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Anaerobic co-digestion of chemical- and ozone-pretreated sludge in hybrid upflow anaerobic sludge blanket reactor

机译:混合上流厌氧污泥床反应器中化学和臭氧预处理污泥的厌氧共消化

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The present study is an attempt to anaerobically co-digest excess sludge from aerobic facility of dairy wastewater treatment plant in a hybrid upflow anaerobic sludge blanket reactor. The sludge was made amenable for anaerobic degradation using ozone and chemical pretreatment. The efficiency of the treatment at optimized condition (pH 11 and ozone dosage 0.06 gO(3)/g suspended solids) showed 68 and 61% of chemical oxygen demand solubilization and suspended solids reduction, respectively. Further, anaerobic co-digestion of pretreated sludge was evaluated in two lab-scale hybrid upflow anaerobic sludge blanket reactors, namely experimental (ER) and control reactors (CR), with 5.6 L working volume for a period of 310 d. Treatment of dairy wastewater at the highest applied organic loading rate of 16.78 kg chemical oxygen demand/m(3) d, the biogas production increased in ER reactor (18.8 L/d) with the introduction of pretreated sludge than in CR reactor (17.9 L/d). The performance of ER reactor is not influenced by anaerobic co digestion of pretreated sludge, because no statistical difference between soluble chemical oxygen demand removal efficiencies of ER and CR reactors.
机译:本研究是在混合上流厌氧污泥毯式反应器中厌氧共消化来自乳品废水处理厂好氧设施的过量污泥的尝试。使用臭氧和化学预处理使污泥适合厌氧降解。在优化条件下(pH 11和臭氧剂量0.06 gO(3)/ g悬浮固体)的处理效率分别显示出68%和61%的化学需氧量溶解和悬浮固体减少。此外,在两个实验室规模的混合上流厌氧污泥毯式反应器(即实验(ER)和对照反应器(CR))中,以5.6 L的工作量在310 d的时间内评估了预处理污泥的厌氧共消化。以最高应用有机负荷率为16.78 kg化学需氧量/ m(3)d处理奶牛废水时,与CR反应器(17.9 L)相比,引入预处理污泥的ER反应器(18.8 L / d)的沼气产量增加/ d)。 ER反应器的性能不受预处理污泥厌氧共消化的影响,因为ER和CR反应器的可溶性化学需氧量去除效率之间没有统计差异。

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