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

被引:0
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作者
Maggetti, C. [1 ]
Pinelli, D. [1 ]
Girometti, E. [1 ]
Papa, E. [2 ]
Medri, V. [2 ]
Landi, E. [2 ]
Avolio, F. [3 ]
Frascari, D. [1 ]
机构
[1] Department of Civil, Chemical, Environmental and Materials Engineering (DICAM), Alma Mater Studiorum – University of Bologna, via Terracini 28, Bologna,40131, Italy
[2] National Research Council of Italy, Institute of Science, Technology and Sustainability for Ceramics (CNR-ISSMC former CNR-ISTEC), Via Granarolo 64, RA, Faenza,48018, Italy
[3] HERA SpA, Direzione Acqua, Viale Carlo Berti Pichat, 2/4, Bologna,40127, Italy
关键词
% reductions - Ammonium removal - Empty bed contact time - Geopolymer - Ion exchange process - Metakaolins - Municipal wastewaters - Nutrient recovery - Performance - Process robustness;
D O I
10.1016/j.chemosphere.2024.143559
中图分类号
学科分类号
摘要
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 mgN L−1 in the inlet = 12 mgN gdry sorbent−1, 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 NH4+ 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 KNO3 (54%w) and NH4NO3 (39%w), two salts largely used in commercial fertilizers. The energy consumption of ammonium removal/recovery with G13 resulted 0.027 kWh m−3treated WW, 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. © 2024 The Authors
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