Fixed-bed dynamic column adsorption study of methylene blue (MB) onto pine cone

The effectiveness of pine cone biomass in the removal of methylene blue (MB) dye from its aqueous solution was tested here by a fixed-bed column adsorption study. The adsorption column breakthrough curves (BTCs) indicated the favourable column dynamics and its dye adsorptive behaviour depends on fee...

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Main Authors: Yagub, Musstafa, Sen, Tushar, Afroze, Sharmeen, Ang, Ha Ming
Format: Journal Article
Published: Taylor & Francis Ltd. 2014
Subjects:
Online Access:http://hdl.handle.net/20.500.11937/28951
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author Yagub, Musstafa
Sen, Tushar
Afroze, Sharmeen
Ang, Ha Ming
author_facet Yagub, Musstafa
Sen, Tushar
Afroze, Sharmeen
Ang, Ha Ming
author_sort Yagub, Musstafa
building Curtin Institutional Repository
collection Online Access
description The effectiveness of pine cone biomass in the removal of methylene blue (MB) dye from its aqueous solution was tested here by a fixed-bed column adsorption study. The adsorption column breakthrough curves (BTCs) indicated the favourable column dynamics and its dye adsorptive behaviour depends on feed flow rate, initial MB dye concentration and column bed height. The results showed that the amount of total sorbed dye, equilibrium dye uptake, mass transfer zone and total percentage of dye removal increased with increase in MB dye concentration and the height of the bed, but decreased with increase in initial flow rate. To determine the fixed-bed column adsorption kinetic parameters, Thomas, Yoon–Nelson and Bed Depth Service Time (BDST) models fitted the experimental BTC obtained from dynamic studies. All these parameters are required for the design of adsorption column and it was found that all three kinetic models were applicable.Thomas model showed that the value of maximum solid-phase concentration (q0) decreased when the flow rate and the height of the bed increased but increased with increasing initial MB dye concentration. The value of Thomas kinetic rate constant (KTh) increased with higher flow rate but decreased with increasing initial MB dye concentration and the height of the bed. Yoon–Nelson model showed that the time required to achieve 50% adsorbate breakthrough, τ fitted well with the experimental data (τ50% exp.) in the entire column adsorption system. The rate constant KYN increased with both increasing flow rate and initial MB dye concentration but decreased with increasing bed height. The BDST model showed that the rate constant (K0) decreased when both the bed heights and the initial MB dye concentration increased, but increased with the increase in flow rate. The value of the volumetric sorption capacity of the bed (N0) increased with increasing flow rate, initial MB dye concentration and bed height. Overall, all the three models were fitted well with the experimental data.
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spelling curtin-20.500.11937-289512017-09-13T15:15:34Z Fixed-bed dynamic column adsorption study of methylene blue (MB) onto pine cone Yagub, Musstafa Sen, Tushar Afroze, Sharmeen Ang, Ha Ming Yoon–Nelson model BTC MB adsorption Thomas model Fixed-bed column The effectiveness of pine cone biomass in the removal of methylene blue (MB) dye from its aqueous solution was tested here by a fixed-bed column adsorption study. The adsorption column breakthrough curves (BTCs) indicated the favourable column dynamics and its dye adsorptive behaviour depends on feed flow rate, initial MB dye concentration and column bed height. The results showed that the amount of total sorbed dye, equilibrium dye uptake, mass transfer zone and total percentage of dye removal increased with increase in MB dye concentration and the height of the bed, but decreased with increase in initial flow rate. To determine the fixed-bed column adsorption kinetic parameters, Thomas, Yoon–Nelson and Bed Depth Service Time (BDST) models fitted the experimental BTC obtained from dynamic studies. All these parameters are required for the design of adsorption column and it was found that all three kinetic models were applicable.Thomas model showed that the value of maximum solid-phase concentration (q0) decreased when the flow rate and the height of the bed increased but increased with increasing initial MB dye concentration. The value of Thomas kinetic rate constant (KTh) increased with higher flow rate but decreased with increasing initial MB dye concentration and the height of the bed. Yoon–Nelson model showed that the time required to achieve 50% adsorbate breakthrough, τ fitted well with the experimental data (τ50% exp.) in the entire column adsorption system. The rate constant KYN increased with both increasing flow rate and initial MB dye concentration but decreased with increasing bed height. The BDST model showed that the rate constant (K0) decreased when both the bed heights and the initial MB dye concentration increased, but increased with the increase in flow rate. The value of the volumetric sorption capacity of the bed (N0) increased with increasing flow rate, initial MB dye concentration and bed height. Overall, all the three models were fitted well with the experimental data. 2014 Journal Article http://hdl.handle.net/20.500.11937/28951 10.1080/19443994.2014.924034 Taylor & Francis Ltd. restricted
spellingShingle Yoon–Nelson model
BTC
MB adsorption
Thomas model
Fixed-bed column
Yagub, Musstafa
Sen, Tushar
Afroze, Sharmeen
Ang, Ha Ming
Fixed-bed dynamic column adsorption study of methylene blue (MB) onto pine cone
title Fixed-bed dynamic column adsorption study of methylene blue (MB) onto pine cone
title_full Fixed-bed dynamic column adsorption study of methylene blue (MB) onto pine cone
title_fullStr Fixed-bed dynamic column adsorption study of methylene blue (MB) onto pine cone
title_full_unstemmed Fixed-bed dynamic column adsorption study of methylene blue (MB) onto pine cone
title_short Fixed-bed dynamic column adsorption study of methylene blue (MB) onto pine cone
title_sort fixed-bed dynamic column adsorption study of methylene blue (mb) onto pine cone
topic Yoon–Nelson model
BTC
MB adsorption
Thomas model
Fixed-bed column
url http://hdl.handle.net/20.500.11937/28951