Fixed-bed biosorption of Cu2+ by polyacrylonitrile-immobilized dead cells of Saccharomyces cerevisiae

Dead cells of Saccharomyces cerevisiae 54 were immobilized by entrappment in polyacrylonitrile. The beads obtained were used to adsorb copper in an up-flow fixed-bed column. The effect of polymer content and cell loading were studied to optimize the porosity and the efficiency in copper removal of the biosorbent beads in a batch system. The optimal concentration of the polyacrylonitrile was assumed to be 12%(w/v) and a concentration of 0.5 g cell dry weight in 1 g polymer was most effective in adsorption of Cu²⁺. The adsorption capacity of this biosorbent was 27 mg Cu²⁺/g dry biomass at 200 mg/l initial concentration of copper ions. Adsorption of Cu²⁺ in a batch system was studied using different initial concentrations of the solute. The optimal conditions in the up-flow column of the following parameters were determined: flow rate, bed height, and initial concentration of Cu²⁺ of the solutions. Results of fixed-bed biosorption showed that breakthrough and saturation time appeared to increase with the bed height, but decrease with the flow rate and the initial concentration. The linearized form of the Thomas equation was used to describe dynamic adsorption of metal ions. As a result, the adsorption capacity of the batch system and the column system was compared. Desorption of copper ions was achieved by washing the column biomass with 0.1 M HCl at an eluent flow rate of 1 ml/min. The reusability of the immobilized biomass was tested in five consecutive adsorption-desorption cycles. The regenerated beads retained over 45% of their original adsorption capacity after five A/D cycles. This revised version was published online in August 2006 with corrections to the Cover Date.     

Copper removal by immobilized Microcystis aeruginosa in continuous flow columns at different bed heights: study of the adsorption/desorption cycle

Microcystis aeruginosa immobilized in a natural polymer was tested for its potential to remove Cu²⁺ ions from aqueous solution in a continuous, downflow packed columnar reactor. Various parameters like flow rate, bed height and contact time required for maximum removal of test metals by the immobilized Microcystis aeruginosa were optimized. An increase in bed height from 2 to 10 cm resulted in an apparent decrease in biosorption capacity from 8.94 to 5.34 mg g^–1, but more Cu²⁺ solution was purified at the higher bed height. Efficiency of metal recovery from Cu²⁺-loaded biomass and its subsequent regeneration was also determined. Immobilized M. aeruginosa was found to be effective in Cu²⁺ removal from solution for up to 10 cycles of adsorption–desorption and 1 M HCl is very efficient desorbent for regeneration of Microcystis biomass for reuse.     

Biosorption of Cr, Cu and Al bySargassum biomass

The biosorption and desorption of Cr, Cu and Al were carried out using brown marine algaeSargassum fluitans biomass, known as the good biosorbent of heavy metals. The content of alginate bound to light metals could be changed by physical and chemical pretreatment. The maximum uptake of Cr, Cu and Al was independent of the alginate content. The maximum uptake of Al was two times(mole basis) than those of Cu and Cr. The aluminum-alginate complex was found in the sorption solution of raw and protonated biomass. Most of Cu, Al and light metals sorbed in the biomass were eluted at pH 1.1. However, only 5 to 10% of Cr sorbed was eluted at pH 1.1. The stoichometric ion exchange between Cu and Ca ion was observed on Cu biosorption with Ca-loaded biomass. A part of Cr ion was bound to biomass as Cr(OH)₂ ⁺ or Cr(OH)²⁺. Al was also bound to biomass as multi-valence ion and interfered with the desorbed Ca ion. The behavior of rawS. fluitans in ten consecutive sorption-desorption cycles has been investigated in a packed bed flow-through-column during a continuous removal of copper from a 35 mg/L aqueous solution at pH 5. The eluant used was a 1%(w/v) CaCl/HCl solution at pH3.     

Cu2+ Removal and recovery by Spi SORB: batch stirred and up-flow packed bed columnar reactor systems

The biosorption of Cu²⁺ by free and poly acrylamide gel (PAG) immobilized Spirulina platensis (SpiSORB) was characterized under batch and continuous packed bed columnar reaction systems. The biosorption of Cu²⁺ was shown to be highest at pH of 6.0 for both types of biomass. The PAG immobilization process did not interfere with the Cu²⁺ binding sites present on biomass leading to cent percent (ca. 250 mg g⁻¹ of dry biomass) retention of biosorption as compared to free cells. Transmission electron microscopy on Cu²⁺ localization revealed that majority of metal is being sequestered by the cell wall only. The infrared spectrum of metal treated S. platensis biomass indicated the possible involvement of amide, amino, and carboxyl groups in metal binding. Up-flow packed bed columnar reactor containing 2.0 g of PAG immobilized S. platensis shown a maximum of 143-fold volume reduction factor at the residence time of 4.6 min for Cu²⁺ alone and found to decrease dramatically when Zn²⁺ is present in a bimetallic solution.     

Metal removal by immobilised and non-immobilised Azolla filiculoides

Milled-sieved and epichlorhydrin-immobilised Azolla biosorbed ca. 363 and 320 mol Cu²⁺ g^–1 from a 100 mg l^–1 solution. Efficiency of Cu²⁺ removal by columns was in the order epichlorohydrin-immobilised Azolla>milled-sieved Azolla>untreated Azolla. The 2.5 g epichlorohydrin-immobilised Azolla column demonstrated complete metal sequestration from ca. 12 l of influent 5 mg Cu²⁺ l^–1 and was still at less than 75% saturation even after ca. 22 l had passed through the column. EDTA effectively desorbed Cu²⁺ with a ca. 55-fold decrease in volume.     

Biosorption of mercury from aqueous solution by Ulva lactuca biomass

The mercury biosorption onto non-living protonated biomass of Ulva lactuca, as an alternative method for mercury removal from aqueous solutions, was investigated. Batch equilibrium tests showed that at pH 3.5, 5.5 and 7 the maxima of mercury uptake values, according to Langmuir adsorption isotherm, were 27.24, 84.74 and 149.25 mg/g, respectively. The ability of Ulva lactuca biomass to adsorb mercury in fixed-bed column, was investigated as well. The influence of column bed height, flow rate and effluent initial concentration of metal was studied. The adsorbed metal ions were easily desorbed from the algal biomass with 0.3 N H₂SO₄ solution. After acid desorption and regeneration with distilled water, the biomass could be reused for other biosorption assays with similar performances.     

The uptake of silver ions by Escherichia coli K12: toxic effects and interaction with copper ions

Summary Growth of Escherichia coli in chloridefree medium in batch culture is inhibited completely at concentrations of AgNO₃ greater than 2.5x10^-6 M. Incubation of non-growing cells in HEPES buffer (pH 7.4) at increasing levels of Ag⁺ results in the progressive saturation of two types of binding site. At one site, the Ag⁺ is not released by washing with 0.1 M nitric acid, and is probably intracellular. Silver bound to the second site is released by acid-washing, but not by buffer washing, and is assumed to be surface-bound. The amounts of Ag⁺ taken up from solution at the two sites is 1.6x10^-7 and 4.6x10^-7 mol (mg dry weight)^-1, respectively. Total accumulation of silver is 67 mg (g dry weight)^-1, similar to literature values found for silver-resistant bacteria. Binding of Ag⁺ at intracellular sites (observed at low [Ag⁺]) appears to be independent of pH. Addition of AgNO₃ to growing cells in mid-exponential phase of growth in concentrations that will inhibit growth results in substantially decreased accumulation of silver. Growth yield in chemostat culture is diminished in the presence of added Ag⁺, but this effect is moderated by added Cu²⁺, which may protect copper sites from Ag⁺ or compete with Ag⁺ for other sites at which Ag⁺ exerts toxic effects. Very small amounts of Cu²⁺ are found in cell samples from the chemostat compared to the substantial amounts of Ag⁺ taken up, but uptake of Cu²⁺ is decreased at higher [Ag⁺]/[Cu²⁺]ratios.     

Cu-ions mediated changes in growth,chlorophyll and other ion contents in a Cu-tolerantKoeleria splendens

The effects of Cu²⁺ on growth, chlorophyll and other ion contents ofKoeleria splendens originated from Cu-contaminated soil have been investigated in nutrient solution. The most evident Cu²⁺ effects concern the root growth, especially the root length. Since in plants grown under lower Cu²⁺ concentrations (4 and 8 μM) root elongation, biomass, chlorophyll, Mg²⁺, Fe²⁺, Ca²⁺ and K⁺ content were increased compared with the control, the development of an adaptive mechanism ofK. splendens to Cu²⁺ is suggested. High Cu²⁺ concentration (160 μM) caused a significant reduction in root length and biomass as well as a decreased rate of chlorophyll biosynthesis. The reduction of growth can be correlated with the toxic effect of Cu²⁺ on photosynthesis, root respiration and protein synthesis in roots. 160 μM Cu²⁺-treatment had a negative influence on the concentrations of Ca²⁺, Fe²⁺, Mg²⁺ and K⁺ and a positive influence on the Cu²⁺ concentration in the plant tissues. Loss of nutrients similar to the senescence response suggests that excess of Cu²⁺ leads to the progressive senescence of the plants. Our results demonstrate the existence of an adaptive mechanism ofK. splendens under low Cu²⁺ concentrations, while high Cu²⁺ quantities cause disturbances in plant function.     

Optimization of flow rate,initial metal ion concentration and biomass density for maximum removal of Cu2+ by immobilized Microcystis

The potential of alginate-immobilized Microcystis packed in a column for maximum removal of Cu²⁺ at different flow rates, biomass, and initial metal ion concentration was assessed in a continuous flow system. Although Cu²⁺ removal did occur at all the flow rates tested, it was maximum (54%) at 0.75-ml min⁻¹ flow rate, 30 μg ml⁻¹ initial metal ion concentration and 0.016 g biomass. Cu²⁺ removal was influenced by inlet metal ion concentration and biomass density. An increase in the biomass concentration from 0.016 to 0.128 g resulted in an apparent increase in percentage removal but the Cu²⁺ adsorbed per unit dry wt. declined. When the flow rate (0.75 ml min⁻¹) and biomass density (0.064 g) were kept constant and the inlet metal ion concentration was varied from 10 to 150 μg ml⁻¹, a 68% removal of Cu²⁺ was obtained at 50 μg ml⁻¹ initial concentration in a time duration of 15 min. The metal-laden columns were efficiently desorbed and regenerated following elution with double distilled water (DDW) (pH 2) (89%). This was followed by 1 mm EDTA > 1 mm NTA > 0.1 mm EDTA > 1 mm HCl > 1 mm HNO₃ > 5 mm CaCl₂ > DDW (pH 7.0) > 1 mm NaHCO₃ > 1 mm CaCl₂. Of the total (2.83 mg) adsorbed Cu²⁺, 1.89 mg (67%) was desorbed by DDW (pH 2) within the first 20 min of elution time. Thereafter the desorption rate slowed down and only 22% (0.632 mg) desorption was obtained in the last 20 min. In contrast to water pH 2, the desorption of Cu²⁺ by 1 mm EDTA was very slow, the maximum being 8% after 40 min of elution. This revised version was published online in July 2006 with corrections to the Cover Date.     

Protective effects of pretreatment with Fe2+, Cu2+, and Rb+ on phoxim poisoning in silkworm,Bombyx mori

BackgroundPhoxim is a widely used organophosphorus pesticide in agriculture. People are paying more and more attention to its toxicity. At present, there is no appropriate way to solve the phoxim poisoning of silkworm, which severely affected the development of sericulture. Fe²⁺, Cu²⁺, Rb⁺ exerted their biological effects through various forms in vivo.MethodsTo evaluate the effect of Fe²⁺/Cu²⁺/Rb⁺ on phoxim poisoning in silkworm, Bombyx mori were treated with fresh mulberry leaves soaked in 2.5 mg/L phoxim for 2 min with 50 mg/L FeCl₂, 150 mg/L CuCl₂, or 0.5 mg/L RbCl from 5 days of the fifth-instar silkworm.ResultsFe²⁺, Cu²⁺, and Rb⁺ pretreatments significantly inhibited the phoxim-induced reduction of survival rate and alleviated the phoxim-induced poisoning symptoms. The protective effects of Fe²⁺, Cu²⁺, and Rb⁺ on phoxim poisoning might be due to their enhancement of superoxide dismutase (SOD), catalase (CAT), and carboxylesterase (CarE) in the hemolymph and fat body of silkworm. This enhancement might reduce reactive oxygen species (ROS) accumulation and oxidative stress (OS) caused by phoxim poisoning. Thereby it reduced the damage to silkworm tissues and cells.ConclusionsThese results showed that Fe²⁺, Cu²⁺, and Rb⁺ treatments protected the silkworm from phoxim poisoning by directly enhancing the activity of SOD, CAT, and CarE enzymes and reducing oxidative stress, but not dependent on the high expression of CYP genes. The use of Fe²⁺, Cu²⁺, and Rb⁺ to enhance the activity of SOD, CAT, and CarE enzymes may be an underlying effective way to solve phoxim poisoning in the silkworm industry.     

Modeling of Pb(II) adsorption by a fixed-bed column

Removal of Pb(II) from an aqueous environment using biosorbents is a cost-effective and environmentally benign method. The biosorption process, however, is little understood for biosorbents prepared from plant materials. In this study, the biosorption process was investigated by evaluating four adsorption models. A fixed-bed column was prepared using a biosorbent prepared from the aquatic plant Hydrilla verticillata. The effect of bed height and flow rate on the biosorption process was investigated. The objective of the study was to determine the ability of H. verticillata to biosorb Pb(II) from an aqueous environment and to understand the process, through modeling, to provide a basis to develop a practical biosorbent column. Experimental breakthrough curves for biosorption of 50 mg L^?1 aqueous Pb(II) using a fixed-bed column with 1.00 cm inner diameter were fitted to the Thomas, Adams-Bohart, Belter, and bed depth service time (BDST) models to investigate the behavior of each model according to the adsorption system and thus understand the adsorption mechanism. Model parameters were evaluated using linear and nonlinear regression methods. The biosorbent removed 65% (82.39 mg g^?1 of biosorbent) of Pb(II) from an aqueous solution of Pb(NO₃)₂ at a flow rate of 5.0 ml min^?1 in a 10 cm column. Na₂CO₃ was used to recover the adsorbed Pb(II) ions as PbCO₃ from the biosorbent. The Pb(II) was completely desorbed at a bed height of 10.0 cm and a flow rate of 5.0 ml min^?1. Fourier transform infrared (FT-IR) analysis of the native biosorbent and Pb(II)-loaded biosorbent indicated that the hydroxyl groups and carboxylic acid groups were involved in the metal bonding process. The FT-IR spectrum of Pb(II)-desorbed biosorbent showed an intermediate peak shift, indicating that Pb(II) ions were replaced by Na⁺ ions through an ion-exchange process. Of the four models tested, the Thomas and BDST models showed good agreement with experimental data. The calculated bed sorption capacity N₀ and rate constant k_a were 31.7 g L^?1 and 13.6 × 10^?4 L mg^?1 min^?1 for the C_t/C₀ value of 0.02. The BDST model can be used to estimate the column parameters to design a large-scale column.     

Biosorption Performance of Multimetal Resistant Fungus Penicillium chrysogenum XJ-1 for Removal of Cu2+ and Cr6+ from Aqueous Solutions

Adsorption for heavy metals via biomaterials such as fungal biomass presents a practical remediation technique for polluted water. Among all known filamentous fungi, Penicillium chrysogenum is widespread in nature and can serve as a biosorbent for heavy metals. In the current study, the ability of P. chrysogenum XJ-1 to remove copper (Cu²⁺) and chromium (Cr⁶⁺) from water was evaluated. The maximum biosorption capacity of XJ-1 for Cu²⁺ reached 42.83 ± 0.57 mg g^?1 dry biomass at pH 5.0 after the equilibrium time of 1.5 h. The maximum biosorption capacity for Cr⁶⁺ at pH 3.0 reached 52.69 ± 1.68 mg g^?1 dry biomass after the equilibrium time of 1.5 h. The biosorption data of XJ-1 biomass were well fitted to the Freundlich isotherm model and the pseudo-second-order Lagergren kinetic model. Laundry powder-treated and HCl-treated XJ-1 biomass significantly enhanced its adsorption capacity to Cu²⁺ and Cr⁶⁺, respectively. HCl and NaOH were suitable desorbents for Cu²⁺/Cr⁶⁺ loading biomass, respectively. Fourier transform infrared spectroscopy analyses revealed that hydroxyl, amine, and sulfonyl groups on the biosorbent contributed to binding Cu²⁺ and Cr⁶⁺ and that carbonyl and carboxyl groups were also vital binding sites of Cu²⁺. Scanning electron microscopy and energy-dispersive x-ray (SEM-EDX) analyses confirmed that considerable amounts of metals were precipitated on the cell surface of XJ-1. Our results suggested that XJ-1 might be used to purify multimetal-contaminated water. This low-cost and eco-friendly biomass of XJ-1 seems to have a broad use in the restoration of metal-contaminated water.     

Copper biosorption in an aerobic bioreactor

Abstract

This study evaluates the biosorption of copper by aerobic biomass that was selected from surface waters of the San Pedro River in Sonora, Mexico. Using a batch system, 73% biosorption of copper was obtained in 75 minutes. Continuous biosorption assays were carried out for 133 days in an ascending flow aerobic reactor packed with zeolite (AFAR-PZ) that was inoculated with a bacterial consortium. Strains were grown until 1g L^?1 of biomass was obtained. Tests using continuous biosorption were performed as follows: (i) the addition of 50 mg Cu²⁺ L^?1 without recirculation of biomass; (ii) the addition of 20 mg Cu²⁺ L^?1without recirculation of biomass; and (iii) the biomass were recirculated with the addition of 20 mg Cu²⁺ L^?1 to pH 3 to 4. The fourth and fifth assays varied pH between 4 and 5, with 20 mg Cu²⁺ L^?1and the biomass recirculated. Biosorption capacity of the first and second assays was 96% on the first day of experimentation. During the third trial 97% of biosorption was obtained during 6 days and the process was improved by varying the pH. Copper biosorption equilibrium was investigated under the same operating conditions. Langmuir adsorption isotherms were used to fit experimental data. The biosorption capacity of aerobic biomass was 3.08 mmol g^?1. It was demonstrated that this biomass is capable of biosorbing copper and this method has potential for the treatment of industrial effluents contaminated with heavy metals.     

Copper(II)-induced secondary structure changes and reduced folding stability of the prion protein

The cellular isoform of the prion protein PrP^C is a Cu²⁺-binding cell surface glycoprotein that, when misfolded, is responsible for a range of transmissible spongiform encephalopathies. As changes in PrP^C conformation are intimately linked with disease pathogenesis, the effect of Cu²⁺ ions on the structure and stability of the protein has been investigated. Urea unfolding studies indicate that Cu²⁺ ions destabilise the native fold of PrP^C. The midpoint of the unfolding transition is reduced by 0.73 ± 0.07 M urea in the presence of 1 mol equiv of Cu²⁺. This equates to an appreciable difference in free energy of unfolding (2.02 ± 0.05 kJ mol^− 1 at the midpoint of unfolding). We relate Cu²⁺-induced changes in secondary structure for full-length PrP(23-231) to smaller Cu²⁺ binding fragments. In particular, Cu²⁺-induced structural changes can directly be attributed to Cu²⁺ binding to the octarepeat region of PrP^C. Furthermore, a β-sheet-like transition that is observed when Cu ions are bound to the amyloidogenic fragment of PrP (residues 90-126) is due only to local Cu²⁺ coordination to the individual binding sites centred at His95 and His110. Cu²⁺ binding does not directly generate a β-sheet conformation within PrP^C; however, Cu²⁺ ions do destabilise the native fold of PrP^C and may make the transition to a misfolded state more favourable.     

Biosorption of copper by fungal melanin

Summary Melanin obtained from Aureobasidium pullulans and Cladosporium resinae was an efficient biosorbent for copper. Copper uptake could be expressed using various adsorption isotherms; melanin from A. pullulans obeyed Freundlich and Langmuir isotherms whereas C. resinae melanin followed the BET isotherm indicating a more complex type of adsorption than in A. pullulans. In general, uptake capacities of melanin were greater than for intact biomass and the higher uptake by pigmented rather than albino biomass could be correlated with the presence of melanin. Cu²⁺ was less readily desorbed from melanin by dilute mineral acids than from intact biomass and again, the relative ease of Cu²⁺ desorption from pre-loaded pigmented or albino biomass was correlated with the presence or absence of melanin. Mg²⁺ and Zn²⁺ appeared to be the most effective cations for desorption with Na⁺ and K⁺ the least effective. The addition of melanin to a coppercontaining culture of the albino strain of A. pullulans resulted in some reduction of toxicity.     

Multi-metal biosorption and bioaccumulation by Exiguobacterium sp. ZM-2

The present work deals with the biosorption performance of dried and non-growing biomasses of Exiguobacterium sp. ZM-2, isolated from soil contaminated with tannery effluents, for the removal of Cd²⁺, Ni²⁺, Cu²⁺, and Zn²⁺ from aqueous solution. The metal concentrations studied were 25 mg/l, 50 mg/l, 100 mg/l, 150 mg/l and 200 mg/l. The effect of solution pH and contact time was also studied. The biosorption capacity was significantly altered by pH of the solution. The removal of metal ions was conspicuously rapid; most of the total sorption occurred within 30 min. The sorption data have been analyzed and fitted to the Langmuir and Freundlich isotherm models. The highest Q_max value was found for the biosorption of Cd²⁺ at 43.5 mg/g in the presence of the non-growing biomass. Recovery of metals (Cd²⁺, Zn²⁺, Cu²⁺ and Ni²⁺) was found to be better when dried biomass was used in comparison to non-growing biomass. Metal removal through bioaccumulation was determined by growing the bacterial strain in nutrient broth amended with different concentrations of metal ions. This multi-metal resistant isolate could be employed for the removal of heavy metals from spent industrial effluents before discharging them into the environment.     

Role of Cations in Accumulation and Release of Phosphate by Acinetobacter Strain 210A

Cells of the strictly aerobic Acinetobacter strain 210A, containing aerobically large amounts of polyphosphate (100 mg of phosphorus per g [dry weight] of biomass), released in the absence of oxygen 1.49 mmol of P_i, 0.77 meq of Mg²⁺, 0.48 meq of K⁺, 0.02 meq of Ca²⁺, and 0.14 meq of NH₄⁺ per g (dry weight) of biomass. The drop in pH during this anaerobic phase was caused by the release of 1.8 protons per PO₄³⁻ molecule. Cells of Acinetobacter strain 132, which do not accumulate polyphosphate aerobically, released only 0.33 mmol of P_i and 0.13 meq of Mg²⁺ per g (dry weight) of biomass but released K⁺ in amounts comparable to those released by strain 210A. Stationary-phase cultures of Acinetobacter strain 210A, in which polyphosphate could not be detected by Neisser staining, aerobically took up phosphate simultaneously with Mg²⁺, the most important counterion in polyphosphate. In the absence of dissolved phosphate in the medium, no Mg²⁺ was taken up. Cells containing polyphosphate granules were able to grow in a Mg-free medium, whereas cells without these granules were not. Mg²⁺ was not essential as a counterion because it could be replaced by Ca²⁺. The presence of small amounts of K⁺ was essential for polyphosphate formation in cells of strain 210A. During continuous cultivation under K⁺ limitation, cells of Acinetobacter strain 210A contained only 14 mg of phosphorus per g (dry weight) of biomass, whereas this element was accumulated in amounts of 59 mg/g under substrate limitation and 41 mg/g under Mg²⁺ limitation. For phosphate uptake in activated sludge, the presence of K⁺ seemed to be crucial.     

Resolution of three forms of superoxide dismutase by immobilised metal affinity chromatography

A new method for separation of three forms of superoxide dismutase (SOD) using immobilised metal affinity chromatography (IMAC) is reported. Fe-, Mn- and Cu/Zn-SODs were eluted sequentially from Cu²⁺-IMAC column with an increasing gradient of a counter ion (NH⁺₄) run in combination with an increasing pH gradient (6.8–7.8). The combined gradient elution method resulted in separation of SODs with high resolution, the three proteins being eluted in electrophoretically homogeneous forms. Similar preparation could not be achieved by either increasing gradient of a counter ion or decreasing pH gradients used separately. The described methodology has been successfully applied for separation of three SODs from a protozoan parasite, indicating that this combined gradient elution system for IMAC offers new possibilities for the high-resolution separation of proteins exhibiting only minor differences in their amino acid composition and structure.     

Biosorption of copper(II) from aqueous solutions by green alga <Emphasis Type="Italic">Cladophora fascicularis</Emphasis>

Biosorption is an effective means of removal of heavy metals from wastewater. In this work the biosorption behavior of Cladophora fascicularis was investigated as a function of pH, amount of biosorbent, initial Cu²⁺ concentration, temperature, and co-existing ions. Adsorption equilibria were well described by Langmuir isotherm models. The enthalpy change for the biosorption process was found to be 6.86 kJ mol⁻¹ by use of the Langmuir constant b. The biosorption process was found to be rapid in the first 30 min. The presence of co-existing cations such as Na⁺, K⁺, Mg²⁺, and Ca²⁺ and anions such as chloride, nitrate, sulfate, and acetate did not significantly affect uptake of Cu²⁺ whereas EDTA substantially affected adsorption of the metal. When experiments were performed with different desorbents the results indicated that EDTA was an efficient desorbent for the recovery of Cu²⁺ from biomass. IR spectral analysis suggested amido or hydroxy, C=O, and C–O could combine strongly with Cu²⁺.     

Copper-Ligand Interactions and Physiological free Radical Processes. Part 2. Influence of Cu2+ Ions on Cu+-Driven Oh Generation and Comparison with Their Effects on Fe2+-Driven Oh Production

In our search to establish a reference ·OH production system with respect to which the reactivity of copper(II) complexes could then be tested, the influence of free Cu²⁺ ions on the Cu⁺/H₂O₂ reaction has been investigated.

This influence depends on the C_Cu²⁺/C_Cu⁺ ratio. At low Cu²⁺ concentrations, ·OH damage to various detector molecules decreases with increasing Cu²⁺ concentrations until C_Cu²⁺/C_Cu⁺ reaches unity. Above this value, ·OH damage increases sharply until C_Cu²⁺/C_Cu⁺ becomes equal to 5 with salicylate and 2 with deoxyribose, ratios for which the protective effect of Cu²⁺ cancels. Finally, at higher concentrations, Cu²⁺ ions logically add their own ·OH production to that normally expected from Cu⁺ ions. The possible origin of this unprecedented alternate effect has been discussed. The possible influence of Cu⁺ ions on the generation of ·OH radicals by water gamma radiolysis has also been tested and, as already established for Cu²⁺ in a previous work, shown to be nonexistent. This definitely confirms that either form of ionised copper cannot scavenge ·OH radicals in the absence of a Iigand.