Biological Co-treatment of H2S and reduction of CO2 to methane in an anoxic biological trickling filter upgrading biogas

被引:17
作者
Dupnock, Trisha L. [1 ]
Deshusses, Marc A. [1 ]
机构
[1] Duke Univ, Dept Civil & Environm Engn, 127C Hudson Hall,Box 90287, Durham, NC 27708 USA
基金
美国国家科学基金会;
关键词
Biotrickling filter; Biogas upgrading; Biological co-treatment; Renewable natural gas; Hydrogen sulfide; BIOTRICKLING FILTER; NITRATE REDUCTION; PILOT-SCALE; PERFORMANCE; HYDROGEN; REMOVAL; SULFIDE; NITRITE;
D O I
10.1016/j.chemosphere.2020.127078
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This study investigated the feasibility of co-treating H2S and CO2 in a biological trickling filter (BTF) inoculated with hydrogenotrophic methanogens (HMs) and nitrate-reducing, sulfur-oxidizing bacteria. This was accomplished by introducing a pure culture of Thiobacillus denitrificans in a BTF that was successfully upgrading a biogas mimic (60:40 CH4:CO2) to >97% methane using an enriched HM consortium. Nitrate was fed as the electron acceptor to oxidize H2S. The results revealed that a severe competition for hydrogen's electrons occurred between carbon dioxide and nitrate. Due to this competition, N:S loading rates of 16:1 were required to achieve >98% H2S removal, a ratio which is four times greater than the theoretical N:S ratio for complete sulfur oxidation. However, such high nitrate loading rates (>50 g NeNO3- m(-3) h(-1)) had a negative impact on the BTF's biogas upgrading performance. An electron balance illustrated the increasing diversion of H-2 electrons towards nitrate reduction as nitrate loading increased. Overall, this study showed that simultaneous biogas upgrading and H2S removal in a single bioreactor is possible, but that achieving high yields for both reactions requires further research in process and culture optimization. (C) 2020 Elsevier Ltd. All rights reserved.
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页数:9
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