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US3923646A Expired / Lapsed US ⏱️ 0.0 years remaining

Hydrodesulfurization with a catalyst formed from an alumina sol containing alpha-alumina monohydrate

Assignee: Universal Oil Products Co
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Filing: 1974-12-13
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Granted: 1975-12-02
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Expires: 1994-12-13
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Abstract

Abstract Sulfur-containing petroleum hydrocarbon fractions are treated at hydrodesulfurization reaction conditions in contact with a catalytic composite comprising a Group VIII metal or metal oxide, a Group VIB metal or metal oxide, and an alumina support or carrier material. The alumina support is characterized by a method of preparation which results in improved hydrodesulfurization activity of the catalytic composite.

Inventors

  • 👤 Lee Hilfman

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 10:51
CPC Classifications
B; B01; B01J; B01J21/00; B01J21/02; B01J21/04; B01J23/00; B01J23/70; B01J23/76; B01J23/84; B01J23/85; C; C10; C10G; C10G45/00; C10G45/02; C10G45/04; C10G45/06; C10G45/08; B01J35/00; B01J35/50; B01J35/51

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 211 words
A PROCESS FOR DESULFURIZING A SULFUR-CONTAINING PETROLEUM HYDROCARBON FRACTION WHICH COMPRISES PASSING SAID PETROLEUM HYDROCARBON FRACTION AND HYDROGEN IN CONTACT WITH A CATALYTIC COMPOSITE AT HYDRODESULFURIZATION REACTION CONDITIONS, SAID CATALYTIC COMPOSITE COMPRISING FROM ABOUT 5 TO ABOUT 20 WT. % GROUP VIB METAL OR METAL OXIDE AND FROM ABOUT 0.1 TO ABOUT 10 WT. % GROUP VIII METAL OR METAL OXIDE ON AN ALUMINA CARRIER MATERIAL, SAID CARRIER MATERIAL HAVING BEN PREPARED BY: A. ADMIXING AND SUSPENDING AN ALPHA-ALUMINA MONOHYDRATE IN A CHLORIDE ANION-CONTAINING ALUMINA SOL HAVING AN ALUMINUM CHLORIDE ANION RATIO OF FROM ABOUT 1:1 TO ABOUT 1.5:1, SAID ALPHA-ALUMINA MONOHYDRATE BEING ADMIXED IN SAID SOL IN AN AMOUNT TO PRIDE, ON GELATION OF SAID SOL, FROM ABOUT 25 TO ABOUT 50 WT. % OF SAID ALUMINA CARRIER MATERIAL; B. COMMINGLING THE RESULTING SUSPENSION WITH AN AMMONIA PRECURSOR AT BELOW GELATION TEMPERATURE, SAID PRECUSOR BEING DECOMPOSABLE TO AMMONIA WITH INCREASING TEMPERATURE; C. DISPERSING THE SUSPENSION OF STEP (B) AS DROPLETS IN A HOT OIL BATH EFFECTING DECOMPOSITION OF SAID PRECURSOR AND THE FORMATION OF HYDROGEL SPHERES THEREIN; D. AGING SAID SPHERES AT AN ELEVATED TEMPERATUE EFFECTING DECOMPOSITION OF THE RESDIUAL AMMONIA PRECUSOR CONTAINED THEREIN, AND E. WASHING, DRYING AND CALCINING THE AGED ALUMINA SPHERES TO FORM SAID ALUMINA CARRIER MATERIAL.
Claim 2
Dependent Claim 211 words
A PROCESS FOR DESULFURIZING A SULFUR-CONTAINING PETROLEUM HYDROCARBON FRACTION WHICH COMPRISES PASSING SAID PETROLEUM HYDROCARBON FRACTION AND HYDROGEN IN CONTACT WITH A CATALYTIC COMPOSITE AT HYDRODESULFURIZATION REACTION CONDITIONS, SAID CATALYTIC COMPOSITE COMPRISING FROM ABOUT 5 TO ABOUT 20 WT. % GROUP VIB METAL OR METAL OXIDE AND FROM ABOUT 0.1 TO ABOUT 10 WT. % GROUP VIII METAL OR METAL OXIDE ON AN ALUMINA CARRIER MATERIAL, SAID CARRIER MATERIAL HAVING BEN PREPARED BY: A. ADMIXING AND SUSPENDING AN ALPHA-ALUMINA MONOHYDRATE IN A CHLORIDE ANION-CONTAINING ALUMINA SOL HAVING AN ALUMINUM CHLORIDE ANION RATIO OF FROM ABOUT 1:1 TO ABOUT 1.5:1, SAID ALPHA-ALUMINA MONOHYDRATE BEING ADMIXED IN SAID SOL IN AN AMOUNT TO PRIDE, ON GELATION OF SAID SOL, FROM ABOUT 25 TO ABOUT 50 WT. % OF SAID ALUMINA CARRIER MATERIAL; B. COMMINGLING THE RESULTING SUSPENSION WITH AN AMMONIA PRECURSOR AT BELOW GELATION TEMPERATURE, SAID PRECUSOR BEING DECOMPOSABLE TO AMMONIA WITH INCREASING TEMPERATURE; C. DISPERSING THE SUSPENSION OF STEP (B) AS DROPLETS IN A HOT OIL BATH EFFECTING DECOMPOSITION OF SAID PRECURSOR AND THE FORMATION OF HYDROGEL SPHERES THEREIN; D. AGING SAID SPHERES AT AN ELEVATED TEMPERATUE EFFECTING DECOMPOSITION OF THE RESDIUAL AMMONIA PRECUSOR CONTAINED THEREIN, AND E. WASHING, DRYING AND CALCINING THE AGED ALUMINA SPHERES TO FORM SAID ALUMINA CARRIER MATERIAL.
Claim 3
Dependent Claim 22 words
The process of claim 1 further characterized in that said Group VIB metal or metal oxide is tungsten or an oxide thereof.
Claim 4
Dependent Claim 22 words
The process of claim 1 further characterized in that said Group VIB metal or metal oxide is molybdenum or an oxide thereof.
Claim 5
Dependent Claim 22 words
The process of claim 1 further characterized in that said Group VIII metal or metal oxide is nickel or an oxide thereof.
Claim 6
Dependent Claim 22 words
The process of claim 1 further characterized in that said Group VIII metal or metal oxide is cobalt or an oxide thereof.
Claim 7
Dependent Claim 20 words
The process of claim 1 further characterized in that said alpha-alumina monohydrate is prepared by the hydrolysis of aluminum alcoholate.
Claim 8
Dependent Claim 14 words
The process of claim 1 further characterized in that said ammonia precursor is hexamethylenetetramine.
Claim 9
Dependent Claim 33 words
The process of claim 1 further characterized in that said ammonia precursor is hexamethylenetetramine and utilized in an amount to effect substantially complete neutralization of said chloride anion contained in said hydrosol mixture.
Claim 10
Dependent Claim 29 words
The process of claim 1 further characterized in that said ammonia precursor is hexamethylenetetramine and utilized from about a 1:4 to about 1.25:1 mole ratio with said acid anion.
Claim 11
Dependent Claim 24 words
The process of claim 1 further characterized in that said oil bath is maintained at a temperature of from about 50* to about 105*C.
Claim 12
Dependent Claim 39 words
The process of claim 1 further characterized in that said hydrogel spheres are aged at a temperature of from about 60* to about 260*C. and at a pressure to maintain the water content thereof in a substantially liquid phase.
Claim 13
Dependent Claim 36 words
The process of claim 1 further characterized in that said hydrogel spheres are aged at a temperature of from about 60* to about 175*C. and at a pressure of from about 40 to about 150 psig.
Claim 14
Dependent Claim 29 words
The process of claim 1 further characterized in that said aged alumina spheres are calcined at a temperature of from about 325* to about 750*C. in an oxidizing atmosphere.

References Cited (Backward Citations)

US3846286A Cited
US3726790A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-12-01 1979-06-02 1979-12-02 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-12-01 1983-06-02 1983-12-02 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-12-01 1987-06-02 1987-12-02 $7700.00 Window Closed / Lapsed

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