GB1471228A - Production of jet fuel - Google Patents

Production of jet fuel

Info

Publication number
GB1471228A
GB1471228A GB2846674A GB2846674A GB1471228A GB 1471228 A GB1471228 A GB 1471228A GB 2846674 A GB2846674 A GB 2846674A GB 2846674 A GB2846674 A GB 2846674A GB 1471228 A GB1471228 A GB 1471228A
Authority
GB
United Kingdom
Prior art keywords
zone
hydrogen
effluent
feed
jet fuel
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
GB2846674A
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 GB1471228A publication Critical patent/GB1471228A/en
Expired legal-status Critical Current

Links

Classifications

    • 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/44—Hydrogenation of the aromatic hydrocarbons
    • C10G45/46—Hydrogenation of the aromatic hydrocarbons characterised by the catalyst used
    • C10G45/48—Hydrogenation of the aromatic hydrocarbons characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
    • 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)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

1471228 Jet fuels LUMMUS CO 26 June 1974 [12 July 1973] 28466/74 Addition to 1399108 Heading C5E Jet fuel is produced by a process in which the aromatic content of a hydrocarbon feed boiling in the range 135-550‹ F. and containing not more than 20 p.p.m. sulphur is reduced in two stages and which comprises the steps of: (a) hydrogenating the feed 43 or 46 in cocurrent contact with a hydrogen-rich gas in a first zone 16 at 250-575‹ F. in the presence of a platinum group metal catalyst; (b) separating the effluent into a gas phase, comprising hydrogen and vaporized liquid materials, and a partially hydrogenated liquid hydrocarbon effluent; (c) hydrogenating the liquid hydrocarbon effluent with a countercurrent of hydrogen in a second zone 18 at 200-550‹ F. in contact with a nickel catalyst; and (d) separating the effluent from the second zone into a gas phase, comprising hydrogen and vaporized liquid material, and a liquid phase effluent 50 comprising the jet fuel. As shown, the two zones 16 and 18 can be arranged in a single reactor 10 with the gaseous portions of the effluents from the two zones being combined in line 18 and recycled to the first zone; fresh hydrogen 48 being passed into the second zone 18. The catalyst used in the first zone can be platinum on alumina and that in the second zone can be nickel on kieselguhr. The feed can be a straight-run kerosene which has been desulphurized to reduce its sulphur content to below 20 p.p.m.
GB2846674A 1971-09-02 1974-06-26 Production of jet fuel Expired GB1471228A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US17736271A 1971-09-02 1971-09-02
US00378617A US3846278A (en) 1971-09-02 1973-07-12 Production of jet fuel

Publications (1)

Publication Number Publication Date
GB1471228A true GB1471228A (en) 1977-04-21

Family

ID=26873190

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2846674A Expired GB1471228A (en) 1971-09-02 1974-06-26 Production of jet fuel

Country Status (5)

Country Link
US (1) US3846278A (en)
DE (1) DE2431436A1 (en)
FR (1) FR2236919B2 (en)
GB (1) GB1471228A (en)
NL (1) NL7408802A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011061576A1 (en) * 2009-11-20 2011-05-26 Total Raffinage Marketing Process for the production of hydrocarbon fluids having a low aromatic content
WO2011061575A1 (en) * 2009-11-20 2011-05-26 Total Raffinage Marketing Process for the production of hydrocarbon fluids having a low aromatic content
US10246652B2 (en) 2013-12-23 2019-04-02 Total Marketing Services Process for the dearomatization of petroleum cuts

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2410038A1 (en) * 1977-11-29 1979-06-22 Inst Francais Du Petrole SELECTIVE HYDROGENATION PROCESS OF GASOLINES CONTAINING BOTH GUM-GENERATING COMPOUNDS AND UNDESIRABLE SULFUR COMPOUNDS
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
US5522983A (en) * 1992-02-06 1996-06-04 Chevron Research And Technology Company Hydrocarbon hydroconversion process
US6495029B1 (en) 1997-08-22 2002-12-17 Exxon Research And Engineering Company Countercurrent desulfurization process for refractory organosulfur heterocycles
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
EP1151060A4 (en) * 1998-12-08 2010-08-18 Exxonmobil Res & Eng Co Production of low sulfur/low aromatics distillates
US7247235B2 (en) * 2003-05-30 2007-07-24 Abb Lummus Global Inc, Hydrogenation of middle distillate using a counter-current reactor

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE642626A (en) * 1963-04-11
US3369998A (en) * 1965-04-30 1968-02-20 Gulf Research Development Co Production of high quality jet fuels by two-stage hydrogenation
US3450784A (en) * 1966-09-22 1969-06-17 Lummus Co Hydrogenation of benzene to cyclohexane
US3527693A (en) * 1968-09-06 1970-09-08 Atlantic Richfield Co Process for making jet fuel

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011061576A1 (en) * 2009-11-20 2011-05-26 Total Raffinage Marketing Process for the production of hydrocarbon fluids having a low aromatic content
WO2011061575A1 (en) * 2009-11-20 2011-05-26 Total Raffinage Marketing Process for the production of hydrocarbon fluids having a low aromatic content
WO2011061612A3 (en) * 2009-11-20 2012-01-05 Total Raffinage Marketing Process for the production of hydrocarbon fluids having a low aromatic content
WO2011061716A3 (en) * 2009-11-20 2012-03-08 Total Raffinage Marketing Process for the production of hydrocarbon fluids having a low aromatic content
RU2566363C2 (en) * 2009-11-20 2015-10-27 Тоталь Маркетин Сервис Method of producing liquid hydrocarbons having low content of aromatic compounds
US9315742B2 (en) 2009-11-20 2016-04-19 Total Marketing Services Process for the production of hydrocarbon fluids having a low aromatic content
US9688924B2 (en) 2009-11-20 2017-06-27 Total Marketing Services Process for the production of hydrocarbon fluids having a low aromatic content
US10246652B2 (en) 2013-12-23 2019-04-02 Total Marketing Services Process for the dearomatization of petroleum cuts

Also Published As

Publication number Publication date
FR2236919A2 (en) 1975-02-07
DE2431436A1 (en) 1975-02-13
US3846278A (en) 1974-11-05
NL7408802A (en) 1975-01-14
FR2236919B2 (en) 1978-01-20

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Legal Events

Date Code Title Description
PS Patent sealed [section 19, patents act 1949]