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US3855385A Expired / Lapsed US ⏱️ 0.0 years remaining

Recovery of rhenium from a spent catalyst

Assignee: Universal Oil Products Co
•
Filing: 1973-11-12
•
Granted: 1974-12-17
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Expires: 1993-11-12
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Abstract

Abstract Rhenium is recovered from a spent platinum-rhenium-alumina catalyst containing molybdenum. The spent catalyst is first treated with sulfuric acid to form a rhenium and molybdenumcontaining aluminum sulfate solution and a platinum-containing residue. The aluminum sulfate solution is processed through a series of contactors in countercurrent contact with an amine solution. The amine-rhenium mole ratio is controlled within a specified range in the various contactors whereby the rhenium is recovered in the amine phase and the molybdenum is recovered in the aluminum sulfate phase.

Inventors

  • 👤 A Derosset
  • 👤 K Morgan

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 23:48
CPC Classifications
C; C01; C01G; C01G39/00; C01G39/003; B; B01; B01J; B01J23/00; B01J23/90; B01J23/92; B01J23/96; C01G47/00; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/584

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 274 words
A PROCESS FOR THE RECOVERY OF RHENIUM FROM A MOLYBDENUM-CONTAINING ALUM SOLUTION RESULTING FROM THE DIGESTION OF A SPENT PLATIUM-RHENIUM CATALYST IN CONCENTRATED SULFURIC ACID, WITH A PLATINUM-CONTAINING RESIDUE HAVING BEEN SEPARATED BY FILTRATION WHICH COMPRISES A. CHANGING SAID ALUM SOLUTION DOWNWARDLY THROUGH A FIRST CONTACTOR COLUMN WITH AN AMINE SOLUTION CHARGED UPWARDLY THERETHROUGH AT CONDITIONS TO MAINTAIN AN AMINE/RHENIUM MOLE RATIO OF FROM ABOUT 1.4 TO ABOUT 1.8 IN THE LOWER OF SAID COLUMN AND EXTRACTING SUBSTANTIALLY ALL OF THE RHENIUM IN SAID ALUM SOLUTION, B. CHANGING THE RESULTING RHENIUM-CONTAINING AMINE SOLUTION UPWARDLY THROUGH A SECOND CONTCTOR COLUMN IN CONTACT WITH AN ALUM SOLUTION CHARGED DOWNWARDLY THERETHROUGH AND CONTAINING SUFFICIENT ADDED RHENIUM TO MAINTAIN AN AMINE/RHENIUM MOLE RATIO IN THE UPPER PORTION OF SAID COLUMN OF FROM ABOUT 0.1 TO ABOUT 1.2, AND STRIPPING SUBSTANTIALLY ALL OF THE MOLYBUDEUM FROM SAID RHENIUMCONTAINING AMINE SOLUTION, AND EXTRACTING A MAJOR PORTION OF THE RHENIUM CONTAINED IN SAID ALUM SOLUTION; C. CHARGING THE RESULTING MOLYBDENUM-CONTAINING ALUM SOLUTION DOWNWARDLY THROUGH THE FIRST CONTACTOR COLUMN IN ADMIXTURE WITH THE FIRST MENTIONED ALUM SOLUTION CHARGED THERETO, AND SEPARATING AND RECOVERING THE MOLYBDENUM-FREE RHENIUM-CONTAINING AMINE SOLUTION; D. DISCHARGING A PORTION OF THE MOLYBDENUM-CONTAINING ALUM SOLUTION PASSING DOWNWARDLY THROUGH SAID FIRST CONTRACTOR COLUMN, AND CHARGING THE REMAINING PORTION DOWNWARDLY THROUGH A THIRD CONTRACTOR COLUMN IN CONTACT WITH AN AMINE SOLUTION CHARGED UPWARDLY THERETHROUGH, EXTRACTING SUBSTANTIALLY ALL OF THE MOLYBDENUM CONTAINED IN SAID ALUM SOLUTION, AND CHARGING THE RESULTING ALUM SOLUTION AND ADDED RHENIUM DOWNWARDLY THROUGH SAID SECOND CONTRACTOR COLUMN IN ACCORDANCE WITH STEP (A), AND CHARGING THE RESULTING AMINE SOLUTION UPWARDLY THROUGH THE SECOND CONTACT COLUMN IN ACCORDANCE WITH STEP (A).
Claim 2
Dependent Claim 274 words
A PROCESS FOR THE RECOVERY OF RHENIUM FROM A MOLYBDENUM-CONTAINING ALUM SOLUTION RESULTING FROM THE DIGESTION OF A SPENT PLATIUM-RHENIUM CATALYST IN CONCENTRATED SULFURIC ACID, WITH A PLATINUM-CONTAINING RESIDUE HAVING BEEN SEPARATED BY FILTRATION WHICH COMPRISES A. CHANGING SAID ALUM SOLUTION DOWNWARDLY THROUGH A FIRST CONTACTOR COLUMN WITH AN AMINE SOLUTION CHARGED UPWARDLY THERETHROUGH AT CONDITIONS TO MAINTAIN AN AMINE/RHENIUM MOLE RATIO OF FROM ABOUT 1.4 TO ABOUT 1.8 IN THE LOWER OF SAID COLUMN AND EXTRACTING SUBSTANTIALLY ALL OF THE RHENIUM IN SAID ALUM SOLUTION, B. CHANGING THE RESULTING RHENIUM-CONTAINING AMINE SOLUTION UPWARDLY THROUGH A SECOND CONTCTOR COLUMN IN CONTACT WITH AN ALUM SOLUTION CHARGED DOWNWARDLY THERETHROUGH AND CONTAINING SUFFICIENT ADDED RHENIUM TO MAINTAIN AN AMINE/RHENIUM MOLE RATIO IN THE UPPER PORTION OF SAID COLUMN OF FROM ABOUT 0.1 TO ABOUT 1.2, AND STRIPPING SUBSTANTIALLY ALL OF THE MOLYBUDEUM FROM SAID RHENIUMCONTAINING AMINE SOLUTION, AND EXTRACTING A MAJOR PORTION OF THE RHENIUM CONTAINED IN SAID ALUM SOLUTION; C. CHARGING THE RESULTING MOLYBDENUM-CONTAINING ALUM SOLUTION DOWNWARDLY THROUGH THE FIRST CONTACTOR COLUMN IN ADMIXTURE WITH THE FIRST MENTIONED ALUM SOLUTION CHARGED THERETO, AND SEPARATING AND RECOVERING THE MOLYBDENUM-FREE RHENIUM-CONTAINING AMINE SOLUTION; D. DISCHARGING A PORTION OF THE MOLYBDENUM-CONTAINING ALUM SOLUTION PASSING DOWNWARDLY THROUGH SAID FIRST CONTRACTOR COLUMN, AND CHARGING THE REMAINING PORTION DOWNWARDLY THROUGH A THIRD CONTRACTOR COLUMN IN CONTACT WITH AN AMINE SOLUTION CHARGED UPWARDLY THERETHROUGH, EXTRACTING SUBSTANTIALLY ALL OF THE MOLYBDENUM CONTAINED IN SAID ALUM SOLUTION, AND CHARGING THE RESULTING ALUM SOLUTION AND ADDED RHENIUM DOWNWARDLY THROUGH SAID SECOND CONTRACTOR COLUMN IN ACCORDANCE WITH STEP (A), AND CHARGING THE RESULTING AMINE SOLUTION UPWARDLY THROUGH THE SECOND CONTACT COLUMN IN ACCORDANCE WITH STEP (A).
Claim 3
Dependent Claim 22 words
The process of claim 1 further characterized in that said amine solution comprises a water-immiscible aliphatic amine in a water-immiscible organic solvent.
Claim 4
Dependent Claim 30 words
The process of claim 1 further characterized in that said amine solution comprises a water-immiscible aliphatic amine with aliphatic chain links in the C5-C18 range, and a water-immiscible organic solvent.
Claim 5
Dependent Claim 31 words
The process of claim 1 further characterized in that said amine solution comprises a water-immiscible aliphatic tertiary amine with aliphatic chain links in the C5-C18 range and a water-immiscible organic solvent.
Claim 6
Dependent Claim 30 words
The process of claim 1 further characterized in that said amine solution comprises a water-immiscible quarternary amine with aliphatic chain links in the C5-C18 range and a water-immiscible organic solvent.
Claim 7
Dependent Claim 18 words
The process of claim 1 further characterized in thAt said amine solution comprises a tridecylamine in kerosine solution.
Claim 8
Dependent Claim 19 words
The process of claim 1 further characterized in that said amine solution comprises methyltridecyl ammonium chloride in kerosine solution.

References Cited (Backward Citations)

US3244475A Cited
US3495934A Cited
US3672874A Cited
US3763303A Cited
US3798305A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1977-12-16 1978-06-17 1978-12-17 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1981-12-16 1982-06-17 1982-12-17 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1985-12-16 1986-06-17 1986-12-17 $7700.00 Window Closed / Lapsed

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