Integration of electrochemical processes in a treatment system for landfill leachates based on a membrane bioreactor

被引:1
|
作者
Mostefaoui, Nabil [1 ,2 ]
Oturan, Nihal [1 ]
Bouafia, Souad Chergui [2 ]
Hien, Sie Alain [1 ,3 ]
Gibert-Vilas, Maxim [1 ]
Lesage, Geoffroy [4 ]
Pechaud, Yoan [1 ]
Tassin, Bruno [5 ]
Oturan, Mehmet [1 ]
Trellu, Clement [1 ]
机构
[1] Univ Gustave Eiffel, Lab Geomateriaux & Environm EA 4508, F-77454 Marne 2, France
[2] Fac Mech Engn & Proc Engn USTHB, Lab React Engn, BP 32, Bab Ezzouar 16111, Algeria
[3] Inst Natl Polytech Houphouet Boigny, Lab des Procedes Ind, Synth Environm & Energies Nouvelles LAPISEN, BP 1313, Yamoussoukro, Cote Ivoire
[4] Univ Montpellier, Inst Europeen Membranes, Ctr Natl Rech Sci CNRS, IEM,UMR 5635, Pl Eugene Bataillon, F-34095 Montpellier, France
[5] Univ Paris Est Creteil, Ecole Ponts, Lab Eau Environm & Syst Urbains, LEESU, 61 Ave Gen Gaulle, F-77455 Creteil, France
关键词
Landfill leachate; Anodic oxidation; Electrocoagulation; Coupled process; Biological treatment; By-product; ADVANCED OXIDATION PROCESSES; DISSOLVED ORGANIC-MATTER; WASTE-WATER; NANOFILTRATION CONCENTRATE; DRINKING-WATER; ELECTROCOAGULATION; FENTON; POLLUTANTS; REMOVAL; MINERALIZATION;
D O I
10.1016/j.scitotenv.2023.168841
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The use of electrocoagulation (EC) and anodic oxidation (AO) processes was studied for improving a treatment system for landfill leachates based on a membrane bioreactor (MBR) and a nanofiltration step. The main limitation of the current full-scale system is related to the partial removal of organic compounds that leads to operation of the nanofiltration unit with a highly concentrated feed solution. Application of the EC before the MBR participated in partial removal of the organic load (40 %) with limited energy consumption (2.8 kWh m-3) but with additional production of iron hydroxide sludge. Only AO allowed for non-selective removal of organic compounds. As a standalone process, AO would require a sharp increase of the energy consumption (116 kWh for 81 % removal of total organic carbon). But using lower electric charge and combining AO with EC and MBR processes would allow for achieving high overall removal yields with limited energy consumption. For example, the overall removal yield of total organic carbon was 65 % by application of AO after EC, with an energy consumption of 21 kWh m  3. Results also showed that such treatment strategy might allow for a significant increase of the biodegradability of the effluent before treatment by the MBR. The MBR might then be dedicated to the removal of the residual organic load as well as to the removal of the nitrogen load. The data obtained in this study also showed that the lower electric charge required for integrating AO in a coupled process would allow for strongly decreasing the formation of undesired by-products such as ClO3  and ClO4  .
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页数:14
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