Faculty Publications
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Item Aerobic sludge granulation and enhanced dicamba removal efficiency in the presence of AQS redox mediator in a lab-scale anaerobic-aerobic treatment method(Elsevier, 2021) Basappa, M.G.; Manu, B.The biodegrading of dicamba was conducted using the anaerobic-aerobic technique for influent concentrations 60-100 mg/L over 187 days of operation. The reactors were stabilized using starch and acclimated to 40 mg/L of dicamba. Dicamba and starch was fed to the anaerobic reactor. Effluent was collected after a hydraulic retention time of 24 h and analyzed in gas chromatography-high-resolution mass spectrometry to detect the biotransformation products. High concentration of benzoates, esters, and fatty acid groups were detected in the anaerobic reactor. Effluent of anaerobic reactor contained high chemical oxygen demand (COD) concentration 400-750 mg/L, which was then fed to the aerobic reactor. After aerobic posttreatment, the overall dicamba and COD removal obtained were >85 and 92% respectively. The aerobic reactor developed a thick granular biomass of up to 7 mm in size, which indicates the bacterial adaptation and hence attainment of stable reactor performance. © 2021 Elsevier B.V. All rights reserved.Item Biological Treatment of 3,6-Dichloro-2-Methoxybenzoic Acid Using Anaerobic-Aerobic Sequential Batch Reactor(Springer Basel info@birkhauser-science.com, 2019) Mahesh, G.B.; Manu, B.A sequential anaerobic-aerobic batch reactor was used to treat 3,6-dichloro-2-methoxybenzoic acid (dicamba) during a long operation period of 340 days in the presence of disodium anthraquinone-2,6-disulphonate (AQS) as redox mediator. The sludge activity was evaluated for different dosages of dicamba over constant hydraulic retention time (HRT), neutral pH (6.5–7.5) and at ambient reactor temperature. Effects of increased dicamba concentration, solids retention time (SRT) and oxidation reduction potential (ORP) on the biodegradation of dicamba was monitored and compared with control reactor containing no dicamba. Results revealed that long operation period, long SRT and ORP were playing important role in the breakdown of dicamba to its transformation products and subsequent removal in the system. The system was capable of degrading the compound completely during long operation period, long SRT and at low ORP in the presence of AQS. Reducing condition in the anaerobic reactor significantly contributed to the treatment process through demethylation, dehalogenation and dechlorination reactions in the presence of different reducing bacteria. The results of GC-HRMS identified the anaerobic transformation products of dicamba as oleic acid (C18H34O2), 9-Octadecenoic acid (Z), 2-hydroxy-1-(hydroxymethyl)ethyl ester (C21H40O4), trans-13-Ocatadecenoic acid (C18H34O2) compounds which were then oxidised in the aerobic reactor. © 2019, Springer Nature Switzerland AG.Item Biodegradation of ametryn and dicamba in a sequential anaerobic-aerobic batch reactor: A case study(IWA Publishing 12 Caxton Street London SW1H 0QS, 2019) Mahesh, G.B.; Manu, B.Agricultural runoff often contains persistent halogenated herbicide compounds like 2-(ethylamino)-4-(isopropylamino)-6-(methylthio)-s-triazine (ametryn) and 3,6-dichloro-2-methoxybenzoic acid (dicamba). These can enter the food chain through drinking water, causing serious effects for people and the environment. A sequential anaerobic reactor followed by an aerobic reactor was operated and investigated for herbicide removal efficiency at constant, three-day, hydraulic retention time (HRT) and organic loading rate (OLR) of 0.2025 kg-COD/m3/d. The effect of the herbicides on anaerobic bacteria was evaluated based on total biogas production and bacterial activity, which indicated that there was no inhibition on the acclimated biomass. The sequential reactor pair removed 72% of ametryn and 78% dicamba, with COD removal efficiencies of 86% and 85% respectively. The different high-performance liquid chromatography (HPLC) peaks indicate that the compounds are biotransformed and this was confirmed by gas chromatograph high resolution mass spectrometry (GC-HRMS). © IWA Publishing 2019.Item Removal of ametryn and organic matter from wastewater using sequential anaerobic-aerobic batch reactor: A performance evaluation study(Academic Press, 2019) Mahesh, G.B.; Manu, B.The present study was aimed to investigate biodegradation of 2-(ethylamino)-4-(isopropylamino)-6-(methylthio)-s-triazine (ametryn) in a laboratory-scale anaerobic sequential batch reactor (ASBR) and followed by aerobic post-treatment. Co-treatment of ametryn with starch is carried out at ambient environmental conditions. The treatment process lasted up to 150 days of operation at a constant hydraulic retention time (HRT) of 24 h and an organic loading rate (OLR) of 0.21–0.215 kg-COD/m3/d. Ametryn concentration of 4 and 6 mg/L was removed completely within 48–50 days of operation with chemical oxygen demand (COD) removal efficiencies >85% at optimum reactor conditions. Ametryn acted as a nutrient/carbon source rather causing toxicity and contributed to methane gas production and sludge granulation in the anaerobic reactor. Biotransformation products of ametryn to cyanuric acid, biuret, and their further conversion to ammonia nitrogen and CO2 are monitored during the study. Adsorption of ametryn on to reactor sludge was negligible, sludge granulation, presence of ANAMMOX bacteria, and low MLVSS/MLSS ratio between 0.68 and 0.72. The study revealed that ametryn removal occurred mainly due to biodegradation and co-metabolism processes. Aerobic post-treatment of anaerobic effluent was able to remove COD up to 95%. The results of this study exhibit that anaerobic-aerobic treatment is feasible due to easy operation, economic, and highly efficient. © 2019 Elsevier LtdItem Enhancement of ametryn biodegradation efficiency using anthraquinone-2,6-disulphonate in anaerobic-aerobic treatment(Gheorghe Asachi Technical University of Iasi, Romania, 2020) Mahesh, M.G.; Manu, B.Ametryn (2-(ethylamino)-4-(isopropylamino)-6-(methylthio)-s-triazine), a herbicide present in different type of wastewater was treated using the anaerobic-aerobic batch reactor in the presence of anthraquinone-2,6-disulphonate (AQS) as a redox mediator. The anaerobic co-treatment process was conducted for an influent ametryn concentration of 8-10 mg/L during 280 days in previously acclimated biomass. Different intermediate compounds of ametryn were identified in the anaerobic effluent using the liquid chromatography-mass spectrophotometer (LC-MS). Low mixed liquor volatile suspended solids/mixed liquor suspended solids (MLVSS/MLSS) ratio between 0.71-0.81 indicated a stable anaerobic performance. Food to microorganism ratio (F/M), sludge age and solids retention time (SRT) for anaerobic reactors observed was 0.19 - 0.27, for 7 days and 64-190 days respectively. The aerobic reactor was coupled sequentially to remove trace organic matter and the intermediate compounds in the anaerobic effluent. In the aerobic reactor, MLVSS/MLSS ratio observed was 0.68-0.75, F/M ratio was 0.166, sludge age 15 days, and SRT 190-310 days. The overall removal efficiency of anaerobic-aerobic treatment was >99% for both ametryn and COD. Anaerobic-aerobic effluent was fed to the micro-algae Chlorella vulgaris and Scenedesmus quadricauda, and the effluent has contributed to algal growth. © 2020 Gheorghe Asachi Technical University of Iasi, Romania. All rights reserved.