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US3905916A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for preparing a hydrotreating catalyst

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1973-04-26
•
Granted: 1975-09-16
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Expires: 1993-04-26
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Abstract

Abstract An improved hydrotreating catalyst is prepared by precipitating the oxides or hydrated oxides of aluminum and silicon from an aqueous solution of water-soluble salts (a mixture of aqueous alkaline aluminate and aqueous alkali metal silicate) at 105*120* F at a pH of 5-9.5 and at an alumina concentration, expressed as Al2O3 of 1.2-5.0 wt. percent. The precipitate is washed, impregnated with Group VI-B and Group VIII metals and the impregnated catalyst is dried. An extrudable slurry is formed and extruded; the extrudate is then dried and calcined. The hydrotreating catalyst contains an oxide of a Group VIB metal and an oxide of a Group VIII metal on an alumina support containing 1-20 wt. percent silica. The conventional spray drying step is omitted in the preparation of the present catalyst.

Inventors

  • 👤 Kenneth L Riley
  • 👤 William T House
  • 👤 John E Hofmann

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 01:14
CPC Classifications
C; C10; C10G; C10G45/00; C10G45/02; C10G45/04; C10G45/06; C10G45/08; B; B01; B01J; B01J23/00; B01J23/70; B01J23/76; B01J23/84; B01J23/85; B01J35/00; B01J35/60; B01J35/61; B01J35/615; B01J35/63; B01J35/635; B01J35/64; B01J35/647; C10G2300/00; C10G2300/10; C10G2300/107; Y; Y10; Y10S; Y10S502/00; Y10S502/506; Y10S502/512

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 204 words
PROCESS FOR PREPARING AN IMPROVED HYDROTREATING CATALYST COMPRISING: A. PRECIPITATING THE OXIDES OR HYDRATED OXIDES OF ALUMINUM AND SILICON FROM AN AQUEOUS SOLUTION OF WATER SOLUBLE SALTS THEREOF AT A TEMPERATURE RANGING FROM ABOUT 105* TO 120*F, AT A RANGE OF PH BETWEEN ABOUT 5 AND 9.5 AND AT AN ALUMINA CONCENTRATION, EXPRESSED AS AL2O3, BETWEEN ABOUT 1.2 TO 5.0 WEIGHT PERCENT, B. WASHING THE PRECIPITATE FROM STEP (A) TO REMOVE IMPURITIES THEREFROM, C. IMPREGNATING THE WASHED PRECIPITATE WITH GROUP VIII AND GROUP VI B METALS, D. DRYING THE IMPREGNATED CATALYST FROM STEP (C), E. ADDING SUFFICIENT WATER TO SAID DRIED IMPREGNATED CATALYST TO PROVIDE AN EXTRUDABLE SLURRY, F. EXTRUDING SAID SLURRY TO FORM AN EXTRUDATE, AND, G. DRYING AND CALCINING SAID EXTRUDATE WHEREBY AN IMPROVED HYDROTREATING CATALYST IS OBTAINED COMPRISING AN OXIDE OF A GROUP VIII METAL AND AN OXIDE OF A GROUP VI B METAL DEPOSITED UPON A SUPPORT MATERIAL CONSISTING ESSENTIALLY OF 1 TO 20 WEIGHT PERCENT SILICA AND THE BALANCE ALUMINA, SAID CATALYST BEING CHARACTERIZED BY EXHIBITING A SURFACE AREA OF AT LEAST ABOUT 190 M2/GM MEASURED IN MICROPORES HAVING A DIAMETER OF 30-80A AND PORE VOLUME LESS THAN ABOUT 0.10ML/GM. AS MACROPORES HAVING DIAMETERS GREATER THAN ABOUT 100 A.
Claim 2
Dependent Claim 204 words
PROCESS FOR PREPARING AN IMPROVED HYDROTREATING CATALYST COMPRISING: A. PRECIPITATING THE OXIDES OR HYDRATED OXIDES OF ALUMINUM AND SILICON FROM AN AQUEOUS SOLUTION OF WATER SOLUBLE SALTS THEREOF AT A TEMPERATURE RANGING FROM ABOUT 105* TO 120*F, AT A RANGE OF PH BETWEEN ABOUT 5 AND 9.5 AND AT AN ALUMINA CONCENTRATION, EXPRESSED AS AL2O3, BETWEEN ABOUT 1.2 TO 5.0 WEIGHT PERCENT, B. WASHING THE PRECIPITATE FROM STEP (A) TO REMOVE IMPURITIES THEREFROM, C. IMPREGNATING THE WASHED PRECIPITATE WITH GROUP VIII AND GROUP VI B METALS, D. DRYING THE IMPREGNATED CATALYST FROM STEP (C), E. ADDING SUFFICIENT WATER TO SAID DRIED IMPREGNATED CATALYST TO PROVIDE AN EXTRUDABLE SLURRY, F. EXTRUDING SAID SLURRY TO FORM AN EXTRUDATE, AND, G. DRYING AND CALCINING SAID EXTRUDATE WHEREBY AN IMPROVED HYDROTREATING CATALYST IS OBTAINED COMPRISING AN OXIDE OF A GROUP VIII METAL AND AN OXIDE OF A GROUP VI B METAL DEPOSITED UPON A SUPPORT MATERIAL CONSISTING ESSENTIALLY OF 1 TO 20 WEIGHT PERCENT SILICA AND THE BALANCE ALUMINA, SAID CATALYST BEING CHARACTERIZED BY EXHIBITING A SURFACE AREA OF AT LEAST ABOUT 190 M2/GM MEASURED IN MICROPORES HAVING A DIAMETER OF 30-80A AND PORE VOLUME LESS THAN ABOUT 0.10ML/GM. AS MACROPORES HAVING DIAMETERS GREATER THAN ABOUT 100 A.
Claim 3
Dependent Claim 54 words
Process as defined in claim 1 wherein said solution of water soluble salts comprises a mixture of an aqueous alkaline aluminate solution and an aqueous alkali metal silicate solution, and said oxides or hydrated oxides are precipitated upon addition to said solution of a mineral acid or an aluminum salt of a mineral acid.
Claim 4
Dependent Claim 17 words
Process as defined in claim 2 wherein precipitation is effected at temperatures ranging from 105* to 120*F.
Claim 5
Dependent Claim 18 words
Process as defined in claim 2 wherein the precipitation is effected at a pH between 5 and 9.5.
Claim 6
Dependent Claim 27 words
Process as defined in claim 2 wherein the alumina concentration, expressed as Al2O3, of said aqueous alkaline aluminate solution is between 1.2 and 1.7 percent by weight.
Claim 7
Dependent Claim 27 words
Process as defined in claim 1 wherein the precipitation is effected in the presence of a compound selected from the group consisting of aldonic acids and aldonates.
Claim 8
Dependent Claim 28 words
Process as defined in claim 6 wherein gluconic acid is employed in amounts ranging from about 0.5 to about 6.0 wt. percent, based on the total Al2O3 content.
Claim 9
Dependent Claim 11 words
Process as defined in claim 6 wherein sodium gluconate is employed.
Claim 10
Dependent Claim 22 words
Process as defined in claim 2 wherein the precipitation is effected over a period of time ranging from 1/4 to 6 hours.
Claim 11
Dependent Claim 23 words
Process as defined in claim 2 wherein upon completion of said precipitation, the precipitate is, washed, impregnated with metals and then flash dried.
Claim 12
Dependent Claim 15 words
Process as defined in claim 1 wherein the Group VIII metal is cobalt or nickel.
Claim 13
Dependent Claim 16 words
Process as defined in claim 1 wherein the Group VI B metal is molybdenum or tungsten.

References Cited (Backward Citations)

US3509044A Cited
US3770618A Cited
US3531398A Cited
US3686095A Cited
US3668116A Cited
US3692698A Cited
US3770617A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-09-15 1979-03-17 1979-09-16 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-09-15 1983-03-17 1983-09-16 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-09-15 1987-03-17 1987-09-16 $7700.00 Window Closed / Lapsed

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