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Updated: Sep 9, 2025

Electrochemically and Bioelectrochemically Induced Ammonium Recovery
Published on: January 22, 2015
Enhanced struvite production via membrane capacitive deionization and electrolysis: interference of humic acid and
Aditya Kurnia Aji Pangestu1, Arseto Yekti Bagastyo1, Ervin Nurhayati1
1Department of Environmental Engineering, Faculty of Civil, Planning, and Geo-Engineering, Institut Teknologi Sepuluh Nopember, 60111, Surabaya, Indonesia.
Abstract:
This study examined struvite crystal formation for nutrient recovery in the presence of coexisting cations and organic substances. Coupled membrane capacitive deionization (MCDI) with sacrificial magnesium anode electrolysis was performed to produce struvite crystals from synthetic wastewater containing ammonium, phosphate, sodium, calcium, and humic acid (HA). In this way, MCDI was employed to adsorb coexisting cations onto the activated carbon (AC) electrode and retain and ions in the effluent. The MCDI effluent was the input for Mg-based electrolysis, which used an AZ31B Mg alloy as the anode to release Mg2+ ions. Various initial Nitrogen/Phosphate (N/P) molar ratios were prepared (i.e. 1:1, 5:1, and 10:1) in the absence and presence of 10 mM competitor ions and 100 mg⋅L-1 of HA. The results showed that MCDI can retain and approximately 84.19 and 78.07%, respectively, which is equivalent to the ion electrosorption capacity of the AC electrode, approximately 15.53 mg⋅g-1 for and 21.45 mg⋅g-1 for . Interestingly, the addition of co-ions, such as Na+ and Ca2+, can remain 2-5 times and in the effluent. After Mg-based electrolysis, and ions increased by approximately 87.32% and 63.65%, respectively. In the presence of Na+, coupling MCDI with the electrolysis process produced up to 0.6195 g of high-purity struvite. Conversely, HA and Ca2+ significantly reduced crystal purity and altered morphology. Under an N/P ratio of 10:1, without co-ions or humic acid, the energy consumption for struvite recovery was 15.88 Wh g-1.
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