SOHIO process legacy waste treatment

Uranium recovery using ion exchange

Journal Article (2019)
Author(s)

Richard I. Foster (The University of Manchester, Korea Atomic Energy Research Institute)

James T.M. Amphlett (Korea Advanced Institute of Science and Technology, The University of Manchester)

Kwang Wook Kim (Korea Atomic Energy Research Institute)

Tim Kerry (TU Delft - (OLD) MSE-3, The University of Manchester)

Keunyoung Lee (Korea Atomic Energy Research Institute)

Clint A. Sharrad (The University of Manchester)

Research Group
(OLD) MSE-3
DOI related publication
https://doi.org/10.1016/j.jiec.2019.09.001 Final published version
More Info
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Publication Year
2019
Language
English
Research Group
(OLD) MSE-3
Volume number
81
Pages (from-to)
144-152
Downloads counter
239

Abstract

The feasibility of employing ion-exchange resins for the selective removal of uranium from a complex waste effluent has been investigated. The source of the effluent is a treatment process to reduce the volume of a spent uranium containing catalyst prior to its immobilisation and disposal in South Korea. Commercial anion exchange and chelation resins have been screened, along with an in-house synthesized polyamine functionalized resin. The Langmuir isotherm model produced the best fit for UO2 2+ binding to all resins, with Purolite MTS957, a mixed sulfonic/phosphonic acid functionalised resin, showing the highest equilibrium adsorption capacity for UO2 2+, 96.15 mg g−1. The Modified Dose-Response Model was found to adequately represent breakthrough across all flow rates used and for all resins tested under dynamic testing conditions. The maximum uranium loading capacities under dynamic conditions for simulant and real wastes were established as 131.52 mg g−1 and 68.62 mg g−1, respectively. Purolite MTS957 effectively decontaminated the real effluent to uranium levels below the Korean release limit of 1 mg L−1. Over 99.9% uranium was successfully eluted from the resin bed in under 20 BV with a mixed sodium carbonate/sulfate eluent.