管理垃圾填埋场沥滤液反渗透浓缩物的新方法:太阳能蒸馏与硬石膏回收和生物处理相结合。

Chemosphere Pub Date : 2024-10-01 Epub Date: 2024-10-18 DOI:10.1016/j.chemosphere.2024.143574
Konstantinos Tsompanoglou, Athanasia Iliopoulou, Petros Mastoras, Athanasios S Stasinakis
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引用次数: 0

摘要

对于垃圾填埋场渗滤液处理厂的运营者来说,反渗透(RO)浓缩物的管理仍然是一项具有挑战性的任务。在这篇文章中,我们提出了一种反渗透浓缩物综合处理方案,该方案将太阳能蒸馏、降低蒸馏物中氨含量的硬石膏沉淀以及上清液的生物处理(混合细菌培养或微藻类培养)结合在一起。在一个配备了地板采暖系统的中试规模太阳能蒸馏器中进行的实验表明,蒸馏物的生产率高达 3.17 升/平方米。蒸馏物的特点是铵态氮的平均浓度较高;在进行的两次实验中,铵态氮的平均浓度分别为 2028 毫克/升和 1358 毫克/升。在这些实验中,NH4+-N 的浓度呈下降趋势,而 COD 则相反。硬石膏回收实验表明,Mg:NH4:PO3 的最佳比例为 2:1:5.8。在这种条件下,NH4+-N 的去除率达到了 88%。在 C 阶段和 D 阶段,分别加入 450 mL 和 600 mL 的上清液,将工艺上清液进一步处理到带有生物载体和活性污泥的 4 L 混合序批式反应器中,NH4+-N 的去除率高于 98%。在加入 150 mL 硬蛋白石上清液的 2 L 生物反应器中(B 阶段)也观察到了类似的去除效果,而进一步将上清液的添加量增加到 200 mL 后,NH4+-N 的消耗急剧停止(C 阶段)。根据为 2 万居民提供服务的垃圾填埋场和反渗透浓缩物日产量 6 立方米的计算结果,建造太阳能蒸馏器所需的面积为 1893 平方米,混合反应器和微藻反应器的体积分别为 54 立方米和 60 立方米。在对重金属和有机微污染物进行表征后,回收的硬石膏固体材料可重新用于肥料工业。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
A new approach on the management of landfill leachate reverse osmosis concentrate: Solar distillation coupled with struvite recovery and biological treatment.

The management of reverse osmosis (RO) concentrate remains a challenging task for operators of Landfill Leachates Treatment Plants. In this article we suggest an integrated treatment scheme for RO concentrate that combines solar distillation, struvite precipitation to reduce ammonia content of the distillate and biological treatment of the supernatant either with mixed cultures of bacteria or with microalgae. Experiments in a pilot-scale solar still, equipped with underfloor heating system, showed that the production rate of the distillate ranged up to 3.17 L/d m2. The distillate was characterized by elevated average concentrations of ammonium nitrogen; 2028 mg/L and 1358 mg/L in the two experiments conducted, respectively. A decreasing trend on concentrations of NH4+-N was noticed during these experiments, while the opposite was observed for COD. Struvite recovery experiments showed that the optimum Mg:NH4:PO3 ratio was that of 2:1:5.8. Under these conditions, the NH4+-N removal reached 88%. Further treatment of the process supernatant into a 4-L hybrid sequencing batch reactor with biocarriers and activated sludge achieved NH4+-N removal higher than 98% in Phases C and D, where 450 and 600 mL of supernatant were added, respectively. Similar removal was also observed in a 2-L bioreactor with microalgae Chlorella sorokiniana when 150 mL of struvite supernatant were added (Phase B) while further increase of the amount of added supernatant to 200 mL resulted to a sharp stop of NH4+-N consumption (Phase C). Calculations for a landfill serving 20,000 inhabitants and a daily RO concentrate production of 6 m3/d showed that the required area for the construction of the solar still was 1893 m2 and the volumes of the hybrid and the microalgae reactor were 54 m3 and 60 m3, respectively. The recovered solid material of struvite process, after characterization for heavy metals and organic micropollutants, could be reused to the fertilizers industry.

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