US4636299A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the manufacture of lubricating oils
Assignee: BP Corp North America Inc
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Filing: 1984-12-24
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Granted: 1987-01-13
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Expires: 2004-12-24
Abstract
Abstract The present invention provides for a process for reducing the pour point of a hydrocarbon feedstock containing nitrogen- and sulfur-containing compounds. Specifically, the hydrocarbon feedstock is passed to an extraction zone wherein N-Methyl-2-pyrrolidone is used to extract a portion of the aromatic compounds. A portion of the extraction zone raffinate is then passed to a hydrotreating zone wherein a portion of the nitrogen and sulfur containing compounds are converted to hydrogen sulfide and ammonia. Subsequently, a portion of the hydrotreating zone effluent is then passed to a dewaxing zone and contacted with a shape selective molecular sieve containing dewaxing catalyst.
Inventors
- 👤 Eugene E. Unmuth
- 👤 John A. Mahoney
- 👤 Ralph J. Bertolacini
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 20:48
CPC Classifications
C; C10; C10G; C10G67/00; C10G67/02; C10G67/04; C10G67/0409; C10G2400/00; C10G2400/10
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
198 words
A process for reducing the pour point of a hydrocarbon feedstock containing nitrogen and sulfur-containing compounds which comprises: passing the hydrocarbon feedstock to a solvent extraction zone wherein N-methyl-2-pyrrolidone is used to extract a portion of the aromatic compounds contained in the hydrocarbon and thereby form an extraction zone raffinate; passing at least a portion of the extraction zone raffinate to a hydrotreating zone wherein hydrogen is contacted with the extraction zone raffinate in the presence of a hydrotreating catalyst at hydrotreating conditions wherein a substantial portion of the nitrogen and sulfur-containing compounds are converted to hydrogen sulfide and ammonia to form a hydrotreating zone effluent; passing at least a portion of the effluent from the hydrotreating zone to a stripping zone wherein hydrogen sulfide and ammonia are removed from the hydrotreating zone effluent to form a stripping zone effluent; and passing at least a portion of the stripping zone effluent to a dewaxing zone wherein hydrogen is contacted with the stripping zone effluent at catalytic dewaxing conditions in the presence of a catalyst composition comprising a shape selective molecular sieve component and a hydrogenation component selected from the group consisting of Group VIB and Group VIII metals.
Claim 2
Dependent Claim
198 words
A process for reducing the pour point of a hydrocarbon feedstock containing nitrogen and sulfur-containing compounds which comprises: passing the hydrocarbon feedstock to a solvent extraction zone wherein N-methyl-2-pyrrolidone is used to extract a portion of the aromatic compounds contained in the hydrocarbon and thereby form an extraction zone raffinate; passing at least a portion of the extraction zone raffinate to a hydrotreating zone wherein hydrogen is contacted with the extraction zone raffinate in the presence of a hydrotreating catalyst at hydrotreating conditions wherein a substantial portion of the nitrogen and sulfur-containing compounds are converted to hydrogen sulfide and ammonia to form a hydrotreating zone effluent; passing at least a portion of the effluent from the hydrotreating zone to a stripping zone wherein hydrogen sulfide and ammonia are removed from the hydrotreating zone effluent to form a stripping zone effluent; and passing at least a portion of the stripping zone effluent to a dewaxing zone wherein hydrogen is contacted with the stripping zone effluent at catalytic dewaxing conditions in the presence of a catalyst composition comprising a shape selective molecular sieve component and a hydrogenation component selected from the group consisting of Group VIB and Group VIII metals.
Claim 3
Dependent Claim
17 words
The process of claim 1 wherein the hydrogention component is a Group VIII noble metal comprising platinum.
Claim 4
Dependent Claim
17 words
The process of claim 1 wherein the hydrogenation component is a Group VIII noble metal comprising palladium.
Claim 5
Dependent Claim
25 words
The process of claim 1 wherein the shape selective molecular sieve component is dispersed within a non-molecular sieve containing porous refractory inorganic oxide matrix component.
Claim 6
Dependent Claim
23 words
The process of claim 4 wherein the hydrogenation component is deposited on the dispersion of shape selective molecular sieve component and matrix components.
Claim 7
Dependent Claim
23 words
The proces of claim 4 wherein the hydrogenation component is deposited on the matrix component of the shape selective molecular sieve component-matrix dispsersion.
Claim 8
Dependent Claim
11 words
The process of claim 4 wherein the matrix component comprises alumina.
Claim 9
Dependent Claim
16 words
The process of claim 1 wherein the molecular sieve comprises an AMS-1B crystalline borosilicate molecular sieve.
Claim 10
Dependent Claim
17 words
The process of claim 1 wherein the shape selective molecular sieve component comprises a ZSM crystalline alumino-silicate.
Claim 11
Dependent Claim
30 words
The process of claim 1 wherein the stripping zone effluent contains less than 10 ppmw nitrogen-containing compounds based on nitrogen and less than 20 ppmw sulfur-containing compounds based on sulfur.
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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) | 1990-01-12 | 1990-07-14 | 1991-01-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-01-12 | 1994-07-14 | 1995-01-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-01-12 | 1998-07-14 | 1999-01-13 | $7700.00 | Window Closed / Lapsed |