期刊
BIORESOURCE TECHNOLOGY
卷 280, 期 -, 页码 143-150出版社
ELSEVIER SCI LTD
DOI: 10.1016/j.biortech.2019.02.007
关键词
H2S; Biogas desulfurization; Modeling; Biotrickling filter
资金
- key projects of National Water Pollution Control and Management of China [2013ZX07315-001-04]
- Natural Science Foundation of Shaanxi Province [2017JM5090]
- Key Laboratory of Membrane Separation of Shaanxi Province
- Innovative Research Team of Xi'an University of Architecture and Technology
This study investigated the characteristics of low H2S concentration biogas biodesulfurization using a lab-scale biotrickling filter (BTF). The influence of operational parameters on H2S removal efficiency and H2S distributions in packed bed was evaluated by establishing a counter-current one-dimensional mull-layer BTF model and statistical analysis of the simulation results. The overall biodesulfurization efficiency of counter-current BTF on treating low H2S concentration was 92.27 +/- 10.30%. The H2S distribution of the BTF packed bed could be predicted by the calibrated BTF model. The influence of the operational parameters on the H2S distribution of the packed bed was following the sequence of pH > empty bed retention time (EBRT) > gas-to-liquid flow ratio (G/L). The biogas biodesulfurization process was strongly related to the sulphide affinity constant. Moreover, a high substrate concentration of the SOB could further accelerate the biodesulfurization process of the biogas with low H2S concentration.
作者
我是这篇论文的作者
点击您的名字以认领此论文并将其添加到您的个人资料中。
推荐
暂无数据