TY - JOUR
T1 - Electrochemical recovery of H2 and nutrients (N, P) from synthetic source separate urine water
AU - Govindan, Kadarkarai
AU - Im, Sung Ju
AU - Muthuraj, Velluchamy
AU - Jang, Am
N1 - Publisher Copyright:
© 2020 Elsevier Ltd
PY - 2021/4
Y1 - 2021/4
N2 - This study examined an electrochemical method of H2 production and nutrient recovery from synthetic source separated urine (SSU). The efficacy of H2 production was examined through hydrogen recovery experiments (HRE) using Ni foam electrodes. Similarly, nutrient (N and P) recovery was also examined in post-nutrient recovery experiments (NRE) with sacrificial Mg electrodes. To achieve higher nutrient recovery in the post-nutrient recovery process, the most important operating parameters (initial solution pH (pHi) and current density) were optimized. Optimization of NRE revealed that > 90% NH3-N and PO43--P could be recovered at 8 mA cm−2 with a pHi of 6–8. Notable NH3-N and PO43--P reduction were observed at an equimolar Mg2+ dissolution ratio (1:1) of Mg2+:NH4+ and a 1.1:1 ratio of Mg2+:PO43− respectively. However, poor total Kjeldahl nitrogen (TKN) reduction was observed. Thus, we anticipate that direct electrochemical conversion of urea to N2 at the anode followed by H2 generation at the cathode is a more sustainable way to reduce TKN. Batch HRE showed that the initial TKN, 1094 mg L−1 (934 mg L−1 from urea-N and 160 mg L−1 from NH4Cl), was significantly reduced to 360 mg L−1 by Ni-Ni electrolysis, whereas around 53.8 g H2 gas was received from this Ni-Ni electrolysis system with a flow rate of 5–5.8 g mol−1 day−1. Overall, this work produced a 68% reduction in TKN due to electrochemical conversion of urea into H2.
AB - This study examined an electrochemical method of H2 production and nutrient recovery from synthetic source separated urine (SSU). The efficacy of H2 production was examined through hydrogen recovery experiments (HRE) using Ni foam electrodes. Similarly, nutrient (N and P) recovery was also examined in post-nutrient recovery experiments (NRE) with sacrificial Mg electrodes. To achieve higher nutrient recovery in the post-nutrient recovery process, the most important operating parameters (initial solution pH (pHi) and current density) were optimized. Optimization of NRE revealed that > 90% NH3-N and PO43--P could be recovered at 8 mA cm−2 with a pHi of 6–8. Notable NH3-N and PO43--P reduction were observed at an equimolar Mg2+ dissolution ratio (1:1) of Mg2+:NH4+ and a 1.1:1 ratio of Mg2+:PO43− respectively. However, poor total Kjeldahl nitrogen (TKN) reduction was observed. Thus, we anticipate that direct electrochemical conversion of urea to N2 at the anode followed by H2 generation at the cathode is a more sustainable way to reduce TKN. Batch HRE showed that the initial TKN, 1094 mg L−1 (934 mg L−1 from urea-N and 160 mg L−1 from NH4Cl), was significantly reduced to 360 mg L−1 by Ni-Ni electrolysis, whereas around 53.8 g H2 gas was received from this Ni-Ni electrolysis system with a flow rate of 5–5.8 g mol−1 day−1. Overall, this work produced a 68% reduction in TKN due to electrochemical conversion of urea into H2.
KW - Economical feasibility
KW - H production
KW - NH-N recovery
KW - PO -P recovery
KW - Post-nutrient recovery
KW - TKN reduction
UR - https://www.scopus.com/pages/publications/85098597177
U2 - 10.1016/j.chemosphere.2020.129361
DO - 10.1016/j.chemosphere.2020.129361
M3 - Article
C2 - 33383251
AN - SCOPUS:85098597177
SN - 0045-6535
VL - 269
JO - Chemosphere
JF - Chemosphere
M1 - 129361
ER -