Removal of Arsenic from Drinking Water by Batch and Continuous Electrocoagulation Processes Using Hybrid Al-Fe Plate Electrodes. Kobya, M., Akyol, A., Demirbas, E., & Oncel, M., S. ENVIRONMENTAL PROGRESS & SUSTAINABLE ENERGY, 33(1):131-140, 2014. abstract bibtex Removals of arsenic from drinking water by electrocoagulation (EC)
process using six different combinations of hybrid electrodes (Al-Fe),
and Al-Al or Fe-Fe electrodes as all anodes and cathodes in a batch mode
were evaluated. The removal process with monopolar series mode at
optimum operating conditions (2.50 A/m(2), 150 mu g/L, and pH 7.0)
indicated that Fe-Al-Al-Fe (anode-cathode-anode-cathode) hybrid plate
electrode pairs were the most efficient choice in terms of arsenic
removal efficiency (96% in 1 min) and operating cost (0.00202
Euro/m(3)). The arsenic removal from drinking water by continuous EC
(CEC) process using Fe-Al-Al-Fe hybrid plate electrode pairs was also
studied with respect to flow rates and initial arsenic concentrations.
The effluent arsenic concentration of 10 mu g/L in the CEC process was
achieved at 3 min for 0.05 L/min (5.9 mu g/L), 8 min for 0.10 L/min (6.3
mu g/L), and 20 min for 0.20 L/min (8.4 mu g/L), respectively. Amounts
of the sludge and operating costs in the CEC process with respect to
some experimental parameters such as operating time (3-20 min) and flow
rate (0.05-0.20 L/min) at 150 mu g/L were determined as 0.0095-0.025
kg/m(3) and 0.009-0.060 Euro/m(3). (c) 2013 American Institute of
Chemical Engineers Environ Prog, 33: 131-140, 2014
@article{
title = {Removal of Arsenic from Drinking Water by Batch and Continuous Electrocoagulation Processes Using Hybrid Al-Fe Plate Electrodes},
type = {article},
year = {2014},
identifiers = {[object Object]},
pages = {131-140},
volume = {33},
id = {f3f96e46-16a6-34f2-a232-fae6ced33e21},
created = {2016-04-28T08:45:55.000Z},
file_attached = {false},
profile_id = {dce7c6b2-57cf-350f-b364-3e8ed99bb344},
group_id = {bfd80d76-e42d-36f1-b5b9-353e1a47eb95},
last_modified = {2016-04-28T08:45:55.000Z},
read = {false},
starred = {false},
authored = {false},
confirmed = {true},
hidden = {false},
citation_key = {ISI:000329309300014},
source_type = {article},
abstract = {Removals of arsenic from drinking water by electrocoagulation (EC)
process using six different combinations of hybrid electrodes (Al-Fe),
and Al-Al or Fe-Fe electrodes as all anodes and cathodes in a batch mode
were evaluated. The removal process with monopolar series mode at
optimum operating conditions (2.50 A/m(2), 150 mu g/L, and pH 7.0)
indicated that Fe-Al-Al-Fe (anode-cathode-anode-cathode) hybrid plate
electrode pairs were the most efficient choice in terms of arsenic
removal efficiency (96% in 1 min) and operating cost (0.00202
Euro/m(3)). The arsenic removal from drinking water by continuous EC
(CEC) process using Fe-Al-Al-Fe hybrid plate electrode pairs was also
studied with respect to flow rates and initial arsenic concentrations.
The effluent arsenic concentration of 10 mu g/L in the CEC process was
achieved at 3 min for 0.05 L/min (5.9 mu g/L), 8 min for 0.10 L/min (6.3
mu g/L), and 20 min for 0.20 L/min (8.4 mu g/L), respectively. Amounts
of the sludge and operating costs in the CEC process with respect to
some experimental parameters such as operating time (3-20 min) and flow
rate (0.05-0.20 L/min) at 150 mu g/L were determined as 0.0095-0.025
kg/m(3) and 0.009-0.060 Euro/m(3). (c) 2013 American Institute of
Chemical Engineers Environ Prog, 33: 131-140, 2014},
bibtype = {article},
author = {Kobya, M and Akyol, A and Demirbas, E and Oncel, M S},
journal = {ENVIRONMENTAL PROGRESS & SUSTAINABLE ENERGY},
number = {1}
}
Downloads: 0
{"_id":"xz7RtchL6Bn84viJg","bibbaseid":"kobya-akyol-demirbas-oncel-removalofarsenicfromdrinkingwaterbybatchandcontinuouselectrocoagulationprocessesusinghybridalfeplateelectrodes-2014","downloads":0,"creationDate":"2016-04-28T08:42:22.133Z","title":"Removal of Arsenic from Drinking Water by Batch and Continuous Electrocoagulation Processes Using Hybrid Al-Fe Plate Electrodes","author_short":["Kobya, M.","Akyol, A.","Demirbas, E.","Oncel, M., S."],"year":2014,"bibtype":"article","biburl":null,"bibdata":{"title":"Removal of Arsenic from Drinking Water by Batch and Continuous Electrocoagulation Processes Using Hybrid Al-Fe Plate Electrodes","type":"article","year":"2014","identifiers":"[object Object]","pages":"131-140","volume":"33","id":"f3f96e46-16a6-34f2-a232-fae6ced33e21","created":"2016-04-28T08:45:55.000Z","file_attached":false,"profile_id":"dce7c6b2-57cf-350f-b364-3e8ed99bb344","group_id":"bfd80d76-e42d-36f1-b5b9-353e1a47eb95","last_modified":"2016-04-28T08:45:55.000Z","read":false,"starred":false,"authored":false,"confirmed":"true","hidden":false,"citation_key":"ISI:000329309300014","source_type":"article","abstract":"Removals of arsenic from drinking water by electrocoagulation (EC)\nprocess using six different combinations of hybrid electrodes (Al-Fe),\nand Al-Al or Fe-Fe electrodes as all anodes and cathodes in a batch mode\nwere evaluated. The removal process with monopolar series mode at\noptimum operating conditions (2.50 A/m(2), 150 mu g/L, and pH 7.0)\nindicated that Fe-Al-Al-Fe (anode-cathode-anode-cathode) hybrid plate\nelectrode pairs were the most efficient choice in terms of arsenic\nremoval efficiency (96% in 1 min) and operating cost (0.00202\nEuro/m(3)). The arsenic removal from drinking water by continuous EC\n(CEC) process using Fe-Al-Al-Fe hybrid plate electrode pairs was also\nstudied with respect to flow rates and initial arsenic concentrations.\nThe effluent arsenic concentration of 10 mu g/L in the CEC process was\nachieved at 3 min for 0.05 L/min (5.9 mu g/L), 8 min for 0.10 L/min (6.3\nmu g/L), and 20 min for 0.20 L/min (8.4 mu g/L), respectively. Amounts\nof the sludge and operating costs in the CEC process with respect to\nsome experimental parameters such as operating time (3-20 min) and flow\nrate (0.05-0.20 L/min) at 150 mu g/L were determined as 0.0095-0.025\nkg/m(3) and 0.009-0.060 Euro/m(3). (c) 2013 American Institute of\nChemical Engineers Environ Prog, 33: 131-140, 2014","bibtype":"article","author":"Kobya, M and Akyol, A and Demirbas, E and Oncel, M S","journal":"ENVIRONMENTAL PROGRESS & SUSTAINABLE ENERGY","number":"1","bibtex":"@article{\n title = {Removal of Arsenic from Drinking Water by Batch and Continuous Electrocoagulation Processes Using Hybrid Al-Fe Plate Electrodes},\n type = {article},\n year = {2014},\n identifiers = {[object Object]},\n pages = {131-140},\n volume = {33},\n id = {f3f96e46-16a6-34f2-a232-fae6ced33e21},\n created = {2016-04-28T08:45:55.000Z},\n file_attached = {false},\n profile_id = {dce7c6b2-57cf-350f-b364-3e8ed99bb344},\n group_id = {bfd80d76-e42d-36f1-b5b9-353e1a47eb95},\n last_modified = {2016-04-28T08:45:55.000Z},\n read = {false},\n starred = {false},\n authored = {false},\n confirmed = {true},\n hidden = {false},\n citation_key = {ISI:000329309300014},\n source_type = {article},\n abstract = {Removals of arsenic from drinking water by electrocoagulation (EC)\nprocess using six different combinations of hybrid electrodes (Al-Fe),\nand Al-Al or Fe-Fe electrodes as all anodes and cathodes in a batch mode\nwere evaluated. The removal process with monopolar series mode at\noptimum operating conditions (2.50 A/m(2), 150 mu g/L, and pH 7.0)\nindicated that Fe-Al-Al-Fe (anode-cathode-anode-cathode) hybrid plate\nelectrode pairs were the most efficient choice in terms of arsenic\nremoval efficiency (96% in 1 min) and operating cost (0.00202\nEuro/m(3)). The arsenic removal from drinking water by continuous EC\n(CEC) process using Fe-Al-Al-Fe hybrid plate electrode pairs was also\nstudied with respect to flow rates and initial arsenic concentrations.\nThe effluent arsenic concentration of 10 mu g/L in the CEC process was\nachieved at 3 min for 0.05 L/min (5.9 mu g/L), 8 min for 0.10 L/min (6.3\nmu g/L), and 20 min for 0.20 L/min (8.4 mu g/L), respectively. Amounts\nof the sludge and operating costs in the CEC process with respect to\nsome experimental parameters such as operating time (3-20 min) and flow\nrate (0.05-0.20 L/min) at 150 mu g/L were determined as 0.0095-0.025\nkg/m(3) and 0.009-0.060 Euro/m(3). (c) 2013 American Institute of\nChemical Engineers Environ Prog, 33: 131-140, 2014},\n bibtype = {article},\n author = {Kobya, M and Akyol, A and Demirbas, E and Oncel, M S},\n journal = {ENVIRONMENTAL PROGRESS & SUSTAINABLE ENERGY},\n number = {1}\n}","author_short":["Kobya, M.","Akyol, A.","Demirbas, E.","Oncel, M., S."],"bibbaseid":"kobya-akyol-demirbas-oncel-removalofarsenicfromdrinkingwaterbybatchandcontinuouselectrocoagulationprocessesusinghybridalfeplateelectrodes-2014","role":"author","urls":{},"downloads":0,"html":""},"search_terms":["removal","arsenic","drinking","water","batch","continuous","electrocoagulation","processes","using","hybrid","plate","electrodes","kobya","akyol","demirbas","oncel"],"keywords":[],"authorIDs":[]}