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Performance of an up-flow anaerobic stage reactor (UASR) in the treatment of pharmaceutical wastewater containing macrolide antibiotics

机译:上流厌氧段反应器(UASR)在处理含有大环内酯类抗生素的制药废水中的性能

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The performance of an up-flow anaerobic stage reactor (UASR) treating pharmaceutical wastewater containing macrolide antibiotics was investigated. Specifically, it was determined whether a UASR could be used as pre-treatment system at an existing pharmaceutical production plant to reduce the antibiotics in the trade effluent. Accordingly, a UASR was developed with an active reactor volume of 11L being divided into four 2.75 L stages. Each stage of the reactor was an up-flow sludge blanket reactor and had a 3-phase separator baffle to retain biomass. The reactor was fed with real pharmaceutical wastewater containing Tylosin and Avilamycin antibiotics and operated with step-wise increases in the reactor organic loading rate (OLR) from 0.43 to 3.73 kg chemical oxygen demand (COD) m~(-3) d~(-1), and then reduced to 1.86, over 279 days. The process performance of the reactor was characterised in terms of its COD removal, Tylosin reduction, pH, VFA production, methane yield and sludge washout. At a total hydraulic retention time (HRT) of 4 d and OLR of 1.86 kg COD m~(-3) d~(-1), COD reduction was 70-75%, suggesting the biomass had acclimated to the antibiotics. Furthermore, an average of 95% Tylosin reduction was achieved in the UASR, indicating that this antibiotic could be degraded efficiently in the anaerobic reactor system. In addition, the influence of elevated Tylosin concentrations on the UASR process performance was studied using additions of Tylosin phosphate concentrate. Results showed similar efficiency for COD removal when Tylosin was present at concentrations ranging from 0 to 400 mgL~(-1) (mean removal over this range was 93%), however, at Tylosin concentrations of 600 and 800 mg L~(-1) there was a slight decline in treatment efficiency at 85% and 75% removal, respectively.
机译:研究了上流厌氧级反应器(UASR)处理含有大环内酯类抗生素的制药废水的性能。具体而言,确定了UASR是否可以在现有制药厂中用作预处理系统,以减少工业废水中的抗生素。因此,开发了一种UASR,其活性反应器体积为11L,分为四个2.75L级。反应器的每个阶段是上流式污泥床反应器,并具有三相分离器挡板以保留生物质。向反应器中注入含泰乐菌素和阿维拉霉素抗生素的实际制药废水,并在反应器有机负荷率(OLR)从0.43逐步增加到3.73 kg化学需氧量(COD)m〜(-3)d〜(- 1),然后在279天内减少到1.86。反应器的工艺性能通过其COD去除,泰乐菌素还原,pH,VFA产生,甲烷收率和污泥冲刷来表征。在4 d的总水力停留时间(HRT)和1.86 kg COD m〜(-3)d〜(-1)的OLR下,COD降低了70-75%,表明生物量已经适应了抗生素。此外,UASR中的泰乐菌素平均降低了95%,这表明该抗生素可以在厌氧反应器系统中有效降解。此外,使用磷酸泰乐菌素浓缩液研究了泰乐菌素浓度升高对UASR工艺性能的影响。结果表明,当泰乐菌素的浓度范围为0至400 mgL〜(-1)时,COD去除效率相似(该范围内的平均清除率为93%),而当泰乐菌素浓度为600和800 mg L〜(-1时)。 )去除率分别为85%和75%时,治疗效率略有下降。

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