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Process for preparing noble metal catalysts

Assignee: Stamicarbon BV
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Filing: 1976-03-09
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Granted: 1977-10-04
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Expires: 1996-03-09
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Abstract

Abstract The invention relates to a process for preparing active noble-metal catalysts on a carbon carrier. In particular, the process comprises adsorbing a salt of the catalytically active metal onto the carbon in an aqueous medium; hydrolyzing said salt to the oxide or hydroxide, by employing a basic reagent; and reducing said oxide or hydroxide to the metal.

Inventors

  • 👤 Abraham van Montfoort
  • 👤 Joseph J. F. Scholten

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-07 12:25
CPC Classifications
C; C10; C10G; C10G35/00; C10G35/04; C10G35/06; C10G35/085; C10G35/09; B; B01; B01J; B01J23/00; B01J23/38; B01J23/40; C01; C01B; C01B21/00; C01B21/082; C01B21/14; C01B21/1409; C01B21/1418

Claims Analysis

Total Claims: 15
Claim 1
Independent Claim 180 words
In a process for preparing active noble-metal catalyst on a carbon carrier by adsorbing at least one water-soluble salt of a catalytically active metal onto the carbon in an aqueous medium, by hydrolyzing said salt by treating the salt with a basic reagent to form the oxide or hydroxide, and by reducing said oxide or hydroxide to the metal, the improvement comprising employing an active carbon having an acid to neutral reaction in water and an internal surface area of at least 300 m 2 /g and up to about 1000 m 2 /g with a particle size between 1 and 60 microns and with an ash content that does not exceed 3.5% by weight, whose ratio between (1) the pore volume, of the pores between 20 to 1000A plug the pores exceeding 1000A and (2) the total pore volume of said particles lies between 0.6 and 1.0 whereby the hydrolysis of the noble metal salt and the reduction of the oxide or hydroxide formed thereby are carried out in a single processing step with liquid hydrolyzing and reducing agents.
Claim 2
Dependent Claim 180 words
In a process for preparing active noble-metal catalyst on a carbon carrier by adsorbing at least one water-soluble salt of a catalytically active metal onto the carbon in an aqueous medium, by hydrolyzing said salt by treating the salt with a basic reagent to form the oxide or hydroxide, and by reducing said oxide or hydroxide to the metal, the improvement comprising employing an active carbon having an acid to neutral reaction in water and an internal surface area of at least 300 m 2 /g and up to about 1000 m 2 /g with a particle size between 1 and 60 microns and with an ash content that does not exceed 3.5% by weight, whose ratio between (1) the pore volume, of the pores between 20 to 1000A plug the pores exceeding 1000A and (2) the total pore volume of said particles lies between 0.6 and 1.0 whereby the hydrolysis of the noble metal salt and the reduction of the oxide or hydroxide formed thereby are carried out in a single processing step with liquid hydrolyzing and reducing agents.
Claim 3
Dependent Claim 28 words
Process according to claim 1, wherein the ratio between the volumes of the macro-pores plus the transition pores and the total pore volume amounts to at least 0.7.
Claim 4
Dependent Claim 12 words
Process according to claim 1, wherein the active carbon has hydrophilic properties.
Claim 5
Dependent Claim 13 words
Process according to claim 1, wherein the active carbon is poor in ash.
Claim 6
Dependent Claim 26 words
Process according to claim 1, wherein the reduction of the noble metal oxide or hydroxide in the presence of hydrolyzing agents is carried out with methanol.
Claim 7
Dependent Claim 25 words
Process according to claim 1, wherein the reduction of the noble oxide or hydroxide in the presence of hydrolyzing agents is carried out with formaldehyde.
Claim 8
Dependent Claim 27 words
Process according to claim 1, wherein the reduction of the noble metal oxide or hydroxide in the presence of hydrolyzing agents is carried out with formic acid.
Claim 9
Dependent Claim 42 words
Process according to claim 1, wherein the reduction of the noble metal oxide or hydroxide in the presence of hydrolyzing agents is carried out with a mixture of at least two members of the group consisting of methanol, formaldehyde and formic acid.
Claim 10
Dependent Claim 33 words
Process according to claim 1, wherein decomposition of the noble metal salt and the reduction of the resulting noble metal oxide of hydroxide are carried out at a temperature of 60°- 100° C.
Claim 11
Dependent Claim 36 words
Process according to claim 1, wherein said salt is one or more salts or complex compounds of the noble metals from Group VIII of the Periodic System of elements which are stable in an acid medium.
Claim 12
Dependent Claim 11 words
Process according to claim 1, whrein a plladium catalyst is prepared.
Claim 13
Dependent Claim 12 words
Process according to claim 1, wherein a palladium platinum catalyst is prepared.
Claim 14
Dependent Claim 185 words
In a process for the preparation of supported catalyst comprising treating at least one water-soluble salt or complex of a noble metal of Group VIII in the presence of a carrier with a base to form the oxide or hydroxide of said salt on the carrier and then reducing said oxide or hydroxide to form the free metal of the oxide or the hydroxide on said carrier, the improvement comprising using as a carrier an active carbon having a large internal surface area whose ratio between (1) the pore volumes of the macro pores plus the transition pores and (2) the total pore volume lies between 0.6 and 1.0, and dispersing the carrier in an aqueous solution of said salt; treating the carrier dispersion of the aqueous solution in a single step with (A) and (B) wherein (A) is a carbonate, or a bicarbonate of an alkali metal or ammonium and (B) is methanol, formic acid, formaldehyde, or mixtures thereof, thereby effecting (a) precipitation of said salt and adsorption of the salt onto the carrier and (b) reduction of the precipitate to the free metal.
Claim 15
Dependent Claim 185 words
In a process for the preparation of supported catalyst comprising treating at least one water-soluble salt or complex of a noble metal of Group VIII in the presence of a carrier with a base to form the oxide or hydroxide of said salt on the carrier and then reducing said oxide or hydroxide to form the free metal of the oxide or the hydroxide on said carrier, the improvement comprising using as a carrier an active carbon having a large internal surface area whose ratio between (1) the pore volumes of the macro pores plus the transition pores and (2) the total pore volume lies between 0.6 and 1.0, and dispersing the carrier in an aqueous solution of said salt; treating the carrier dispersion of the aqueous solution in a single step with (A) and (B) wherein (A) is a carbonate, or a bicarbonate of an alkali metal or ammonium and (B) is methanol, formic acid, formaldehyde, or mixtures thereof, thereby effecting (a) precipitation of said salt and adsorption of the salt onto the carrier and (b) reduction of the precipitate to the free metal.

References Cited (Backward Citations)

US3138560A Cited
US3663166A Cited
US3736266A Cited
US3804779A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-10-03 1981-04-04 1981-10-04 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-10-03 1985-04-04 1985-10-04 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-10-03 1989-04-04 1989-10-04 $7700.00 Window Closed / Lapsed

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