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Abstract: The adsorption of a large reactive dye, Reactive Black 5, onto four adsorbents has been studied. A commercial active carbon, F400, was selected as a standard and two active carbons prepared from bamboo, a biomaterial. The two bamboo derived carbons, BACX2 and BACX6 had high specific surface areas, namely, 2123 and 1400m2/g, respectively. A fourth widely used adsorbent, bone char, was also tested. The adsorption capacities for F400, bone char, BACX2 and BACX6 were 198, 160, 286 and 473mg/g, respectively. A series of batch kinetics were carried out to investigate the rate and possible mechanism of Reactive Black 5 adsorption. Two pseudo-kinetic models and one intraparticle diffusion model were tested. The experimental concentration versus time decay curves were best explained by the intraparticle diffusion model. [Copyright &y& Elsevier]

The aim of this study was to develop a feasible and cost effective method to produce amine functionalized multi-walled carbon nanotubes (CNT-NH 2 ) and investigate the ability of this CNT-NH 2 material to adsorb anionic dyes in single and binary (mixture of dyes) systems. For this purpose, pristine CNTs were functionalized by primary and secondary functional groups namely (-NH2) and (-NH), respectively. Acid Blue 45 (AB45) and Acid Black 1 (AB1) were used as anionic dye models for adsorption. FTIR, SEM, BET, Raman Spectra, and Zeta potential measurements have been employed for characterizing the synthetic nanocomposite and these techniques indicated that the amino functionalized CNTs have been favorably synthesized. The effects of different operational parameters including pH, initial dye concentration, adsorbent dosage, and salt on dye removal were evaluated. The dye adsorption isotherm and kinetics were also studied. The results of this study indicated that the stronger interactions between CNT-NH 2 and AB1 suggest a higher adsorption of AB45 compared to AB1 in both single and binary dye systems. Moreover, the maximum adsorption capacities of the studied functionalized nanotube in single dye solutions, for AB45 and AB1 were 714 and 666 mg g −1 , respectively. These capacities are exceptionally high for the removal of acid dyes. It was found that AB45 and AB1 adsorption on the CNT-NH 2 followed the Langmuir isotherm model and pseudo-second order kinetics model in both single and binary systems. According to the results of this study the CNT-NH 2 were an effective adsorbent to remove anionic dyes from single and binary systems. [ABSTRACT FROM AUTHOR]

In this work, rice husk cellulosic sorbents are produced by both chemical and biological pretreatment. The results indicate that the sorbent pretreated by sodium hydroxide (NaOH) and hydrogen peroxide (H 2 O 2 ) contains up to 87.75% cellulosic concentration. Acetylated sorbents produced from both NaOH/H 2 O 2 and Aspergillus flavus pretreated rice husks are compared with raw rice husk and non-acetylated rice husk sorbents for oil sorption capacities. By plotting oil uptake capacity against contact time, the optimum theoretical sorption capacity of acetylated chemical pretreated rice husk sorbent is 28.2 g/g RMG 386 after 15 min dripping. The sorption data shows that the modified rice husk sorbents achieve saturation after only 3–5 min of contact with both RMG 386 marine diesel and corn oil. The experimental data of acetylated chemical pretreated rice husk sorbent is analyzed using the pseudo-first order, the pseudo-second order and the intraparticle diffusion models. The model results indicate that the pseudo-second order model accurately correlates with the oil sorption data. In terms of the equilibrium isotherm analysis, the Freundlich model provides the best fit to the experimental data. As a result, the acetylated rice husk sorbent has shown to significantly outperform the non-acetylated sorbent with a high oleophilic and hydrophobic capacity with up to 19.66 g/g RMG 386 oil uptake capacity compared to 8.26 g/g by the non-acetylated rice husk sample in an aqueous medium. [ABSTRACT FROM AUTHOR]

Abstract: The sorption of arsenate onto chitosan flakes has been studied. Chitosan, a natural, non-toxic, biodegradable polysaccharide is derived by the deacetylation of chitin, a major component of crustacean shells of prawn, crab or shrimp. Its main attributes correspond to its polycationic nature and the abundance of amine functional groups. Chitosans have received increasing attention as renewable polymeric materials for the treatment of metal contaminated water and wastewater. The effect of initial pH on the sorption isotherm has been studied for two initial concentration ranges of arsenate (0–3000μgL−1 and 0–10,000μgL−1) on chitosan. The equilibrium data have been modelled using Langmuir and Freundlich type isotherms at three initial pH values. The maximum adsorption capacity occurs at an initial pH 3.5 and empirical correlations have been developed to model the effect of pH on the sorption isotherm parameters. Each initial pH i value, namely, 3.5, 4.0 and 4.5, corresponded to a fixed final pH e value, namely, 4.69, 6.40 and 6.73 respectively. A series of batch kinetic experiments has been carried out at different initial pH values. The arsenate sorption process appears to be completed after 30min, however, a previously unreported phenomenon was observed, namely, a steady desorption of arsenate. There is a natural buffering effect from the chitosan. The batch kinetic data have been correlated using the pseudo-first order, pseudo-second order and pseudo-first order reversible models; this latter model was modified to incorporate the arsenate desorption step as a function of the changing system pH. [Copyright &y& Elsevier]

Abstract: The ability of a new ion exchange resin to remove zinc ions from effluent has been studied. The equilibrium exchange capacity has been determined as 2.7mmol/g resin and analysed using the Langmuir, Freundlich and Redlich–Peterson equations. The Redlich–Peterson gave the best-fit to the experimental data. A series of kinetic studies were carried out in an agitated batch reactor. Three variables were studied, initial zinc ion concentration, resin mass and resin particle size. The results were analysed using three kinetic models, pseudo-first order, pseudo-second order and the Elovich model. The results were compared on the basis of SSE values and the best-fit correlation of the experimental data was obtained using the Elovich model which suggests a chemisorption process. [Copyright &y& Elsevier]