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Integration of acidogenic and methanogenic processes for simultaneous production of biohydrogen and methane from wastewater treatment

机译:整合产酸和产甲烷工艺,可同时处理废水中的生物氢和甲烷

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Feasibility of integrating acidogenic and methanogenic processes for simultaneous production of biohydrogen (H_2) and methane (CH_4) was studied in two separate biofilm reactors from wastewater treatment. Acidogenic bioreactor (acidogenic sequencing batch biofilm reactor, AcSBBR) was operated with designed synthetic wastewater [organic loading rate (OLR) 4.75 kg COD/m~3-day] under acidophilic conditions (pH 6.0) using selectively enriched acidogenic mixed consortia. The resultant outlet from AcSBBR composed of fermentative soluble intermediates (with residual carbon source), was used as feed for subsequent methanogenic bioreactor (methanogenic/anaerobic sequencing batch biofilm reactor, AnSBBR, pH 7.0) to generate additional biogas (CH_4) utilizing residual organic composition employing anaerobic mixed consortia. During the stabilized phase of operation (after 60 days) AcSBBR showed H_2 production of 16.91 mmol/day in association with COD removal efficiency of 36.56% (SDR_A-1.736kgCOD/m~3-day). AnSBBR showed additional COD removal efficiency of 54.44% (SDR_M-1.071 kg COD/m~3-day) along with CH_4 generation. Integration of the acidogenic and methanogenic processes enhanced substrate degradation efficiency (SDR_T-4.01kgCOD/m~3-day) along with generation of both H_2 and CH_4 indicating sustainability of the process.
机译:在两个独立的废水处理生物膜反应器中,研究了整合产酸和产甲烷工艺同时生产生物氢(H_2)和甲烷(CH_4)的可行性。产酸生物反应器(产酸测序批处理生物膜反应器,AcSBBR)与设计合成废水[有机负荷率(OLR)4.75 kg COD / m〜3天]在嗜酸条件(pH 6.0)下使用选择性富集的产酸混合财团进行操作。 AcSBBR的最终出口由发酵可溶性中间体(具有残留碳源)组成,用作后续产甲烷生物反应器(甲烷/厌氧测序批生物膜反应器,AnSBBR,pH 7.0)的进料,从而利用残留有机成分生成其他沼气(CH_4)雇用厌氧混合财团。在稳定运行阶段(60天后),AcSBBR显示H_2的产量为16.91 mmol /天,COD去除效率为36.56%(SDR_A-1.736kgCOD / m〜3天)。 AnSBBR显示,随着CH_4的产生,额外的COD去除效率为54.44%(SDR_M-1.071 kg COD / m〜3天)。产酸和产甲烷过程的整合提高了底物的降解效率(SDR_T-4.01kgCOD / m〜3天),同时产生了H_2和CH_4,表明了该过程的可持续性。

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