Degradation and monitoring of acetamiprid, thiabendazole and their transformation products in an agro-food industry effluent during solar photo-Fenton treatment in a raceway pond reactor

Chemosphere ◽  
2015 ◽  
Vol 130 ◽  
pp. 73-81 ◽  
Author(s):  
Irene Carra ◽  
Carla Sirtori ◽  
Laura Ponce-Robles ◽  
José Antonio Sánchez Pérez ◽  
Sixto Malato ◽  
...  
Científica ◽  
2016 ◽  
Vol 44 (3) ◽  
pp. 310
Author(s):  
Crislaine Trevisan da Rocha Ribeiro Ferrari ◽  
Aziza Kamal Genena ◽  
Daiane Cristina Lenhard

2020 ◽  
Vol 277 ◽  
pp. 124117
Author(s):  
Joanna Boguniewicz-Zablocka ◽  
Iwona Klosok-Bazan ◽  
Arianna Callegari ◽  
Andrea G. Capodaglio

2019 ◽  
pp. 297-316
Author(s):  
Mihir Kumar Purkait ◽  
Piyal Mondal ◽  
Chang-Tang Chang

2021 ◽  
Vol 164 ◽  
pp. 106014
Author(s):  
Elisabeth Cuervo Lumbaque ◽  
Renata M. Cardoso ◽  
Adriano de Araújo Gomes ◽  
Sixto Malato ◽  
José A. Sánchez Pérez ◽  
...  

2016 ◽  
Vol 18 ◽  
pp. 25-32 ◽  
Author(s):  
Sofie Van Den Hende ◽  
Jolien Beyls ◽  
Pieter-Jan De Buyck ◽  
Diederik P.L. Rousseau

2007 ◽  
Vol 56 (2) ◽  
pp. 71-77 ◽  
Author(s):  
J. Lobos ◽  
C. Wisniewski ◽  
M. Heran ◽  
A. Grasmick

This work focuses on the performances of two immersed membrane bioreactors used for the treatment of easily biodegradable organic matter present in food industry effluents, for the purpose of water reuse. Two reactor functioning modes (continuous and sequencing) were compared in terms of organic carbon removal and of membrane permeability. For each working mode, pollutant removal was very high, treated water quality presented a low COD concentration (<125 mg.L−1), no solids in suspension and low turbidity (<0.5 NTU). The quality of the treated water (including germ removal) enabled its reuse on site. Moreover, by developing high biomass concentrations in the reactor, excess sludge production remained very low (<0.1 gVSS.gCOD−1). The performances appeared slightly better for the continuous system (lower COD concentration in the effluent, <50 mg.L−1, and lower sludge production). In terms of filtration, a distinct difference was observed between continuous and sequencing systems; transmembrane pressure showed a small and constant evolution rate in continuous membrane bioreactor (CMBR) although it appeared more difficult to control in sequencing membrane bioreactor (SMBR) probably due to punctually higher permeate flow rate and modified suspension properties. The rapid evolution of membrane permeability observed in SMBR was such that more frequent chemical cleaning of the membrane system was required.


2018 ◽  
Vol 26 (5) ◽  
pp. 4324-4336 ◽  
Author(s):  
Elizângela Pinheiro da Costa ◽  
Sue Ellen C. Bottrel ◽  
Maria Clara V. M. Starling ◽  
Mônica M. D. Leão ◽  
Camila Costa Amorim

2020 ◽  
Vol 8 (6) ◽  
pp. 104469
Author(s):  
Fernando Morgan-Sagastume ◽  
Simon Bengtsson ◽  
Giulia De Grazia ◽  
Tomas Alexandersson ◽  
Luca Quadri ◽  
...  

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