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Improvement of COD and color removal from UASB treated poultry manure wastewater using Fenton's oxidation

机译:使用芬顿氧化法改善UASB处理的家禽粪便废水中的COD和脱色

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The applicability of Fenton's oxidation as an advanced treatment for chemical oxygen demand (COD) and color removal from anaerobically treated poultry manure wastewater was investigated. The raw poultry manure wastewater, having a pH of 7.30 (±0.2) and a total COD of 12,100 (±910) mg/L was first treated in a 15.7 L of pilot-scale up-flow anaerobic sludge blanket (UASB) reactor. The UASB reactor was operated for 72 days at mesophilic conditions (32 ± 2 ℃) in a temperature-controlled environment with three different hydraulic retention times (HRT) of 15.7, 12 and 8.0 days, and with organic loading rates (OLR) between 0.650 and 1.783 kg COD/(m~3 day). Under 8.0 days of HRT, the UASB process showed a remarkable performance on total COD removal with a treatment efficiency of 90.7% at the day of 63. The anaerobically treated poultry manure wastewater was further treated by Fenton's oxidation process using Fe~(2+) and H_2O_2 solutions. Batch tests were conducted on the UASB effluent samples to determine the optimum operating conditions including initial pH, effects of H_2O_2 and Fe~(2+) dosages, and the ratio of H_2O_2/Fe~(2+). Preliminary tests conducted with the dosages of 100mg Fe~(2+)/L and 200 mg H_2O_2/L showed that optimal initial pH was 3.0 for both COD and color removal from the UASB effluent. On the basis of preliminary test results, effects of increasing dosages of Fe~(2+) and H_2O_2 were investigated. Under the condition of 400 mg Fe~(2+)/L and 200 mg H_2O_2/L, removal efficiencies of residual COD and color were 88.7% and 80.9%, respectively. Under the subsequent condition of 100 mg Fe~(2+)/L and 1200 mg H_2O_2/L, 95% of residual COD and 95.7% of residual color were removed from the UASB effluent. Results of this experimental study obviously indicated that nearly 99.3% of COD of raw poultry manure wastewater could be effectively removed by a UASB process followed by Fenton's oxidation technology used as a post-treatment unit.
机译:研究了Fenton氧化作为厌氧处理的家禽粪便废水中化学需氧量(COD)和脱色的高级处理方法的适用性。首先在15.7 L的中试规模厌氧污泥床(UASB)反应器中处理pH为7.30(±0.2),总COD为12,100(±910)mg / L的家禽粪便废水。 UASB反应器在中温条件下(32±2℃)在温度控制的环境中运行72天,三个不同的水力停留时间(HRT)为15.7、12和8.0天,有机负荷率(OLR)为0.650和1.783千克COD /(m〜3天)。在HRT的8.0天下,UASB工艺在去除COD方面表现出显着的性能,在63天时的处理效率为90.7%。厌氧处理的家禽粪便废水经过Fenton氧化处理后使用Fe〜(2+)和H_2O_2解决方案。对UASB废水样品进行了分批测试,以确定最佳操作条件,包括初始pH,H_2O_2和Fe〜(2+)剂量的影响以及H_2O_2 / Fe〜(2+)的比例。以100mg Fe〜(2 +)/ L和200mg H_2O_2 / L的剂量进行的初步测试表明,最佳的初始pH值对于UASB废水的COD和脱色均为3.0。在初步试验结果的基础上,研究了增加Fe〜(2+)和H_2O_2用量的效果。在400 mg Fe〜(2 +)/ L和200 mg H_2O_2 / L的条件下,残留COD和颜色的去除效率分别为88.7%和80.9%。在随后的100 mg Fe〜(2 +)/ L和1200 mg H_2O_2 / L的条件下,从UASB废水中去除了95%的残留COD和95.7%的残留色。该实验研究的结果显然表明,UASB工艺,Fenton氧化技术作为后处理装置可以有效去除近99.3%的家禽粪便废水的COD。

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