1989
DOI: 10.1002/ep.3300080212
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Biodenitrification of uranium refinery wastewaters

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Cited by 13 publications
(12 citation statements)
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“…The need to dilute waste streams with very high NO 3 − concentration was also noted to be necessary for the denitrification of wastes with high NO 3 − content from nuclear fuel processing (Clarkson et al, 1991, Francis & Makin, 1991, Lawson, 1981, Walker et al, 1989. It is important to note that for the biotreatment of wastewaters from DNEG manufacture, groundwater instead of deionized water was used on site in the factory; this represented a cost savings of between 1 and 2 orders of magnitude with respect to the cost of standard laboratory assays.…”
Section: Discussionmentioning
confidence: 97%
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“…The need to dilute waste streams with very high NO 3 − concentration was also noted to be necessary for the denitrification of wastes with high NO 3 − content from nuclear fuel processing (Clarkson et al, 1991, Francis & Makin, 1991, Lawson, 1981, Walker et al, 1989. It is important to note that for the biotreatment of wastewaters from DNEG manufacture, groundwater instead of deionized water was used on site in the factory; this represented a cost savings of between 1 and 2 orders of magnitude with respect to the cost of standard laboratory assays.…”
Section: Discussionmentioning
confidence: 97%
“…Bioremediation of pollution generated by organic compounds is feasible if microbes able to use the pollutant as a C-source are available (Gibson & Subramanian, 1984). However, bioremediation of sites polluted with inorganic N-sources such as ammonium, nitrate, and nitrite requires not only microbes able to use these compounds as an N-source, but also an assimilable C-source to provide the energy required for N-metabolism (Blaszczyk, 1993, Clarkson et al, 1991, Francis & Makin, 1991, Kaplan et al, 1987, Smith et al, 1994, Walker et al, 1989. Complex microbial communities in biological treatment plants are able to cope with low concentrations of nitrate (<50 mg/L) similar to those found in natural environments (Fossing et al, 1996).…”
Section: Discussionmentioning
confidence: 97%
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“…The highest contributor of TN removal was found to be the HYCEM digester rather than the aeration tank or SBR. This shows significant amount of biological carbon source was consumed for denitrification as shown in the general biological denitrification equation [18]: Balance gas with higher recirculation ratio and it directly supports the occurrence of the denitrification process in the digester. The correlation between NO 3 − removal rate and recirculation ratio was found to be strong from regression analysis (the coefficient of correlation ≒0.82).…”
Section: Analysis Hycem Digester Performance and Biogas Compositionmentioning
confidence: 98%
“…A cheaper alternative is the application of bioremediative processes using microorganisms. However, when biological treatment plants receive wastewater with nitrate concentrations above 0.1 M, the system is poisoned and most of the cells are killed (Krishnamachari and Clarkson, 1993;Walker et al, 1989). One approach used to overcome this problem is the prior dilution of wastewater to relatively low nitrate levels before feeding it into the plant.…”
Section: Introductionmentioning
confidence: 98%