Patent US4456700A successfully refreshed from Google Patents.
← Back to Patent Explorer
US4456700A Expired / Lapsed US ⏱️ 0.0 years remaining

Catalyst for residua demetalation and desulfurization

Assignee: Mobil Oil AS
•
Filing: 1982-11-12
•
Granted: 1984-06-26
•
Expires: 2002-11-12
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A demetalation and desulfurization catalyst for metal and sulfur containing petroleum oils, e.g., residua containing hydrocarbon components, comprising a hydrogenating component composited on a refractory base, e.g., alumina, having a substantially higher pore volume and more pore volume distributed within the 0-100 ANGSTROM diameter range than such previously known catalysts and method of using same; said catalyst possesses superior aging characteristics.

Inventors

  • 👤 Stephen M. Oleck
  • 👤 Howard S. Sherry

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 22:27
CPC Classifications
B; B01; B01J; B01J35/00; B01J35/60; B01J35/66; B01J23/00; B01J23/70; B01J23/76; B01J23/84; B01J23/85; B01J23/88; B01J23/882; B01J23/883; B01J35/61; B01J35/615; B01J35/63; B01J35/635; B01J35/64; B01J35/647; C; C10; C10G; C10G2300/00; C10G2300/10; C10G2300/107

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 120 words
A hydrometalation-desulfurization catalyst comprising a hydrogenating component which comprises a Group VI-B metal oxide or sulfide and a Group VIII metal oxide or sulfide composited with a porous alumina base, said catalyst having at least about 25% of the volume of the pores with a diameter within the range of about 0 to 30 Å, at least about 50% of the volume of the pores with a diameter within the range of about 0 to 100 Å and further having a pore volume of from about 0.80 to about 0.95 cc/gram and an average pore diameter of about 145 Å to about 170 Å and a surface area of about 180 m 2 /gram to about 220 m 2 /gram.
Claim 2
Dependent Claim 120 words
A hydrometalation-desulfurization catalyst comprising a hydrogenating component which comprises a Group VI-B metal oxide or sulfide and a Group VIII metal oxide or sulfide composited with a porous alumina base, said catalyst having at least about 25% of the volume of the pores with a diameter within the range of about 0 to 30 Å, at least about 50% of the volume of the pores with a diameter within the range of about 0 to 100 Å and further having a pore volume of from about 0.80 to about 0.95 cc/gram and an average pore diameter of about 145 Å to about 170 Å and a surface area of about 180 m 2 /gram to about 220 m 2 /gram.
Claim 3
Dependent Claim 33 words
The catalyst as claimed in claim 1 wherein said hydrogenating component consists essentially of about 2 to about 10 weight percent cobalt oxide and about 5 to about 20 weight percent molybdenum oxide.
Claim 4
Dependent Claim 18 words
The catalyst as claimed in claim 1 wherein the hydrogenating component consists of sulfides of cobalt and molybdenum.
Claim 5
Dependent Claim 33 words
The catalyst as claimed in claim 1 wherein said hydrogenating component consists essentially of about 2 to about 10 weight percent nickel oxide and about 5 to about 20 weight percent molybdenum oxide.
Claim 6
Dependent Claim 18 words
The catalyst as claimed in claim 1 wherein the hydrogenating component consists of sulfides of nickel and molybdenum.
Claim 7
Dependent Claim 79 words
The catalyst of claim 1 wherein the pore volume distribution is further defined as follows: at least 70% of the volume of the pores with a diameter within the range of about 0 to about 150 Å, at least 90% of the volume of the pores with a diameter within the range of about 0 to about 200 Å and no more than about 10% of the volume of the pores with a diameter greater than about 200 Å
Claim 8
Dependent Claim 16 words
The catalyst as claimed in claim 1 wherein said alumina consists essentially of gamma phase alumina.
Claim 9
Dependent Claim 47 words
The catalyst as claimed in claim 2 wherein said catalyst is produced by impregnating gamma phase alumina pellets with appropriate amounts of a suitable molybdenum compound and a cobalt compound and then calcining the dried pellets at about 1000° F. for about 3 to about 10 hours.

References Cited (Backward Citations)

US3770618A Cited
US3900427A Cited
US3830728A Cited
US4066574A Cited
US4009125A Cited
US4035261A Cited
US4089774A Cited
US4013547A Cited
US4051021A Cited
US4278566A Cited
US4328127A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1987-06-26 1987-12-26 1988-06-26 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1991-06-26 1991-12-26 1992-06-26 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1995-06-26 1995-12-26 1996-06-26 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag