Jung Jin-Young, Chung Yun-Chul, Shin Hang-Sik, Son Dae-Hee
Environment and Process Technology Division, Korea Institute of Science and Technology, 39-1 Hawolgok-dong, Sungbuk-ku, Seoul 136-791, South Korea.
Water Res. 2004 Jan;38(2):347-54. doi: 10.1016/j.watres.2003.09.025.
The modified zeo-SBR is recommended for a new nitrogen removal process that has a special function of consistent ammonium exchange and bioregeneration of zeolite-floc. Three sets of sequencing batch reactors, control, zeo-SBR, and modified zeo-SBR were tested to assess nitrogen removal efficiency. The control reactor consisted of anoxic-fill, aeration-mixing, settling, and decanting/idle phases, meaning that nitrogen removal efficiency was dependent on the decanting volume in a cycle. The zeo-SBR reactor was operated in the same way as the control reactor, except for daily addition of powdered zeolite in the SBR reactor. The operating order sequences in the zeo-SBR were changed in the modified zeo-SBR. Anoxic-fill phase was followed by aeration-mixing phase in the zeo-SBR, while aeration-mixing phase was followed by anoxic-fill phase in the modified zeo-SBR to carry NH4(+)-N over to the next operational cycle and to reduce total nitrogen concentration in the effluent. In the modified zeo-SBR, nitrification and biological regeneration occurred during the initial aeration-mixing phase, while denitrification and ammonium adsorption occurred in the following anoxic-fill phase. The changed operational sequence in the modified zeo-SBR to adapt the ammonium adsorption and biological regeneration of the zeolite-floc could enhance nitrogen removal efficiency. As a result of the continuous operation, the nitrogen removal efficiencies of the control and zeo-SBR were in 68.5-70.9%, based on the 33% of decanting volume for a cycle. The zeo-SBR showed a consistent ammonium exchange and bio-regeneration in the anoxic-fill and aeration-mixing phases, respectively. Meanwhile, the effluent total nitrogen of the modified zeo-SBR showed 50-60 mg N/L through ammonium adsorption of the zeolite-floc when the influent ammonium concentration was 315 mg N/L, indicating the T-N removal efficiency was enhanced over 10% in the same HRT and SRT conditions as those of control and zeo-SBR reactors. The ammonium adsorption capacity was found to be 6-7 mg NH4(+)-N/g FSS that is equivalent to 40 mg NH4(+)-N/L of ammonium nitrogen removal.
改良型沸石序批式反应器(modified zeo-SBR)被推荐用于一种新型的脱氮工艺,该工艺具有沸石絮体持续铵交换和生物再生的特殊功能。测试了三组序批式反应器,即对照组、沸石序批式反应器(zeo-SBR)和改良型沸石序批式反应器,以评估脱氮效率。对照组反应器由缺氧填充、曝气混合、沉淀和滗水/闲置阶段组成,这意味着脱氮效率取决于一个周期内的滗水量。沸石序批式反应器的运行方式与对照组反应器相同,只是在序批式反应器(SBR)中每天添加粉末状沸石。改良型沸石序批式反应器改变了沸石序批式反应器(zeo-SBR)的运行顺序。在沸石序批式反应器(zeo-SBR)中,缺氧填充阶段之后是曝气混合阶段,而在改良型沸石序批式反应器中,曝气混合阶段之后是缺氧填充阶段,以便将NH4(+)-N带入下一个运行周期并降低出水的总氮浓度。在改良型沸石序批式反应器中,硝化作用和生物再生发生在初始曝气混合阶段,而反硝化作用和铵吸附发生在随后的缺氧填充阶段。改良型沸石序批式反应器中改变的运行顺序以适应沸石絮体的铵吸附和生物再生,可以提高脱氮效率。连续运行的结果是,基于一个周期33%的滗水量,对照组和沸石序批式反应器(zeo-SBR)的脱氮效率在68.5 - 70.9%之间。沸石序批式反应器(zeo-SBR)分别在缺氧填充和曝气混合阶段表现出一致的铵交换和生物再生。同时,当进水铵浓度为315 mg N/L时,改良型沸石序批式反应器的出水总氮通过沸石絮体的铵吸附显示为50 - 60 mg N/L,这表明在与对照组和沸石序批式反应器相同的水力停留时间(HRT)和污泥停留时间(SRT)条件下,总氮去除效率提高了10%以上。发现铵吸附容量为6 - 7 mg NH4(+)-N/g FSS,相当于去除40 mg NH4(+)-N/L的铵态氮。