ES406277A1 - Production of jet fuel - Google Patents

Production of jet fuel

Info

Publication number
ES406277A1
ES406277A1 ES406277A ES406277A ES406277A1 ES 406277 A1 ES406277 A1 ES 406277A1 ES 406277 A ES406277 A ES 406277A ES 406277 A ES406277 A ES 406277A ES 406277 A1 ES406277 A1 ES 406277A1
Authority
ES
Spain
Prior art keywords
jet fuel
production
aromatics
kerosene
preheated
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
ES406277A
Other languages
Spanish (es)
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
CB&I Technology Inc
Original Assignee
Lummus Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Lummus Co filed Critical Lummus Co
Publication of ES406277A1 publication Critical patent/ES406277A1/en
Expired legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0446—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
    • B01J8/0449—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds
    • B01J8/0453—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds the beds being superimposed one above the other
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/08—Jet fuel

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Liquid Carbonaceous Fuels (AREA)

Abstract

A process for producing jet fuel from a petroleum fraction having a boiling range within the temperature range of about 135 DEG F. to about 550 DEG F., such as kerosene. The feed is mixed with hydrogen, and liquid recycle, preheated if necessary, and subjected to two-stage hydrogenation of aromatics to reduce the aromatics content and improve the smoke point.
ES406277A 1971-09-02 1972-09-01 Production of jet fuel Expired ES406277A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US17736271A 1971-09-02 1971-09-02

Publications (1)

Publication Number Publication Date
ES406277A1 true ES406277A1 (en) 1975-07-01

Family

ID=22648306

Family Applications (1)

Application Number Title Priority Date Filing Date
ES406277A Expired ES406277A1 (en) 1971-09-02 1972-09-01 Production of jet fuel

Country Status (11)

Country Link
US (1) US3767562A (en)
JP (1) JPS5442005B2 (en)
AU (1) AU469380B2 (en)
CA (1) CA983420A (en)
DE (1) DE2242331A1 (en)
ES (1) ES406277A1 (en)
FI (1) FI59810C (en)
FR (1) FR2151059B1 (en)
GB (1) GB1399108A (en)
IT (2) IT962225B (en)
NL (1) NL176583C (en)

Families Citing this family (37)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA1033680A (en) * 1973-07-12 1978-06-27 Lummus Company (The) Production of jet fuel
US4427534A (en) 1982-06-04 1984-01-24 Gulf Research & Development Company Production of jet and diesel fuels from highly aromatic oils
US4849093A (en) * 1987-02-02 1989-07-18 Union Oil Company Of California Catalytic aromatic saturation of hydrocarbons
US5183556A (en) * 1991-03-13 1993-02-02 Abb Lummus Crest Inc. Production of diesel fuel by hydrogenation of a diesel feed
DE4235450A1 (en) * 1991-11-05 1993-05-06 Rieter Ingolstadt Spinnereimaschinenbau Ag, 8070 Ingolstadt, De METHOD AND DEVICE FOR DETERMINING THE DIAMETER OF A REEL AT A SPINNING SITE OF A SPINNING MACHINE
US5393408A (en) * 1992-04-30 1995-02-28 Chevron Research And Technology Company Process for the stabilization of lubricating oil base stocks
US6296757B1 (en) 1995-10-17 2001-10-02 Exxon Research And Engineering Company Synthetic diesel fuel and process for its production
US5689031A (en) 1995-10-17 1997-11-18 Exxon Research & Engineering Company Synthetic diesel fuel and process for its production
US5906728A (en) * 1996-08-23 1999-05-25 Exxon Chemical Patents Inc. Process for increased olefin yields from heavy feedstocks
US5942197A (en) * 1996-08-23 1999-08-24 Exxon Research And Engineering Co Countercurrent reactor
US5888376A (en) * 1996-08-23 1999-03-30 Exxon Research And Engineering Co. Conversion of fischer-tropsch light oil to jet fuel by countercurrent processing
US5766274A (en) 1997-02-07 1998-06-16 Exxon Research And Engineering Company Synthetic jet fuel and process for its production
US5882505A (en) * 1997-06-03 1999-03-16 Exxon Research And Engineering Company Conversion of fisher-tropsch waxes to lubricants by countercurrent processing
US6495029B1 (en) 1997-08-22 2002-12-17 Exxon Research And Engineering Company Countercurrent desulfurization process for refractory organosulfur heterocycles
US5928497A (en) * 1997-08-22 1999-07-27 Exxon Chemical Pateuts Inc Heteroatom removal through countercurrent sorption
CA2243267C (en) 1997-09-26 2003-12-30 Exxon Research And Engineering Company Countercurrent reactor with interstage stripping of nh3 and h2s in gas/liquid contacting zones
US6497810B1 (en) 1998-12-07 2002-12-24 Larry L. Laccino Countercurrent hydroprocessing with feedstream quench to control temperature
US6569314B1 (en) 1998-12-07 2003-05-27 Exxonmobil Research And Engineering Company Countercurrent hydroprocessing with trickle bed processing of vapor product stream
US6579443B1 (en) 1998-12-07 2003-06-17 Exxonmobil Research And Engineering Company Countercurrent hydroprocessing with treatment of feedstream to remove particulates and foulant precursors
US6623621B1 (en) 1998-12-07 2003-09-23 Exxonmobil Research And Engineering Company Control of flooding in a countercurrent flow reactor by use of temperature of liquid product stream
US6835301B1 (en) 1998-12-08 2004-12-28 Exxon Research And Engineering Company Production of low sulfur/low aromatics distillates
US6514403B1 (en) * 2000-04-20 2003-02-04 Abb Lummus Global Inc. Hydrocracking of vacuum gas and other oils using a cocurrent/countercurrent reaction system and a post-treatment reactive distillation system
US6617871B2 (en) * 2001-07-09 2003-09-09 Rambus Inc. Methods and apparatus for bi-directional signaling
US7247235B2 (en) * 2003-05-30 2007-07-24 Abb Lummus Global Inc, Hydrogenation of middle distillate using a counter-current reactor
CN100434155C (en) * 2003-08-18 2008-11-19 国际壳牌研究有限公司 Distribution device
JP4643966B2 (en) * 2004-10-01 2011-03-02 Ｊｘ日鉱日石エネルギー株式会社 Process for producing hydrorefined gas oil, hydrorefined gas oil and gas oil composition
EP1836279A1 (en) * 2004-12-23 2007-09-26 The Petroleum Oil and Gas Corporation of South Afr. A process for catalytic conversion of fischer-tropsch derived olefins to distillates
EP1836284B1 (en) * 2004-12-23 2018-08-22 The Petroleum Oil and Gas Corporation of South Afr. Synthetically derived distillate kerosene and its use
US8022258B2 (en) 2005-07-05 2011-09-20 Neste Oil Oyj Process for the manufacture of diesel range hydrocarbons
US8303804B2 (en) * 2008-10-06 2012-11-06 Exxonmobil Research And Engineering Company Process to improve jet fuels
WO2011061575A1 (en) * 2009-11-20 2011-05-26 Total Raffinage Marketing Process for the production of hydrocarbon fluids having a low aromatic content
WO2011061576A1 (en) 2009-11-20 2011-05-26 Total Raffinage Marketing Process for the production of hydrocarbon fluids having a low aromatic content
US9334451B2 (en) * 2010-03-15 2016-05-10 Saudi Arabian Oil Company High quality middle distillate production process
EP3517591A1 (en) 2011-02-15 2019-07-31 Neste Oil Oyj Use of renewable oil in hydrotreatment process
FR3015514B1 (en) 2013-12-23 2016-10-28 Total Marketing Services IMPROVED PROCESS FOR DESAROMATIZATION OF PETROLEUM CUTTERS
CA3004679A1 (en) 2015-11-23 2017-06-01 Shell Internationale Research Maatschappij B.V. Conversion of biomass into a liquid hydrocarbon material
CA3005405C (en) * 2015-11-23 2023-10-10 Shell Internationale Research Maatschappij B.V. Conversion of biomass into a liquid hydrocarbon material

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2952626A (en) * 1957-08-05 1960-09-13 Union Oil Co Mixed-phase hydrofining of hydrocarbon oils
US3147210A (en) * 1962-03-19 1964-09-01 Union Oil Co Two stage hydrogenation process
GB1141809A (en) * 1965-10-04 1969-02-05 British Petroleum Co Improvements relating to the desulphurisation and hydrogenation of aromatic hydrocarbons
US3450784A (en) * 1966-09-22 1969-06-17 Lummus Co Hydrogenation of benzene to cyclohexane
US3513085A (en) * 1967-09-06 1970-05-19 Arnold M Leas Producing isoparaffins and naphthenes from hydrocarbons
US3573198A (en) * 1969-02-10 1971-03-30 Universal Oil Prod Co Smoke point improvement of jet fuel kerosene fractions

Also Published As

Publication number Publication date
GB1399108A (en) 1975-06-25
FI59810B (en) 1981-06-30
AU4563572A (en) 1974-02-21
FI59810C (en) 1981-10-12
CA983420A (en) 1976-02-10
AU469380B2 (en) 1976-02-12
JPS5442005B2 (en) 1979-12-12
JPS4834906A (en) 1973-05-23
FR2151059B1 (en) 1976-08-13
IT962225B (en) 1973-12-20
DE2242331A1 (en) 1973-03-08
US3767562A (en) 1973-10-23
NL7211962A (en) 1973-03-06
NL176583C (en) 1985-05-01
FR2151059A1 (en) 1973-04-13
IT962255B (en) 1973-12-20

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