Adsorption on activated carbon is one of the methods applied for removal of heavy metals from water and wastewater contaminated with these elements. Ion exchange is a predominating mechanism in the process of sorption of ions. In case of sorption of heavy metals cations various surface aggregates are formed. Other processes, such as reduction and oxidation, and precipitation in the pores of insoluble compounds (e.g. hydroxides, carbonates) also occur. The processes behind the formation of aggregates with various degrees of resistance have a particular effect on the selectivity of ion exchange on activated carbons. The chemical composition of activated carbon surface – in particular, the presence of oxygen groups capable of ion exchange – shows the most significant effect during adsorption of heavy metals ions. Typically, the surface of the activated carbons produced with the steam-gaseous method has functional groups both of acidic and alkaline character that are capable of exchanging cations as well as anions. Carbon materials with no functional groups can also sorb protons. This is possible due to the fact that dislocated electrons π in the solutions act as Lewis base. There are a number of methods currently being investigated that would allow for improving the efficiency of adsorption of heavy metals. In the presented work the effect of ultrasonic field on the adsorption of cadmium from the model solutions was analyzed. Various configurations of ultrasonic field applied in the process of adsorption were investigated. Ultrasounds were generated in the UP 400S disintegrator. In the first phase the activated carbon in the form of granules was modified with the ultrasonic field of acoustic power density of 42,5 W/cm2or 85,0 W/cm2, at the amplitude of 30 and 60 µm, and at the exposure time of 5, 10, 15 and 20 min. Modified activated carbons were used for sorption of cadmium ions from the solutions at the initial concentrations ranging from 2,24 do 11,2 mg/dm3. The adsorption of cadmium on the activated carbon modified with ultrasounds (at the amplitude of 30 µm and 60 µm) and at the shortest exposure time (i.e. 5 min.) was higher than on the initial activated carbon. The most favorable results were obtained for the activated carbon modified with ultrasonic field with the acoustic power density of 42,5 W/cm3 and the exposure time of 10 min. The efficiency of cadmium adsorption for the highest concentration increased from 50% (the initial activated carbon) to 63%. Also, the work included the analysis of the effect of ultrasonic field on the cadmium solution with the activated carbon in the form of granules in the first phase of static adsorption. In this case, no significant differences in the adsorption capacities were observed. Also, the effect of ultrasounds on the solution used for the adsorption of cadmium did not have an impact on the efficiency of adsorption. In the final phase of the investigations the effect of sonification on the adsorption of cadmium on the powdery activated carbon was analyzed. The control sample was mechanically mixed for 5 min, and the remaining samples were subjected to the ultrasonic field at various amplitudes but with the same exposure time. The efficiency of adsorption combined with ultrasounds was significantly higher. The final concentrations during the adsorption without ultrasounds were in the range of 0,291 to 1,778 mg/dm3 whereas for the adsorption combined with ultrasounds these concentrations ranged from 0,13 to 0,748 mg/dm3.
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The study on adsorption of heavy metals (Cd(II), Ni(II) and Pb(II)) at the Al2O3-SiO2/electrolyte solution interface is presented in this paper. The influence of ionic strength, pH, background electrolyte (NaClO4) concentration and composition of metal oxide on adsorption of Cd(II), Ni(II) and Pb(II) from solution of initial concentration ranged from 1×10-6 to 1×10-3 mol/dm3 in the mentioned system was investigated. The adsorptions edge parameters (pH50% and pH10-90%) for different concentrations of electrolyte were presented. The adsorption measurements were complemented by the potentiometric titration of Al2O3-SiO2 suspensions and electrophoretic measurements. Charge reversal point (CR2) can be observed for solution concentration of 10-3 mol/dm3 as a result of Cd(II), Ni(II) and Pb(II) ions adsorption.
PL
Kadm, ołów i nikiel są toksycznymi metalami ciężkim, który stanowią wciąż poważne zagrożenie dla organizmów żywych. W środowisku naturalnym oraz w wielu procesach technologicznych mamy do czynienia ze skomplikowanymi układami gdzie występują obok siebie tlenki typu Al2O3-SiO2 oraz jony metali ciężkich. Przeprowadzono badania adsorpcji jonów niklu, kadmu i ołowiu dla różnych stężeń początkowych, w funkcji pH dla układów AS1, AS3, AS8/roztwór NaCl. Kształt krzywych adsorpcji w funkcji pH ma postać krawędzi adsorpcji. Wzrost stężenia początkowego jonów metali ciężkich, powoduje przesunięcie krawędzi w kierunku zasadowym skali pH. Wyznaczono charakterystyczne parametry krawędzi adsorpcji tj. pH50% i apH10-90%, w oparciu o zależność adsorpcji od pH stosując model TLM, obliczono równieS stałe reakcji adsorpcji jonów Ni(II), Cd(II), Pb(II) metodą optymalizacji numerycznej. Zależność gęstości ładunku powierzchniowego od pH w obecności jonów metali ciężkich, jest w dobrej korelacji z zależnością adsorpcji jonów Ni(II), Cd(II), Pb(II) od pH. Adsorpcja badanych jonów na powierzchni AS1, AS3, AS8 prowadzi do wzrostu stężenia grup ujemnie naładowanych.
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