dc.contributor.author | Bergmann, M. E. Henry | |
dc.contributor.author | Bouzek, K. | |
dc.contributor.author | Rittel, A. | |
dc.contributor.author | Koparal, Ali Savaş | |
dc.contributor.author | Paidar, M. | |
dc.date.accessioned | 2019-10-18T19:02:32Z | |
dc.date.available | 2019-10-18T19:02:32Z | |
dc.date.issued | 2004 | |
dc.identifier.issn | 0016-4232 | |
dc.identifier.uri | https://hdl.handle.net/11421/10675 | |
dc.description.abstract | The rotating cathode cell is an electrochemical reactor for treatment of process effluent by removal of metal ions in solution. Initial experiments were carried out using a small laboratory unit. In order to develop full-scale industrial size units rated at up to 500 Amp, while holding development costs to a minimum, the system was mathematically modelled in order to characterise the main parameters. Various models were used, with a range of complexities. By calculations using actual data and optimising the models used, a full-scale barrel with cascaded rotating cells, and a multi-stage reactor were brought to the production stage with a minimum ox expensive full-scale practical experiments. | en_US |
dc.language.iso | ger | en_US |
dc.rights | info:eu-repo/semantics/closedAccess | en_US |
dc.title | Modern engineering as exemplified by the development & modelling of the rotating cathode cell [Modernes engineering am beispiel der entwicklung und modellierung der wälzkathodenzelle] | en_US |
dc.type | article | en_US |
dc.relation.journal | Galvanotechnik | en_US |
dc.contributor.department | Anadolu Üniversitesi | en_US |
dc.identifier.volume | 95 | en_US |
dc.identifier.issue | 2 | en_US |
dc.identifier.startpage | VIII+470 | en_US |
dc.identifier.endpage | 490 | en_US |
dc.relation.publicationcategory | Makale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı | en_US |
dc.contributor.institutionauthor | Koparal, Ali Savaş | |