GB1401515A - Production of jet fuel - Google Patents
Production of jet fuelInfo
- Publication number
- GB1401515A GB1401515A GB4048172A GB4048172A GB1401515A GB 1401515 A GB1401515 A GB 1401515A GB 4048172 A GB4048172 A GB 4048172A GB 4048172 A GB4048172 A GB 4048172A GB 1401515 A GB1401515 A GB 1401515A
- Authority
- GB
- United Kingdom
- Prior art keywords
- hydrogen
- mixed
- olefinic
- stream
- range
- 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
Links
- 239000000446 fuel Substances 0.000 title abstract 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract 5
- 229910052739 hydrogen Inorganic materials 0.000 abstract 5
- 239000001257 hydrogen Substances 0.000 abstract 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract 4
- 229930195733 hydrocarbon Natural products 0.000 abstract 4
- 150000002430 hydrocarbons Chemical class 0.000 abstract 4
- 239000003054 catalyst Substances 0.000 abstract 3
- 239000003350 kerosene Substances 0.000 abstract 3
- 239000007788 liquid Substances 0.000 abstract 3
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 abstract 2
- NPXOKRUENSOPAO-UHFFFAOYSA-N Raney nickel Chemical compound [Al].[Ni] NPXOKRUENSOPAO-UHFFFAOYSA-N 0.000 abstract 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 abstract 2
- 238000009835 boiling Methods 0.000 abstract 2
- 239000000203 mixture Substances 0.000 abstract 2
- 239000003208 petroleum Substances 0.000 abstract 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Substances [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 abstract 2
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 abstract 2
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 abstract 2
- 239000013638 trimer Substances 0.000 abstract 2
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 abstract 1
- 239000004215 Carbon black (E152) Substances 0.000 abstract 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 abstract 1
- 239000005977 Ethylene Substances 0.000 abstract 1
- 239000005909 Kieselgur Substances 0.000 abstract 1
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 abstract 1
- 239000007868 Raney catalyst Substances 0.000 abstract 1
- 229910000564 Raney nickel Inorganic materials 0.000 abstract 1
- 150000001336 alkenes Chemical class 0.000 abstract 1
- IAQRGUVFOMOMEM-UHFFFAOYSA-N butene Natural products CC=CC IAQRGUVFOMOMEM-UHFFFAOYSA-N 0.000 abstract 1
- 125000004432 carbon atom Chemical group C* 0.000 abstract 1
- 238000007710 freezing Methods 0.000 abstract 1
- 230000008014 freezing Effects 0.000 abstract 1
- 239000000295 fuel oil Substances 0.000 abstract 1
- -1 heavy naphtha Substances 0.000 abstract 1
- 239000000395 magnesium oxide Substances 0.000 abstract 1
- 229910052759 nickel Inorganic materials 0.000 abstract 1
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 abstract 1
- 239000003921 oil Substances 0.000 abstract 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 abstract 1
- 229910052697 platinum Inorganic materials 0.000 abstract 1
- 239000000377 silicon dioxide Substances 0.000 abstract 1
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 abstract 1
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
1401515 Jet fuel LUMMUS CO 31 Aug 1972 [2 Sept 1971] 40481/72 Heading C5E A petroleum fraction 62 boiling in the kerosene range is mixed with a mixture 60 of branched-chain olefinic hydrocarbons having an average of 9 to 16 carbon atoms per molecule. The mixture is passed from line 42 through a catalyst bed 16 at 200-75‹ F. in admixture with a cocurrent of hydrogen. The liquid effluent from the bed 16 is contacted at 250-450‹ F. with a countercurrent of hydrogen in the catalyst bed 18 to produce a stream 50 of jet fuel. If the feed does not need to be preheated the fresh kerosene enters at 43 and the olefinic feed is mixed from line 41. The olefinic hydrocarbon can be olefin oligomers, e.g. propylene trimers and tetramers, butene trimers and tetramers, and mixed oligomers of butenes with ethylene and/or propylene, boiling in the range 280- 525‹ F. The petroleum fraction 62 generally boils in the range 300-550‹ F. and can be a hydrodesulphurized straight-run kerosene, heavy naphtha, furnace oil or catalytically cracked cycle oil. The mixed feed generally comprises 10-50 volume per cent of the olefinic hydrocarbons. The gaseous effluents from the zones 16 and 18, comprising hydrogen and normally liquid hydrocarbons, are cooled at 52, 30 and 32 and separated at 34 into a stream 36 of recycle hydrogen and a liquid stream 44 which is recycled. The catalysts used can be Raney nickel or Ni, Pt or Pd on alumina, silica, kieselguhr, diatomaceous earth, magnesia or zirconia. The hydrogen introduced at 26 can be cold. The jet fuels produced can have aromatics contents of below 1 volume per cent and freezing points below - 57‹ F.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US17743971A | 1971-09-02 | 1971-09-02 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB1401515A true GB1401515A (en) | 1975-07-16 |
Family
ID=22648594
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB4048172A Expired GB1401515A (en) | 1971-09-02 | 1972-08-31 | Production of jet fuel |
Country Status (11)
| Country | Link |
|---|---|
| US (1) | US3775291A (en) |
| JP (1) | JPS5418281B2 (en) |
| AU (1) | AU469396B2 (en) |
| CA (1) | CA981201A (en) |
| DE (1) | DE2242330A1 (en) |
| ES (1) | ES406278A1 (en) |
| FI (1) | FI60228C (en) |
| FR (1) | FR2151058B1 (en) |
| GB (1) | GB1401515A (en) |
| IT (1) | IT962256B (en) |
| NL (1) | NL176582C (en) |
Families Citing this family (22)
| 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 |
| 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 |
| 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 (en) * | 1997-05-12 | 1998-11-19 | Basf Ag | Process for the catalytic gas phase hydrogenation of olefins |
| 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 |
| 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 |
| 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 |
| 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 (en) * | 2004-04-30 | 2005-12-01 | Siemens Ag | Method and device for determining the efficiency of a heat exchanger |
| 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)
| 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 |
-
1971
- 1971-09-02 US US00177439A patent/US3775291A/en not_active Expired - Lifetime
-
1972
- 1972-08-15 CA CA149,450A patent/CA981201A/en not_active Expired
- 1972-08-16 AU AU45634/72A patent/AU469396B2/en not_active Expired
- 1972-08-21 FI FI2313/72A patent/FI60228C/en active
- 1972-08-23 JP JP8441372A patent/JPS5418281B2/ja not_active Expired
- 1972-08-28 IT IT52398/72A patent/IT962256B/en active
- 1972-08-29 DE DE2242330A patent/DE2242330A1/en not_active Withdrawn
- 1972-08-31 GB GB4048172A patent/GB1401515A/en not_active Expired
- 1972-08-31 FR FR7230997A patent/FR2151058B1/fr not_active Expired
- 1972-09-01 NL NLAANVRAGE7211961,A patent/NL176582C/en not_active IP Right Cessation
- 1972-09-01 ES ES406278A patent/ES406278A1/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| CA981201A (en) | 1976-01-06 |
| FR2151058B1 (en) | 1976-08-13 |
| JPS5418281B2 (en) | 1979-07-06 |
| FI60228B (en) | 1981-08-31 |
| NL176582C (en) | 1985-05-01 |
| DE2242330A1 (en) | 1973-03-08 |
| AU469396B2 (en) | 1976-02-12 |
| FR2151058A1 (en) | 1973-04-13 |
| US3775291A (en) | 1973-11-27 |
| FI60228C (en) | 1981-12-10 |
| JPS4832903A (en) | 1973-05-04 |
| NL7211961A (en) | 1973-03-06 |
| ES406278A1 (en) | 1975-09-16 |
| AU4563472A (en) | 1974-02-21 |
| IT962256B (en) | 1973-12-20 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PS | Patent sealed [section 19, patents act 1949] | ||
| PCNP | Patent ceased through non-payment of renewal fee |