电渗析
磷酸
废水
反渗透
化学
流出物
制浆造纸工业
工业废水处理
膜
废物管理
环境科学
环境工程
有机化学
生物化学
工程类
作者
Lior Monat,Wei Zhang,Alice Jarošíková,Hao Haung,Roy Bernstein,Oded Nir
标识
DOI:10.1021/acssuschemeng.2c03132
摘要
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.
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