Abstract:1,2-Benzenedicarboxylic acid esters, commonly referred to as phthalate esters, form a group of compounds that are mainly used as plasticizers in polymers. Because phthalate esters are not chemically bound to the plastics, they can be released easily from products and migrate into the food or water that comes into direct contact. Due to their widespread use, they are considered as ubiquitous environmental pollutants. Phthalate esters are regarded as endocrine disrupting compounds by means of their carcinogenic … Show more
“…The findings are in line with earlier literature [69][70][71] which found that adsorption onto materials of natural origin is characterized by complex mechanisms, related to the heterogeneous surface of natural adsorbents and presence of a diversity of functional groups on the surface of a biomass. Therefore, several physical and chemical interactions may occur together during the sorption process.…”
Section: Proposed Adsorption Mechanismsupporting
confidence: 92%
“…Calculations were made of the free energy (ΔG ), enthalpy (ΔH ) and entropy (ΔS ) of the systems, using Eqs. (8)(9)(10): Chitosan cross-linked with glutaraldehyde 113.00 Pb 2þ [54] GLA-cross-linked metal-complexed chitosan 105.26 Pb 2þ [55] Chitosan/cotton fibers 101.53 Pb 2þ [56] Wheat bran 79.40 Pb 2þ [57] Chitosan/clay beads 72.31 Cd 2þ [58] Chitosan-alginate beads 60.27 Pb 2þ [59] Fly ash porous pellet 45.54 Pb 2þ [60] Wheat straw 41.84 Ni 2þ [61] Seed husk of Calophyllum inophyllum 34.51 Pb 2þ [62] Chitosan/glutaraldehyde 32.90 Cd 2þ [63] Hazelnut shell 28.18 Pb 2þ [64] Hyacinth roots 24.94 Pb 2þ [65] De-oiled allspice husk 20.79 Pb 2þ [66] Coal fly ash 18.98 Cd 2þ [67] Tea factory waste 18.42 Ni 2þ [68] Al-impregnated fly ash 15.75 Ni 2þ [69] Chitosan/cotton fibers (via Schiff base bond) 15.74 Cd 2þ [56] Wheat bran 12.00 Ni 2þ [70] Chitosan/cotton fibers (via Schiff base bond) 7.63 Ni 2þ [56] Results of the present study are marked in bold. where ΔG o (kJ/mol) is the change in the free energy of the system, ΔH o (kJ/mol) is the change in the free enthalpy of the system, ΔS o (kJ mol À1 K À1 ) is the change in the free entropy of the system, R (8.314 J mol À1 K À1 ) is the gas constant, K c is the reaction equilibrium constant, and T (K) is the temperature.The changes in enthalpy and entropy were calculated based on the plot of lnK c vs. 1/T, using its slope (À ΔH o R ) and y-axis intercept…”
The application of biomass derived from the nuisance fresh‐water diatom species Didymosphenia geminata toward the adsorption and removal of heavy‐metal ions from water is reported. The cell‐free polysaccharide‐based stalks of these diatoms are used as adsorbents to remove harmful metal ions: Pb(II), Ni(II), and Cd(II). Detailed analyses of the adsorption kinetics using both pseudo‐first‐order model and pseudo‐second‐order models are performed. The results show a strong correspondence to a pseudo‐second‐order kinetic model. The Langmuir and Freundlich models are used to describe the adsorption isotherms. The correlation coefficients (r2) of the Langmuir model are equal to 0.994 (Pb2+), 0.995 (Cd2+), and 0.995 (Ni2+), and the r2 for the Freundlich model are equal to 0.991 (Pb2+), 0.991 (Cd2+), and 0.987 (Ni2+). The experimental data for all metal ions strongly support the Langmuir isotherm model. It is shown that stalks of D. geminata exhibit exceptional sorption capacity (qm) for Pb(II) ions of 175.48 mg g−1. Additionally, a high sorption capacity for Cd(II) (145.86 mg g−1), and Ni(II) (130.27 mg g−1) is observed. The thermodynamic aspects of the adsorption process of selected metal ions are also discussed. Preliminary tests investigating applications of D. geminata stalks for sewage purification from galvanic industry and battery and accumulator production were performed. These comprehensive studies show that D. geminata can be robustly applied for the removal of harmful metal ions from wastewater.
“…The findings are in line with earlier literature [69][70][71] which found that adsorption onto materials of natural origin is characterized by complex mechanisms, related to the heterogeneous surface of natural adsorbents and presence of a diversity of functional groups on the surface of a biomass. Therefore, several physical and chemical interactions may occur together during the sorption process.…”
Section: Proposed Adsorption Mechanismsupporting
confidence: 92%
“…Calculations were made of the free energy (ΔG ), enthalpy (ΔH ) and entropy (ΔS ) of the systems, using Eqs. (8)(9)(10): Chitosan cross-linked with glutaraldehyde 113.00 Pb 2þ [54] GLA-cross-linked metal-complexed chitosan 105.26 Pb 2þ [55] Chitosan/cotton fibers 101.53 Pb 2þ [56] Wheat bran 79.40 Pb 2þ [57] Chitosan/clay beads 72.31 Cd 2þ [58] Chitosan-alginate beads 60.27 Pb 2þ [59] Fly ash porous pellet 45.54 Pb 2þ [60] Wheat straw 41.84 Ni 2þ [61] Seed husk of Calophyllum inophyllum 34.51 Pb 2þ [62] Chitosan/glutaraldehyde 32.90 Cd 2þ [63] Hazelnut shell 28.18 Pb 2þ [64] Hyacinth roots 24.94 Pb 2þ [65] De-oiled allspice husk 20.79 Pb 2þ [66] Coal fly ash 18.98 Cd 2þ [67] Tea factory waste 18.42 Ni 2þ [68] Al-impregnated fly ash 15.75 Ni 2þ [69] Chitosan/cotton fibers (via Schiff base bond) 15.74 Cd 2þ [56] Wheat bran 12.00 Ni 2þ [70] Chitosan/cotton fibers (via Schiff base bond) 7.63 Ni 2þ [56] Results of the present study are marked in bold. where ΔG o (kJ/mol) is the change in the free energy of the system, ΔH o (kJ/mol) is the change in the free enthalpy of the system, ΔS o (kJ mol À1 K À1 ) is the change in the free entropy of the system, R (8.314 J mol À1 K À1 ) is the gas constant, K c is the reaction equilibrium constant, and T (K) is the temperature.The changes in enthalpy and entropy were calculated based on the plot of lnK c vs. 1/T, using its slope (À ΔH o R ) and y-axis intercept…”
The application of biomass derived from the nuisance fresh‐water diatom species Didymosphenia geminata toward the adsorption and removal of heavy‐metal ions from water is reported. The cell‐free polysaccharide‐based stalks of these diatoms are used as adsorbents to remove harmful metal ions: Pb(II), Ni(II), and Cd(II). Detailed analyses of the adsorption kinetics using both pseudo‐first‐order model and pseudo‐second‐order models are performed. The results show a strong correspondence to a pseudo‐second‐order kinetic model. The Langmuir and Freundlich models are used to describe the adsorption isotherms. The correlation coefficients (r2) of the Langmuir model are equal to 0.994 (Pb2+), 0.995 (Cd2+), and 0.995 (Ni2+), and the r2 for the Freundlich model are equal to 0.991 (Pb2+), 0.991 (Cd2+), and 0.987 (Ni2+). The experimental data for all metal ions strongly support the Langmuir isotherm model. It is shown that stalks of D. geminata exhibit exceptional sorption capacity (qm) for Pb(II) ions of 175.48 mg g−1. Additionally, a high sorption capacity for Cd(II) (145.86 mg g−1), and Ni(II) (130.27 mg g−1) is observed. The thermodynamic aspects of the adsorption process of selected metal ions are also discussed. Preliminary tests investigating applications of D. geminata stalks for sewage purification from galvanic industry and battery and accumulator production were performed. These comprehensive studies show that D. geminata can be robustly applied for the removal of harmful metal ions from wastewater.
“…As reported in Table , the extraction efficiency ranged between 10–12 and 2–3% for HMHA and 3MSH, respectively, depending on the concentration level. The extraction efficiency values obtained are comparable to similar methods that use DI‐SPME extraction for the determination of other compounds, such as polycyclic aromatic hydrocarbons , phthalate esters , and pesticides . It must be noted that, in several studies , the extraction efficiency was considerably improved when using HS‐SPME extraction instead of DI‐SPME, especially when analyzing non‐polar compounds.…”
Section: Resultssupporting
confidence: 58%
“…Moreover, SPME generally provides low detection limits and good reproducibility both in headspace and in direct immersion (DI) mode [23][24][25][26]. In DI mode, SPME was successfully tested in aqueous systems for the determination of organic compounds [27][28][29][30][31], proving a promising alternative to conventional extraction methods.…”
Direct immersion solid-phase microextraction with gas chromatography and mass spectrometry for the determination of specific biomarkers of human sweat in melted snowTo provide a reliable tool for investigating diffusion processes of the specific components of the human odor 3-hydroxy-3-methylhexanoic acid and 3-methyl-3-sulfanylhexan-1-ol through the snowpack, we developed and optimized an analytical method based on direct immersion solid-phase microextraction followed by gas chromatography with mass spectrometry. Direct immersion solid-phase microextraction was performed using polyacrylate fibers placed in aqueous solutions containing 3-hydroxy-3-methylhexanoic acid and 3-methyl-3-sulfanylhexan-1-ol. After optimization, absorption times of 120 min provided a good balance to shorten the analysis time and to obtain suitable amounts of extractable analytes. The extraction efficiency was improved by increasing the ionic strength of the solution. Although the absolute extraction efficiency ranged between 10 and 12% for 3-hydroxy-3-methylhexanoic acid and 2-3% for 3-methyl-3-sulfanylhexan-1-ol, this method was suitable for analyzing 3-hydroxy-3-methylhexanoic acid and 3-methyl-3-sulfanylhexan-1-ol concentrations of at least 0.04 and 0.20 ng/mL, respectively. The precision of the direct immersion solid-phase microextraction method ranged between 8 and 16%. The variability within a batch of six fibers was 10-18%. The accuracy of the method provided values of 88-95 and 86-101% for 3-hydroxy-3-methylhexanoic acid and 3-methyl-3-sulfanylhexan-1-ol, respectively. The limit of detection (and quantification) was 0.01 ng/mL (0.04 ng/mL) for 3-hydroxy-3-methylhexanoic acid and 0.06 ng/mL (0.20 ng/mL) for 3-methyl-3-sulfanylhexan-1-ol. The signal versus concentration was linear for both compounds (r 2 = 0.973-0.979). The stability of these two compounds showed that 3-hydroxy-3-methylhexanoic acid was more stable in water than 3-methyl-3-sulfanylhexan-1-ol. We applied the method to environmental samples in correspondence with an olfactory target buried previously.
“…Extraction techniques which frequently are used include liquid extraction method such as LLE LPME , dispersive liquid–liquid microextraction , SPE , SPME , and stir bar sorptive extraction . In the past decades, SPE as a popular sample preparation technique in environmental, food, and biomedical analyses has been applied .…”
In the present study, for the first time, we successfully employed zeolite/Fe3O4 as a new magnetic nanoparticle sorbent in magnetic solid-phase extraction for determining phthalates in aqueous samples. Gas chromatography with flame ionization detection was used to detect the target analytes as a powerful instrumental analysis. Affecting parameters in the extraction process, including the amount of adsorbent, adsorption and desorption time, and volume of desorption solvent, were optimized using a response surface methodology based on central composite design. Under the optimum conditions, the linear range for dibutyl phthalate and bis(2-ethylhexyl phthalate) was varied in the interval of 10-1700 and 10-1200 μg/L, respectively. Limits of detection were 2.80 μg/L for dibutyl phthalate and 3.20 μg/L for bis(2-ethylhexyl phthalate). The recovery value for the extraction of target analytes was between 97 and 111%. The repeatability and reproducibility of the new proposed method were obtained: 10-13% and 13-13.5%, respectively. The increased sensitivity in using the proposed method has been demonstrated. Compared with previous methods, the new proposed method is an accurate, rapid, and reliable sample-pretreatment method.
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