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Degradation of phenol in an upflow anaerobic sludge blanket (UASB) reactor at ambient temperature

机译:室温下上流厌氧污泥层(UASB)反应器中的苯酚降解

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A synthetic wastewater containing phenol as sole substrate was treated in a 2.8 L upflow anaerobic sludge blanket (UASB) reactor at ambient temperature. The operation conditions and phenol removal efficiency were discussed, microbial population in the UASB sludge was identified based on DNA cloning, and pathway of anaerobic phenol degradation was proposed. Phenol in wastewater was degraded in an UASB reactor at loading rate up to 18 gCOD/(L centre dot d), with a 1:1 recycle ratio, at 26+- 1 deg C, pH 7.0-7.5. An UASB reactor was able to remove 99 percent of phenol up to 1226 mg/L in wastewater with 24 h of hydraulic retention time(HRT). For HRT below 24 h, phenol degradation efficiency decreased with HRT, from 95.4 percent at 16 h to 93.8 percent at 12 h. It further deteriorated to 88.5 percent when HRT reached 8 h. When the concentration of influent phenol of the reactor was 1260 mg/L( corresponding COD 3000 mg/L), with the HRT decreasing(from 40 h to 4 h, corresponding COD loading increasing), the biomass yields tended to increase from 0.265 to 3.08 g/(L centre dot d). While at 12 h of HRT, the biomass yield was lower. When HRT was 12 h, the methane yield was 0.308 L/(gCOD removed), which was the highest. Throughout the study, phenol was the sole organic substrate. The effluent contained only residual phenol without any detectable intermediates, such as benzoate, 4-hydrobenzoate or volatile fatty acids (VFAs). Based on DNA cloning analysis, the sludge was composed of five groups of microorganisms. Desulfotomaculum and Clostridium were likely responsible for the conversion of phenol to benzoate, which was further degraded by Syntrophus to acetate and H_2/CO_2. Methanogens lastly converted acetate and H_2/CO_2 TO methane. The role of epsilon-Proteobacteria was, however, unsure.
机译:在环境温度下,将含有苯酚作为唯一底物的合成废水在2.8 L上流厌氧污泥层(UASB)反应器中进行处理。讨论了操作条件和去除苯酚的效率,基于DNA克隆鉴定了UASB污泥中的微生物种群,并提出了厌氧降解苯酚的途径。废水中的苯酚在UASB反应器中以高达18 gCOD /(L中心点d)的加载速率在26±1摄氏度,pH 7.0-7.5下以1:1的循环比降解。 UASB反应器能够在24小时的水力停留时间(HRT)下去除废水中99%的苯酚,最高可达1226 mg / L。对于低于24小时的HRT,苯酚的降解效率随HRT的降低而降低,从16小时的95.4%降至12小时的93.8%。当HRT达到8小时时,它进一步恶化为88.5%。当反应器进水苯酚浓度为1260 mg / L(对应化学需氧量3000 mg / L)时,随着HRT的降低(从40 h降至4 h,对应化学需氧量增加),生物质产率倾向于从0.265增加至3.08 g /(L中心点d)。在HRT停留12小时时,生物量产量较低。当HRT为12 h时,甲烷产量为0.308 L /(除去的gCOD),这是最高的。在整个研究过程中,苯酚是唯一的有机底物。废水仅含有残留的苯酚,而没有任何可检测的中间体,例如苯甲酸酯,4-氢苯甲酸酯或挥发性脂肪酸(VFA)。根据DNA克隆分析,污泥由五组微生物组成。 Desulfotomaculum和梭状芽胞杆菌可能是苯酚向苯甲酸酯转化的原因,苯并四氢呋喃进一步将其降解为乙酸盐和H_2 / CO_2。产甲烷菌最后将乙酸盐和H_2 / CO_2转化为甲烷。但是,不确定ε-细菌的作用。

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