2021
DOI: 10.1016/j.ijbiomac.2021.08.144
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Preparation of clinoptilolite/starch/CoFe2O4 magnetic nanocomposite powder and its elimination properties for cationic dyes from water and wastewater

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Cited by 89 publications
(40 citation statements)
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“…The maximum adsorption capacity of CVD, MBD, and MVD to the desired composite was determined as 32.84 mg•g −1 , 31.81 mg•g −1 , and 31.15 mg•g −1 , respectively. Finally, the ad(de)sorption experiments' results showed that the synthesized nanocomposite adsorbent has an excellent ability to adsorb cationic dyes after several consecutive cycles [28].…”
Section: Introductionmentioning
confidence: 94%
“…The maximum adsorption capacity of CVD, MBD, and MVD to the desired composite was determined as 32.84 mg•g −1 , 31.81 mg•g −1 , and 31.15 mg•g −1 , respectively. Finally, the ad(de)sorption experiments' results showed that the synthesized nanocomposite adsorbent has an excellent ability to adsorb cationic dyes after several consecutive cycles [28].…”
Section: Introductionmentioning
confidence: 94%
“…The employed adsorbent reduced the amount of American Dye Manufacturers Institute (ADMI) parameter in dye-containing wastewater from 938 to 224 (76.119 %) and the values of chemical oxygen demand (COD), biological oxygen demand (BOD) and total organic carbon (TOC) were also reduced. [70] Another study reported improvement in adsorption performance of double-network hydrophobic-hydrogel in a mixed system, compared to a single system. [62] This is due to the decreased intensity of dyes in the mixed system, caused by decreased value of λ max (wavelength of maximum absorbance) for each dye.…”
Section: Simultaneous Removal Of Dyes From a Mixturementioning
confidence: 99%
“…[1]. Copyright (2017), Institution of Chemical Engineers and Elsevier B.V., (b) Effect of interaction time (pH 9, initial content 10 mg/L, adsorbent 1.25 g/L, temperature 25 °C).Reprinted with permission from Ref [70]…”
mentioning
confidence: 99%
“…After mixing the K 2 Cr 2 O 7 solution with a suspension of Chlorella vulgaris ZBS1 cells, samples of the solution were taken for analysis for the content of Cr (VI) ions every 20 min, for 120 min. The effect of temperature on the adsorption equilibrium was investigated by varying the temperature from 298 to 328 K. To study the kinetic behavior of the adsorption process of Cr(VI) from aqueous solutions, kinetic models of pseudo-first order, pseudo-second order, the Morris-Weber model describing intraporous diffusion, and the Elovich model were used; calculations were carried out according to formulas (3, 4 , 5 , and 6) [ 3 , 26 , 27 , 28 , 29 , 30 , 31 , 32 , 44 ]: here, q t and q e are the adsorption capacity of Cr (VI) per gram of adsorbent (mg/g), k 1 (1/min)—the constant adsorption rate, k 2 (g/mg·min)—the constant quasi-square velocity of the kinetic model. K int —the constant diffusion rate inside the particles, C i —corresponds to the effects of the boundary layer, α—the initial adsorption rate (mg/g· min), β—the desorption constant (g/mg).…”
Section: Experimental Partmentioning
confidence: 99%