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Description: W14-Proceedings
Moving Bed Biofilm Reactor for Selenium Removal from FGD and Mine Effluents
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Description: W14-Proceedings
Moving Bed Biofilm Reactor for Selenium Removal from FGD and Mine Effluents

Moving Bed Biofilm Reactor for Selenium Removal from FGD and Mine Effluents

Moving Bed Biofilm Reactor for Selenium Removal from FGD and Mine Effluents

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Description: W14-Proceedings
Moving Bed Biofilm Reactor for Selenium Removal from FGD and Mine Effluents
Abstract
Biological selenium removal was studied in laboratory models of MBBR`s treating authentic wastewaters. The MBBR-effluents were treated with coagulation and flocculation for solids removal. Glucose or Micro C was added as carbon sources. Results from treatment of an FGD effluent from a power plant in a two-stage MBBR at 30°C showed that total selenium could be reduced from 250 ppb to 10-20 ppb. The feed also contained 90 ppm of NO3-N which was reduced to below 0.2 ppm in the process. Treatment of a mine effluent in a two-stage MBBR at temperatures down to 6° C reduced the selenium from 38 ppb to 3-5 ppb. NO3-N was reduced from 23 to below 0.2 ppm across the process. Another mine effluent with significantly higher concentration of total selenium, 560 ppb, but relatively low NO3-N, 1.5 ppm, was treated at temperatures down to 10°C in a two-stage MBBR. Total selenium was reduced to 6-20 ppb. The results demonstrate that MBBR can be a viable option for removal of selenium and nitrate from both FGD and mine effluents. The development is ongoing to optimize the MBBR design as well as the post-treatment.
Biological selenium removal was studied in laboratory models of MBBR`s treating authentic wastewaters. The MBBR-effluents were treated with coagulation and flocculation for solids removal. Glucose or Micro C was added as carbon sources. Results from treatment of an FGD effluent from a power plant in a two-stage MBBR at 30°C showed that total selenium could be...
Author(s)
Caroline DaleMaria EkenbergMikael SjölinFlemming WessmanJens Morän
SourceProceedings of the Water Environment Federation
Document typeConference Paper
PublisherWater Environment Federation
Print publication date Oct, 2014
ISSN1938-6478
DOI10.2175/193864714815939426
Volume / Issue2014 / 13
Content sourceWEFTEC
Copyright2014
Word count201

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Description: W14-Proceedings
Moving Bed Biofilm Reactor for Selenium Removal from FGD and Mine Effluents
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Description: W14-Proceedings
Moving Bed Biofilm Reactor for Selenium Removal from FGD and Mine Effluents
Abstract
Biological selenium removal was studied in laboratory models of MBBR`s treating authentic wastewaters. The MBBR-effluents were treated with coagulation and flocculation for solids removal. Glucose or Micro C was added as carbon sources. Results from treatment of an FGD effluent from a power plant in a two-stage MBBR at 30°C showed that total selenium could be reduced from 250 ppb to 10-20 ppb. The feed also contained 90 ppm of NO3-N which was reduced to below 0.2 ppm in the process. Treatment of a mine effluent in a two-stage MBBR at temperatures down to 6° C reduced the selenium from 38 ppb to 3-5 ppb. NO3-N was reduced from 23 to below 0.2 ppm across the process. Another mine effluent with significantly higher concentration of total selenium, 560 ppb, but relatively low NO3-N, 1.5 ppm, was treated at temperatures down to 10°C in a two-stage MBBR. Total selenium was reduced to 6-20 ppb. The results demonstrate that MBBR can be a viable option for removal of selenium and nitrate from both FGD and mine effluents. The development is ongoing to optimize the MBBR design as well as the post-treatment.
Biological selenium removal was studied in laboratory models of MBBR`s treating authentic wastewaters. The MBBR-effluents were treated with coagulation and flocculation for solids removal. Glucose or Micro C was added as carbon sources. Results from treatment of an FGD effluent from a power plant in a two-stage MBBR at 30°C showed that total selenium could be...
Author(s)
Caroline DaleMaria EkenbergMikael SjölinFlemming WessmanJens Morän
SourceProceedings of the Water Environment Federation
Document typeConference Paper
PublisherWater Environment Federation
Print publication date Oct, 2014
ISSN1938-6478
DOI10.2175/193864714815939426
Volume / Issue2014 / 13
Content sourceWEFTEC
Copyright2014
Word count201

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Caroline Dale# Maria Ekenberg# Mikael Sjölin# Flemming Wessman# Jens Morän. Moving Bed Biofilm Reactor for Selenium Removal from FGD and Mine Effluents. Alexandria, VA 22314-1994, USA: Water Environment Federation, 2018. Web. 12 Oct. 2025. <https://www.accesswater.org?id=-282237CITANCHOR>.
Caroline Dale# Maria Ekenberg# Mikael Sjölin# Flemming Wessman# Jens Morän. Moving Bed Biofilm Reactor for Selenium Removal from FGD and Mine Effluents. Alexandria, VA 22314-1994, USA: Water Environment Federation, 2018. Accessed October 12, 2025. https://www.accesswater.org/?id=-282237CITANCHOR.
Caroline Dale# Maria Ekenberg# Mikael Sjölin# Flemming Wessman# Jens Morän
Moving Bed Biofilm Reactor for Selenium Removal from FGD and Mine Effluents
Access Water
Water Environment Federation
December 22, 2018
October 12, 2025
https://www.accesswater.org/?id=-282237CITANCHOR