4.7 Article

Integrated assessment of sulfate-based AOPs for pharmaceutical active compound removal from wastewater

期刊

JOURNAL OF CLEANER PRODUCTION
卷 260, 期 -, 页码 -

出版社

ELSEVIER SCI LTD
DOI: 10.1016/j.jclepro.2020.121014

关键词

Advanced oxidation process; Sulfate radical; Environmental impact; Advanced wastewater treatment; Pharmaceuticals; Life cycle assessment

资金

  1. European Union's Horizon 2020 research and innovation program under the Marie Sklodowska-Curie - TreatRec ITN-EID project [642904]
  2. Spanish Ministry of Science, Innovation and Universities [CTM 2017-85385-C2-1-R, RTI 2018-097471-B-C21]
  3. State Agency of Investigation [CTM 2017-85385-C2-1-R, RTI 2018-097471-B-C21]
  4. EU FEDER program [CTM 2017-85385-C2-1-R, RTI 2018-097471-B-C21]
  5. Economy and Knowledge Department of the Catalan Government [2017 SGR 1318]

向作者/读者索取更多资源

Advanced oxidation processes (AOPs) have been proposed as tertiary treatments for municipal WWTP effluents. UV-activated peroxydisulfate (PDS) and peroxymonosulfate (PMS) are viable technological alternatives for treating secondary WWTP effluent containing PhACs. This article examines the feasibility of applying UV/PDS and UV/PMS technologies at pilot scale, assessing their energy and cost requirements. In addition, life cycle assessment (LCA) impacts associated with the treatment of 1 m(3) of wastewater with an effective average pharmaceutical active compounds (PhACs) removal of 80% has also been evaluated. Photolysis (UV) treatment alone was not capable of degrading PhACs to a sufficient extent in WWTP secondary effluent. The addition of 0.4 mmol of PDS or PMS, applying 416 mJ/cm(2 )of UV fluence, resulted in average removals of 84% and 85% for UV/PDS and UV/PMS, respectively. The electrical energy (kWh) required to degrade the mix of PhACs by one order of magnitude in 1 m(3) of contaminated water was calculated as 0.9 kWh/m(3)/order and 0.8 kWh/m(3)/order 4 for UV/PDS and UV/PMS, respectively. However, the overall cost, including operation, materials and maintenance, of applying UV/PDS and UV/PMS, based on an average PhAC removal of 80%, was 0.088 (sic)/m(3) and 0.280 (sic)/m(3), respectively. From the sustainability assessment, the factors with the greatest environmental footprint for the UV/PDS process were chemical production (PDS: 52.9%, PMS: 85%) and electricity consumption (UV/PDS: 33.4%, UV/PMS: 11.2). Finally, the normalized environmental impact analysis showed that UV/PDS was associated with an environmental footprint three times lower than UV/PMS. The overall assessment revealed that UV/PDS is preferable to UV/PMS to remove PhACs in secondary effluents of municipal WWTPs having a lower economic and environmental impact. (C) 2020 Elsevier Ltd. All rights reserved.

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