Capturing of carbon dioxide by hydrogen derived from excess renewable energy (e.g., wind mills) to methane in a microbially catalyzed process offers an attractive technology for biogas production and upgrading. This bioconversion process is catalyzed by hydrogenotrophic methanogens, which are known to be sensitive to ammonia. In this study, the tolerance of the biogas process under supply of hydrogen, to ammonia toxicity was studied under mesophilic and thermophilic conditions. When the initial hydrogen partial pressure was 0.5 atm, the methane yield at high ammonia load (7 g NH+-N L) was 41.0% and 22.3% lower than that at low ammonia load (1 g NH+-N L) in mesophilic and thermophilic condition, respectively. Meanwhile no significant effect on the biogas composition was observed. Moreover, we found that hydrogentrophic methanogens were more tolerant to the ammonia toxicity than acetoclastic methanogens in the hydrogen enriched biogas production and upgrading processes. The highest methane production yield was achieved under 0.5 atm hydrogen partial pressure in batch reactors at all the tested ammonia levels. Furthermore, the thermophilic methanogens at 0.5 atm of hydrogen partial pressure were more tolerant to high ammonia levels (≥5 g NH+-N L), compared with mesophilic methanogens. The present study offers insight in developing resistant hydrogen enriched biogas production and upgrading processes treating ammonia-rich waste streams.
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机译:在微生物催化的过程中,将源自过量可再生能源(例如,风车)的氢气捕获的二氧化碳捕获为甲烷,为沼气的生产和升级提供了有吸引力的技术。这种生物转化过程由对氢敏感的氢营养型产甲烷菌催化。在这项研究中,研究了在嗜温和嗜热条件下,沼气工艺在氢气供应下对氨毒性的耐受性。当初始氢气分压为0.5 atm时,在中温和嗜热条件下,高氨负荷(7 g NH + -NL)时的甲烷产率比低氨负荷(1 g NH + -NL)时的甲烷产率低41.0%,低22.3%,分别。同时,未观察到对沼气组成的显着影响。此外,我们发现在富氢沼气的生产和升级过程中,氢营养型产甲烷菌比乙酰碎裂型产甲烷菌更能耐受氨中毒。在所有测试的氨水平下,在间歇反应器中,氢气分压为0.5 atm时,甲烷产量最高。此外,与中温产甲烷菌相比,在氢分压为0.5 atm时,嗜热产甲烷菌更能耐受高氨含量(≥5 g NH + -N L)。本研究提供了开发耐氢富集沼气生产和升级处理富氨废物流工艺的见识。
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