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US4357232A
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Method for enhancing catalytic activity
Assignee: Mobil Oil AS
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Filing: 1981-01-15
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Granted: 1982-11-02
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Expires: 2001-01-15
Abstract
Abstract Catalytically dewaxed lubricating base stock oils that have improved resistance to oxidation are produced by pretreating the waxy furfural raffinate with a zeolite sorbent prior to dewaxing with a zeolite catalyst such as ZSM-5, and conducting the dewaxing at a reduced temperature not to exceed about 675 DEG -700 DEG F.
Inventors
- 👤 Robert E. Holland
- 👤 Samuel A. Tabak
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 05:31
CPC Classifications
C; C10; C10G; C10G67/00; C10G67/02; C10G67/06; C10G2400/00; C10G2400/10
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
307 words
In a process for preparing a high quality lube base stock oil having a predetermined pour point in the range of about -25° to +30° F. from waxy crude oil, which process comprises: extracting a distillate fraction that boils within the range of 450° to 1100° F. or a deasphalted short residuum fraction of said waxy crude with a solvent selective for aromatic hydrocarbons to yield a raffinate from which undesirable compounds have been removed; contacting the raffinate and hydrogen gas with a dewaxing catalyst under dewaxing conditions effective to impart said predetermined pour point, said catalyst comprising a first crystalline zeolite having a dry crystal framework density of not less than about 1.6 grams per cubic centimeter and a constraint index of about 1 to about 12, thereby converting wax contained in the raffinate to lower boiling hydrocarbons; and, topping the dewaxed raffinate to remove therefrom components of a low molecular weight; the improvement, whereby the resistance to oxidation of said dewaxed raffinate is increased, which comprises: pretreating said raffinate, prior to dewaxing, with a sorbent comprising a second crystalline zeolite having an effective pore diameter equal to or larger than said first crystalline zeolite, said pretreating being conducted under a combination of conditions selected from a temperature of about 35° to about 350° F., a pressure of 0 to 3000 psig, and a contact time equivalent to a LHSV of 0.1 to 100 hr. -1 , said combination being effective to provide a pretreated raffinate characterized by an initial equilibrium temperature not exceeding about 675° to 700° F. and at least 25° F. lower than that obtained with said raffinate without pretreatment when dewaxed at about 1 LHSV; and dewaxing said raffinate at a temperature not to exceed the lesser of said equilibrium temperature of said raffinate without pretreatment minus 25° F., or 700° F.
Claim 2
Dependent Claim
307 words
In a process for preparing a high quality lube base stock oil having a predetermined pour point in the range of about -25° to +30° F. from waxy crude oil, which process comprises: extracting a distillate fraction that boils within the range of 450° to 1100° F. or a deasphalted short residuum fraction of said waxy crude with a solvent selective for aromatic hydrocarbons to yield a raffinate from which undesirable compounds have been removed; contacting the raffinate and hydrogen gas with a dewaxing catalyst under dewaxing conditions effective to impart said predetermined pour point, said catalyst comprising a first crystalline zeolite having a dry crystal framework density of not less than about 1.6 grams per cubic centimeter and a constraint index of about 1 to about 12, thereby converting wax contained in the raffinate to lower boiling hydrocarbons; and, topping the dewaxed raffinate to remove therefrom components of a low molecular weight; the improvement, whereby the resistance to oxidation of said dewaxed raffinate is increased, which comprises: pretreating said raffinate, prior to dewaxing, with a sorbent comprising a second crystalline zeolite having an effective pore diameter equal to or larger than said first crystalline zeolite, said pretreating being conducted under a combination of conditions selected from a temperature of about 35° to about 350° F., a pressure of 0 to 3000 psig, and a contact time equivalent to a LHSV of 0.1 to 100 hr. -1 , said combination being effective to provide a pretreated raffinate characterized by an initial equilibrium temperature not exceeding about 675° to 700° F. and at least 25° F. lower than that obtained with said raffinate without pretreatment when dewaxed at about 1 LHSV; and dewaxing said raffinate at a temperature not to exceed the lesser of said equilibrium temperature of said raffinate without pretreatment minus 25° F., or 700° F.
Claim 3
Dependent Claim
30 words
The process described in claim 1 wherein said first crystalline zeolite is selected from the group consisting of ZSM-5, ZSM-11, intergrowths of ZSM-5 and ZSM-11, ZSM-12, ZSM-23, ZSM-38 and ZSM-48.
Claim 4
Dependent Claim
35 words
The process described in claim 1 wherein said first and said second crystalline zeolite are each individually selected from the group consisting of ZSM-5, ZSM-11, intergrowths of ZSM-5 and ZSM-11, ZSM-12, ZSM-23, ZSM-38 and ZSM-48.
Claim 5
Dependent Claim
19 words
The process described in claim 3 wherein said first and said second crystalline zeolite have the same crystal structure.
Claim 6
Dependent Claim
23 words
The process described in claim 3 wherein said first and said second zeolite have the same crystal structure and the same chemical compositions.
Claim 7
Dependent Claim
28 words
The process described in claim 2 or 3 or 4 or 5 wherein said crystalline zeolites are selected from the group consisting of ZSM-5, ZSM-11 and intergrowths thereof.
Claim 8
Dependent Claim
14 words
The process described in claim 2 wherein said second crystalline zeolite is hydrogen mordenite.
Claim 9
Dependent Claim
23 words
The process described in claim 7 wherein said first crystalline zeolite is selected from the group consisting of ZSM-5, ZSM-11 and intergrowths thereof.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1985-11-01 | 1986-05-03 | 1986-11-02 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-11-01 | 1990-05-03 | 1990-11-02 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-11-01 | 1994-05-03 | 1994-11-02 | $7700.00 | Window Closed / Lapsed |