TY - JOUR
T1 - Hydrogen-fed biofilm reactors reducing selenate and sulfate
T2 - Community structure and capture of elemental selenium within the biofilm
AU - Ontiveros-Valencia, Aura
AU - Penton, Christopher
AU - Krajmalnik-Brown, Rosa
AU - Rittmann, Bruce
N1 - Publisher Copyright: © 2016 Wiley Periodicals, Inc.
PY - 2016/8/1
Y1 - 2016/8/1
N2 - Remediation of selenate (SeO4 2−) contamination through microbial reduction is often challenging due to the presence of sulfate (SO4 2−), which can lead to competition for the electron donor and the co-production of toxic H2S. Microbial reduction of SeO4 2− in the presence of SO4 2− was studied in two hydrogen-based membrane biofilm reactors (MBfRs). One MBfR was initiated with SO4 2−-reducing conditions and gradually shifted to SeO4 2− reduction. The second MBfR was developed with a SeO4 2−-reducing biofilm, followed by SO4 2− introduction. Biofilms within both MBfRs achieved greater than 90% SeO4 2− reduction, even though the SeO4 2− concentration ranged from 1,000–11,000 μg/L, more than 20–200 times the maximum contaminant level for drinking water (50 μg/L). Biofilm microbial community composition, assessed by 16S rRNA gene-based amplicon pyrosequencing, was distinct between the two MBfRs and was framed by alterations in SeO4 2− loading. Specifically, high SeO4 2− loading resulted in communities mainly composed of denitrifying bacteria (e.g., Denitratisoma and Dechloromonas). In contrast, low loading led to mostly sulfate-reducing bacteria (i.e., Desulfovibrio) and sulfur-oxidizing bacteria (i.e., Sulfuricurvum and Sulfurovum). SeO4 2− was reduced to elemental selenium (Se°), which was visualized within the biofilm as crystalloid aggregates, with its fate corresponding to that of biofilm solids. In conclusion, microbial biofilm communities initiated under either SeO4 2− or SO4 2−-reducing conditions attained high SeO4 2− removal rates even though their microbial community composition was quite distinct. Biotechnol. Bioeng. 2016;113: 1736–1744.
AB - Remediation of selenate (SeO4 2−) contamination through microbial reduction is often challenging due to the presence of sulfate (SO4 2−), which can lead to competition for the electron donor and the co-production of toxic H2S. Microbial reduction of SeO4 2− in the presence of SO4 2− was studied in two hydrogen-based membrane biofilm reactors (MBfRs). One MBfR was initiated with SO4 2−-reducing conditions and gradually shifted to SeO4 2− reduction. The second MBfR was developed with a SeO4 2−-reducing biofilm, followed by SO4 2− introduction. Biofilms within both MBfRs achieved greater than 90% SeO4 2− reduction, even though the SeO4 2− concentration ranged from 1,000–11,000 μg/L, more than 20–200 times the maximum contaminant level for drinking water (50 μg/L). Biofilm microbial community composition, assessed by 16S rRNA gene-based amplicon pyrosequencing, was distinct between the two MBfRs and was framed by alterations in SeO4 2− loading. Specifically, high SeO4 2− loading resulted in communities mainly composed of denitrifying bacteria (e.g., Denitratisoma and Dechloromonas). In contrast, low loading led to mostly sulfate-reducing bacteria (i.e., Desulfovibrio) and sulfur-oxidizing bacteria (i.e., Sulfuricurvum and Sulfurovum). SeO4 2− was reduced to elemental selenium (Se°), which was visualized within the biofilm as crystalloid aggregates, with its fate corresponding to that of biofilm solids. In conclusion, microbial biofilm communities initiated under either SeO4 2− or SO4 2−-reducing conditions attained high SeO4 2− removal rates even though their microbial community composition was quite distinct. Biotechnol. Bioeng. 2016;113: 1736–1744.
KW - TEM-EDX
KW - biofilm
KW - pyrosequencing
KW - selenate
KW - sulfate
KW - sulfur-oxidizers
UR - http://www.scopus.com/inward/record.url?scp=84977142614&partnerID=8YFLogxK
UR - http://www.scopus.com/inward/citedby.url?scp=84977142614&partnerID=8YFLogxK
U2 - 10.1002/bit.25945
DO - 10.1002/bit.25945
M3 - Article
C2 - 26804665
SN - 0006-3592
VL - 113
SP - 1736
EP - 1744
JO - Biotechnology and bioengineering
JF - Biotechnology and bioengineering
IS - 8
ER -