Syngas biomethanation using trickle bed reactor, impact of external hydrogen addition at high loading rate.xlsx
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https://figshare.com/articles/dataset/Syngas_biomethanation_using_trickle_bed_reactor_impact_of_external_hydrogen_addition_at_high_loading_rate_xlsx/28738172/1
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Syngas is a mixture of CO, CO<sub>2</sub>, and H<sub>2</sub> produced from gasification carbon-containing feedstocks. Syngas can be biologically converted into methane (CH<sub>4</sub>) using microbial consortia at lower energy input compared to conventional catalytic processes called syngas biomethanation. However, challenges such as H<sub>2</sub> limitation, poor gas solubility, and cell damage from mechanical agitation impact conversion efficiency. Trickle bed reactors (TBRs) offer a promising solution to these challenges by enhancing gas-liquid transfer through biofilm formation on packing material while minimizing shear stress, thus improving CH<sub>4</sub> productivity. Accordingly, this study investigated the effect of external hydrogen (H<sub>2</sub>) injection on syngas biomethanation using two thermophilic TBRs at 51 ˚C. One TBR (TBR Control) was fed with syngas containing 15% CO, while the other received additional H<sub>2 </sub>(TBR Test). Both TBRs effectively converted syngas to CH<sub>4</sub>, but TBR Test achieved higher performance, with over 90% CH<sub>4</sub> conversion efficiency at a gas loading rate of 15 m<sup>3</sup>/m<sup>3</sup>·d and a peak CH<sub>4</sub> production rate of 4.5 mmol/L_bed·h at 20 m<sup>3</sup>/m<sup>3</sup>·d. Volatile fatty acid concentrations remained low. 16S rRNA sequencing analysis showed dominance of <i>Methanobacterium</i>, indicating methanogenesis-driven activity. Overall, the study highlights the benefit of H<sub>2</sub> injection during syngas biomethanation and suggests future work should focus on optimizing reactor control to further enhance capacity.
合成气(Syngas)是由含碳原料经气化制备的一氧化碳(CO)、二氧化碳(CO₂)与氢气(H₂)的混合气体。相较于传统催化工艺,合成气可通过微生物菌群(microbial consortia)实现生物转化以生成甲烷(CH₄),该转化过程即合成气生物甲烷化(syngas biomethanation),且其能量输入更低。然而,氢气限制、气体溶解性不佳以及机械搅拌引发的细胞损伤等问题,会对转化效率产生不利影响。滴流床反应器(Trickle Bed Reactors, TBRs)可为上述挑战提供颇具前景的解决方案:其通过在填料表面形成生物膜强化气液传质,同时可有效降低剪切应力,进而提升甲烷产率。据此,本研究在51℃条件下,采用两台嗜热型滴流床反应器,探究了外源氢气(H₂)补加对合成气生物甲烷化的影响。其中一台反应器(对照组TBR)以含15%一氧化碳的合成气为进料,另一台实验组TBR则额外补加氢气。两台反应器均成功将合成气转化为甲烷,但实验组TBR的性能更优:在气体负荷为15 m³/(m³·d)时,甲烷转化效率超过90%;在20 m³/(m³·d)的负荷下,甲烷产率峰值可达4.5 mmol/(L_床·h)。体系内挥发性脂肪酸浓度始终维持在较低水平。16S核糖体RNA(16S rRNA)测序分析结果显示,产甲烷杆菌属(Methanobacterium)为菌群优势菌属,表明体系的核心代谢活性为产甲烷途径。综上,本研究证实了合成气生物甲烷化过程中补加氢气的积极作用,并建议未来研究应聚焦于反应器调控优化,以进一步提升系统产能。
提供机构:
Bilgiç, Begüm; Feng, Lu; Abera, Getachew Birhanu; Os Andersen, Thea; Horn, Svein Jarle; Sposób, Michal
创建时间:
2025-04-06



