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REMOVAL OF AMMONIUM NITROGEN FROM PRETREATED DOMESTIC SEWAGE USING A NATURAL ION EXCHANGER

机译:使用天然离子交换剂从预处理的生活污水中去除氨氮

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Ammonium nitrogen was removed from pretreated domestic sewage using a natural zeolite-clinoptilolite, applying a column with downflow regime. The pretreated wastewater had an average total ammonium nitrogen (TAN) of 23 mg l~(-1). Ion exchange was allowed to take place under normal sewage treatment plant conditions and tropical temperature setting. The sorption capacity of the natural clinoptilolite was studied with the column fitted to a chemically enhanced primary treatment (CEPT)-upflow anaerobic sludge blanket (UASB) system, operating at 33℃. Optimal operational cation exchange capacity (CEC) of 14 g TAN kg~(-1) zeolite was obtained for the zeolite granulometry of 1-2.5 mm in a reversible way. The treatment was done at 3.9 bed volumes (BV) per day, and breakthrough was attained after about 560 BV. Regeneration of exhausted zeolite was effected with a 25 g NaCl l~(-1) salt solution, rendering the column amenable to reuse. Employing a 3-column test and bed contact times of 6, 2.6 and 1.1 minutes, the use of pretreated wastewater with average concentration of 38 mg NH_4~+-N l~(-1) showed that the operational cation exchange capacity also depended on flow rate, with the removal efficiency decreasing from 95 to 47 % with increase in the flow rate. Overall, the approach of removing TAN from digested sewage offers potential to recover the TAN from the domestic wastewater, thus minimizing the need for subsequent nitrification-denitrification of the whole water volume.
机译:使用天然沸石-斜发沸石,通过向下流动的色谱柱从预处理的生活污水中除去铵氮。预处理废水的平均总氨氮(TAN)为23 mg l〜(-1)。允许在正常污水处理厂条件和热带温度设定下进行离子交换。色谱柱安装在化学增强的一级处理(CEPT)-上流厌氧污泥层(UASB)系统上,在33℃下运行,研究了天然斜发沸石的吸附能力。对于1-2.5 mm沸石粒度,以可逆方式获得了14 g TAN kg〜(-1)沸石的最佳阳离子交换容量(CEC)。该治疗以每天3.9床体积(BV)进行,约560 BV后获得突破。用25 g NaCl -1(-1)盐溶液进行废沸石的再生,使色谱柱易于重复使用。通过3柱测试,床接触时间分别为6、2.6和1.1分钟,使用平均浓度为38 mg NH_4〜+ -N l〜(-1)的预处理废水表明,阳离子交换容量也取决于流量,随着流量的增加,去除效率从95%降低到47%。总体而言,从消化污水中去除TAN的方法提供了从生活废水中回收TAN的潜力,从而最大程度地减少了随后对整个水量进行硝化-反硝化的需求。

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