Modelling U(VI) Reduction by Pseudomonas stutzeri

Pseudomonas stutzeri, a facultative anaerobe sourced from soil in a uranium mine in Limpopo, South Africa, reduced uranium-6 (U(VI)) to uranium-4 (U(IV)) in batches under a relatively high initial U(VI) concentration ranging from 30 to 400 mg/L (pH 5 to 6). U(VI) reduction was rapid during the first...

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Main Authors: S. Chabalala, E. Chirwa
Format: Article
Language:English
Published: AIDIC Servizi S.r.l. 2012-06-01
Series:Chemical Engineering Transactions
Online Access:https://www.cetjournal.it/index.php/cet/article/view/7360
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spelling doaj-d3530f32e67e4adc998da8aa4c21e4ac2021-02-22T21:07:59ZengAIDIC Servizi S.r.l.Chemical Engineering Transactions2283-92162012-06-012710.3303/CET1227045Modelling U(VI) Reduction by Pseudomonas stutzeriS. ChabalalaE. ChirwaPseudomonas stutzeri, a facultative anaerobe sourced from soil in a uranium mine in Limpopo, South Africa, reduced uranium-6 (U(VI)) to uranium-4 (U(IV)) in batches under a relatively high initial U(VI) concentration ranging from 30 to 400 mg/L (pH 5 to 6). U(VI) reduction was rapid during the first 4 to 6 h of incubation followed by slower reduction rates at incubation times longer than 6 hours. Equilibrium conditions were only obtained after incubation for 24 h. The reduced U(VI) was recovered in solution as a hydroxide which was determined to consist of U(IV). A kinetic model based on enzyme kinetics produced the best fit of the optimised model to experimental data of U(VI) versus time in batch cultures of Pseudomonas stutzeri. The parameters: maximum specific uranium-6 reduction rate coefficient (ku), half velocity concentration (Ku), and uranium-6 reduction capacity of cells (Tc) were estimated using the data from the 200 mg/L batch. The parameters obtained in the 200 mg/L batch were then used to simulate the concentration in the other batches at lower and higher initial U(VI) concentrations. The reduction capacity Tc remained stable but a loss of accuracy was observed with increasing initial U(VI) concentration. Numerous batch experiments were conducted to establish kinetic parameters that will be used later for scale-up purposes. The knowledge gained from such processes will be of practical value in predicting effluent response to diverse loading conditions.https://www.cetjournal.it/index.php/cet/article/view/7360
collection DOAJ
language English
format Article
sources DOAJ
author S. Chabalala
E. Chirwa
spellingShingle S. Chabalala
E. Chirwa
Modelling U(VI) Reduction by Pseudomonas stutzeri
Chemical Engineering Transactions
author_facet S. Chabalala
E. Chirwa
author_sort S. Chabalala
title Modelling U(VI) Reduction by Pseudomonas stutzeri
title_short Modelling U(VI) Reduction by Pseudomonas stutzeri
title_full Modelling U(VI) Reduction by Pseudomonas stutzeri
title_fullStr Modelling U(VI) Reduction by Pseudomonas stutzeri
title_full_unstemmed Modelling U(VI) Reduction by Pseudomonas stutzeri
title_sort modelling u(vi) reduction by pseudomonas stutzeri
publisher AIDIC Servizi S.r.l.
series Chemical Engineering Transactions
issn 2283-9216
publishDate 2012-06-01
description Pseudomonas stutzeri, a facultative anaerobe sourced from soil in a uranium mine in Limpopo, South Africa, reduced uranium-6 (U(VI)) to uranium-4 (U(IV)) in batches under a relatively high initial U(VI) concentration ranging from 30 to 400 mg/L (pH 5 to 6). U(VI) reduction was rapid during the first 4 to 6 h of incubation followed by slower reduction rates at incubation times longer than 6 hours. Equilibrium conditions were only obtained after incubation for 24 h. The reduced U(VI) was recovered in solution as a hydroxide which was determined to consist of U(IV). A kinetic model based on enzyme kinetics produced the best fit of the optimised model to experimental data of U(VI) versus time in batch cultures of Pseudomonas stutzeri. The parameters: maximum specific uranium-6 reduction rate coefficient (ku), half velocity concentration (Ku), and uranium-6 reduction capacity of cells (Tc) were estimated using the data from the 200 mg/L batch. The parameters obtained in the 200 mg/L batch were then used to simulate the concentration in the other batches at lower and higher initial U(VI) concentrations. The reduction capacity Tc remained stable but a loss of accuracy was observed with increasing initial U(VI) concentration. Numerous batch experiments were conducted to establish kinetic parameters that will be used later for scale-up purposes. The knowledge gained from such processes will be of practical value in predicting effluent response to diverse loading conditions.
url https://www.cetjournal.it/index.php/cet/article/view/7360
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