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Fed batch production of hydrogen from palm oil mill effluent using anaerobic microflora

机译:使用厌氧菌群从棕榈油厂废水中补料分批生产氢气

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摘要

Anaerobic production of hydrogen from palm oil mill effluent (POME) by microflora was investigated in 5-1 bioreactor at 60℃ and pH 5.5. POME sludge was collected from the anaerobic pond of a POME treatment plant at a palm oil mill and used as a source of inocula. A batch reactor was found to yield a total of 4708 ml H_2/(l POME) and the maximum evolution rate was 454 ml-H_2/(l POMEh). A fed batch process was conducted after 50 h. Two liters of reaction medium was removed and 21 of fresh POME was added to the reactor every 24 h (15 times). The reproducibility of the fed batch process checked by changing the feeding time every 8h (10 times). A yield of 2382 ml H_2/(l POME) and 2419 ml H_2/(l POME) at maximum evolution rate of 313 ml H_2/(l POME h) and 436 ml H_2/(l POME h) were obtained, respectively. Throughout the study, methane gas was not observed in the evolved gas mixture.
机译:在5-1生物反应器中,于60℃和pH 5.5下,研究了由微生物区系从棕榈油厂废水(POME)厌氧制氢。在棕榈油厂从POME处理厂的厌氧池收集POME污泥,并将其用作接种源。发现间歇反应器总共产生4708ml H_2 /(l POMEh),最大析出速率为454 ml-H_2 /(l POMEh)。 50小时后进行补料分批处理。每24小时(15次)除去两升反应介质,并向反应器中加入21份新鲜的POME。通过每8小时(10次)更改一次进料时间来检查分批进料过程的可重复性。在最大析出速率为313 ml H_2 /(l POME h)和436 ml H_2 /(l POME h)的情况下,分别获得了2382 ml H_2 /(l POMEh)和2419 ml H_2 /(l POME)的产量。在整个研究过程中,在混合气体中未观察到甲烷气体。

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