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US3969273A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for preparing phosphated alumina extrudates

Assignee: WR Grace and Co
•
Filing: 1975-04-24
•
Granted: 1976-07-13
•
Expires: 1995-04-24
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Abstract

Abstract A process for the preparation of phosphate-containing extruded alumina catalyst supports is disclosed. Due to their particular characteristics, these supports find application in hydrocarbon conversion catalysts and especially in catalysts for the hydrotreating of petroleum feedstocks.

Inventors

  • 👤 Stanley Monty Brown
  • 👤 David Nelson Wallace

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 04:09
CPC Classifications
B; B01; B01J; B01J27/00; B01J27/14; B01J27/186; B01J27/188; B01J27/16; C; C10; C10G; C10G45/00; C10G45/02; C10G45/04; C10G45/06; C10G45/08

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 116 words
A process for preparing extruded alumina catalyst supports containing 1 to 10% phosphate which consists essentially of the steps of: a. precipitating the aluminum salt selected from the group consisting of aluminum sulfate, nitrate, and chloride with sodium or potassium aluminate within a pH range of 6.5 to 10.5, within a temperature range of 90° to 190°F. and with an alumina concentration in the precipitation slurry of from 1 to 8%, b. washing the precipitate so as to remove contaminating cations and anions, c. drying the washed hydrogel, and recovering an alumina powder, d. adding a solution of water soluble phosphate containing compound, while mulling the alumina powder, e. extruding, drying and calcining the mulled material.
Claim 2
Dependent Claim 116 words
A process for preparing extruded alumina catalyst supports containing 1 to 10% phosphate which consists essentially of the steps of: a. precipitating the aluminum salt selected from the group consisting of aluminum sulfate, nitrate, and chloride with sodium or potassium aluminate within a pH range of 6.5 to 10.5, within a temperature range of 90° to 190°F. and with an alumina concentration in the precipitation slurry of from 1 to 8%, b. washing the precipitate so as to remove contaminating cations and anions, c. drying the washed hydrogel, and recovering an alumina powder, d. adding a solution of water soluble phosphate containing compound, while mulling the alumina powder, e. extruding, drying and calcining the mulled material.
Claim 3
Dependent Claim 18 words
The process according to claim 1 wherein the water soluble phosphate-containing compound is phosphoric acid or ammonium phosphate.
Claim 4
Dependent Claim 19 words
The process according to claim 1 wherein the dried extrusions are calcined for 2 to 3 hours at 1300°F.
Claim 5
Dependent Claim 137 words
A process for preparing catalysts for hydrotreating petroleum feedstocks which comprise the steps of: a. precipitating an aluminum salt selected from the group consisting of aluminum sulfate, aluminum nitrate, aluminum chloride with sodium or potassium aluminate within a pH range of 6.5 to 10.5, within a temperature range of 90° to 190°F., and with an alumina (Al 2 O 3 ) concentration in the precipitation slurrry of from 1 to 8%, b. washing the precipitate so as to remove contaminating cations and anions, c. drying the washed hydrogel, and recovering an alumina powder d. adding a solution of water soluble phosphate-containing compound while mulling the alumina powder, e. extruding, drying, and calcining the mulled material, f. impregnating the extrudates with solutions of salts of Group VIB and iron Group VIII metals, g. drying and calcining the catalyst.
Claim 6
Dependent Claim 137 words
A process for preparing catalysts for hydrotreating petroleum feedstocks which comprise the steps of: a. precipitating an aluminum salt selected from the group consisting of aluminum sulfate, aluminum nitrate, aluminum chloride with sodium or potassium aluminate within a pH range of 6.5 to 10.5, within a temperature range of 90° to 190°F., and with an alumina (Al 2 O 3 ) concentration in the precipitation slurrry of from 1 to 8%, b. washing the precipitate so as to remove contaminating cations and anions, c. drying the washed hydrogel, and recovering an alumina powder d. adding a solution of water soluble phosphate-containing compound while mulling the alumina powder, e. extruding, drying, and calcining the mulled material, f. impregnating the extrudates with solutions of salts of Group VIB and iron Group VIII metals, g. drying and calcining the catalyst.
Claim 7
Dependent Claim 18 words
The process according to claim 4 wherein the water soluble phosphate-containing compound is phosphoric acid or ammonium phosphate.
Claim 8
Dependent Claim 45 words
The process according to claim 4 wherein the iron Group VIII metal is present in a concentration of from 0.5 to 8 percent and the Group VIB metal is present in a concentration of from 5 to 25 percent by weight of the final catalyst.
Claim 9
Dependent Claim 25 words
The process according to claim 6 wherein the iron Group VIII metal is nickel or cobalt and the Group VIB metal is molybdenum or tungsten.

References Cited (Backward Citations)

US2441297A Cited
US3617528A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-07-13 1980-01-12 1980-07-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-07-13 1984-01-12 1984-07-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-07-13 1988-01-12 1988-07-13 $7700.00 Window Closed / Lapsed

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