Method for recovering rhodium from hydroformylation products
View Patent ↗According to the invention, rhodium is recovered from hydroformylation products (feed material) by thermally processing the feed material in the presence of an adsorbent and, optionally, with the additional action of hydrogen.
1. A process for recovering rhodium present in the aldehyde—or aldehyde group-containing polyfunctional compounds of the decompressed crude products of the hydroformylation of olefinically unsaturated compounds, which comprises heating the hydroformylation products in the presence of activated carbon, high surface-area polysilicic acid, high surface-area aluminum oxide or high surface-area aluminum oxide hydrate as solid adsorbent and in the presence of hydrogen under pressures of from 0.1 to 15 MPa to temperatures of from 50 to 200° C.
2. The process as claimed in claim 1 , wherein the hydroformylation products are heated to temperatures of from 70 to 150° C.
3. The process as claimed in claim 1 , wherein the hydrogen is employed in pure form or mixed with inert gases.
4. The process as claimed in claim 1 , wherein hydrogen is employed in at least stoichiometric amount relative to rhodium.
5. The process as claimed in claim 1 , wherein from 100 to 2000 mol of hydrogen are used per mol of rhodium.
6. The process as claimed in claim 1 , wherein the heating of the hydroformylation products is carried out under pressures of from 5 to 10 MPa.
7. The process as claimed in claim 1 , wherein the heating of the hydroformylation products takes place on an adsorbent disposed as fixed bad.
8. The process as claimed in claim 7 , wherein space velocities of from 0.10 to 2.5 V react mixt. /V adsorbent ·h] are maintained in the heating of the hydroformylation products.
9. The process as claimed in claim 1 , wherein the adsorbent is suspended in the hydroformylation product.
10. The process as claimed in claim 9 , wherein from 1 to 5 parts by weight of adsorbent are suspended per 100 parts by weight of rhodium-containing hydroformylation product.
11. The process of claim 3 wherein the hydrogen is used in pure form.
12. The process of claim 5 wherein the amount of hydrogen used is 300 to 1200 mole.
13. The process of claim 8 wherein the space velocities are 1.0 to 1.5.
14. The process of claim 10 wherein 1.5 to 3.5 parts by weight of adsorbent are suspended.