dc.contributor.author |
Vlyssides, AG |
en |
dc.contributor.author |
Loizidou, M |
en |
dc.contributor.author |
Karlis, PK |
en |
dc.contributor.author |
Zorpas, AA |
en |
dc.date.accessioned |
2014-03-01T01:48:47Z |
|
dc.date.available |
2014-03-01T01:48:47Z |
|
dc.date.issued |
1999 |
en |
dc.identifier.issn |
10440631 |
en |
dc.identifier.uri |
https://dspace.lib.ntua.gr/xmlui/handle/123456789/25594 |
|
dc.relation.uri |
http://www.scopus.com/inward/record.url?eid=2-s2.0-0032666762&partnerID=40&md5=2fe4aacac1d10922e3b7bc9388729618 |
en |
dc.subject.other |
Azo dyes |
en |
dc.subject.other |
Biochemical oxygen demand |
en |
dc.subject.other |
Biodegradation |
en |
dc.subject.other |
Biological sewage treatment |
en |
dc.subject.other |
Color removal (water treatment) |
en |
dc.subject.other |
Composition effects |
en |
dc.subject.other |
Electrochemical electrodes |
en |
dc.subject.other |
Electrolysis |
en |
dc.subject.other |
Hydrochloric acid |
en |
dc.subject.other |
Industrial waste disposal |
en |
dc.subject.other |
Oxidation |
en |
dc.subject.other |
Textile processing |
en |
dc.subject.other |
Reactive dyes |
en |
dc.subject.other |
Wastewater treatment |
en |
dc.title |
Textile dye wastewater treatment with the use of an electrolysis system |
en |
heal.type |
journalArticle |
en |
heal.publicationDate |
1999 |
en |
heal.abstract |
Textile Dye Wastewater (TDW) from a reactive azo dyeing process was treated by an electrochemical oxidation method using Ti/Pt as anode and Stainless Steel 304 as cathode. Due to the strong oxidizing potential of the chemicals produced (chlorine, oxygen, hydroxyl radicals and other oxidants) when the wastewater was passed through the electrolytic cell the organic pollutants were oxidized to carbon dioxide and water. A number of experiments were run in a batch, laboratory-scale, pilot-plant, and the results are reported here according to residence time and initial addition of HCl in raw wastewater. When of 2 ml of HCl 36% were added and after 18 minutes of electrolysis at 0.89 A/cm2, COD was reduced by 86%, BOD5 was reduced by 71%, ADMI color units were reduced by 100%. The biodegradability of the wastewater was improved because the COD/BOD ratio decreased from 2.16 to 1.52. At the same time the mean energy consumption was 21 kwh per kg of COD. These results indicate that this electrolytic method could be used for effective TDW oxidation or as a feasible detoxification and color removal pretreatment stage for biological post treatment. |
en |
heal.publisher |
Technomic Publ Co Inc, Lancaster, PA, United States |
en |
heal.journalName |
Hazardous and Industrial Wastes - Proceedings of the Mid-Atlantic Industrial Waste Conference |
en |
dc.identifier.spage |
147 |
en |
dc.identifier.epage |
156 |
en |