Enhanced Adsorptive Removal of Dyes Using Mandarin Peel Biochars via Chemical Activation with NH<sub>4</sub>Cl and ZnCl<sub>2</sub>

This study examined differences in the adsorption kinetics, isotherms, and thermodynamics of the dyes (methyl orange and fast green FCF) by pristine (M–biochar) and chemical activated mandarin peel biochars (MN–biochar and MZ–biochar). The specific surface area (1085.0 m<sup>2</sup>/g) a...

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Main Authors: Hyunjun Park, Jiseok Kim, Yong-Gu Lee, Kangmin Chon
Format: Article
Language:English
Published: MDPI AG 2021-05-01
Series:Water
Subjects:
Online Access:https://www.mdpi.com/2073-4441/13/11/1495
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author Hyunjun Park
Jiseok Kim
Yong-Gu Lee
Kangmin Chon
author_facet Hyunjun Park
Jiseok Kim
Yong-Gu Lee
Kangmin Chon
author_sort Hyunjun Park
collection DOAJ
description This study examined differences in the adsorption kinetics, isotherms, and thermodynamics of the dyes (methyl orange and fast green FCF) by pristine (M–biochar) and chemical activated mandarin peel biochars (MN–biochar and MZ–biochar). The specific surface area (1085.0 m<sup>2</sup>/g) and pore volume (0.194 cm<sup>3</sup>/g) of MZ-biochar much higher than those of the M–biochar (specific surface area = 8.5 m<sup>2</sup>/g, pore volume = 0.016 cm<sup>3</sup>/g) and MN–biochar (specific surface area = 181.1 m<sup>2</sup>/g, pore volume = 0.031 cm<sup>3</sup>/g). The equilibrium adsorption capacities (mg/g) of MO and FG using M–biochar (MO = 0.95, FG = 0.78) MN–biochar (MO = 2.52, FG = 2.13), and MZ–biochar (MO = 16.27, FG = 12.44) have well-matched the pseudo-second-order model (R<sup>2</sup> ≥ 0.952) compared with the pseudo-first-order model (R<sup>2</sup> ≥ 0.008). Furthermore, the better explanation of the adsorption behavior of dyes by the Freundlich isotherm model (R<sup>2</sup> ≥ 0.978) than the Langmuir isotherm model (R<sup>2</sup> ≥ 0.881) supports the assumption that the multilayer adsorption governed the adsorption of dyes using mandarin peel biochars. The adsorptions of dyes were significantly dependent on the solution pH and temperature since the electrostatic and spontaneous endothermic reactions governed their removal using the pristine and chemical activated mandarin peel biochars.
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spelling doaj.art-f806c55742e74d51976a8b46ba0638c22023-11-21T21:35:20ZengMDPI AGWater2073-44412021-05-011311149510.3390/w13111495Enhanced Adsorptive Removal of Dyes Using Mandarin Peel Biochars via Chemical Activation with NH<sub>4</sub>Cl and ZnCl<sub>2</sub>Hyunjun Park0Jiseok Kim1Yong-Gu Lee2Kangmin Chon3Department of Environmental Engineering, College of Engineering, Kangwon National University, Kangwondaehak-gil, 1, Chuncheon-si 24341, Gangwon-do, KoreaDepartment of Environmental Engineering, College of Engineering, Kangwon National University, Kangwondaehak-gil, 1, Chuncheon-si 24341, Gangwon-do, KoreaDepartment of Environmental Engineering, College of Engineering, Kangwon National University, Kangwondaehak-gil, 1, Chuncheon-si 24341, Gangwon-do, KoreaDepartment of Environmental Engineering, College of Engineering, Kangwon National University, Kangwondaehak-gil, 1, Chuncheon-si 24341, Gangwon-do, KoreaThis study examined differences in the adsorption kinetics, isotherms, and thermodynamics of the dyes (methyl orange and fast green FCF) by pristine (M–biochar) and chemical activated mandarin peel biochars (MN–biochar and MZ–biochar). The specific surface area (1085.0 m<sup>2</sup>/g) and pore volume (0.194 cm<sup>3</sup>/g) of MZ-biochar much higher than those of the M–biochar (specific surface area = 8.5 m<sup>2</sup>/g, pore volume = 0.016 cm<sup>3</sup>/g) and MN–biochar (specific surface area = 181.1 m<sup>2</sup>/g, pore volume = 0.031 cm<sup>3</sup>/g). The equilibrium adsorption capacities (mg/g) of MO and FG using M–biochar (MO = 0.95, FG = 0.78) MN–biochar (MO = 2.52, FG = 2.13), and MZ–biochar (MO = 16.27, FG = 12.44) have well-matched the pseudo-second-order model (R<sup>2</sup> ≥ 0.952) compared with the pseudo-first-order model (R<sup>2</sup> ≥ 0.008). Furthermore, the better explanation of the adsorption behavior of dyes by the Freundlich isotherm model (R<sup>2</sup> ≥ 0.978) than the Langmuir isotherm model (R<sup>2</sup> ≥ 0.881) supports the assumption that the multilayer adsorption governed the adsorption of dyes using mandarin peel biochars. The adsorptions of dyes were significantly dependent on the solution pH and temperature since the electrostatic and spontaneous endothermic reactions governed their removal using the pristine and chemical activated mandarin peel biochars.https://www.mdpi.com/2073-4441/13/11/1495adsorptionammonium chloridebiochardyesfast green FCFmandarin peel
spellingShingle Hyunjun Park
Jiseok Kim
Yong-Gu Lee
Kangmin Chon
Enhanced Adsorptive Removal of Dyes Using Mandarin Peel Biochars via Chemical Activation with NH<sub>4</sub>Cl and ZnCl<sub>2</sub>
Water
adsorption
ammonium chloride
biochar
dyes
fast green FCF
mandarin peel
title Enhanced Adsorptive Removal of Dyes Using Mandarin Peel Biochars via Chemical Activation with NH<sub>4</sub>Cl and ZnCl<sub>2</sub>
title_full Enhanced Adsorptive Removal of Dyes Using Mandarin Peel Biochars via Chemical Activation with NH<sub>4</sub>Cl and ZnCl<sub>2</sub>
title_fullStr Enhanced Adsorptive Removal of Dyes Using Mandarin Peel Biochars via Chemical Activation with NH<sub>4</sub>Cl and ZnCl<sub>2</sub>
title_full_unstemmed Enhanced Adsorptive Removal of Dyes Using Mandarin Peel Biochars via Chemical Activation with NH<sub>4</sub>Cl and ZnCl<sub>2</sub>
title_short Enhanced Adsorptive Removal of Dyes Using Mandarin Peel Biochars via Chemical Activation with NH<sub>4</sub>Cl and ZnCl<sub>2</sub>
title_sort enhanced adsorptive removal of dyes using mandarin peel biochars via chemical activation with nh sub 4 sub cl and zncl sub 2 sub
topic adsorption
ammonium chloride
biochar
dyes
fast green FCF
mandarin peel
url https://www.mdpi.com/2073-4441/13/11/1495
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