US3899442A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Recovery and reactivation of rhodium hydroformylation catalysts
Assignee: United States Department of Agriculture
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Filing: 1974-01-31
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Granted: 1975-08-12
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Expires: 1994-01-31
Abstract
Abstract Soluble rhodium materials are concentrated in the residue from the distillation of hydroformylated products resulting from the reaction of unsaturated hydrocarbons, unsaturated fatty acids, or unsaturated fatty compounds with carbon monoxide and hydrogen in the presence of a supported rhodium catalyst. An active catalyst was provided when the rhodium was recovered and resupported. The same rhodium was recovered and resupported 10 times with no significant loss in activity.
Inventors
- 👤 John P Friedrich
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 21:09
CPC Classifications
B; B01; B01J; B01J31/00; B01J31/40; B01J31/4015; B01J31/4023; B01J31/4038; B01J31/4046; B01J31/16; B01J31/1616; B01J31/18; B01J31/1845; B01J31/185; B01J31/24; C; C07; C07C; C07C45/00; C07C45/49; C07C45/50; C07C67/00; C07C67/30; C07C67/333; C07C67/343; C07C67/347; B01J21/00; B01J21/02; B01J21/04; B01J21/06; B01J21/08; B01J2231/00; B01J2231/30; B01J2231/32; B01J2231/321; B01J2531/00; B01J2531/80; B01J2531/82; B01J2531/822; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/584
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
189 words
IN A METHOD FOR RECOVERING AND REACTIVATING RHODIUM CATALYSTS IN A PROCESS WHEREIN UNSATURATED HYDROCARBONS, OR UNSATURATED FATTY COMPOUNDS ARE HYDROFORMYLATED AT TEMPERATURES OF ABOUT 100* TO 300*C, WITH HYDROGEN AND CARBON MONOXIDE UNDER PRESSURES OF FROM ATMOSPHERIC PRESSURE TO 3000 P.S.I.G. IN THE PRESENCE OF A CATALYST CONSISTING OF RHODIUM METAL ON A RELATIVELY INERT SUPPORT ADMIXEDD WITH A TRISUBSTITUTED PHOSPHINE, AND WHEREIN THE HYDROFORMYLATED REACTION PRODUCTS ARE FILTERED AND DISTILLED LEAVING A RESIDUE WHICH CONTAINS ESSENTIALLY ALL OF THE SOLUBLE RHODIUM, THE IMPROVEMENT COMPRISING THE FOLLOWING STEPS: A. MIXING SAID RESIDUE WITH A REFRACTORY CATALYST SUPPORT, B. VOLATILIZING AND CARBONIZING ESSENTIALLY ALL ORGANIC MATERIALS PRESENT IN THE MIXTURE RESULTING FROM STEP (B) BY HEATING SAID MIXTURE TO FROM 150* TO 450*C, IN AN ATMOSPHERE SUCH THAT VOLATILE MATERIALS GIVEN OFF WILL BE PREVENTED FROM IGNITING, C. REACTING IN A SUITABLE VESSEL ESSENTIALLY ALL OF THE CARBON-IZED MATERIAL REMAINING FROM STEP (B) WITH OXYGEN CONTAINED IN AIR AT A TEMPERATURE OF FROM 350* TO 1000*C, FOR A LENGTH OF TIME SUFFICIENT TO FORM CARBON DIOXIDE AND WATER, AND D. COOLING SAID VESSEL AND REMOVING THE RESULTING RESUPPORTED CATALYST.
Claim 2
Dependent Claim
189 words
IN A METHOD FOR RECOVERING AND REACTIVATING RHODIUM CATALYSTS IN A PROCESS WHEREIN UNSATURATED HYDROCARBONS, OR UNSATURATED FATTY COMPOUNDS ARE HYDROFORMYLATED AT TEMPERATURES OF ABOUT 100* TO 300*C, WITH HYDROGEN AND CARBON MONOXIDE UNDER PRESSURES OF FROM ATMOSPHERIC PRESSURE TO 3000 P.S.I.G. IN THE PRESENCE OF A CATALYST CONSISTING OF RHODIUM METAL ON A RELATIVELY INERT SUPPORT ADMIXEDD WITH A TRISUBSTITUTED PHOSPHINE, AND WHEREIN THE HYDROFORMYLATED REACTION PRODUCTS ARE FILTERED AND DISTILLED LEAVING A RESIDUE WHICH CONTAINS ESSENTIALLY ALL OF THE SOLUBLE RHODIUM, THE IMPROVEMENT COMPRISING THE FOLLOWING STEPS: A. MIXING SAID RESIDUE WITH A REFRACTORY CATALYST SUPPORT, B. VOLATILIZING AND CARBONIZING ESSENTIALLY ALL ORGANIC MATERIALS PRESENT IN THE MIXTURE RESULTING FROM STEP (B) BY HEATING SAID MIXTURE TO FROM 150* TO 450*C, IN AN ATMOSPHERE SUCH THAT VOLATILE MATERIALS GIVEN OFF WILL BE PREVENTED FROM IGNITING, C. REACTING IN A SUITABLE VESSEL ESSENTIALLY ALL OF THE CARBON-IZED MATERIAL REMAINING FROM STEP (B) WITH OXYGEN CONTAINED IN AIR AT A TEMPERATURE OF FROM 350* TO 1000*C, FOR A LENGTH OF TIME SUFFICIENT TO FORM CARBON DIOXIDE AND WATER, AND D. COOLING SAID VESSEL AND REMOVING THE RESULTING RESUPPORTED CATALYST.
Claim 3
Dependent Claim
17 words
A method as described in claim 1, wherein the refractory catalyst support is alumina, silica, or firebrick.
Claim 4
Dependent Claim
26 words
A method as described in claim 1, wherein the mixture resulting from step (a) contains from 0.1 to 10 weight percent rhodium based on rhodium metal.
Claim 5
Dependent Claim
27 words
A method as described in claim 3, wherein the mixture resulting from step (a) is volatilized and carbonized at a temperature of from 150* to 300* C.
Claim 6
Dependent Claim
31 words
A method as described in claim 1, wherein the carbonized material remaining from step (b) is heated in the presence of air to a temperature of from 500* to 700* C.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1978-08-11 | 1979-02-10 | 1979-08-12 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1982-08-11 | 1983-02-10 | 1983-08-12 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1986-08-11 | 1987-02-10 | 1987-08-12 | $7700.00 | Window Closed / Lapsed |