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Combined chemical and biological oxidation of penicillin formulation effluent

机译:青霉素制剂废水的化学和生物氧化联合

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Antibiotic formulation effluent is well known for its important contribution to environmental pollution due to its fluctuating and recalcitrant nature. In the present study, the chemical treatability of penicillin formulation effluent (average filtered CODo = 830 mg/l; average soluble CODo = 615 mg/l; pH(o) = 6.9) bearing the active substances penicillin Amoxicillin Trihydrate (C16H19N3O5S . 3H(2)O) and the P-lactamase inhibitor Potassium Clavulanate (C8H8KNO5) has been investigated. For this purpose, the penicillin formulation effluent was subjected to ozonation (applied ozone dose = 2500 mg/(1 x h)) at varying pH (2.5-12.0) and O-3 + H2O2 (perozonation) at different initial H2O2 concentrations (= 2-40 mM) and pH 10.5. According to the experimental results, the overall Chemical Oxygen Demand (COD) removal efficiency varied between 10 and 56% for ozonation and 30% (no H2O2) and 83% (20 mM H2O2) for the O-3 + H2O2 process. The addition of H2O2 improved the COD removal rates considerably even at the lowest studied H2O2 concentration. An optimum H2O2 concentration of 20 mM existed at which the highest COD removal efficiency and abatement kinetics were obtained. The ozone absorption rate ranged between 53% (ozonation) and 68% (perozonation). An ozone input of 800 mg/l in 20 min was sufficient to achieve the highest BOD5/COD (biodegradability) ratio (=0.45) and BOD5 value (109 mg/l) for the pre-treated penicillin formulation effluent. After the establishment of optimum ozonation and perozonation conditions, mixtures of synthetic domestic wastewater+raw, ozonated and perozonated penicillin formulation effluent were subjected to biological activated sludge treatment at a food-to-microorganisms (F/M) ratio of 0.23 mg COD/(mg MLSS x d), using a consortium of acclimated microorganisms. COD removal efficiencies of the activated sludge process were 71, 81 and 72% for pharmaceutical wastewater containing synthetic domestic wastewater mixed with either raw, ozonated or perozonated formulation effluent, respectively. The ultimate COD value obtained after 24-h biotreatment of the synthetic domestic wastewater+pre-ozonated formulation effluent mixture was around 100 mg/l instead of 180 mg/l which was the final COD obtained for the wastewater mixture containing raw formulation effluent, indicating that pre-ozonation at least partially removed the non-biodegradable COD fraction of the formulation effluent.
机译:抗生素制剂废水由于其波动和顽强的性质而对环境污染具有重要贡献,因此众所周知。在本研究中,含有活性物质青霉素三水合阿莫西林(C16H19N3O5S.CH)的青霉素制剂流出物(平均过滤的CODo = 830 mg / l;平均可溶性CODo = 615 mg / l; pH(o)= 6.9)的化学可处理性。 2)O)和β-内酰胺酶抑制剂克拉维酸钾(C8H8KNO5)已被研究。为此,在不同的初始H2O2浓度(= 2)下,在不同的pH(2.5-12.0)和O-3 + H2O2(过臭氧化)下,对青霉素制剂流出物进行臭氧处理(施加的臭氧剂量= 2500 mg /(1 xh))。 -40 mM)和pH 10.5。根据实验结果,总的化学需氧量(COD)去除效率在臭氧化处理中介于10%到56%之间,在O-3 + H2O2工艺中介于30%(没有H2O2)和83%(20 mM H2O2)之间。即使在研究的最低H2O2浓度下,添加H2O2仍可显着提高COD去除率。存在的最佳H2O2浓度为20 mM,在该浓度下可获得最高的COD去除效率和减排动力学。臭氧吸收率介于53%(臭氧化)和68%(过臭氧化)之间。在20分钟内输入800 mg / l的臭氧足以使预处理的青霉素制剂流出物达到最高的BOD5 / COD(生物降解性)比(= 0.45)和BOD5值(109mg / l)。在确定最佳的臭氧化和过臭氧化条件后,将合成生活废水+原始,臭氧化和过臭氧化青霉素制剂流出物的混合物以食品与微生物(F / M)之比为0.23 mg COD /()进行生物活性污泥处理。 mg MLSS xd),使用适应微生物的联盟。活性污泥工艺的化学需氧量去除效率分别为71%,81%和72%,对于制药废水,其中含有合成的生活废水,混合了生化,臭氧化或过臭氧化的配方废水。合成生活废水+预臭氧处理的配方废水混合物经过24小时生物处理后获得的最终COD值约为100 mg / l,而不是180 mg / l,后者是含原料配方废水的废水混合物的最终COD,表明预臭氧化至少部分去除了制剂流出物中不可生物降解的COD部分。

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