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Enhancement of bioenergy production from organic wastes by two-stage anaerobic hydrogen and methane production process

机译:两阶段厌氧制氢和甲烷生产工艺可提高有机废物的生物能生产能力

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The present study investigated a two-stage anaerobic hydrogen and methane process for increasing bioenergy production from organic wastes. A two-stage process with hydraulic retention time (HRT) 3d for hydrogen reactor and 12d for methane reactor, obtained 11% higher energy compared to a single-stage methanogenic process (HRT 15d) under organic loading rate (OLR) 3gVS/(Ld). The two-stage process was still stable when the OLR was increased to 4.5gVS/(Ld), while the single-stage process failed. The study further revealed that by changing the HRT_(hydrogen):HRT_(methane) ratio of the two-stage process from 3:12 to 1:14, 6.7%, more energy could be obtained. Microbial community analysis indicated that the dominant bacterial species were different in the hydrogen reactors (Thermoanaerobacterium thermosaccharolyticum-like species) and methane reactors (Clostridium thermocellum-like species). The changes of substrates and HRT did not change the dominant species. The archaeal community structures in methane reactors were similar both in single- and two- stage reactors, with acetoclastic methanogens Methanosarcina acetivorans-like organisms as the dominant species.
机译:本研究调查了两阶段厌氧制氢和甲烷工艺,以增加有机废物的生物能生产。在有机负荷率(OLR)为3gVS /(Ld)的条件下,氢气反应器的水力停留时间(HRT)为3d,甲烷反应器的水力停留时间为12d的两步法比单步产甲烷法(HRT 15d)的能量高11%。 )。当OLR增加到4.5gVS /(Ld)时,两阶段过程仍然稳定,而单阶段过程失败。研究进一步表明,通过将两阶段过程的HRT_(氢):HRT_(甲烷)比率从3:12更改为1:14,可得到6.7%的能量。微生物群落分析表明,在氢反应器(解热嗜热厌氧杆菌样)和甲烷反应器(类似热纤梭菌)中,优势细菌种类有所不同。底物和HRT的变化并没有改变优势种。甲烷反应器中的古细菌群落结构在单级反应器和两级反应器中都相似,其中以乙酰碎屑性产甲烷菌为样的拟吞噬乙炔甲烷菌。

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