Patent US3974227A successfully refreshed from Google Patents.
US3974227A
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Acid extracted-alkalized/carbon catalyst support with coordination complex catalyst and method of manufacture
Assignee: Rhone Progil SA
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Filing: 1975-03-20
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Granted: 1976-08-10
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Expires: 1995-03-20
Abstract
Abstract A catalyst for hydrogenation, hydroformylation, olefin oxidation and similar reactions is prepared by treating activated carbon first with a volatile acid and then with a basic substance to provide a suitable support for the catalyst, and then adsorbing onto such support a coordination complex of a transition metal. The adsorption of the catalyst onto the support may be effected in situ during the hydrogenation, hydroformylation, oxidation, etc. reaction.
Inventors
- 👤 Jean Berthoux
- 👤 Jacques-Pierre Martinaud
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 05:06
CPC Classifications
C; C07; C07C; C07C45/00; C07C45/49; C07C45/50; B; B01; B01J; B01J21/00; B01J21/18; B01J31/00; B01J31/16; B01J31/1616; B01J31/18; B01J31/1845; B01J31/185; B01J31/20; B01J2231/00; B01J2231/30; B01J2231/32; B01J2231/321; B01J2531/00; B01J2531/80; B01J2531/82; B01J2531/822; B01J2531/824; B01J2531/827; B01J2531/828; B01J2531/84; B01J2531/847; Y; Y02; Y02P; Y02P20/00; Y02P20/50
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
310 words
A process for the preparation of a supported catalyst of a coordination complex of a transition metal useful in liquid phase reactions of olefin hydrogenation, hydroformylation and oxidation, of pre-activated carbon comprising: contacting said pre-activated carbon with an amount of aqueous solution of a volatile acid sufficient to substantially eliminate by reaction therewith the acid-extractable impurities in said carbon, said aqueous solution of volatile acid comprising 0.5 to 20% by weight of said acid and being present in a large excess -- compared with the quantity theoretically needed to eliminate the acid-extractable impurities -- during its contact with said pre-activated carbon; drying said acid treated pre-activated carbon; treating said dried, acid treated, pre-activated carbon to render the carbon alkaline with an aqueous solution of a mineral basic substance containing 1 × 10 - 1 to 1 × 10 - 3 moles of said mineral basic substance from the group consisting of alkali and alkaline-earth hydroxides and alkali carbonates per liter of solution, said aqueous solution of mineral basic substance being present in a large excess -- such that the ratio of its final concentration to its starting concentration is approximately one -- during the contact with said dried, acid treated, pre-activated carbon; drying the so base-treated carbon; and depositing said coordination complex on the so-treated carbon in liquid phase, wherein said coordination complex has the formula [M Cl x H y (CO) z L t ] wherein M is the metal nickel, rhodium, palladium, iridium or platinum; x + y = 1 when M is rhodium or iridium; x and y = 0 for the other metals; the total of x + y + z + t = 4; and L is a ligand selected from the group consisting of aliphatic and aromatic phosphites, aminophosphines, and -- where y = 1 and z = 0 -- aliphatic and aromatic phosphines.
Claim 2
Dependent Claim
310 words
A process for the preparation of a supported catalyst of a coordination complex of a transition metal useful in liquid phase reactions of olefin hydrogenation, hydroformylation and oxidation, of pre-activated carbon comprising: contacting said pre-activated carbon with an amount of aqueous solution of a volatile acid sufficient to substantially eliminate by reaction therewith the acid-extractable impurities in said carbon, said aqueous solution of volatile acid comprising 0.5 to 20% by weight of said acid and being present in a large excess -- compared with the quantity theoretically needed to eliminate the acid-extractable impurities -- during its contact with said pre-activated carbon; drying said acid treated pre-activated carbon; treating said dried, acid treated, pre-activated carbon to render the carbon alkaline with an aqueous solution of a mineral basic substance containing 1 × 10 - 1 to 1 × 10 - 3 moles of said mineral basic substance from the group consisting of alkali and alkaline-earth hydroxides and alkali carbonates per liter of solution, said aqueous solution of mineral basic substance being present in a large excess -- such that the ratio of its final concentration to its starting concentration is approximately one -- during the contact with said dried, acid treated, pre-activated carbon; drying the so base-treated carbon; and depositing said coordination complex on the so-treated carbon in liquid phase, wherein said coordination complex has the formula [M Cl x H y (CO) z L t ] wherein M is the metal nickel, rhodium, palladium, iridium or platinum; x + y = 1 when M is rhodium or iridium; x and y = 0 for the other metals; the total of x + y + z + t = 4; and L is a ligand selected from the group consisting of aliphatic and aromatic phosphites, aminophosphines, and -- where y = 1 and z = 0 -- aliphatic and aromatic phosphines.
Claim 3
Dependent Claim
14 words
A process in accordance with claim 1 wherein said volatile acid is hydrochloric acid.
Claim 4
Dependent Claim
27 words
A process according to claim 1 wherein said aqueous solution of volatile acid is present in an amount of 5 - 20 ml. per gm. of carbon.
Claim 5
Dependent Claim
22 words
A process in accordance with claim 1 wherein said mineral basic substance is sodium hydroxide, calcium hydroxide, barium hhydroxide, or sodium carbonate.
Claim 6
Dependent Claim
55 words
A process in accordance with claim 1 wherein said aqueous solution of acid contains 1 to 10% by weight of acid, and said basic mineral substance comprises an aqueous solution of said mineral substance containing 5 × 10 - 2 to 5 × 10 - 3 moles of said basic substance per liter of solution.
Claim 7
Dependent Claim
13 words
A supported catalyst comprising a product obtained by the process of claim 1.
Claim 8
Dependent Claim
64 words
A process in accordance with claim 1 for preparing a supported catalyst wherein said depositing of said coordination complex on said carbon comprises: mixing, in reactor, an olefin, hydrogen, carbon monoxide, a solvent comprising an aliphatic ketone, said coordination complex of a transition metal, and said carbon; and carrying out a hydroformylation reaction and simultaneously fixing the active catalyst on the activated carbon support.
Claim 9
Dependent Claim
160 words
A process in accordance with claim 1 for the preparation of a supported catalyst of a coordination complex of a transition metal useful in liquid phase reactions of olefin hydrogenation, hydroformylation and oxydation, from pre-activated carbon, comprising: contacting said pre-activated carbon with 5 - 20 ml of an aqueous 0.5 - 20% solution of a volatile acid per gram of pre-activated carbon, at room temperature for 5 - 24 hours, said volatile acid being selected from the group consisting of hydrochloric acid, formic acid and acetic acid; drying said acid-treated pre-activated carbon; contacting said dried, acid-treated, pre-activated carbon with 50 - 100 parts by weight, per part by weight of said carbon, of an aqueous solution containing 1 × 10 - 1 to 1 × 10 - 3 mols per liter of a mineral basic substance selected from the group consisting of sodium hydroxide, calcium hydroxide, barium hydroxide and sodium carbonate, for 5 - 24 hours; and drying said carbon.
Claim 10
Dependent Claim
43 words
A process in accordance with claim 1 wherein the step of depositing said coordination complex on the acid and base-treated pre-activated carbon in liquid phase comprises: mixing said complex and said so-treated pre-activated carbon in a solvent in which adsorption can take place.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-08-10 | 1980-02-09 | 1980-08-10 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-08-10 | 1984-02-09 | 1984-08-10 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-08-10 | 1988-02-09 | 1988-08-10 | $7700.00 | Window Closed / Lapsed |