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US3954449A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the recovery of noble metals

Assignee: Patheon Austria GmbH and Co KG
•
Filing: 1974-07-11
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Granted: 1976-05-04
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Expires: 1994-07-11
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Abstract

Abstract A process for the recovery of noble metals emanating from the surface of catalysts used in high pressure gas reactions involving absorbing the noble metal dispersed in the reaction gas in an intercepting bed formed of acid-soluble metal oxides in which the external boundary surface of the intercepting bed is 1.5 to 20 times the cross-sectional area of the catalyst bed surface, the thickness of the intercepting bed, in the direction of gas flow through the material thereof, is 20 to 40 mm., and the flow of the reaction gases in the intercepting bed is in a direction parallel to the plane of the supporting base of the bed.

Inventors

  • 👤 Hermann Rudorfer
  • 👤 Anton Wagner
  • 👤 Franz Prammer
  • 👤 Friedrich Klausner

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 15:03
CPC Classifications
C; C01; C01B; C01B21/00; C01B21/20; C01B21/24; C01B21/26; C01B21/267; B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/64; B01J; B01J8/00; B01J8/02; B01J8/0207

Claims Analysis

Total Claims: 3
Claim 1
Independent Claim 273 words
A process for the recovery of a noble metal which has volatilised or become detached in a very finely divided state from the surface of a noble metal catalyst gauze in an exothermic reaction of a gaseous mixture, preferably a mixture of ammonia and air to form nitrous gases, carried out under an excess pressure of at least one atmosphere gauge, said process comprising: providing, downstream of said gauze in the direction of gas flow therefrom, a noble metal absorbing and intercepting bed formed of granular acid-soluble alkaline earth metal oxide material, said bed being in the form of channels filled by said material and separated by open channels extending in the direction of gas flow from said gauze to said bed, said bed having a total external gas incident surface of 1.5 to 20 times the cross-sectional area encompassed by said material filled channels and said open channels taken in a plane transverse to said direction, said bed being maintained at a temperature of from about 600° to 900°C; passing the gaseous reaction mixture, after having passed the noble metal catalyst gauze, in said direction into a portion of said open channels; then directing said gaseous reaction mixture transverse to said direction through said material filled channels, thereby removing noble metal from said gaseous reaction mixture, and into the remainder of said open channels, said material filled channels having a thickness in the direction of gaseous flow therethrough of 20 to 40 mm; and thereafter, when the intercepting action of said material of said bed has been exhausted, recovering the noble metal removed by said bed by dissolving said material in acid.
Claim 2
Dependent Claim 273 words
A process for the recovery of a noble metal which has volatilised or become detached in a very finely divided state from the surface of a noble metal catalyst gauze in an exothermic reaction of a gaseous mixture, preferably a mixture of ammonia and air to form nitrous gases, carried out under an excess pressure of at least one atmosphere gauge, said process comprising: providing, downstream of said gauze in the direction of gas flow therefrom, a noble metal absorbing and intercepting bed formed of granular acid-soluble alkaline earth metal oxide material, said bed being in the form of channels filled by said material and separated by open channels extending in the direction of gas flow from said gauze to said bed, said bed having a total external gas incident surface of 1.5 to 20 times the cross-sectional area encompassed by said material filled channels and said open channels taken in a plane transverse to said direction, said bed being maintained at a temperature of from about 600° to 900°C; passing the gaseous reaction mixture, after having passed the noble metal catalyst gauze, in said direction into a portion of said open channels; then directing said gaseous reaction mixture transverse to said direction through said material filled channels, thereby removing noble metal from said gaseous reaction mixture, and into the remainder of said open channels, said material filled channels having a thickness in the direction of gaseous flow therethrough of 20 to 40 mm; and thereafter, when the intercepting action of said material of said bed has been exhausted, recovering the noble metal removed by said bed by dissolving said material in acid.
Claim 3
Dependent Claim 18 words
A process as claimed in claim 1, wherein said noble metal is a metal of the platinum group.

References Cited (Backward Citations)

US2226113A Cited
US2226149A Cited
US2920953A Cited
US3515541A Cited
US3627497A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-05-04 1979-11-03 1980-05-04 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-05-04 1983-11-03 1984-05-04 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-05-04 1987-11-03 1988-05-04 $7700.00 Window Closed / Lapsed

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