Abstract
Since 2004 pilot plant trials have been conducted with various contactors and different ionic
liquids for petrochemical model feeds as well as real refinery feeds. Our pilot plant contains
several columns (rotating disc contactor, Kuhni, pulsed disc and donut column) with a height of
6 m and 5 cm diameter. Up to 100 kg of ionic liquid and 200 L of feed are applied in experiments.
In this paper the hydrodynamic and mass transfer performance of a rotating disc contactor has
been characterised for toluene/heptane, a model FCC (fluid catalytic cracker) feed and a real
LCCS (Light Catalytically Cracked Spirit) refinery feed using 3-methyl-N-butyl-pyridinum
dicyanamide as the ionic liquid. Experiments with the real LCCS feed demonstrated comparable
extraction performance to the model FCC feed. Over the past five years the same batches of ionic
liquids have been repeatedly regenerated by evaporation and reused. The studies revealed that,
although coloration occurs, the extraction performance of the ionic liquids has not changed even
after several years of usage. After the real LCCS refinery feed experiments, validation with the
toluene/heptane model feed confirmed unchanged extraction performance.
Original language | English |
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Title of host publication | Proceedings of the 19th International Solvent Extraction Conference - ISEC 2011, 3-7 October 2011, Santiago, Chile |
Pages | 1-7 |
Publication status | Published - 2011 |
Event | 19th International Solvent Extraction Conference (ISEC 2011), October 3-7, 2011, Santiago, Chile - Santiago, Chile Duration: 3 Oct 2011 → 7 Oct 2011 https://gecamin.com/isec2011/index.php?option=com_content&view=frontpage&Itemid=1&lang=en |
Conference
Conference | 19th International Solvent Extraction Conference (ISEC 2011), October 3-7, 2011, Santiago, Chile |
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Abbreviated title | ISEC 2011 |
Country/Territory | Chile |
City | Santiago |
Period | 3/10/11 → 7/10/11 |
Internet address |