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Fermentative hydrogen production from beet sugar factory wastewater treatment in a continuous stirred tank reactor using anaerobic mixed consortia

机译:甜菜制糖厂废水在厌氧混合财团的连续搅拌釜反应器中进行发酵制氢

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摘要

A low pH, ethanol-type fermentation process was evaluated for wastewater treatment and bio-hydrogen production from acidic beet sugar factory wastewater in a continuous stirred tank reactor (CSTR) with an effective volume of 9.6 L by anaerobic mixed cultures in this present study. After inoculating with aerobic activated sludge and operating at organic loading rate (OLR) of 12 kgCOD·m-3·d-1, HRT of 8h, and temperature of 35℃ for 28 days, the CSTR achieved stable ethanol-type fermentation. When OLR was further increased to 18 kgCOD·m-3·d-1, on the 53rd day, ethanol-type fermentation dominant microflora was enhanced. The liquid fermentation products, including volatile fatty acids (VFAs) and ethanol, stabilized at 1493mg·L-1 in the bioreactor. Effluent pH, oxidation-reduction potential (ORP), and alkalinity ranged at 4.1-4.5, -250-(-290) mV, and 230-260mgCaCO3·L-1. The specific hydrogen production rate of anaerobic activated sludge was 0.1 L'gMLVSS-1· d-1 and the COD removal efficiency was 45%. The experimental results showed that the CSTR system had good operation stability and microbial activity, which led to high substrate conversion rate and hydrogen production ability.
机译:通过厌氧混合培养,评估了低pH,乙醇型发酵工艺用于废水处理和酸性甜菜制糖厂废水在连续搅拌釜反应器(CSTR)中的有效容量为9.6 L的酸性甜菜制糖厂废水的生产。接种好氧活性污泥,并在有机负荷率(OLR)为12 kgCOD·m-3·d-1,HRT为8h,温度为35℃的条件下运行28天后,CSTR达到了稳定的乙醇型发酵。当OLR进一步增加至18 kgCOD·m-3·d-1时,在第53天,乙醇型发酵优势菌群得到增强。生物反应器中的液体发酵产物,包括挥发性脂肪酸(VFAs)和乙醇,稳定在1493mg·L-1。出水pH,氧化还原电位(ORP)和碱度分别为4.1-4.5,-250-(-290)mV和230-260mgCaCO3·L-1。厌氧活性污泥的比产氢率为0.1 L'gMLVSS-1·d-1,COD去除率为45%。实验结果表明,CSTR系统具有良好的操作稳定性和微生物活性,可提高底物转化率和产氢能力。

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