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Model-based analyses of chromate, selenate and sulfate reduction in a methane-based membrane biofilm reactor
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Abstract Selenate (SeO4 2−) and sulfate (SO4 2−) are frequently present together with chromate (CrO4 2−) in certain industrial wastewaters. SeO4 2− and CrO4 2− are required to be reduced while SO4 2− reduction should be minimized to avoid the production of toxic sulfide. In this study, a modified biofilm model was employed to investigate the interactions between CrO4 2−, SeO4 2− and SO4 2− bioreduction in a methane (CH4)-based membrane biofilm reactor (MBfR). The model was calibrated using steady-state experimental data of two reported CH4-based MBfRs reducing these oxyanions. The modeling results suggested that the majority of methanotrophs (>80%) were located in the outer layer of the biofilm, while the oxyanions-reducing bacteria preferred to grow close to the membrane. The introduction of SeO4 2− or SO4 2− enriched selenate/sulfate-reducing bacteria (SeRB/SRB) but decreased the abundance of chromate-reducing bacteria (CRB). A biofilm thickness of >300 μm, an HRT of higher than 4 h and an influent dissolved oxygen concentration of 0.3 mg /L were favorable for simultaneous high-level CrO4 2− and SeO4 2− removal. A two-stage MBfR system with optimized operational conditions showed promise in retaining high-purity (>98%) selenium nanoparticles when treating both CrO4 2− and SeO4 2− impacted wastewaters. Moreover, the model indicated that efficient CrO4 2− removal (>90%) along with minor SO4 2− reduction (<10%) could be realized via maintaining appropriate biofilm thickness (200-250 μm) and influent dissolved oxygen (0.7–0.8 mg /L) in a single MBfR. These findings offer insights for the design and operation of CH4-based technology for remediating CrO4 2− contaminated industrial wastewaters.
Model-based analyses of chromate, selenate and sulfate reduction in a methane-based membrane biofilm reactor
Graphical abstract Display Omitted
Abstract Selenate (SeO4 2−) and sulfate (SO4 2−) are frequently present together with chromate (CrO4 2−) in certain industrial wastewaters. SeO4 2− and CrO4 2− are required to be reduced while SO4 2− reduction should be minimized to avoid the production of toxic sulfide. In this study, a modified biofilm model was employed to investigate the interactions between CrO4 2−, SeO4 2− and SO4 2− bioreduction in a methane (CH4)-based membrane biofilm reactor (MBfR). The model was calibrated using steady-state experimental data of two reported CH4-based MBfRs reducing these oxyanions. The modeling results suggested that the majority of methanotrophs (>80%) were located in the outer layer of the biofilm, while the oxyanions-reducing bacteria preferred to grow close to the membrane. The introduction of SeO4 2− or SO4 2− enriched selenate/sulfate-reducing bacteria (SeRB/SRB) but decreased the abundance of chromate-reducing bacteria (CRB). A biofilm thickness of >300 μm, an HRT of higher than 4 h and an influent dissolved oxygen concentration of 0.3 mg /L were favorable for simultaneous high-level CrO4 2− and SeO4 2− removal. A two-stage MBfR system with optimized operational conditions showed promise in retaining high-purity (>98%) selenium nanoparticles when treating both CrO4 2− and SeO4 2− impacted wastewaters. Moreover, the model indicated that efficient CrO4 2− removal (>90%) along with minor SO4 2− reduction (<10%) could be realized via maintaining appropriate biofilm thickness (200-250 μm) and influent dissolved oxygen (0.7–0.8 mg /L) in a single MBfR. These findings offer insights for the design and operation of CH4-based technology for remediating CrO4 2− contaminated industrial wastewaters.
Model-based analyses of chromate, selenate and sulfate reduction in a methane-based membrane biofilm reactor
Wang, Zhen (author) / Chen, Xueming (author) / Zhao, He-Ping (author)
2021-10-05
Article (Journal)
Electronic Resource
English
Elsevier | 2022
|DOAJ | 2019
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