FI60228C - Foerfarande foer framstaellning av jetbraensle - Google Patents

Foerfarande foer framstaellning av jetbraensle Download PDF

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Publication number
FI60228C
FI60228C FI2313/72A FI231372A FI60228C FI 60228 C FI60228 C FI 60228C FI 2313/72 A FI2313/72 A FI 2313/72A FI 231372 A FI231372 A FI 231372A FI 60228 C FI60228 C FI 60228C
Authority
FI
Finland
Prior art keywords
reaction zone
process according
mixture
zone
liquid
Prior art date
Application number
FI2313/72A
Other languages
English (en)
Finnish (fi)
Other versions
FI60228B (fi
Inventor
Morgan Chuan-Yuan Sze
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
Application granted granted Critical
Publication of FI60228B publication Critical patent/FI60228B/fi
Publication of FI60228C publication Critical patent/FI60228C/fi

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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)

Claims (15)

1. Förfarande för framställning av jetbränsle, känneteck-n a t därav, att (a) en blandning innehällande en väsentligen inom kokningsinter-vallet för petroleum kokande petroleumfraktion, som är huvudsak-ligen fri frän svavelhaltiga föroreningar, och en blandning av förgrenade olefinkolväten innehällande i genomsnitt S~l6 kolato-mer i molekylen ledes i medström med en rikligt med väte innehällande gas genom en första reaktionszon, som har en arbetstem-peratur inom intervallen 93-302°C och förhöjt tryck, i beröring med en hydreringskatalysator, (b) frän den första reaktionszonen uttages en gasfas-utflödesström bestäende av väte och förängad vätska, samt en delvis hydrerad vätskefas-utflödesström, (c) nämnda vätskefas-utflödesström ledes tili en andra reaktionszon, som har en arbetstemperatur inom intervallen 122-232°C och förhöjt tryck, (d) nämnda vätskefas-ut.f lödesström hydreras genom inledning av en rikligt med väte innehällande gas i den andra reaktionszonen i motström tili utflödesströmmen, i beröring med en hydreringskatalysator, och (e) frän den nämnda andra reaktionszonen uttages en gasfas-utflödesström bestäende av väte och förängade vätskor samt en vätskefas- utflödesström, som bestär av jetbränsle.
2. Förfarande enligt patentkravet 1, kännetecknat därav, att blandningen enligt steg (a) förvärmes innan den in-ledes i den första reaktionszonen.
3. Förfarande enligt patentkravet 2, kännet ec knat därav, att gasfas-utflödesströmmarna frän den första och den andra reaktionszonen förenas och ledes tili indirekt värmeväx-ling med beskickningsströmmen tili den första reaktionszonen, sä att nämnda gasfas-utflödesströmmar kyles och nämnda beskicknings-ström förvärmes.
4. Förfarande enligt patentkravet 1, kännetecknat därav, att gasfas-utflödesströmmarna frän den första och den andra reaktionszonen kyles sä längt, att de i dem ingäende förängade vätskekomponenterna kondenseras, och nämnda vätskekompo-nenter avskiljes frän de kvarvarande gaskomponenterna och äter-föres säsom vätskebeskickning tili den första reaktionszonen.
5. Förfarande enligt patentkravet 4, kännetecknat
FI2313/72A 1971-09-02 1972-08-21 Foerfarande foer framstaellning av jetbraensle FI60228C (fi)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US17743971A 1971-09-02 1971-09-02
US17743971 1971-09-02

Publications (2)

Publication Number Publication Date
FI60228B FI60228B (fi) 1981-08-31
FI60228C true FI60228C (fi) 1981-12-10

Family

ID=22648594

Family Applications (1)

Application Number Title Priority Date Filing Date
FI2313/72A FI60228C (fi) 1971-09-02 1972-08-21 Foerfarande foer framstaellning av jetbraensle

Country Status (11)

Country Link
US (1) US3775291A (sv)
JP (1) JPS5418281B2 (sv)
AU (1) AU469396B2 (sv)
CA (1) CA981201A (sv)
DE (1) DE2242330A1 (sv)
ES (1) ES406278A1 (sv)
FI (1) FI60228C (sv)
FR (1) FR2151058B1 (sv)
GB (1) GB1401515A (sv)
IT (1) IT962256B (sv)
NL (1) NL176582C (sv)

Families Citing this family (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA1042021A (en) * 1975-04-10 1978-11-07 Universite D'ottawa/ University Of Ottawa Method and apparatus for carrying out hydro-genation reactions
US5183556A (en) * 1991-03-13 1993-02-02 Abb Lummus Crest Inc. Production of diesel fuel by hydrogenation of a diesel feed
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
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
US5942197A (en) * 1996-08-23 1999-08-24 Exxon Research And Engineering Co Countercurrent reactor
US5906728A (en) * 1996-08-23 1999-05-25 Exxon Chemical Patents Inc. Process for increased olefin yields from heavy feedstocks
US5766274A (en) 1997-02-07 1998-06-16 Exxon Research And Engineering Company Synthetic jet fuel and process for its production
DE19719833A1 (de) * 1997-05-12 1998-11-19 Basf Ag Verfahren zur katalytischen Gasphasenhydrierung von Olefinen
US5882505A (en) * 1997-06-03 1999-03-16 Exxon Research And Engineering Company Conversion of fisher-tropsch waxes to lubricants by countercurrent processing
US5928497A (en) * 1997-08-22 1999-07-27 Exxon Chemical Pateuts Inc Heteroatom removal through countercurrent sorption
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
US6569314B1 (en) 1998-12-07 2003-05-27 Exxonmobil Research And Engineering Company Countercurrent hydroprocessing with trickle bed processing of vapor product stream
US6497810B1 (en) 1998-12-07 2002-12-24 Larry L. Laccino Countercurrent hydroprocessing with feedstream quench to control temperature
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
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
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
DE102004021423A1 (de) * 2004-04-30 2005-12-01 Siemens Ag Verfahren und Einrichtung zur Ermittlung der Leistungsfähigkeit eines Wärmetauschers
US7892418B2 (en) * 2005-04-11 2011-02-22 Oil Tech SARL Process for producing low sulfur and high cetane number petroleum fuel
EP2792729A1 (en) 2013-04-17 2014-10-22 XTLgroup bv Process for hydroprocessing a liquid feed comprising hydrocarbons into fuel components

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3125503A (en) * 1964-03-17 Preparation of a jet fuel
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
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
US3594307A (en) * 1969-02-14 1971-07-20 Sun Oil Co Production of high quality jet fuels by two-stage hydrogenation
US3493491A (en) * 1969-05-21 1970-02-03 Atlantic Richfield Co Blending hydrogenated fractions to make a jet fuel

Also Published As

Publication number Publication date
NL176582C (nl) 1985-05-01
FR2151058A1 (sv) 1973-04-13
FR2151058B1 (sv) 1976-08-13
JPS4832903A (sv) 1973-05-04
US3775291A (en) 1973-11-27
FI60228B (fi) 1981-08-31
CA981201A (en) 1976-01-06
GB1401515A (en) 1975-07-16
ES406278A1 (es) 1975-09-16
DE2242330A1 (de) 1973-03-08
IT962256B (it) 1973-12-20
JPS5418281B2 (sv) 1979-07-06
AU469396B2 (en) 1976-02-12
AU4563472A (en) 1974-02-21
NL7211961A (sv) 1973-03-06

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