GB842544A - Process for producing high calorific value aviation fuels - Google Patents
Process for producing high calorific value aviation fuelsInfo
- Publication number
- GB842544A GB842544A GB9374/59A GB937459A GB842544A GB 842544 A GB842544 A GB 842544A GB 9374/59 A GB9374/59 A GB 9374/59A GB 937459 A GB937459 A GB 937459A GB 842544 A GB842544 A GB 842544A
- Authority
- GB
- United Kingdom
- Prior art keywords
- heavy fraction
- raffinate
- boiling point
- pentane
- butane
- 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
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
- C10L1/06—Liquid carbonaceous fuels essentially based on blends of hydrocarbons for spark ignition
-
- 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
- C10G21/00—Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
-
- 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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Aviation jet fuels are obtained by catalytically reforming a petroleum fraction having an initial boiling point above 60 DEG C. and a final boiling point below 150 DEG C. using a platinum-containing catalyst, separating by fractional distillation from the resulting reformate a heavy fraction having an initial boiling point above 80 DEG C. extracting the heavy fraction with a solvent to obtain a raffinate free from aromatics and blending the raffinate with a minor proportion of a butane or a pentane. The feedstock, which may be a straight run naphtha, or a catalytically or thermally reformed or cracked naphtha, is contacted with an acidic platinum catalyst at 480 DEG C. to 570 DEG C. under a partial pressure of hydrogen of 100 to 900 pounds per square inch. The heavy fraction may be further fractionated to remove material boiling above 135 DEG C. The heavy fraction is extracted with a mixture of diethylene glycol, dipropylene glycol and water, or with other glycols or nitrobenzene or sulphur dioxide, in a solvent ratio between 5:1 and 20:1 by volume, at 125 DEG C. to 155 DEG C. and with sufficient pressure to maintain the liquid phase. The raffinate is blended with up to 6% by weight of normal or iso-butane, or with up to 30% by weight of normal, iso- or neo-pentane. Examples are given.
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL249479D NL249479A (en) | 1959-03-18 | ||
BE588708D BE588708A (en) | 1959-03-18 | ||
GB9374/59A GB842544A (en) | 1959-03-18 | 1959-03-18 | Process for producing high calorific value aviation fuels |
US847088A US3030299A (en) | 1959-03-18 | 1959-10-19 | Production of jet fuels |
DES67606A DE1113782B (en) | 1959-03-18 | 1960-03-16 | Process for the production of an aircraft fuel |
FR821501A FR1252350A (en) | 1959-03-18 | 1960-03-16 | Process for preparing aviation fuels |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB9374/59A GB842544A (en) | 1959-03-18 | 1959-03-18 | Process for producing high calorific value aviation fuels |
Publications (1)
Publication Number | Publication Date |
---|---|
GB842544A true GB842544A (en) | 1960-07-27 |
Family
ID=9870742
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB9374/59A Expired GB842544A (en) | 1959-03-18 | 1959-03-18 | Process for producing high calorific value aviation fuels |
Country Status (5)
Country | Link |
---|---|
US (1) | US3030299A (en) |
BE (1) | BE588708A (en) |
DE (1) | DE1113782B (en) |
GB (1) | GB842544A (en) |
NL (1) | NL249479A (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE615315A (en) * | 1961-03-22 | |||
US3242066A (en) * | 1961-11-01 | 1966-03-22 | Socony Mobil Oil Co Inc | Method of producing high octane gasoline and jet fuels having a luminometer number of at least 150 |
US3328288A (en) * | 1963-09-26 | 1967-06-27 | Mobil Oil Corp | Production of supersonic jet fuels |
US3328289A (en) * | 1963-09-26 | 1967-06-27 | Mobil Oil Corp | Jet fuel production |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2899377A (en) * | 1959-08-11 | Manufacture of low odor solvents | ||
US2028121A (en) * | 1932-05-13 | 1936-01-14 | Edeleanu Gmbh | High octane number gasoline and method of manufacture |
US2249461A (en) * | 1937-08-17 | 1941-07-15 | Standard Oil Co | Manufacture of antiknock gasoline |
US2510673A (en) * | 1947-12-04 | 1950-06-06 | Pure Oil Co | Reforming gasoline |
US2689208A (en) * | 1951-01-31 | 1954-09-14 | Universal Oil Prod Co | Hydrocarbon conversion process |
US2697684A (en) * | 1951-11-28 | 1954-12-21 | Standard Oil Dev Co | Reforming of naphthas |
US2874114A (en) * | 1954-10-29 | 1959-02-17 | Shell Dev | Process for preparing aviation base stock and aviation gasoline |
NL101545C (en) * | 1954-12-31 | |||
US2914460A (en) * | 1956-05-29 | 1959-11-24 | Exxon Research Engineering Co | Method for aromatization of light naphthas |
-
0
- BE BE588708D patent/BE588708A/xx unknown
- NL NL249479D patent/NL249479A/xx unknown
-
1959
- 1959-03-18 GB GB9374/59A patent/GB842544A/en not_active Expired
- 1959-10-19 US US847088A patent/US3030299A/en not_active Expired - Lifetime
-
1960
- 1960-03-16 DE DES67606A patent/DE1113782B/en active Pending
Also Published As
Publication number | Publication date |
---|---|
US3030299A (en) | 1962-04-17 |
BE588708A (en) | |
DE1113782B (en) | 1961-09-14 |
NL249479A (en) |
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