Response Surface Modelling of Methylene Blue Adsorption onto Seaweed, Coconut Shell and Oak Wood Hydrochars

Adsorption of methylene blue (MB) dye from an aqueous solution onto hydrochars produced from brown seaweed (<i>Fucus Serratus</i>) (FS-HC), coconut shell (CS-HC), and oak wood (Oak-HC) at different temperatures (200–250 °C) was investigated in a batch system. Response surface modelling (...

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Main Authors: Eric Danso-Boateng, Melissa Fitzsimmons, Andrew B. Ross, Ted Mariner
Format: Article
Language:English
Published: MDPI AG 2023-03-01
Series:Water
Subjects:
Online Access:https://www.mdpi.com/2073-4441/15/5/977
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author Eric Danso-Boateng
Melissa Fitzsimmons
Andrew B. Ross
Ted Mariner
author_facet Eric Danso-Boateng
Melissa Fitzsimmons
Andrew B. Ross
Ted Mariner
author_sort Eric Danso-Boateng
collection DOAJ
description Adsorption of methylene blue (MB) dye from an aqueous solution onto hydrochars produced from brown seaweed (<i>Fucus Serratus</i>) (FS-HC), coconut shell (CS-HC), and oak wood (Oak-HC) at different temperatures (200–250 °C) was investigated in a batch system. Response surface modelling (RSM) was used to investigate the effect of initial MB concentration (50–300 mg/L), contact time (0–240 min), and solution pH (2–12) on the adsorption process. RSM was also used to model and optimise these parameters for efficient adsorption. Kinetic and isotherms studies were carried out to study the adsorption mechanism onto the hydrochars. It was found that the best adsorbent from the RSM model was FS-HC200, and the optimal conditions for greater MB dye uptake were lower initial MB concentration (50 mg/L), pH 6 and contact time of 84 min; removing >99% of MB. Langmuir and Redlich–Peterson isotherm models fitted the adsorption of MB onto hydrochars prepared at 200 and 250 °C. Freundlich and Redlich–Peterson isotherms were suitable for hydrochars produced at 220 °C. FS-HCs have the highest maximum adsorption capacity of MB of about (8.60–28.57) mg/g calculated from the Langmuir isotherm. The adsorption process for all the hydrochars followed a pseudo-second-order model (R<sup>2</sup> = 0.96–1.00), and film diffusion and intraparticle diffusion were the rate-determining steps. Therefore, this work identifies cheap adsorbents from biowaste that are effective for the removal of cationic pollutants from wastewater.
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spelling doaj.art-11ec49337790441781b57fbbae556c202023-11-17T08:55:45ZengMDPI AGWater2073-44412023-03-0115597710.3390/w15050977Response Surface Modelling of Methylene Blue Adsorption onto Seaweed, Coconut Shell and Oak Wood HydrocharsEric Danso-Boateng0Melissa Fitzsimmons1Andrew B. Ross2Ted Mariner3School of Chemical and Process Engineering, University of Leeds, LS2 9JT, UKSchool of Chemical and Process Engineering, University of Leeds, LS2 9JT, UKSchool of Chemical and Process Engineering, University of Leeds, LS2 9JT, UKSchool of Chemical and Process Engineering, University of Leeds, LS2 9JT, UKAdsorption of methylene blue (MB) dye from an aqueous solution onto hydrochars produced from brown seaweed (<i>Fucus Serratus</i>) (FS-HC), coconut shell (CS-HC), and oak wood (Oak-HC) at different temperatures (200–250 °C) was investigated in a batch system. Response surface modelling (RSM) was used to investigate the effect of initial MB concentration (50–300 mg/L), contact time (0–240 min), and solution pH (2–12) on the adsorption process. RSM was also used to model and optimise these parameters for efficient adsorption. Kinetic and isotherms studies were carried out to study the adsorption mechanism onto the hydrochars. It was found that the best adsorbent from the RSM model was FS-HC200, and the optimal conditions for greater MB dye uptake were lower initial MB concentration (50 mg/L), pH 6 and contact time of 84 min; removing >99% of MB. Langmuir and Redlich–Peterson isotherm models fitted the adsorption of MB onto hydrochars prepared at 200 and 250 °C. Freundlich and Redlich–Peterson isotherms were suitable for hydrochars produced at 220 °C. FS-HCs have the highest maximum adsorption capacity of MB of about (8.60–28.57) mg/g calculated from the Langmuir isotherm. The adsorption process for all the hydrochars followed a pseudo-second-order model (R<sup>2</sup> = 0.96–1.00), and film diffusion and intraparticle diffusion were the rate-determining steps. Therefore, this work identifies cheap adsorbents from biowaste that are effective for the removal of cationic pollutants from wastewater.https://www.mdpi.com/2073-4441/15/5/977<i>Fucus Serratus</i>hydrocharhydrothermal carbonisationmethylene blueresponse surface modellingseaweed
spellingShingle Eric Danso-Boateng
Melissa Fitzsimmons
Andrew B. Ross
Ted Mariner
Response Surface Modelling of Methylene Blue Adsorption onto Seaweed, Coconut Shell and Oak Wood Hydrochars
Water
<i>Fucus Serratus</i>
hydrochar
hydrothermal carbonisation
methylene blue
response surface modelling
seaweed
title Response Surface Modelling of Methylene Blue Adsorption onto Seaweed, Coconut Shell and Oak Wood Hydrochars
title_full Response Surface Modelling of Methylene Blue Adsorption onto Seaweed, Coconut Shell and Oak Wood Hydrochars
title_fullStr Response Surface Modelling of Methylene Blue Adsorption onto Seaweed, Coconut Shell and Oak Wood Hydrochars
title_full_unstemmed Response Surface Modelling of Methylene Blue Adsorption onto Seaweed, Coconut Shell and Oak Wood Hydrochars
title_short Response Surface Modelling of Methylene Blue Adsorption onto Seaweed, Coconut Shell and Oak Wood Hydrochars
title_sort response surface modelling of methylene blue adsorption onto seaweed coconut shell and oak wood hydrochars
topic <i>Fucus Serratus</i>
hydrochar
hydrothermal carbonisation
methylene blue
response surface modelling
seaweed
url https://www.mdpi.com/2073-4441/15/5/977
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