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Influence of hydrogen on the reductive dechlorination of tetrachloroethene (PCE) to ethene in a methanogenic biofilm reactor: role of mass transport phenomena
This study investigated the influence of H2 bulk liquid concentration in the range 2–120 µmol L−1 on the kinetics of vinyl chloride (VC) formation from tetrachloroethene (PCE) and VC dechlorination to ethene in a methanogenic biofilm reactor containing Dehalococcoides spp. as the putative dechlorina...
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Published in: | Journal of chemical technology and biotechnology (1986) 2006-09, Vol.81 (9), p.1520-1529 |
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Main Authors: | , , , , |
Format: | Article |
Language: | English |
Subjects: | |
Citations: | Items that this one cites Items that cite this one |
Online Access: | Get full text |
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Summary: | This study investigated the influence of H2 bulk liquid concentration in the range 2–120 µmol L−1 on the kinetics of vinyl chloride (VC) formation from tetrachloroethene (PCE) and VC dechlorination to ethene in a methanogenic biofilm reactor containing Dehalococcoides spp. as the putative dechlorinating micro‐organism. Both VC formation and dechlorination showed a definite increase in rate with increasing H2 bulk liquid concentration, following a pattern typical of Michaelis–Menten kinetics. The estimated maximum VC formation rate (81.7 ± 9.4 µmol L−1 h−1; mean value ± 90% confidence interval) was about ten times higher than the estimated maximum VC dechlorination rate (8.2 ± 1.0 µmol L−1 h−1), while the estimated apparent half‐velocity coefficient for H2 for VC formation (1.5 ± 1.4 µmol H2 L−1) was more than six times lower than that for VC dechlorination (9.1 ± 5.1 µmol H2 L−1), confirming that the last step of PCE dechlorination (i.e. conversion of VC to ethene) was much more H2‐sensitive than the previous ones. The estimated maximum methane formation rate was 462.1 ± 213.5 µmol L−1 h−1 and the estimated apparent half‐velocity coefficient was 104.7 ± 89.4 µmol H2 L−1. Experiments at different temperatures indicated the presence of severe internal (diffusional) mass transfer limitations and, in turn, of steep H2 concentration gradients through the biofilm, which strongly influenced the estimated apparent half‐velocity coefficients for H2 use. The results of this study emphasise the importance of considering mass transfer phenomena when predicting the rate of PCE dechlorination and the outcome of competition for H2 in natural or engineered bioremediation systems. Copyright © 2006 Society of Chemical Industry |
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ISSN: | 0268-2575 1097-4660 |
DOI: | 10.1002/jctb.1562 |