Catalyst recycling via specific non-covalent adsorption on modified silicas
| Authors | |
|---|---|
| Publication date | 2013 |
| Journal | Dalton Transactions |
| Volume | Issue number | 42 | 10 |
| Pages (from-to) | 3609-3616 |
| Organisations |
|
| Abstract |
This article describes a new strategy for the recycling of a homogeneous hydroformylation catalyst, by selective adsorption of the catalyst to tailor-made supports after a batchwise reaction. The separation of the catalyst from the product mixture is based on selective non-covalent supramolecular interactions between a ligand and the support. Changing the solvent releases the active catalyst back into the reactor and allows a subsequent batch reaction with the recycled active catalyst. For this purpose, the bidentate NixantPhos ligand has been equipped with a pyridine group. The corresponding rhodium pre-catalyst [Rh(Nix-py)(acac)] (acac = acetylacetonate) forms a very selective, active and highly stable catalyst, and able to reach a turnover number (TON) of 170 000 in a single run (reaction performed in nearly neat 1-octene, S/C ratio of 200 000, at 140 degrees C, 20 bars syngas pressure). Various commercially available supports have been explored in binding studies and recycling experiments. The end-capped silica-alumina performs the best so far with respect to ligand-adsorbing properties for the current purpose. Although this system has not been fully optimized, four recycling runs could be performed successfully.
|
| Document type | Article |
| Language | English |
| Published at | https://doi.org/10.1039/c2dt32047a |
| Downloads |
Catalyst_recycling.pdf
(Final published version)
|
| Permalink to this page | |
