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采用偏高岭土 K 基地质聚合物从城市废水中去除和回收氨的离子交换过程的开发。

Development of an ion exchange process for ammonium removal and recovery from municipal wastewater using a metakaolin K-based geopolymer.

机构信息

Department of Civil, Chemical, Environmental and Materials Engineering (DICAM), Alma Mater Studiorum - University of Bologna, via Terracini 28, 40131, Bologna, Italy.

National Research Council of Italy, Institute of Science, Technology and Sustainability for Ceramics (CNR-ISSMC former CNR-ISTEC), Via Granarolo 64, 48018, Faenza, RA, Italy.

出版信息

Chemosphere. 2024 Nov;367:143559. doi: 10.1016/j.chemosphere.2024.143559. Epub 2024 Oct 21.

Abstract

Ion exchange represents a promising process for ammonium removal from municipal wastewater (MWW), in order to recover it for fertilizer production. Previous studies on ammonium ion exchange neglected the assessment of process robustness and the optimization the desorption/recovery step. This study aimed at developing a continuous-flow process of ammonium removal/recovery based on a metakaolin K-based geopolymer, named G13. Process robustness was assessed by operating 7 adsorption/desorption cycles with two types of MWW. These tests resulted in satisfactory and constant performances: operating capacity at 40 mg L in the inlet = 12 mg g, bed volumes of treated MWW at the selected breakpoint = 199-226, ammonium adsorption yield = 88-91%. Empty bed contact time (EBCT) was decreased from 10 to 5 min without any reduction in performances. The NH adsorption process was effectively simulated by the Thomas model, allowing a model-based assessment of the effect of EBCT reductions on process performances. An innovative desorption procedure led to high ammonium recovery yields (86-100%) and to a desorbed product composed primarily of KNO (54%) and NHNO (39%), two salts largely used in commercial fertilizers. The energy consumption of ammonium removal/recovery with G13 resulted 0.027 kWh m, with a relevant reduction in comparison to traditional nitrification/denitrification, whereas the operational cost resulted equal to 60-110% of the cost of the benchmark process. These results show that G13 is a promising material to recover ammonium in a circular economy approach.

摘要

离子交换是从城市废水中(MWW)去除铵的一种很有前途的方法,以便回收它用于肥料生产。以前关于铵离子交换的研究忽视了过程稳健性的评估和解吸/回收步骤的优化。本研究旨在基于偏高岭土 K 基地质聚合物 G13 开发一种连续流动的铵去除/回收工艺。通过用两种类型的 MWW 进行 7 次吸附/解吸循环来评估过程稳健性。这些测试产生了令人满意且稳定的性能:在进水浓度为 40 mg/L 时的操作容量为 12 mg/g,选择的突破点处理的 MWW 床体积为 199-226,铵吸附产率为 88-91%。空床接触时间(EBCT)从 10 分钟减少到 5 分钟,而性能没有任何降低。NH 吸附过程通过 Thomas 模型得到了有效模拟,允许基于模型评估 EBCT 降低对过程性能的影响。一种创新的解吸程序导致了高的铵回收产率(86-100%)和主要由 KNO(54%)和 NHNO(39%)组成的解吸产物,这两种盐大量用于商业肥料。用 G13 去除/回收铵的能耗为 0.027 kWh/m,与传统的硝化/反硝化相比有显著降低,而操作成本相当于基准工艺成本的 60-110%。这些结果表明,G13 是一种很有前途的材料,可以在循环经济方法中回收铵。

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