Optimising batch adsorbers for the removal of zinc from effluents using a sodium diimidoacetate ion exchange resin

Alireza Bazargan; Tsz Him Shek; Chi Wai Hui; Gordon McKay

doi:10.1007/s10450-016-9857-y

Optimising batch adsorbers for the removal of zinc from effluents using a sodium diimidoacetate ion exchange resin

Alireza Bazargan^*, Tsz Him Shek, Chi Wai Hui, Gordon McKay

^*Corresponding author for this work

CSE Sustainable Development

Research output: Contribution to journal › Article › peer-review

14 Citations (Scopus)

Abstract

An ion exchange resin, based on the sodium diimidoacetate structure, has been tested for the removal of zinc ions from effluents. After employing three isotherm models, namely, Langmuir, Freundlich and Langmuir–Freundlich to measure and analyse equilibrium isotherms, a series of agitated batch experiments have been carried out to optimise the removal of zinc ions in a two-stage batch system. The first optimisation model involves minimising the total amount of resin required to achieve a specific percentage zinc removal. The second optimisation study involves minimising the total batch contact time to achieve a certain percentage zinc removal.

Original language	English
Pages (from-to)	477-489
Number of pages	13
Journal	Adsorption
Volume	23
Issue number	4
DOIs	https://doi.org/10.1007/s10450-016-9857-y
Publication status	Published - 1 May 2017

Keywords

Batch adsorption
Ion exchange
Optimisation
Two-stage adsorption
Zinc

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abstract = "An ion exchange resin, based on the sodium diimidoacetate structure, has been tested for the removal of zinc ions from effluents. After employing three isotherm models, namely, Langmuir, Freundlich and Langmuir–Freundlich to measure and analyse equilibrium isotherms, a series of agitated batch experiments have been carried out to optimise the removal of zinc ions in a two-stage batch system. The first optimisation model involves minimising the total amount of resin required to achieve a specific percentage zinc removal. The second optimisation study involves minimising the total batch contact time to achieve a certain percentage zinc removal.",

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AU - Bazargan, Alireza

AU - Shek, Tsz Him

AU - Hui, Chi Wai

AU - McKay, Gordon

PY - 2017/5/1

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N2 - An ion exchange resin, based on the sodium diimidoacetate structure, has been tested for the removal of zinc ions from effluents. After employing three isotherm models, namely, Langmuir, Freundlich and Langmuir–Freundlich to measure and analyse equilibrium isotherms, a series of agitated batch experiments have been carried out to optimise the removal of zinc ions in a two-stage batch system. The first optimisation model involves minimising the total amount of resin required to achieve a specific percentage zinc removal. The second optimisation study involves minimising the total batch contact time to achieve a certain percentage zinc removal.

AB - An ion exchange resin, based on the sodium diimidoacetate structure, has been tested for the removal of zinc ions from effluents. After employing three isotherm models, namely, Langmuir, Freundlich and Langmuir–Freundlich to measure and analyse equilibrium isotherms, a series of agitated batch experiments have been carried out to optimise the removal of zinc ions in a two-stage batch system. The first optimisation model involves minimising the total amount of resin required to achieve a specific percentage zinc removal. The second optimisation study involves minimising the total batch contact time to achieve a certain percentage zinc removal.

KW - Batch adsorption

KW - Ion exchange

KW - Optimisation

KW - Two-stage adsorption

KW - Zinc

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JO - Adsorption

JF - Adsorption

IS - 4

ER -

Optimising batch adsorbers for the removal of zinc from effluents using a sodium diimidoacetate ion exchange resin

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Keywords

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