Adsorption of gold(III), platinum(IV) and palladium(II) onto glycine modified crosslinked chitosan resin

The adsorption of Au(III), Pt(IV) and Pd(II) onto glycine modified crosslinked chitosan resin (GMCCR) has been investigated. The parameters studied include the effects of pH, contact time, ionic strength and the initial metal ion concentrations by batch method. The optimal pH for the adsorption of Au(III), Pt(IV) and Pd(II) was found to range from 1.0 to 4.0 and the maximum uptake was obtained at pH 2.0 for Au(III), Pt(IV) and Pd(II). The results obtained from equilibrium adsorption studies are fitted in various adsorption models such as Langmuir and Freundlich and the model parameters have been evaluated. The maximum adsorption capacity of GMCCR for Au(III), Pt(IV) and Pd(II) was found to be 169.98, 122.47 and 120.39mg/g, respectively. The kinetic data was tested using pseudo-first-order and pseudo-second-order kinetic models and an intraparticle diffusion model. The correlation results suggested that the pseudo-second-order model was the best choice among all the kinetic models to describe the adsorption behavior of Au(III), Pt(IV) and Pd(II) onto GMCCR. Various concentrations of HCl, thiourea and thiourea-HCl solutions were used to desorb the adsorbed precious metal ions from GMCCR. It was found that 0.7M thiourea-2M HCl solution provided effectiveness of the desorption of Au(III), Pt(IV) and Pd(II) from GMCCR. The modification of glycine on crosslinked chitosan resin (CCR) was studied by Fourier transform infrared spectrometry (FTIR) and scanning electron microscopy (SEM).     

Adsorption behaviour of Fe(II) and Fe(III) ions in aqueous solution on chitosan and cross-linked chitosan beads

A batch adsorption system was applied to study the adsorption of Fe(II) and Fe(III) ions from aqueous solution by chitosan and cross-linked chitosan beads. The adsorption capacities and rates of Fe(II) and Fe(III) ions onto chitosan and cross-linked chitosan beads were evaluated. Chitosan beads were cross-linked with glutaraldehyde (GLA), epichlorohydrin (ECH) and ethylene glycol diglycidyl ether (EGDE) in order to enhance the chemical resistance and mechanical strength of chitosan beads. Experiments were carried out as function of pH, agitation period, agitation rate and concentration of Fe(II) and Fe(III) ions. Langmuir and Freundlich adsorption models were applied to describe the isotherms and isotherm constants. Equilibrium data agreed very well with the Langmuir model. The kinetic experimental data correlated well with the second-order kinetic model, indicating that the chemical sorption was the rate-limiting step. Results also showed that chitosan and cross-linked chitosan beads were favourable adsorbers.     

Synthesis and characterization of carboxymethyl-polyaminate chitosan and its adsorption behavior toward a reactive dye

Carboxymethyl-polyaminate chitosan (DETA-CMCHS), a novel kind of amphoteric chitosan derivative, was prepared and characterized by elemental analysis, and by IR and ¹H NMR spectroscopy. The adsorption behavior of Reactive Blue (RB2) on DETA-CMCHS was also studied. Results showed that the maximum value of adsorption capacity was 1185.71 mg/g at pH 3. The adsorption kinetic behavior was fitted with a second-order reaction rate equation. The adsorption was an exothermic, irreversible and entropy-reduced process according to thermodynamic parameters, such as standard Gibbs free-energy change, enthalpy change, and entropy change, all of which were calculated from adsorption equilibrium data.     

Characteristics of molybdate-impregnated chitosan beads (MICB) in terms of arsenic removal from water and the application of a MICB-packed column to remove arsenic from wastewater

The removal of arsenic (As) species, such as As(III) and As(V), from water by molybdate-impregnated chitosan beads (MICB) in both batch and continuous operations was studied. The effects of pH, temperature, coexisting ions, and arsenic concentrations were studied in batch tests. Studies on the kinetic adsorption of MICB, the recovery of arsenic by the desorption solution, and the reuse of MICB were also carried out. The practicality and efficiency of an MCIB-packed column on arsenic removal were evaluated in a continuous system on industrial arsenic-containing wastewater discharged during the manufacture of GaAs supports. The results indicate that MICB favor the adsorption of both As(V) and As(III). The optimal pH value for As(III) and As(V) removal was 5. The adsorption of arsenic on the MICB is most likely an exothermic reaction. The effect of coexisting ions was varied and depended on their concentrations and species. The optimal desorption solution for arsenic recovery was 1M H2SO4, which resulted in a 95% efficiency for As(III) and 99% for As(V). In the continuous tests, the MICB-packed column exhibited excellent arsenic removal from wastewater without any pretreatment. These results provide strong evidence of the potential of MICB for removing As from industrial wastewaters.     

Chestnut pellicle for the recovery of gold

Recovery of Au(III) from hydrochloric acid medium by using crosslinked chestnut pellicle (CCP) gel was studied. Strong selectivity was observed for Au(III) showing negligible affinity for other precious metals and some base metal ions tested. The adsorption isotherm study exhibited the maximum loading capacity of the gel as high as 10.6 mol or about 2.1 kg gold per kg dry weight of gel. The reduction of Au(III) ion to elemental form during adsorption process is expected to be the reason of high selectivity and high capacity for Au(III). Kinetic studies at various temperatures confirm an endothermic adsorption process following the pseudo-first order rate law.     

Preparation and important functional properties of water-soluble chitosan produced through Maillard reaction

The objective of this research was to improve the solubility of chitosan at neutral or basic pH using the Maillard-type reaction method. To prepare the water-soluble chitosans, various chitosans and saccharides were used under various operating conditions. Biological and physicochemical properties of the chitosan-saccharide derivatives were investigated as well. Results indicated that the solubility of modified chitosan is significantly greater than that of native chitosan, and the chitosan-maltose derivative remained soluble when the pH approached 10. Among chitosan-saccharide derivatives, the solubility of chitosan-fructose derivative was highest at 17.1 g/l. Considering yield, solubility and pH stability, the chitosan-glucosamine derivative was deemed the optimal water-soluble derivative. Compared with the acid-soluble chitosan, the chitosan-glucosamine derivative exhibited high chelating capacity for Zn(2+), Fe(2+) and Cu(2+) ions. Relatively high antibacterial activity against Escherichia coli and Staphylococcus aureus was noted for the chitosan-glucosamine derivative as compared with native chitosan. Results suggest that the water-soluble chitosan produced using the Maillard reaction may be a promising commercial substitute for acid-soluble chitosan.     

Interaction of metal ions with nucleic acids and related compounds. II. Studies on Au(III)-nucleic acid system

The nature of interaction of Au(III) with nucleic acids was studied by using methods such as uv and ir spectrophotometry, viscometry, pH titrations, and melting-temperature measurements. Au(III) is found to interact slowly with nucleic acids over a period of several hours. The uv spectra of native calf-thymus DNA 9pH 5.6 acetate buffer containing (0.01M NaCIO₄) showed a shift in λ max to high wavelengths and an increase in optical density at 260 nm. There was a fourfold decrease in viscosity (expressed as η_sp/c). The reaction was faster at pH 4.0 and also with denatured DNA (pH 5.6) and whole yeast RNA (pH 5.6). The order of preference of Au(III) (as deduced from the time of completion of reaction) for the nucleic acids in RNA > denatured DNA > DNA. The reaction was found to be completely reversible with respect KCN. Infrared spectra of DNA-Au(III) complexes showed binding to both the phosphate and bases of DNA. The same conclusions were also arrived at by melting-temperature studies of Au(III)-DNA system. pH titrations showed liberation of two hydroxylions at r = 0.12 [r = moles of HAuCl₄ added per mole of DNA-(P)] and one hydrogen ion at r = 0.5. The probable binding sites could be N(1)/N(7) of adenine, N(7) and/or C(6)O of guanine, N(3) of cytosine and N(3) of thymine. DNAs differing in their (G = C)-contents [Clostridium perfingens DNA(G = C, 29%), salmon sperm DNA (G + C, 42%) and Micrococcus lysodeikticus DNA(G + C, 29%), salmon sperm DNA (G = C, 72%)] behaved differently toward Au(III). The hyperchromicity observed for DNAs differing in (G + C)-content and cyanide reversal titrations indicate selectivity toward ( A + T)-rich DNA at lw values of r. Chemical analysis and job's continuous variation studies indicated the existence of possible complexes above and below r = 1. The results indicate that Au(III) ions probably bind to hte phosphate group in the initial stages of the reaction, particularly at low values of r, and participation of the base interaction also increases. Cross-linking of the two strands by Au(III) may take place, but a complete collapse of the doulbe helix is not envisaged. It is probable that tilting of the bases or rotaiton of the bases around the glucosidic bond, resulting in a significant distrotion of the double helix, might take place due to binding of Au(III) to DNA.     

Comparative studies on the adsorption of Cr(VI) ions on to various sorbents

The adsorption of Cr(VI) ions onto various sorbents (chitin, chitosan, ion exchangers; Purolite CT-275 (Purolite I), Purolite MN-500 (Purolite II) and Amberlite XAD-7) was investigated. Batch adsorption experiments were carried out as a function of pH, agitation period and concentration of Cr(VI) ions. The optimum pH for Cr(VI) adsorption was found as 3.0 for chitin and chitosan. The Cr(VI) uptake by ion exchangers was not very sensitive to changes in the pH of the adsorption medium. The maximum chromium sorption occurred at approximately 50 min for chitin, 40 min for Purolite II and 30 min for chitosan, Purolite I and Amberlite XAD-7. The suitability of the Freundlich and Langmuir adsorption models were also investigated for each chromium-sorbent system. Adsorption isothermal data could be accurately interpreted by the Langmuir equation for chitosan, chitin, Purolite I and Purolite II and by the Freundlich equation for chitosan, chitin and Amberlite XAD-7. The chromium(VI) ions could be removed from the sorbents rapidly by treatment with an aqueous EDTA solution and at the same time the sorbent regenerated and also could be used again to adsorb by heavy metal ions. The results showed that, chitosan, which is a readily available, economic sorbent, was found suitable for removing chromium from aqueous solution.     

Adsorption of humic acid from aqueous solution onto irradiation-crosslinked carboxymethylchitosan

This paper presents the adsorption of humic acid from aqueous solution onto crosslinked chitosan derivative (carboxymethylchitosan), formed by additionless irradiation technique. The surface charge and swelling properties of crosslinked samples were investigated. The adsorption of humic acid onto crosslinked carboxymethylchitosan was carried out by the batch method at room temperature, and it was found to be strongly pH-dependent. Maximum amount of humic acid was adsorbed under acidic conditions at the optimum pH value of 3.5. Adsorption kinetic studies indicated the adsorption process was transport-limited at the same pH. The adsorption isotherm analysis data under various initial humic acid concentrations confirms that experimental data fitted well into the Langmuir equation. X-ray photoelectron spectroscopy (XPS) revealed that the amino groups of carboxymethylated chitosan were protonated, suggesting the formation of organic complex between the protonated amino groups and humic acid. From these preliminary evaluations, it was concluded that crosslinked carboxymethylated chitosan derivatives have a great potential in water treatment for the removal of humic acid and other polarized or electrically charged species.     

Adsorption of allopurinol and ketotifen by chitosan

The experimental work of studying the adsorption of ketotifen and allopurinol by chitosan focused on determining the solubilities and the adsorption isotherms of the adsorbates employed in this study. The adsorption of the aforementioned compounds by chitosan was studied using the rotating bottle method. The concentrations, both before and after the attainment of equilibrium, were determined with the aid of a reversed-phase high-performance liquid chromatography column. The results of these studies demonstrated that ketotifen and allopurinol are both adsorbed by chitosan. The nonlinear Langmuir-like and the Freundlich models both were applied to the experimental data. The correlation coefficients obtained from the nonlinear Langmuir-like model were better than those obtained from Freundlich model, suggesting that allopurinol and ketotifen interacted with certain specific binding sites on the chitosan surface. The allopurinol adsorption experiments indicated that the particle size of chitosan and therefore the surface area can significantly affect the Langmuir capacity constant, while the affinity constants are statistically the same. As expected from the solubility studies, the ketotifen adsorption experiments at 2 different pHs (7 and 10) showed that the adsorption affinity at pH 10 was much higher than at pH 7. What was not expected was that the capacity constants were significantly different, suggesting that further studies are needed using common ion buffers and multicomponent adsorption for the proper mechanism to be determined.     

Effect of chitosan type on protein and water recovery efficiency from surimi wash water treated with chitosan-alginate complexes

Previous research has shown that soluble protein recovery by chitosan (Chi) complexes with polyanions such as alginate (Alg) is more effective than using chitosan alone. In this study, Chi-Alg complexes were used to recover soluble proteins from surimi wash water (SWW) slightly acidified to pH 6. Six Chi samples differing in molecular weight (MW) and degree of deacetylation (DD) were used at 20, 40 and 100mg/L SWW Chi-Alg complexes prepared with a Chi:Alg mixing ratio previously optimized (MR=0.2). FTIR analysis of the solids recovered revealed the three characteristic amide bands observed in the same region for untreated SWW confirming protein adsorption by Chi-Alg. The superior effectiveness of Chi complexes was confirmed but differences among chitosan types could not be correlated to MW and DD. Experimental Chi samples with 94%, 93%, 75% and 93% DD and 22, 47, 225 and 3404 x 10(3)Da, respectively, showed 73-76% protein adsorption while a commercial chitosan sample with 84% DD and 3832 x 10(3)Da had 74-83% protein adsorption. An experimental chitosan, SY-1000 with 94% DD and 1.5 x 10(6)Da, showed the highest protein adsorption (79-86%) and turbidity reduction (85-92%) when used at 20mg/L SWW.     

Kinetic studies on the interaction of gold (III) with nucleic acids. IV. RNA-Au (III) system.

The kinetics of the interaction of Au(III) with whole yeast RNA has been studied using UV-spectrophotometry. The reaction is second order with respect to the nucleotide unit of RNA and first order with respect to Au(III) in the respective stoichiometry of 2 : 1. The effects of initial composition, temperature, ionic strength, pH and chloride ion on the kinetics have been studied. Activation energy is found to be 11.5 kcal/mol. Effect of ionic strength indicates that both the positively charged and neutral species of Au(III) take part in the rate limiting step, the former being dominant at low ionic strength. A plausible mechanism has been proposed which involves the interaction of two nucleotide units of RNA with one species of Au(III) in the rate limiting step.     

Removal of molybdate from water by adsorption onto ZnCl2 activated coir pith carbon

Removal and recovery of molybdate from aqueous solution was investigated using ZnCl2 activated carbon developed from coir pith. Studies were conducted to delineate the effects of contact time, adsorbent dose, molybdate concentration, pH and temperature. Two theoretical adsorption isotherms, namely, Langmuir and Freundlich were used to describe the experimental results. The Langmuir adsorption capacity (Q0) was found to be 18.9 mg molybdate/g of the adsorbent. Adsorption followed second order kinetics. Studies were performed at different pH values to find out the pH at which maximum adsorption occurred. The pH effect and desorption studies showed that ion exchange and chemisorption mechanism were involved in the adsorption process. Thermodynamic parameters such as DeltaG0, DeltaH0 and DeltaS0 for the adsorption were evaluated. Effect of foreign ions on adsorption of molybdate has been examined. The results showed that ZnCl2 activated coir pith carbon was effective for the removal and recovery of molybdate from water.     

Influence of molecular weight and pH on adsorption of chitosan at the surface of large and giant vesicles

This paper describes the mechanisms of adsorption of chitosan, a positively charged polyelectrolyte, on the DOPC lipid membrane of large and giant unilamellar vesicles (respectively, LUVs and GUVs). We observe that the variation of the zeta potential of LUVs as a function of chitosan concentration is independent on the chitosan molecular weight (Mw). This result is interpreted in terms of electrostatic interactions, which induce a flat adsorption of the chitosan on the surface of the membrane. The role of electrostatic interactions is further studied by observing the variation of the zeta potential as a function of the chitosan concentration for two different charge densities tuned by the pH. Results show a stronger chitosan-membrane affinity at pH 6 (lipids are negatively charged, and 40% chitosan amino groups are protonated) than at pH 3.4 (100% of protonated amino groups but zwitterionic lipids are positively charged) which confirms that adsorption is of electrostatic origin. Then, we investigate the stability of decorated LUVs and GUVs in a large range of pH (6.0 < pH < 12.0) in order to complete a previous study made in acidic conditions [Quemeneur et al. Biomacromolecules 2007, 8, 2512-2519]. A comparative study of the variation of the zeta potential as a function of the pH (2.0 < pH < 12.0) reveals a difference in behavior between naked and chitosan-decorated LUVs. This result is further confirmed by a comparative observation by optical microscopy of naked and chitosan-decorated GUVs in basic conditions (6.0 < pH < 12.0): at pH > 10.0, in the absence of chitosan, the vesicles present complex shapes, contrary to the chitosan-decorated vesicles which remain spherical, confirming thus that chitosan remains adsorbed on vesicles in basic conditions up to pH = 12.0. These results, in addition with our previous data, show that the chitosan-decorated vesicles are stable over a very broad range of pH (2.0 < pH < 12.0), which holds promise for their in vivo applications. Finally, the quantification of the chitosan adsorption on a LUV membrane is performed by zeta potential and fluorescence measurements. The fraction of membrane surface covered by chitosan is estimated to be lower than 40 %, which corresponds to the formation of a flat layer of chitosan on the membrane surface on an electrostatic basis.     

A Mechanistic Study of Au(III) Removal from Solution by Bacillus subtilis

Bacteria–Au interactions control the fate of Au in a variety of geologic systems. Although previous studies have determined that non-metabolizing Bacillus subtilis cells can remove Au(III) from solution via cell surface adsorption reactions, and that upon removal Au(III) is rapidly reduced to Au(I) and remains bound to the cell surface, the mechanism of Au(III) removal by B. subtilis is poorly understood. This study provides further constraints on the mechanisms responsible for Au(III) removal by B. subtilis by conducting batch Au(III) removal experiments as a function of pH and Au loading (Au:biomass ratio) using biomass with and without two different types of treatment: (1) a treatment to remove extracellular polymeric substances (EPS) from the biomass, and (2) a treatment to irreversibly block surface sulfhydryl sites from Au binding. The experimental results suggest that Au(III) removal can be attributed primarily to Au complexation with bacterial sulfhydryl sites, but that Au–amino binding is also important under some conditions. Our experiments also suggest that Au–sulfhydryl binding occurs predominantly on EPS molecules produced by B. subtilis, and that Au–amino binding is also important and is located within the bacterial cell envelope. These findings are the first to constrain the location of sulfhydryl-binding sites for B. subtilis biomass, and they are the first to demonstrate the important role played by bacterial EPS in the process of Au adsorption and reduction by bacteria.     

Adsorption properties of congo red from aqueous solution onto N,O-carboxymethyl-chitosan

N,O-carboxymethyl-chitosans (N,O-CMC) with different degree of substitution (DS) were synthesized under heterogeneous conditions by controlling the reaction temperature. The factors influencing adsorption capacity of N,O-CMC such as the DS of N,O-CMC, initial pH value of the dye solution and adsorption temperature for anionic dye congo red (CR) were investigated. Compared with chitosan (78.90 mg/g), N,O-CMC with the DS of 0.35 exhibited much higher adsorption capacity (330.62 mg/g) for CR at the same adsorption conditions. The adsorption kinetics and isotherms showed that the sorption processes were better fitted by pseudo-second-order equation and the Langmuir equation, respectively. The adsorption mechanism of N,O-CMC was also discussed by means of IR and XPS spectra. The results in this study indicated that N,O-CMC was an attractive candidate for removing CR from the dye wastewater.     

Synthesis of anionic poly(ethylene glycol) derivative for chitosan surface modification in blood-contacting applications

To improve blood compatibility, chitosan surface was modified by the complexa-tion-interpenetration method using an anionic derivative of poly(ethylene glycol) (PEG). Methoxypoly(ethylene glycol) sulfonate (MPEG sulfonate)-modified chitosan was prepared by allowing the base polymer to swell in an acidic medium, followed by polyelectrolyte complexation and interpenetration of MPEG sulfonate with the chitosan matrix. Addition of a strong base collapsed the base polymer to permanently immobilize the modifying agent on the surface. Electron spectroscopy for chemical analysis (ESCA) confirmed the presence of MPEG sulfonate on chitosan and the high resolution Cls peak showed an increase in -C—O- which is indicative of the ethylene oxide residues. The number of adherent platelets and the extent of platelet activation was significantly reduced on MPEG sulfonate-modified chitosan. Compared to an average of more than 66 fully activated platelets on unmodified chitosan surface, only 3.0 contact-adherent platelets were present on MPEG sulfonate-modified chitosan. Plasma recalcification time, a measure of the intrinsic coagulation reaction, was about 11.5 min in contact with modified chitosan. The results of this study show that chitosan surface can be modified by the complexation-interpenetration method with anionic PEG derivative. Surface-immobilized MPEG sulfonate was effective in preventing plasma protein adsorption and platelet adhesion and activation by the steric repulsion mechanism.     

Reversible immobilization of catalase on fibrous polymer grafted and metal chelated chitosan membrane

Poly(itaconic acid) grafted and/or Fe(III) ions incorporated chitosan membranes were used for reversible immobilization of catalase (from bovine liver) via adsorption. The influences of pH and initial catalase concentration on the immobilization capacities of the CH-g-poly(IA) and CH-g-poly(IA)-Fe(III) membranes have been investigated in a batch system. Maximum catalase adsorption onto CH-g-poly(IA) and CH-g-poly(IA)-Fe(III) membrane were found to be 6.3 and 37.8 mg/g polymer at pH 5.0 and 6.5, respectively. The CH-g-poly(IA)-Fe(III) membrane with high catalase adsorption capacity was used in the rest of the study. The K_m value for immobilized catalase on CH-g-poly(IA)-Fe(III) (25.8 mM) was higher about 1.6-fold than that of free enzyme (13.5 mM). Optimum operational temperature was observed at 40 °C, a 5 °C higher than that of the free enzyme and was significantly broader. The optimum operational pH was same for both free and immobilized catalase (pH 7.0). Thermal stability was found to increase with immobilization. Free catalase lost all its activity within 20 days whereas immobilized catalase lost 23% of its activity during the same incubation period. It was observed that the same support enzyme can be repeatedly used for immobilization of catalase after regeneration without significant loss in adsorption capacity or enzyme activity. In addition, the CH-g-poly(IA)-Fe(III) membrane prepared in this work showed promising potential for various biotechnological applications.     

Effect of bipolar membrane electrobasification on chitosanase activity during chitosan hydrolysis

Chitosanase is an enzyme that hydrolyzes chitosan, a beta-(1-4) glucosamine polymer, into size-specific oligomers that have pharmaceutical and biological properties. The aim of the present work was to use the bipolar membrane technology, in particular the OH(-) stream produced by water splitting, for inactivation of chitosanase at alkaline pH in order to terminate the enzymatic reaction producing chitosan oligomers. The objectives consisted of studying the effect of pH: (a) on the stability of chitosanase, and (b) on the catalytic activity of chitosanase during chitosan hydrolysis. The enzyme was found to be stable in the pH range of 3-8 during at least 7h, and partially lost its activity after 1h at pH 8. The catalytic activity of chitosanase during chitosan hydrolysis decreased after pH adjustment by electrobasification. The reaction rate decreased by 50% from pH 5.5 to 6, whereas the reaction was completely inhibited at pH>7. The decrease of reaction rate was due to chitosan substrate insolubilization and chitosanase denaturation at alkaline pH values.     

Adhesion and growth of HUVEC endothelial cells on films of enzymatically functionalized chitosan with phenolic compounds

Human Umbilical Vein Endothelial Cell (HUVEC) growth on chitosan films and its enzymatically functionalized derivatives films with ferulic acid (FA) and ethyl ferulate (EF) was assessed by evaluating cell adhesion, morphology and cell viability. The results indicated that chitosan derivative films improved protein adsorption properties compared to chitosan films. The HUVEC cell morphology showed well attachment and spread phenotype on chitosan derivative films compared to those growing on chitosan films which did not spread and remained round. Evaluation of cell viability revealed improvement of cell adhesion on chitosan derivative films compared to chitosan film depending on the quantity of oxidized phenols grafted on chitosan. In addition, FA-/EF-chitosan films allowed almost similar cell adhesion. Furthermore, cell adhesion was increased with the film thickness. These results suggested that the oxidized phenols grafting on chitosan is a promising process to enhance cell adhesion, growth and creating useful functional biomaterials.