US4458024A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for hydrotreating petroleum residua and catalyst therefor
Assignee: Mobil Oil AS
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Filing: 1982-02-08
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Granted: 1984-07-03
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Expires: 2002-02-08
Abstract
Abstract A single stage catalyst system and process for using same in a single stage operation for hydrodewaxing and hydrotreating petroleum residua is disclosed. The catalyst comprises a ZSM-5 type zeolite in an alumina binder having specified metals content and pore volume characteristics.
Inventors
- 👤 Stephen M. Oleck
- 👤 Robert C. Wilson, Jr.
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 23:53
CPC Classifications
C; C10; C10G; C10G45/00; C10G45/58; C10G45/60; C10G45/64; B; B01; B01J; B01J29/00; B01J29/04; B01J29/06; B01J29/40; B01J29/48; B01J2229/00; B01J2229/10; B01J2229/26; B01J2229/30; B01J2229/42
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
97 words
A catalyst composition consisting essentially of 10-30 wt. % of a ZSM-5 type zeolite, 90-70 wt. % of alumina, based on alumina plus zeolite, and 10-25 wt. %, based on total catalyst and expressed as oxides, of at least one Group VIII metal selected from the group consisting of nickel, cobalt and iron, and at least one Group VIB metal, said catalyst having about 80% of its pore volume in pores no greater than 100 Angstrom units in diameter and at least 90% of its pore volume in pores no greater than 150 Angstrom units in diameter.
Claim 2
Dependent Claim
97 words
A catalyst composition consisting essentially of 10-30 wt. % of a ZSM-5 type zeolite, 90-70 wt. % of alumina, based on alumina plus zeolite, and 10-25 wt. %, based on total catalyst and expressed as oxides, of at least one Group VIII metal selected from the group consisting of nickel, cobalt and iron, and at least one Group VIB metal, said catalyst having about 80% of its pore volume in pores no greater than 100 Angstrom units in diameter and at least 90% of its pore volume in pores no greater than 150 Angstrom units in diameter.
Claim 3
Dependent Claim
19 words
The catalyst composition of claim 1 wherein said zeolite is present in an amount of from 15-25 wt. %.
Claim 4
Dependent Claim
34 words
The catalyst of claim 1 wherein the zeolite component of said catalyst is selected from the group consisting essentially of ZSM-5, ZSM-11, ZSM-12, ZSM-35, and ZSM-38 and wherein said zeolites may be base exchanged.
Claim 5
Dependent Claim
13 words
The catalyst of claim 3 wherein the zeolitic component is ZSM-5 or HZSM-5.
Claim 6
Dependent Claim
35 words
The catalyst of claim 1 wherein said ZSM-5 type zeolite is present in an amount of about 15 wt. % and said catalyst contains about 15.5 wt. %, expressed as oxides, of molybdenum and nickel.
Claim 7
Dependent Claim
35 words
The catalyst of claim 1 wherein said ZSM-5 type zeolite is present in an amount of about 20 wt. % and said catalyst contains about 22 wt. %, expressed as oxides, of molybdenum and nickel.
Claim 8
Dependent Claim
12 words
The catalyst of claim 5 wherein said ZSM-5 type zeolite is ZSM-5.
Claim 9
Dependent Claim
12 words
The catalyst of claim 6 wherein said ZSM-5 type zeolite is ZSM-5.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-07-03 | 1988-01-02 | 1988-07-03 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-07-03 | 1992-01-02 | 1992-07-03 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-07-03 | 1996-01-02 | 1996-07-03 | $7700.00 | Window Closed / Lapsed |