← Back to Patent Explorer
US4636299A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the manufacture of lubricating oils

Assignee: BP Corp North America Inc
•
Filing: 1984-12-24
•
Granted: 1987-01-13
•
Expires: 2004-12-24
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

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.

References Cited (Backward Citations)

US3175970A Cited
US3682813A Cited
US3652448A Cited
US3755138A Cited
US3617475A Cited
US3880747A Cited
US3929616A Cited
US4124489A Cited
US4213847A Cited
US4272362A Cited
EP0079778A1 Cited
US4515680A Cited

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

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag