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采用混合上流式厌氧污泥-生物炭床反应器强化稻壳热气化焦油溶液的厌氧消化。

Enhanced anaerobic digestion of tar solution from rice husk thermal gasification with hybrid upflow anaerobic sludge-biochar bed reactor.

机构信息

College of Environment and Ecology, Chongqing University, 400045, PR China; Material Cycles Division, National Institute for Environmental Studies, Tsukuba 305-8506, Japan.

Material Cycles Division, National Institute for Environmental Studies, Tsukuba 305-8506, Japan; School of Environmental Science and Engineering, Nanjing Tech University, Nanjing 211816, PR China.

出版信息

Bioresour Technol. 2022 Mar;347:126688. doi: 10.1016/j.biortech.2022.126688. Epub 2022 Jan 8.

Abstract

Tar generated as a by-product during biomass gasification contains a high concentration of refractory organic matters. In this study, a hybrid upflow anaerobic sludge-biochar bed reactor was established for tar treatment, and the methane yield was 120-154 NmL-CH/g-COD, 20-30% higher than the control reactor. COD removal and methane production significantly decreased in both reactors when the influent tar concentration was doubled from 4954 mg-COD/L to 9964 mg-COD/L. When the influent concentration was reduced, the biochar packed reactor showed a faster recovery. Batch tests confirmed that higher tar concentration inhibited methane production and induced longer lagphase. Biochar addition effectively relieved the inhibition and prolonged the retention of organic matters. SEM observation and 16S rRNA analysis suggested that biochar also acted as the microbe's carrier, and promoted the growth of some microbes. The results of this study provide new ideas for tar treatment.

摘要

在生物质气化过程中产生的焦油是一种高浓度的难处理有机物。本研究建立了一种上流式厌氧污泥-生物炭床混合反应器来处理焦油,甲烷产率为 120-154 NmL-CH/g-COD,比对照反应器高 20-30%。当进水焦油浓度从 4954mg-COD/L 增加到 9964mg-COD/L 时,两个反应器的 COD 去除率和甲烷产量均显著下降。当进水浓度降低时,生物炭填充反应器表现出更快的恢复能力。批处理实验证实,较高的焦油浓度会抑制甲烷生成并导致更长的迟滞期。生物炭的添加能有效缓解抑制作用并延长有机物的停留时间。SEM 观察和 16S rRNA 分析表明,生物炭还可以作为微生物的载体,促进一些微生物的生长。本研究结果为焦油处理提供了新的思路。

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