2014
DOI: 10.1016/j.cej.2013.08.087
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Catalytic non-thermal plasma reactor for mineralization of endosulfan in aqueous medium: A green approach for the treatment of pesticide contaminated water

Abstract: Supporting Information1. Characterization of the ceria catalyst Nitrogen adsorption-desorption isothermThe N2 adsorption -desorption isotherms shown in Fig. S1. The BET surface area of the ceria was deduced from adsorption -desorption isotherms it is around 89 m2/g and pore size19.2 Aº and pore volume 0.073 cc/g. X-ray diffractionThe formation of ceria fluorite structure was confirmed by XRD pattern as shown in Fig. S2 (JCPDF#810792).The crystal size calculated from the Debye-Scherrer method and it was found … Show more

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Cited by 78 publications
(12 citation statements)
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“…The concentrations of H 2 O 2 ranged from 0.174 to 2.7 mM for antibiotics solutions in water with slightly higher values (0.21 to 3.6 mM) observed for antibiotics in the meat effluent. Similar results have been reported by previous authors 49,50 . Focusing on the degradation of antibiotics by DBD plasma, Hama Aziz et al .…”
Section: Resultssupporting
confidence: 93%
“…The concentrations of H 2 O 2 ranged from 0.174 to 2.7 mM for antibiotics solutions in water with slightly higher values (0.21 to 3.6 mM) observed for antibiotics in the meat effluent. Similar results have been reported by previous authors 49,50 . Focusing on the degradation of antibiotics by DBD plasma, Hama Aziz et al .…”
Section: Resultssupporting
confidence: 93%
“…The highly reactive species of plasma interact with the pesticide compounds resulting in their degradation. The existing studies on pesticide degradation in water and soil surfaces using nonthermal plasma exhibits the potentiality of the technique (Kim, Kim, & Kang, 2007) (Bai, Chen, Yang, Guo, & Zhang, 2010) (Reddy, Mahammadunnisa, & Subrahmanyam, 2014) (Sarangapani et al, 2016).…”
Section: Introductionmentioning
confidence: 99%
“…For Evolich model, q t versus ln t was plotted in accordance with the linear form of the Eq. (8) as mentioned: q t = α + β lnt (8) where q t is the sorption capacity at time t, β and α are the Evolich constant determined from slope and intercept of the plot respectively. The parameters of Evolich model were calculated as shown in Table 8.…”
Section: Adsorption Kineticsmentioning
confidence: 99%
“…Hence, it is prerequisite to remove methylene blue from waste water. The various methods available for the treatment of dye contaminated water are chemical precipitation, membrane filtration, ion exchange, membrane bioreactor, carbon adsorption and coprecipitation/adsorption [6,[8][9][10][11][12][13]. However, chemical and biological methods cannot be used because of the non biodegradable nature of most of the dyes [14].…”
Section: Introductionmentioning
confidence: 99%