of the best-fit equilibrium "constant" for the bidentate-mononuclear complex had to be adjusted with pH to adequately fit the isotherm data. Although spectroscopy provided some evidence for multinuclear surface complex formation at surface loadings approaching site saturation at pH >/=6.5, the assumption of a bidentate-mononuclear surface complex provided acceptable fits of the sorption data over the entire range of conditions studied. Regressing edge data in the absence of isotherm and spectroscopic data resulted in a fair number of surface-species/site-type combinations that provided acceptable fits of the edge data, but unacceptable fits of the isotherm data. A linear relationship between logK((triple bond FeO)2Zn) and pH was found, given by logK((triple bond FeO)2Znat1g/l)=2.058 (pH)-6.131. In addition, a surface activity coefficient term was introduced to the model to reduce the ionic strength dependence of sorption. The results of this research and previous work with Pb(II) indicate that the existing thermodynamic framework for the modified TLM is able to reproduce the metal sorption data only over a limited range of conditions. For this reason, much work still needs to be done in fine-tuning the thermodynamic framework and databases for the TLM.

Journal Article↗

Lead sorption onto ferrihydrite. 1. A macroscopic and spectroscopic assessment.

In this research, traditional macroscopic studies were complemented with XAS analyses to elucidate the mechanisms controlling Pb(II) sorption onto ferrihydrite as a function of pH, ionic strength, and adsorbate concentrations. Analyses of XANES and XAFS studies demonstrate that Pb(II) ions predominantly sorb onto ferrihydrite via inner-sphere complexation, not retaining their primary hydration shell upon sorption. At higher pH values (pH > or = 5.0), edge-sharing bidentate complexes are mainly formed on the oxide surface with two Fe atoms located at approximately 3.34 A. In contrast, XAS studies on Pb(II) sorption onto ferrihydrite, at pH 4.5, reveal two distinct Pb-Fe bond average radial distances of 3.34 and 3.89 A, suggestive of a mixture of monodentate and bidentate sorption complexes present at the oxide surface. Interestingly, at constant pH, the configuration of the sorption complex is independent of the adsorbate concentration. Hence, Pb(II) sorption to a highly disordered adsorbent such as ferrihydrite can be described by one average type of mechanism. Overall, this information will aid scientists and engineers in improving the current models that predict and manage the fate of toxic metals, such as Pb(II), in the aquatic and soil environments.

Adsorption↗

Lead sorpion onto ferrihydrite. 2. Surface complexation modeling.

Few studies have combined molecular- and macroscopic-scale investigations with surface complexation model (SCM) development to predict trace metal speciation and partitioning in aqueous systems over a broad range of conditions. In this work, an extensive collection of new macroscopic and spectroscopic data was used to assess the ability of the modified triple-layer model (TLM) to predict single-solute lead(II [Pb(II)] sorption onto 2-line ferrihydrite in NaNO3 solutions as a function of pH, ionic strength, and concentration. Regression of constant-pH isotherm data together with potentiometric titration and pH edge data was a much more rigorous test of the TLM than fitting pH edge data alone. When combined with spectroscopic data, the choices of feasible surface species/site types were limited to a few. In agreement with the spectroscopic data, very good fits of the isotherm data were obtained with a two-species, one-site model using the bidentate-mononuclear/monodentate-mononuclear species pairs, ((is equivalent)FeO)2Pb/(is equivalent)FeOHPb2+ and ((is equivalent)FeO)2Pb/ (is equivalent)FeOPb+-NO3-. Regressing edge data in the absence of isotherm and spectroscopic data resulted in a fair number of surface-species/site-type combinations that provided acceptable fits of the edge data but unacceptable fits of the isotherm data. Surprisingly, best-fit equilibrium "constants" for the Pb(II) surface complexes required adjustment outside the pH range of 4.5-5.5 in order to fit the isotherm data. In addition, a surface activity term was needed to reduce the ionic strength dependence of sorption forthe species pair, ((is equivalent)FeO)2Pb/(is equivalent)FeOHPb2+. In light of this, the ability of existing SCMs to predict Pb(II) sorption onto 2-line ferrihydrite over a wide range of conditions seems questionable. While many advances have been made over the past decade, much work still needs to be done in fine-tuning the thermodynamic framework and databases for the SCMs.

Adsorption↗

Lead sorption onto ferrihydrite. 3. Multistage contacting.

Few studies have demonstrated the practical application of surface complexation models, calibrated with fundamental macroscopic and spectroscopic metal sorption data, in helping to solve industrial trace metal emissions problems. In this work, multistage ferrihydrite sorption systems are evaluated for their effectiveness in reducing single-solute lead(II) [Pb(II)] concentrations in contaminated water streams to very low levels. Experimental data and modeling results indicate that a multistage sorption system can significantly reduce Pb(II) effluent concentrations for the same total amount of sorbent or, alternatively, dramatically lower total sorbent consumption for the same effluent Pb(II) concentration. Model predictions were generated using a steady-state, multistage, equilibrium adsorber model that was specifically developed for and integrated into 0LI Systems' Environmental Simulation Program. The modified triple-layer model was used to simulate Pb(II) surface-liquid equilibria within the adsorber model. Engineering screening evaluations indicate that a 2-3-stage sorption process can provide significant economic savings when compared to a 1-stage process operating with the same target effluent Pb(II) concentration. Additional equilibrium stages beyond 2 or 3 provide diminishing economic returns. The major economic driver for multiple contacting stages is reduced capital investment and operating costs for sludge handling, dewatering, and disposal.

Adsorption↗