The removal of lignin and phenol from paper mill effluents by electrocoagulation
dc.authorid | 8668083700 | |
dc.authorid | 7004919568 | |
dc.authorid | 6506609920 | |
dc.authorid | 35835158000 | |
dc.contributor.author | U?urlu M. | |
dc.contributor.author | Gürses A. | |
dc.contributor.author | Do?ar C. | |
dc.contributor.author | Yalçin M. | |
dc.date.accessioned | 20.04.201910:49:12 | |
dc.date.accessioned | 2019-04-20T21:44:59Z | |
dc.date.available | 20.04.201910:49:12 | |
dc.date.available | 2019-04-20T21:44:59Z | |
dc.date.issued | 2008 | |
dc.department | Bayburt Üniversitesi | en_US |
dc.description.abstract | This study aims to investigate the treatment of paper mill effluents using electrocoagulation. Removal of lignin, phenol, chemical oxygen demand (COD) and biological oxygen demand (BOD) from paper mill effluents was investigated at various current intensities by using different electrodes (Al and Fe) and at various electrolysis times (1.0, 2.5, 5.0 and 7.5 min). It was observed that the experiments carried out at 12 V, an electrolysis time of 2 min and a current intensity of 77.13 mA were sufficient for the removal of these pollutants with each electrode. The removal capacities of the process using an Al electrode were 80% of lignin, 98% of phenol, 70% of BOD, and 75% of COD after 7.5 min. Using an Fe electrode the removal capacities were 92%, 93%, 80% and 55%, respectively. In addition, it was found that removal of lignin, phenol, BOD and COD increased with increasing current intensity. In the experiments carried out at different current intensities, higher removal can be explained through a decrease in intra-resistance of solution and consequently an increase at the transfer speed of organic species to electrodes. It was also found that Al electrode performs higher efficiency than Fe electrode except for COD removal. However, the time required for removal of BOD was more than that of COD. The results suggest that electrocoagulation could be considered as an effective alternative to paper mill effluents treatment. © 2007 Elsevier Ltd. All rights reserved. | en_US |
dc.identifier.doi | 10.1016/j.jenvman.2007.01.007 | |
dc.identifier.endpage | 428 | |
dc.identifier.issn | 0301-4797 | |
dc.identifier.issue | 3 | |
dc.identifier.startpage | 420 | |
dc.identifier.uri | https://dx.doi.org/10.1016/j.jenvman.2007.01.007 | |
dc.identifier.uri | https://hdl.handle.net/20.500.12403/985 | |
dc.identifier.volume | 87 | |
dc.language.iso | en | en_US |
dc.relation.ispartof | Journal of Environmental Management | en_US |
dc.relation.publicationcategory | Makale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı | en_US |
dc.rights | info:eu-repo/semantics/closedAccess | en_US |
dc.subject | BOD | |
dc.subject | COD | |
dc.subject | Electrocoagulation | |
dc.subject | Lignin | |
dc.subject | Paper mill effluents | |
dc.subject | Phenol | |
dc.subject | iron | |
dc.subject | lignin | |
dc.subject | phenol | |
dc.subject | biochemical oxygen demand | |
dc.subject | chemical oxygen demand | |
dc.subject | coagulation | |
dc.subject | efficiency measurement | |
dc.subject | effluent | |
dc.subject | electrode | |
dc.subject | electrokinesis | |
dc.subject | experimental study | |
dc.subject | industrial waste | |
dc.subject | lignin | |
dc.subject | performance assessment | |
dc.subject | phenol | |
dc.subject | removal experiment | |
dc.subject | waste treatment | |
dc.subject | article | |
dc.subject | biochemical oxygen demand | |
dc.subject | chemical oxygen demand | |
dc.subject | controlled study | |
dc.subject | effluent | |
dc.subject | electric current | |
dc.subject | electric potential | |
dc.subject | electric resistance | |
dc.subject | electrode | |
dc.subject | electrolysis | |
dc.subject | industrial waste | |
dc.subject | paper industry | |
dc.subject | velocity | |
dc.subject | waste component removal | |
dc.subject | waste water management | |
dc.subject | Aluminum | |
dc.subject | Electrocoagulation | |
dc.subject | Electrodes | |
dc.subject | Industrial Waste | |
dc.subject | Iron | |
dc.subject | Lignin | |
dc.subject | Oxygen | |
dc.subject | Paper | |
dc.subject | Phenol | |
dc.subject | Time Factors | |
dc.subject | Waste Disposal, Fluid | |
dc.subject | Water Pollutants, Chemical | |
dc.subject | BOD | |
dc.subject | COD | |
dc.subject | Electrocoagulation | |
dc.subject | Lignin | |
dc.subject | Paper mill effluents | |
dc.subject | Phenol | |
dc.subject | iron | |
dc.subject | lignin | |
dc.subject | phenol | |
dc.subject | biochemical oxygen demand | |
dc.subject | chemical oxygen demand | |
dc.subject | coagulation | |
dc.subject | efficiency measurement | |
dc.subject | effluent | |
dc.subject | electrode | |
dc.subject | electrokinesis | |
dc.subject | experimental study | |
dc.subject | industrial waste | |
dc.subject | lignin | |
dc.subject | performance assessment | |
dc.subject | phenol | |
dc.subject | removal experiment | |
dc.subject | waste treatment | |
dc.subject | article | |
dc.subject | biochemical oxygen demand | |
dc.subject | chemical oxygen demand | |
dc.subject | controlled study | |
dc.subject | effluent | |
dc.subject | electric current | |
dc.subject | electric potential | |
dc.subject | electric resistance | |
dc.subject | electrode | |
dc.subject | electrolysis | |
dc.subject | industrial waste | |
dc.subject | paper industry | |
dc.subject | velocity | |
dc.subject | waste component removal | |
dc.subject | waste water management | |
dc.subject | Aluminum | |
dc.subject | Electrocoagulation | |
dc.subject | Electrodes | |
dc.subject | Industrial Waste | |
dc.subject | Iron | |
dc.subject | Lignin | |
dc.subject | Oxygen | |
dc.subject | Paper | |
dc.subject | Phenol | |
dc.subject | Time Factors | |
dc.subject | Waste Disposal, Fluid | |
dc.subject | Water Pollutants, Chemical | |
dc.title | The removal of lignin and phenol from paper mill effluents by electrocoagulation | en_US |
dc.type | Article | en_US |