Treatment of Citrus Juice Process Wastewater with UASB and Biogas Production

Sevgi Güneş Durak, Seren Acarer, Güler Türkoğlu Demirkol
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Abstract

A lab-scale up-flow anaerobic sludge blanket (UASB) reactor was used for biogas production from the citrus juice process wastewater (CPWW). The volume of the reactor was 11.5 L. During 200 days of the reactor, the organic loading rate (OLR) value changed from 1.8-21.9 kgCOD./m3.d, upflow velocities (Vup) 0.1-5.2 m/h and hydraulic retention time (HRT) changed from 0.042 to 4.16 days. The reactor showed a stable performance at all organic loadings. The COD removal efficiencies obtained from the experiments are 71.5 ± 21% and 83.3 ± 16.3% for total and soluble COD, respectively. The acetic acid concentration changed from 135 to 650 mg/L. The temperature was kept in the range of 35.1 ± 1.4 oC, the pH in the range of 6.6 ± 0.2, and the alkalinity was controlled daily and kept in the range of 411 ± 273 CaCO3 mg/L. After anaerobic reactions, 6283 ± 3476 m3/d biogas was produced and the methane concentration in the biogas was 65.5 ± 11.5%. Depending on the methane production, the annual energy value potential that can be obtained from the existing UASB reactor is estimated as 48,768 kWh.
UASB联合产气法处理柑桔汁加工废水
采用实验室规模上流式厌氧污泥毯反应器(UASB)对柑桔汁生产废水进行了产气研究。反应器容积为11.5 l,在反应器运行200 d期间,有机负载量(OLR)值在1.8 ~ 21.9 kgcod /m3之间变化。d,上升流速(Vup)为0.1 ~ 5.2 m/h,水力停留时间(HRT)为0.042 ~ 4.16 d。该反应器在各种有机负荷下均表现出稳定的性能。总COD去除率为71.5±21%,可溶性COD去除率为83.3±16.3%。乙酸浓度从135 ~ 650 mg/L变化。温度控制在35.1±1.4℃,pH控制在6.6±0.2,碱度控制在411±273 CaCO3 mg/L。厌氧反应后产沼气6283±3476 m3/d,沼气中甲烷浓度为65.5±11.5%。根据甲烷产量的不同,现有UASB反应器每年可获得的能源价值潜力估计为48,768千瓦时。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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