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Treatment of Antibiotic Fermentation-Based Pharmaceutical Wastewater Using Anaerobic and Aerobic Moving Bed Biofilm Reactors Combined with Ozone/Hydrogen Peroxide Process

机译:厌氧和好氧移动床生物膜反应器结合臭氧/过氧化氢工艺处理抗生素发酵型制药废水

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摘要

A continuously operated laboratory scale anaerobic and aerobic moving bed biofilm reactors (MBBRs) combined with O_3/H_2O_2 process was experimented for antibiotic fermentation-based pharmaceutical wastewater. The experimental results indicated that 26.6% of chemical oxygen demand (COD) was removed, and 931-75 mg/L of volatile fatty acids (VFAs) was produced under the optimum conditions of the anaerobic MBBR at an influent pH of 6.5, hydraulic retention time (HRT) of 12 hr and organic loading rate (OLR) of 13 kg COD/(m~3•d) for the hydrolysis/acidification process. In addition, 91-0% of COD was removed at 1.5 m~3/h of aeration rate with the aerobic MBBR. The shape of bacteria inside the bio-carriers was characterized by a scanning electron microscope. The anaerobic MBBR bacteria were observed as long bacilli, and the aerobic MBBR bacteria were observed as mainly cocci and short bacilli. Finally, the residual non-biodegraded pollutants were mineralized by O_3/H_2O_2 oxidation with 0.5 of H_2O_2/O_3 molar ratio and 15 min of reaction time. The total removal efficiencies of COD and color reached 99.2 and 98.7%, respectively. Thus, this method might offer an effective way to treat wastewater from the pharmaceutical industry.
机译:连续运行的实验室规模的厌氧和好氧移动床生物膜反应器(MBBR)结合O_3 / H_2O_2工艺进行了实验,以抗生素发酵为基础的制药废水。实验结果表明,在厌氧MBBR的最佳条件下,进水pH值为6.5,水力保持力最大时,去除了26.6%的化学需氧量(COD),并生产了931-75 mg / L的挥发性脂肪酸(VFA)水解/酸化过程的时间(HRT)为12小时,有机负载率(OLR)为13千克COD /(m〜3•d)。另外,用好氧MBBR以1.5 m〜3 / h的曝气速率去除了91-0%的COD。生物载体内部细菌的形状通过扫描电子显微镜表征。厌氧MBBR细菌为长杆菌,好氧MBBR细菌主要为球菌和短杆菌。最后,残留的非生物降解污染物通过O_3 / H_2O_2氧化以0.5的H_2O_2 / O_3摩尔比和15分钟的反应时间被矿化。 COD和颜色的总去除效率分别达到99.2和98.7%。因此,该方法可能提供一种处理制药工业废水的有效方法。

著录项

  • 来源
    《Environmental progress》 |2014年第1期|170-177|共8页
  • 作者单位

    Key Laboratory of Functional Inorganic Material Chemistry, Ministry of Education of the People's Republic of China,Department of Environmental Science, Heilongjiang University, Harbin 150080 People's Republic of China,Key Laboratory of Chemical Engineering Process & Technology for High-efficiency Conversion, Department of Environmental Science, Heilongjiang University, Harbin 150080, People's Republic of China;

    College of Environmental Science and Engineering, Department of Environmental Science, Beijing Forestry University,Beijing, 100083 People's Republic of China;

    Key Laboratory of Chemical Engineering Process & Technology for High-efficiency Conversion, Department of Environmental Science, Heilongjiang University, Harbin 150080, People's Republic of China;

    Key Laboratory of Functional Inorganic Material Chemistry, Ministry of Education of the People's Republic of China,Department of Environmental Science, Heilongjiang University, Harbin 150080 People's Republic of China,Key Laboratory of Chemical Engineering Process & Technology for High-efficiency Conversion, Department of Environmental Science, Heilongjiang University, Harbin 150080, People's Republic of China;

    Key Laboratory of Functional Inorganic Material Chemistry, Ministry of Education of the People's Republic of China,Department of Environmental Science, Heilongjiang University, Harbin 150080 People's Republic of China;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    moving bed biofilm reactor; antibiotic fermentation-based pharmaceutical wastewater; hydrolysis/acidification; aerobic biological process; O_3/H_2O_2 process;

    机译:移动床生物膜反应器;基于抗生素发酵的制药废水;水解/酸化;有氧生物过程O_3 / H_2O_2过程;
  • 入库时间 2022-08-17 13:28:11

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