TY - JOUR
T1 - Circular Process for Phosphoric Acid Plant Wastewater Facilitated by Selective Electrodialysis
AU - Monat, Lior
AU - Zhang, Wei
AU - Jarošíková, Alice
AU - Haung, Hao
AU - Bernstein, Roy
AU - Nir, Oded
N1 - Funding Information:
This work was supported by the Israeli Ministry of Science and Technology, Grant 3-15505. L.M., W.Z., and H.H. acknowledge the support of the Kreitman Negev Scholarship for Distinguished PhD Students from BGU.
Publisher Copyright:
© 2022 American Chemical Society.
PY - 2022/9/5
Y1 - 2022/9/5
N2 - Phosphoric acid production generates large volumes of industrial wastewater that cannot be treated efficiently by existing processes because of its low pH and high precipitation potential. At present, the wastewater is generally stored in evaporation ponds that are prone to breaches, leakage, and flooding. We developed an alternative three-step process for the treatment of phosphoric acid wastewater including selective electrodialysis, reverse osmosis, and neutralization. Testing the process with synthetic wastewater yielded promising results. An exceptional Na/Ca selectivity (up to 18.3) was observed in low-pH electrodialysis, enabling the separation of concentrated H2SO4 without gypsum scaling. Sulfate removal from the electrodialysis diluate prevented scaling in the subsequent high-recovery (>90%) reverse osmosis step, generating high-quality water. Finally, the acidity remaining in the reverse osmosis concentrate was neutralized using phosphate rock which also enabled P recovery. The electric power requirement of the process was estimated to be 4.4 kWh per m3 of wastewater, from which 0.78 m3 of clean water (conductivity 1.4-4.4 μS cm-1), ∼3 kg H2SO4, and ∼2.5 kg P were recovered. Overall, lab-scale results indicate that this process would be a sustainable and techno-economically viable solution for the treatment of hazardous wastewater byproducts of the phosphoric acid industry.
AB - Phosphoric acid production generates large volumes of industrial wastewater that cannot be treated efficiently by existing processes because of its low pH and high precipitation potential. At present, the wastewater is generally stored in evaporation ponds that are prone to breaches, leakage, and flooding. We developed an alternative three-step process for the treatment of phosphoric acid wastewater including selective electrodialysis, reverse osmosis, and neutralization. Testing the process with synthetic wastewater yielded promising results. An exceptional Na/Ca selectivity (up to 18.3) was observed in low-pH electrodialysis, enabling the separation of concentrated H2SO4 without gypsum scaling. Sulfate removal from the electrodialysis diluate prevented scaling in the subsequent high-recovery (>90%) reverse osmosis step, generating high-quality water. Finally, the acidity remaining in the reverse osmosis concentrate was neutralized using phosphate rock which also enabled P recovery. The electric power requirement of the process was estimated to be 4.4 kWh per m3 of wastewater, from which 0.78 m3 of clean water (conductivity 1.4-4.4 μS cm-1), ∼3 kg H2SO4, and ∼2.5 kg P were recovered. Overall, lab-scale results indicate that this process would be a sustainable and techno-economically viable solution for the treatment of hazardous wastewater byproducts of the phosphoric acid industry.
KW - Acidic wastewater
KW - cleaner mineral processing
KW - phosphate rock
KW - pond water
KW - reverse osmosis
KW - wet process
UR - http://www.scopus.com/inward/record.url?scp=85137637622&partnerID=8YFLogxK
U2 - 10.1021/acssuschemeng.2c03132
DO - 10.1021/acssuschemeng.2c03132
M3 - Article
AN - SCOPUS:85137637622
SN - 2168-0485
VL - 10
SP - 11567
EP - 11576
JO - ACS Sustainable Chemistry and Engineering
JF - ACS Sustainable Chemistry and Engineering
IS - 35
ER -