US4137148A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Manufacture of specialty oils
Assignee: Mobil Oil AS
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Filing: 1977-07-20
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Granted: 1979-01-30
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Expires: 1997-07-20
Abstract
Abstract Specialty oils of very low pour point and excellent stability, such as transformer oils and refrigerator oils, are produced from waxy crude distillates by solvent refining, catalytic dewaxing over a zeolite catalyst in the nature of zeolite ZSM-5 and hydrotreating.
Inventors
- 👤 Bernard M. Gillespie
- 👤 Michael S. Sarli
- 👤 Kenneth W. Smith
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 02:34
CPC Classifications
C; C10; C10G; C10G45/00; C10G45/58; C10G45/60; C10G45/64; C10G2400/00; C10G2400/12
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
191 words
A process for preparing high quality specialty oil from waxy crude oil which comprises separating from said waxy crude a distillate fraction thereof having an initial boiling point of at least about 450° F. and a final boiling point less than about 1050° F., extracting said distillate fraction with a solvent selective for aromatic hydrocarbons to yield a raffinate from which undesirable compounds have been removed, catalytically dewaxing the raffinate in the presence of hydrogen to a pour point not higher than about -30° F. by contacting said raffinate at a temperature of 500° to 675° F. with a dewaxing catalyst comprising an aluminosilicate zeolite having a silica/alumina ratio above 12 and a constraint index between 1 and 12 thereby forming dewaxed raffinate and lower boiling hydrocarbons, hydrotreating the dewaxed raffinate by contact at a temperature of 425° to 600° F. with a hydrotreating catalyst comprising a hydrogenation component on a non-acidic support, and topping the raffinate subsequent to dewaxing to remove therefrom said lower boiling hydrocarbons, whereby directly recovering substantially all of the remainder of said dewaxed raffinate, said remainder having a pour point not higher than about -30° F.
Claim 2
Dependent Claim
191 words
A process for preparing high quality specialty oil from waxy crude oil which comprises separating from said waxy crude a distillate fraction thereof having an initial boiling point of at least about 450° F. and a final boiling point less than about 1050° F., extracting said distillate fraction with a solvent selective for aromatic hydrocarbons to yield a raffinate from which undesirable compounds have been removed, catalytically dewaxing the raffinate in the presence of hydrogen to a pour point not higher than about -30° F. by contacting said raffinate at a temperature of 500° to 675° F. with a dewaxing catalyst comprising an aluminosilicate zeolite having a silica/alumina ratio above 12 and a constraint index between 1 and 12 thereby forming dewaxed raffinate and lower boiling hydrocarbons, hydrotreating the dewaxed raffinate by contact at a temperature of 425° to 600° F. with a hydrotreating catalyst comprising a hydrogenation component on a non-acidic support, and topping the raffinate subsequent to dewaxing to remove therefrom said lower boiling hydrocarbons, whereby directly recovering substantially all of the remainder of said dewaxed raffinate, said remainder having a pour point not higher than about -30° F.
Claim 3
Dependent Claim
20 words
A process according to claim 1 wherein said dewaxing catalyst comprising an aluminosilicate zeolite comprises ZSM-5 and a hydrogenation metal.
Claim 4
Dependent Claim
20 words
A process according to claim 1 wherein the effluent of said catalytic dewaxing step is cascaded to the hydrotreating step.
Claim 5
Dependent Claim
20 words
A process according to claim 2 wherein the effluent of said catalytic dewaxing step is cascaded to the hydrotreating step.
Claim 6
Dependent Claim
22 words
A process according to claim 1 wherein said topping of dewaxed raffinate is conducted between the catalytic dewaxing and the hydrotreating step.
Claim 7
Dependent Claim
22 words
A process according to claim 2 wherein said topping of dewaxed raffinate is conducted between the catalytic dewaxing and the hydrotreating step.
Claim 8
Dependent Claim
20 words
A process according to claim 1 wherein said raffinate is partially dewaxed by solvent dewaxing before said catalytic dewaxing step.
Claim 9
Dependent Claim
20 words
A process according to claim 2 wherein said raffinate is partially dewaxed by solvent dewaxing before said catalytic dewaxing step.
Claim 10
Dependent Claim
34 words
A process according to claim 2 wherein said raffinate is partially dewaxed by solvent dewaxing before the catalytic dewaxing step, and the effluent of said catalytic dewaxing step is cascaded to the hydrotreating step.
Claim 11
Dependent Claim
23 words
The process described in claim 9 wherein said topping of dewaxed raffinate is conducted between the catalytic dewaxing step and the hydrotreating step.
Claim 12
Dependent Claim
43 words
A process according to claim 2 wherein said raffinate is catalytically dewaxed to a pour point not higher than about -40° F., and wherein said remainder of said directly recovered dewaxed raffinate has a pour point of not higher than about -40° F.
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) | 1982-01-29 | 1982-07-31 | 1983-01-30 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-01-29 | 1986-07-31 | 1987-01-30 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-01-29 | 1990-07-31 | 1991-01-30 | $7700.00 | Window Closed / Lapsed |