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US3883419A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for preparing platinum-tin reforming catalysts and use thereof

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1973-10-17
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Granted: 1975-05-13
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Expires: 1993-10-17
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Abstract

Abstract Supported platinum group metal-tin hydrocarbon conversion catalysts are prepared by (1) impregnating a refractory inorganic oxide support with an aqueous solution of a halogen acid containing a platinum group metal component; (2) drying the platinum group metal impregnated carrier; (3) impregnating the dried platinum group metal impregnate with a solution of a divalent tin compound in a non-oxidizing and non-reducing atmosphere; and (4) drying the resulting impregnate.

Inventors

  • 👤 Takuji Itoh
  • 👤 Ikuo Akitsuki

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 00:30
CPC Classifications
B; B01; B01J; B01J23/00; B01J23/38; B01J23/54; B01J23/56; B01J23/62; B01J23/622; B01J23/626; C; C10; C10G; C10G35/00; C10G35/04; C10G35/06; C10G35/085; C10G35/09

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 112 words
A PROCESS FOR PREPARING A HYDROCARBON CONVERSION CATALYST COMPRISING A COMPLEX COMPOUND OF A PLATINUM GROUP METAL COMPONENT AND A TIN COMPONENT CONTAINED ON A REFRACTORY INORGANIC OXIDE CARRIER WHICH COMPRISES: A. IMPREGNATING SAID REFRACTORY INORGANIC OXIDE CARRIER WITH AN AQUEOUS SOLUTION OF A HALOGEN ACID CONTAINING A PLATINUM GROUP METAL COMPONENT; B. DRYING THE PLATINUM GROUP METAL COMPONENT IMPREGNATED CARRIER; C. IMPREGNATING THE DRIED PLATINUM GROUP METAL COMPONENTIMPREGNATED CARRIER WITH A SOLUTION OF A DIVALENT TIN COMPOUND, SAID IMPREGNATION CONDUCTED IN A NON-OXIDIZING AND NON-REDUCING ATMOSPHERE; D. DRYING THE CARRIER IMPREGNATED WITH SAID PLATINUM GROUP COMPONENT AND TI COMPONENT; AND E. CALCINING THE DRIED IMPREGNATE OF STEP (D) AT ELEVATED TEMPERATURES.
Claim 2
Dependent Claim 112 words
A PROCESS FOR PREPARING A HYDROCARBON CONVERSION CATALYST COMPRISING A COMPLEX COMPOUND OF A PLATINUM GROUP METAL COMPONENT AND A TIN COMPONENT CONTAINED ON A REFRACTORY INORGANIC OXIDE CARRIER WHICH COMPRISES: A. IMPREGNATING SAID REFRACTORY INORGANIC OXIDE CARRIER WITH AN AQUEOUS SOLUTION OF A HALOGEN ACID CONTAINING A PLATINUM GROUP METAL COMPONENT; B. DRYING THE PLATINUM GROUP METAL COMPONENT IMPREGNATED CARRIER; C. IMPREGNATING THE DRIED PLATINUM GROUP METAL COMPONENTIMPREGNATED CARRIER WITH A SOLUTION OF A DIVALENT TIN COMPOUND, SAID IMPREGNATION CONDUCTED IN A NON-OXIDIZING AND NON-REDUCING ATMOSPHERE; D. DRYING THE CARRIER IMPREGNATED WITH SAID PLATINUM GROUP COMPONENT AND TI COMPONENT; AND E. CALCINING THE DRIED IMPREGNATE OF STEP (D) AT ELEVATED TEMPERATURES.
Claim 3
Dependent Claim 13 words
The process of claim 1 wherein said divalent tin component is stannous chloride.
Claim 4
Dependent Claim 16 words
The process of claim 1 wherein said aqueous solUtion employed in step (a) contains hydrochloric acid.
Claim 5
Dependent Claim 18 words
The process of claim 1 wherein said platinum group metal component employed in step (a) is chloroplatinic acid.
Claim 6
Dependent Claim 17 words
The process of claim 1 wherein said solution employed in step (c) in an aliphatic alcohol solution.
Claim 7
Dependent Claim 10 words
The process of claim 1 wherein said carrier is alumina.
Claim 8
Dependent Claim 94 words
The process for preparing a hydrocarbon conversion catalyst comprising a complex compound of a platinum component and stannous chloride contained on alumina which comprises: a. impregnating the said alumina with an aqueous solution of hydrochloric acid containing a platinum component; b. drying said platinum component-alumina impregnate; c. impregnating the dried platinum componentalumina impregnate with a solution of stannous chloride in a non-oxidizing and non-reducing atmosphere; d. drying the impregnate from step (c); and e. calcining said dried impregnate from step (d) by heating the same at a temperature varying from 400* to about 700*C.
Claim 9
Dependent Claim 94 words
The process for preparing a hydrocarbon conversion catalyst comprising a complex compound of a platinum component and stannous chloride contained on alumina which comprises: a. impregnating the said alumina with an aqueous solution of hydrochloric acid containing a platinum component; b. drying said platinum component-alumina impregnate; c. impregnating the dried platinum componentalumina impregnate with a solution of stannous chloride in a non-oxidizing and non-reducing atmosphere; d. drying the impregnate from step (c); and e. calcining said dried impregnate from step (d) by heating the same at a temperature varying from 400* to about 700*C.
Claim 10
Dependent Claim 113 words
An improved hydrocarbon conversion catalyst comprising a complex compound of a platinum group component and a tin component contained on a refractory inorganic oxide carrier, said catalyst prepared by a process comprising: a. impregnating said refractory inorganic oxide carrier with an aqueous solution of a halogen acid containing a platinum group metal component; b. drying the platinum group metal componentimpregnated carrier; c. impregnating the dried platinum group metal component-impregnated carrier with a solution of a divalent tin compound, said impregnation conducted in a non-oxidizing and non-reducing atmosphere; and d. drying the carrier impregnated with said platinum group component and tin component; and (e) calcining the dried impregnate of step (d) at elevated temperatures.
Claim 11
Dependent Claim 113 words
An improved hydrocarbon conversion catalyst comprising a complex compound of a platinum group component and a tin component contained on a refractory inorganic oxide carrier, said catalyst prepared by a process comprising: a. impregnating said refractory inorganic oxide carrier with an aqueous solution of a halogen acid containing a platinum group metal component; b. drying the platinum group metal componentimpregnated carrier; c. impregnating the dried platinum group metal component-impregnated carrier with a solution of a divalent tin compound, said impregnation conducted in a non-oxidizing and non-reducing atmosphere; and d. drying the carrier impregnated with said platinum group component and tin component; and (e) calcining the dried impregnate of step (d) at elevated temperatures.
Claim 12
Dependent Claim 127 words
A naphtha reforming process which comprises contacting a naphtha feed stock and hydrogen under reforming conditions with a catalyst comprising a complex compound of a platinum group metal component and a tin component contained on a refractory inorganic oxide carrier, said catalyst prepared by the method comprising: a. impregnating said refractory inorganic oxide carrier with an aqueous solution of halogen acid containing a platinum group metal component; b. drying the platinum group metal componentimpregnated carrier; c. impregnating the dried platinum group metal component-impregnated carrier with a solution of a divalent tin compound, said impregnation conducted in a non-oxidizing and non-reducing atmosphere; and d. drying the carrier impregnated with said platinum group component and tin component; and e. calcining the dried impregnate of step (d) at elevated temperatures.
Claim 13
Dependent Claim 127 words
A naphtha reforming process which comprises contacting a naphtha feed stock and hydrogen under reforming conditions with a catalyst comprising a complex compound of a platinum group metal component and a tin component contained on a refractory inorganic oxide carrier, said catalyst prepared by the method comprising: a. impregnating said refractory inorganic oxide carrier with an aqueous solution of halogen acid containing a platinum group metal component; b. drying the platinum group metal componentimpregnated carrier; c. impregnating the dried platinum group metal component-impregnated carrier with a solution of a divalent tin compound, said impregnation conducted in a non-oxidizing and non-reducing atmosphere; and d. drying the carrier impregnated with said platinum group component and tin component; and e. calcining the dried impregnate of step (d) at elevated temperatures.

References Cited (Backward Citations)

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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) 1978-05-12 1978-11-11 1979-05-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-05-12 1982-11-11 1983-05-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-05-12 1986-11-11 1987-05-13 $7700.00 Window Closed / Lapsed

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