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US4645585A Expired / Lapsed US ⏱️ 0.0 years remaining

Production of fuels, particularly jet and diesel fuels, and constituents thereof

Assignee: The Broken Hill Proprietary Company Pty Ltd
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Filing: 1985-02-27
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Granted: 1987-02-24
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Expires: 2005-02-27
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Abstract

Abstract A first aspect of the invention is concerned with fuels and particularly jet and diesel fuels which comprise blends of substituted mono cyclohexane material and two ring non-fused cyloalkane material. The first material may be n-propylcyclohexane or n-butylcyclohexane. The second material may be nuclear substituted bicyclohexyl and may include cyclohexylbenzene. A second aspect of the invention concerns producing constituents for the fuel from heavy aromatic materials by breaking down the heavy aromatics to naphthas, separating light napthas and other constituents of the fuel before reforming a heavy naptha fraction to provide a BTX fraction which may be treated by hydroalkylation or pyrolysis to provide two ring non-fused cycloalkanes. The product may be enriched by hydrogenation.

Inventors

  • 👤 Noam White

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 13:05
CPC Classifications
C; C10; C10G; C10G47/00; C10L; C10L1/00; C10L1/04; F; F02; F02B; F02B3/00; F02B3/06

Claims Analysis

Total Claims: 19
Claim 1
Independent Claim 92 words
A method of producing a fuel comprising: hydroprocessing fused polynuclear aromatic compounds to produce a product rich in mononuclear cycloalkanes and mononuclear aromatics comprising a kerosene fraction, a distillate fraction, light gases, light naphtha having a boiling point less than about 65° C., indan, hydrindan, decalin, n-propylcylohexane, n-butylcyclohexane and a naphtha fraction having a boiling range of about 180°-190° C.; converting at least a portion of said product rich in mononuclear cycloalkanes and mononuclear aromatics into two-ring, non-fused cycloalkane compounds; and mixing said two-ring non-fused cycloalkanes with at least one alkylated cycloalkane.
Claim 2
Independent Claim 92 words
A method of producing a fuel comprising: hydroprocessing fused polynuclear aromatic compounds to produce a product rich in mononuclear cycloalkanes and mononuclear aromatics comprising a kerosene fraction, a distillate fraction, light gases, light naphtha having a boiling point less than about 65° C., indan, hydrindan, decalin, n-propylcylohexane, n-butylcyclohexane and a naphtha fraction having a boiling range of about 180°-190° C.; converting at least a portion of said product rich in mononuclear cycloalkanes and mononuclear aromatics into two-ring, non-fused cycloalkane compounds; and mixing said two-ring non-fused cycloalkanes with at least one alkylated cycloalkane.
Claim 3
Dependent Claim 15 words
The method according to claim 1, wherein said mononuclear cycloalkane compounds include a six-carbon ring.
Claim 4
Dependent Claim 19 words
The method according to claim 1, wherein said hydroprocessing step includes hydrotreating and hydrocracking said fused polynuclear aromatic compounds.
Claim 5
Dependent Claim 26 words
The method according to claim 1 wherein said kerosene and distillate fractions are separated from said product of said hydroprocessing step prior to said conversion step.
Claim 6
Dependent Claim 49 words
The method according to claim 1 wherein at least one member of the group consisting of light gases, light naphtha having a boiling point less than about 65° C., n-propylcyclohexane, n-butylcyclohexane, indan, hydrindan and decalin is separated from said product of said hydroprocessing step prior to said conversion step.
Claim 7
Dependent Claim 23 words
The method according to claim 5, wherein said at least one member is separated from said product of said hydroprocessing step by distillation.
Claim 8
Dependent Claim 43 words
The method according to claim 1, wherein said naphtha fraction having a boiling range of about 180°-190° C. is reformed to produce a BTX-rich liquid product and at least a portion of said BTX-rich liquid product is converted to said two-ring non-fused cycloalkanes.
Claim 9
Dependent Claim 26 words
The method according to claim 7, wherein said at least a portion of said BTX-rich liquid product is converted to said two-ring non-fused cycloalkane by hydroalkylation.
Claim 10
Dependent Claim 22 words
The method according to claim 8, wherein said hydroalkylation is followed by hydrogenation to increase the yield of two-ring non-fused cycloalkane compounds.
Claim 11
Dependent Claim 26 words
The method according to claim 7, wherein said at least a portion of said BTX-rich liquid product is converted to said two-ring non-fused cycloalkane by pyrolysis.
Claim 12
Dependent Claim 22 words
The method according to claim 10, wherein said pyrolysis is followed by hydrogenation to increase the yield of two-ring non-fused cycloalkane compounds.
Claim 13
Dependent Claim 15 words
The method according to claim 1, wherein said alkylated cycloalkane comprises a n-propylcyclohexane or n-butylcyclohexane.
Claim 14
Dependent Claim 14 words
The method according to claim 1, wherein said two-ring non-fused cycloalkane comprises nuclear-substituted bicyclohexyl.
Claim 15
Dependent Claim 15 words
The method according to claim 13, wherein said two-ring non-fused cycloalkane further comprises nuclear-substituted cyclohexylbenzene.
Claim 16
Dependent Claim 29 words
The method according to claim 1, further comprising mixing up to about 10% biphenyl with said mixture of said two-ring non-fused cycloalkane and said at least one alkylated cycloalkane.
Claim 17
Dependent Claim 38 words
The method according to claim 1, further comprising mixing at least one member selected from the group consisting of hydrindane, decaline and tetralin with said mixture of said two-ring non-fused cycloalkane and said at least one alkylated cycloalkane.
Claim 18
Dependent Claim 38 words
The method according to claim 1, wherein said mixture of said two-ring non-fused cycloalkane and said at least one alkylated cycloalkane has a smoke point greater than 20 mm and a freezing point less than minus 30° C.
Claim 19
Dependent Claim 36 words
The method according to claim 1, wherein said mixture of said two-ring non-fused cycloalkane and said at least one alkylated cycloalkane has a cetane number greater than 40 and a freezing point less than 5° C.

References Cited (Backward Citations)

US3533938A Cited
US3540999A Cited
US3544448A Cited
US3623973A Cited
US3726788A Cited
US3719586A Cited
US3784617A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1990-02-23 1990-08-25 1991-02-24 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1994-02-23 1994-08-25 1995-02-24 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1998-02-23 1998-08-25 1999-02-24 $7700.00 Window Closed / Lapsed

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