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Simultaneous biohydrogen production and wastewater treatment in biofilm configured anaerobic periodic discontinuous batch reactor using distillery wastewater

机译:利用酿酒厂废水的生物膜结构厌氧间歇式间歇间歇反应器中同时进行生物氢生产和废水处理

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Biohydrogen (H_2) production with simultaneous wastewater treatment was studied in anaerobic sequencing batch biofilm reactor (AnSBBR) using distillery wastewater as substrate at two operating pH values. Selectively enriched anaerobic mixed consortia sequentially pretreated with repeated heat-shock (100 ℃; 2h) and acid (pH -3.0; 24h) methods, was used as parent inoculum to startup the bioreactor. The reactor was operated at ambient temperature (28±2℃) with detention time of 24h in periodic discontinuous batch mode. Experimental data showed the feasibility of hydrogen production along with substrate degradation with distillery wastewater as substrate. The performance of the reactor was found to be dependent on the operating pH. Adopted acidophilic microenvir-onment (pH 6.0) favored H_2 production (H_2 production rate—26 mmol H_2/day; specific H_2 production—6.98 mol H_2/kgCOD_R-day) over neutral microenvironment (H_2 production rate—7mmolH_2/day; specific H_2 production—1.63molH_2/kgCOD_R-day). However, COD removal efficiency was found to be effective in operated neutral microenvironment (pH 7—69.68%; pH 6.0—56.25%). The described process documented the dual benefit of renewable energy generation in the form of H_2 with simultaneous wastewater treatment utilizing it as substrate.
机译:在两个操作pH值下,以酿酒厂废水为底物,在厌氧测序分批生物膜反应器(AnSBBR)中研究了同时进行废水处理的生物氢(H_2)生产。选择性富集的厌氧混合财团依次用反复的热休克(100℃; 2h)和酸(pH -3.0; 24h)方法预处理,作为母体接种物启动生物反应器。反应器在环境温度(28±2℃)下,以不连续的间歇间歇模式在24h的停留时间下运行。实验数据表明,以酿酒厂废水为底物,制氢和底物降解的可行性。发现反应器的性能取决于操作pH。与中性微环境(H_2产生率—7mmolH_2 /天;特定的H_2产生)相比,采用的嗜酸微环境(pH 6.0)有利于H_2产生(H_2产生率-26 mmol H_2 /天;比H_2产生-6.98 mol H_2 / kgCOD_R-day)。 -1.63molH_2 / kgCOD_R-day)。但是,发现COD去除效率在操作的中性微环境(pH 7-69.68%; pH 6.0-56.25%)中有效。所描述的过程记录了以H_2形式产生可再生能源的双重好处,同时利用其作为底物进行废水处理。

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