US4992605A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Production of hydrocarbons with a relatively high cetane rating
Assignee: Ministry of Natural Resources and Wildlife
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Filing: 1989-01-27
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Granted: 1991-02-12
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Expires: 2009-01-27
Abstract
Abstract There is described a process for producing hydrocarbon products in the diesel boiling range, comprising mainly C15-C18 paraffins and being highly effective as diesel fuel ignition improvers. The process comprises hydroprocessing vegetable oils such as canola, sunflower, soybean and rapeseed oils or some fatty acids in hydroprocessing temperatures (350 DEG -450 DEG C.), pressures (4.8-15.2 MPa) and liquid hourly space velocity (LHSV) of 0.5-5.0 hr-1 depending on the type and purity of the feedstock. Commercially available hydroprocessing catalysts may be used.
Inventors
- 👤 Wayne K. Craig
- 👤 Douglas W. Soveran
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-06 12:24
CPC Classifications
C; C11; C11C; C11C3/00; C11C3/12; C11C3/123; C10; C10L; C10L1/00; C10L1/04; C11C3/126; C10G; C10G2300/00; C10G2300/10; C10G2300/1011; C10G2400/00; C10G2400/04; F; F02; F02B; F02B3/00; F02B3/06; Y; Y02; Y02E; Y02E50/00; Y02E50/10; Y02P; Y02P30/00; Y02P30/20
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
135 words
A process for producing liquid paraffinic hydrocarbons in the C 15 -C 18 range, effective as diesel fuel cetane rating improvers, comprising: (a) hydroprocessing a feedstock selected from a group consisting of canola oil, sunflower oil, soybean oil, rapeseed oil, palm oil and fatty acid fraction of tall oil by contacting the feedstock with gaseous hydrogen under conditions of temperature and pressure including selected temperatures from about 350° C. to about 450° C. in the presence of a hydroprocessing catalyst, the conditions effective to cause hydrogenation, hydrotreating and hydrocracking of the feedstock to convert the feedstock a mixture of compounds including mainly a diesel fuel boiling range fraction consisting predominately of C 15 -C 18 straight-chain paraffins, (b) separating the mixture of compounds; and (c) removing from the mixture the diesel fuel boiling range fraction.
Claim 2
Dependent Claim
135 words
A process for producing liquid paraffinic hydrocarbons in the C 15 -C 18 range, effective as diesel fuel cetane rating improvers, comprising: (a) hydroprocessing a feedstock selected from a group consisting of canola oil, sunflower oil, soybean oil, rapeseed oil, palm oil and fatty acid fraction of tall oil by contacting the feedstock with gaseous hydrogen under conditions of temperature and pressure including selected temperatures from about 350° C. to about 450° C. in the presence of a hydroprocessing catalyst, the conditions effective to cause hydrogenation, hydrotreating and hydrocracking of the feedstock to convert the feedstock a mixture of compounds including mainly a diesel fuel boiling range fraction consisting predominately of C 15 -C 18 straight-chain paraffins, (b) separating the mixture of compounds; and (c) removing from the mixture the diesel fuel boiling range fraction.
Claim 3
Dependent Claim
47 words
The process of claim 1 wherein the conditions include a temperature in the range from about 350° C. to about 450°, a hydrogen partial pressure in the range from about 4.8 MPa to about 15.2 MPa and a liquid hourly space velocity of 0.5-5.0 hr -1 .
Claim 4
Dependent Claim
35 words
The process of claim 2 wherein the feedstock consists of the fatty acid fraction of tall oil and the temperature is in the range 380°-450° C., and the pressure is in the range 4.8-13.8 MPa.
Claim 5
Dependent Claim
29 words
The process of claim 3 wherein the feedstock consists of canola oil, the temperature is in the range 350°-450° C. and the pressure is in the range 4.8-13.8 MPa.
Claim 6
Dependent Claim
29 words
The process of claim 2 wherein the feedstock consists of sunflower oil, the temperature is in the range 350°-450° C. and the pressure is in the range 4.8-13.8 MPa.
Claim 7
Dependent Claim
29 words
The process of claim 2 wherein the feedstock consists of soybean oil, the temperature is in the range 350°-450° C. and the pressure is in the range 4.8-13.8 MPa.
Claim 8
Dependent Claim
29 words
The process of claim 2 wherein the feedstock consists of rapeseed oil, the temperature is in the range 380°-450° C. and the pressure is in the range 8.2-15.2 MPa.
Claim 9
Dependent Claim
29 words
The process of claim 2 wherein the feedstock consists of palm oil, the temperature is in the range 360°-450° C. and the pressure is in the range 4.8-13.8 MPa.
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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) | 1994-02-11 | 1994-08-13 | 1995-02-12 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1998-02-11 | 1998-08-13 | 1999-02-12 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2002-02-11 | 2002-08-13 | 2003-02-12 | $7700.00 | Window Closed / Lapsed |