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EN
The aim of the study was to compare the removal efficiency of toxic heavy metal ions: chromium(VI), nickel(II) and copper(II) as well as metal-complex dyes from aqueous solution using Lewatite VPOC 1065 and AdsorbsiaTM As500. The point of zero charge (pHPZC) of both sorbents and the influence of the initial concentration on the sorption process of Ni(II), Cu(II), Cr(VI), C.I. Acid Red 183 (AR183), C.I. Reactive Blue 21 (RB21) and nickel(II) phthalocyanine-tetrasulfonic acid tetrasodium salt (NiPc-TSATSS) were studied to determine the maximum sorption capacity. Kinetic studies were also carried out for the most effective sorbent-sorbate systems. The concentration effect of both hydrochloric acid and auxiliaries on the removal yield was also taken into account. As was found, Lewatit VPOC 1065 can be successfully applied for the treatment of textile wastewaters containing metal complex dyes and heavy metal ions. The highest sorption capacity, qe = 816.1 mg/g, was found for C.I. Acid Red 183.
PL
Wśród zanieczyszczeń środowiska na szczególną uwagę zasługują metale ciężkie oraz metalobarwniki, które emitowane są do środowiska z różnych gałęzi przemysłu. Z uwagi na ich negatywny wpływ na organizmy żywe niezwykle istotnym jest ich usuwanie z wód i ścieków z wykorzystaniem różnych metod, wśród których adsorpcja odgrywa istotną rolę. Celem pracy było porównanie efektywności usuwania toksycznych jonów metali ciężkich: Cr(VI), Ni(II), Cu(II) oraz metalobarwników :C.I. Acid Red 183, C.I. Reactive Blue 21, soli tetrasodowej kompleksu nikluikwasu ftalocyjanino-tetrasulfonowego z roztworów wodnych z wykorzystaniem jonitu Lewatit VPOC 1065 oraz tlenku AdsorbsiaTM As500. Wyznaczono pHPZC obu sorbentów oraz zbadano wpływ stężenia początkowego na proces sorpcji badanych sorbatów oraz kinetykę procesu sorpcji dla najbardziej efektywnego układu sorbent-sorbat. W badaniach uwzględniono także wpływ stężenia kwasu chlorowodorowego oraz wpływ substancji pomocniczych na proces sorpcji.
PL
Przedstawiono zastosowanie jonitów amfoterycznych oraz anionitów o różnej zasadowości grup funkcyjnych w procesie separacji, sorpcji i odzysku jonów metali szlachetnych ze szczególnym uwzględnieniem palladu. Zwrócono uwagę na właściwości fizykochemiczne anionitów (struktura, szkielet), ich pojemności sorpcyjne, możliwości desorpcji zatrzymanych jonów oraz mechanizm sorpcji jonów metali szlachetnych. W wybranych przypadkach (tam, gdzie warunki prowadzenia procesu sorpcji były identyczne) dokonano porównania otrzymanych wyników typując jonity najbardziej korzystne, mogące mieć duże znaczenie technologiczne.
EN
A review, with 41 refs. of properties (structure, skeleton, sorption capacity) of amphoteric and anion exchange resins, and their application, esp. for the sepn. of Pd ions.
PL
Przedstawiono zastosowanie włókien oraz jonitów chelatujących w procesie sorpcji i separacji jonów metali szlachetnych, ze szczególnym uwzględnieniem palladu. Zwrócono przede wszystkim uwagę na właściwości wspomnianych wymieniaczy jonowych, ich pojemności jonowymienne, selektywność względem metali szlachetnych i pospolitych, możliwość ich desorpcji oraz zatężania i separacji.
EN
A review, with 127 refs., of com. and synthetic resins and fibers with dithizone, thiol, (iso) thiourea, guanidine, thiosemicarbazide, dithiocarbamide, phosphonic, piperazine, imidazole, pyridine, hydrazone, hydrazide, formazane, amine and quaternary ammonium functional groups or macrocyclic ligands used for sepn. of Pd and other noble metals from aq. Solns.
EN
The sorption equilibrium and kinetics of Sunset Yellow dye in aqueous solutions on the weak base anion exchange resin — Amberlite FPA51 were examined in this paper. The influences of phase contact time, solution pH, initial dye concentration and temperature were studied by the batch method. The amounts of dye sorbed at equilibrium changed from 9.9 to 48.7 mg/g with the increasing initial concentrations in the range 100–500 mg/L. The experimental data were analyzed by the Langmuir, Freundlich, Temkin and Dubinin-Radushkevich models of adsorption. The maximum monolayer capacity was 130.6 mg/g. The sorption free energy was equal to 14.6 kJ/mol and revealed the nature of the ion exchange mechanism in this system. The kinetic data were modelled using the pseudo-first order, pseudo-second order and intraparticle diffusion equations.
EN
The strong base acrylic anion exchangers, Amberlite IRA-458, was used as an adsorbent for the investigation of acid dyes (Acid Orange 7, Acid Orange 10 and Acid Red 88) adsorption kinetics and isotherms. The pseudo-fi rst order and pseudo-second order kinetic models were used to analyze the kinetic data and good agreement between the experimental and calculated amounts of dye adsorbed at equilibrium were obtained for the pseudo-second order kinetic models for the entire investigated concentrations domain in the case all three investigated dyes. The adsorption equilibrium data were analyzed by the Langmuir and Freundlich isotherm models with the best fitting being the first one.
EN
Palladium(II) sorption was studied in hydrochloric acid solutions with sodium chloride addition onto Dowex MSA-1 and Dowex MSA-2 resins by means of the static method. The dependence between the amount of palladium(II) ions sorbed at time tin a disequilibrium state (qt) as well as the sorption capacities (qe) and phases contact time were obtained. The results were applied in kinetic studies using the pseudo-fi rst (Lagergren equation) and pseudo-second order kinetic equations (linear form of Blanchard equation proposed by Ho, PSO). Moreover, the equilibrium studies were caried out at ambient temperature and fitted to the Langmuir and Freundlich isotherms. The AFM pictures of the surface of anion exchange resins before and after the loading process were also recorded. Both resins exhibit high selectivity towards palladium(II) ions. The sorption capacities are in the range 7–10 mg/g for both resins under discussion in all examined solutions. Th e pseudo-second order kinetic equation and the Langmuir isotherm show the best fit with the experimental data.
EN
Ion exchange is Ion exchange is found more and more signifi cant importance in metal processing, and hydrometallurgy in general, not only for the removal of impurities but also for the reconcentration process of metal ions. The ion exchange method (dynamic method) was applied in the preconcentration of palladium(II) ions from the chloride solutions with sodium chloride addition. Varion resins such as the strongly basic anion exchange resins: Varion ADM and Varion ATM and the weakly basic anion exchange resin Varion ADAM were taken into account during the sorption process. The selectivity series were obtained based on the breakthrough curves of palladium(II) ions determined by means of dynamic method. Moreover, the distribution coefficients: weight and bed as well as the working anion exchange capacities were calculated. From the Varion resins — Varion ADAM is the most promising in the preconcentration of Pd(II).
EN
The weakly basic anion exchangers of the functional tertiary amine gropus with the polystyrene skeleton: Amberlyst A-21 and with acrylic skeleton: Amberlite IRA-67 were investigated as adsorbents of Remazol Black B from aqueous solutions. Experiments were carried out as function of contact time (1–240 min.), initial dye concentration (50–500 mg/dm3), pH (1–12), temperature (298–318 K) and ionic strength (NaCl). The results indicate that the investigated anion exhchangers are suitab;e as adsorbent material of Remazol Black B from aqueous solutions
11
Content available remote Application of ion exchange methods in recovery of Pd(II) ions : a review
EN
Literature data on sorption and separation of noble metal ions, especially Pd(II), on various modified chelating and commercially available ion exchangers have been reviewed.
PL
Dokonano przeglądu literatury na temat sorpcji i rozdzielenia metali szlachetnych, ze szczególnym uwzlgednieneim Pd(II), na rozmaitych modyfikowanych jonitach chela-tujących oraz na innych jonitach dostępnych w handlu.
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