2020
DOI: 10.3390/polym12061313
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Polystyrene Magnetic Nanocomposites as Antibiotic Adsorbents

Abstract: There are different ways for antibiotics to enter the aquatic environment, with wastewater treatment plants (WWTP) considered to be one of the main points of entrance. Even treated wastewater effluent can contain antibiotics, since WWTP cannot eliminate the presence of antibiotics. Therefore, adsorption can be a sustainable option, compared to other tertiary treatments. In this direction, a versatile synthesis of poly(styrene-block-acrylic acid) diblock copolymer/Fe3O4 magnetic nanocomposite (abbreviated as P(… Show more

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Cited by 41 publications
(11 citation statements)
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“…The Langmuir isotherm model is defined by the following equation [ 37 ]: where q e is the equilibrium adsorption volume (mg·g −1 ), Q is the monolayer saturation adsorption volume (mg·g −1 ), c e is the EtBr concentration in the working fluid at adsorption equilibrium (mg·L −1 ), and k L is a constant related to the temperature or enthalpy change of the adsorption process. The Freundlich isotherm model is defined by the following equation [ 38 ]: where k F and n are Freundlich constant related to the temperature or enthalpy change of the adsorption process. The Dubinin-Radushkevich isotherm model is defined by the following equation [ 39 ]: where K ad is the isotherm constant with respect to Dubinin-Radushkevich; q s is the theoretical adsorption amount; and ε is the Polanyi potential, which is calculated as follows [ 40 ]: for the parameters in Dubinin-Radushkevich equation, the value of the average adsorption energy ( E ) can be calculated, which represents the free energy used for the transfer of 1 mol of ions from the solution to the surface of the adsorbent, and it can be calculated from the following equation [ 41 ]: …”
Section: Resultsmentioning
confidence: 99%
“…The Langmuir isotherm model is defined by the following equation [ 37 ]: where q e is the equilibrium adsorption volume (mg·g −1 ), Q is the monolayer saturation adsorption volume (mg·g −1 ), c e is the EtBr concentration in the working fluid at adsorption equilibrium (mg·L −1 ), and k L is a constant related to the temperature or enthalpy change of the adsorption process. The Freundlich isotherm model is defined by the following equation [ 38 ]: where k F and n are Freundlich constant related to the temperature or enthalpy change of the adsorption process. The Dubinin-Radushkevich isotherm model is defined by the following equation [ 39 ]: where K ad is the isotherm constant with respect to Dubinin-Radushkevich; q s is the theoretical adsorption amount; and ε is the Polanyi potential, which is calculated as follows [ 40 ]: for the parameters in Dubinin-Radushkevich equation, the value of the average adsorption energy ( E ) can be calculated, which represents the free energy used for the transfer of 1 mol of ions from the solution to the surface of the adsorbent, and it can be calculated from the following equation [ 41 ]: …”
Section: Resultsmentioning
confidence: 99%
“…Porous polymeric materials with tunable pore size and controllable morphology have been effectively used as matrices for the deposition of fine particles [8,9]. It is well known that the styrene-divinylbenzene co-polymers are mechanically and chemically stable as well as they have high adsorption abilities towards many organics [10,11]. Also, their distinct features of including abundant surface functional groups enable them to be applied as efficient adsorbents for binding organic molecules [12].…”
Section: Introductionmentioning
confidence: 99%
“…Adsorption is widely used in water and wastewater treatment [ 17 , 18 , 19 , 20 , 21 , 22 , 23 , 24 , 25 , 26 , 27 , 28 ], which is one of the most effective technology [ 29 , 30 , 31 , 32 , 33 , 34 ]. Adsorption process between liquid and solid phase is strongly affected from temperature [ 35 ].…”
Section: Introductionmentioning
confidence: 99%