GB800666A - Improvements relating to motor fuels - Google Patents
Improvements relating to motor fuelsInfo
- Publication number
- GB800666A GB800666A GB33704/55A GB3370455A GB800666A GB 800666 A GB800666 A GB 800666A GB 33704/55 A GB33704/55 A GB 33704/55A GB 3370455 A GB3370455 A GB 3370455A GB 800666 A GB800666 A GB 800666A
- Authority
- GB
- United Kingdom
- Prior art keywords
- boiling fraction
- give
- per cent
- lower boiling
- reformate
- 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
- 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
- C10G59/00—Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha
- C10G59/02—Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha plural serial stages only
- C10G59/04—Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha plural serial stages only including at least one catalytic and at least one non-catalytic reforming step
-
- 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
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)
- Catalysts (AREA)
Abstract
High octane motor fuels are produced by fractionating a catalytic reformate into a higher and a lower boiling fraction and thermally reforming each, the lower boiling fraction under conditions of greater severity, and blending the products to give a gasoline having a research clear octane number of at least 90. The cut between the two fractions is preferably in the range of 110-150 DEG C. The thermal reforming conditions may be 538-650 DEG C. and 200-1200 p.s.i.g. and are such that the conversion to C3 and lower hydrocarbons on the lower boiling fraction is 20-35 per cent by weight and on the higher boiling fraction is 5-20 per cent by weight. The process is particularly applicable to a reformate obtained by catalytically reforming a naphtha in the presence of a platinum on alumina catalyst. In an example such a reformate is distilled cutting at 130 DEG C.; the higher boiling fraction is reformed at 750 p.s.i.g. and 554 DEG C. to give 7 per cent wt. C3 and lighter and the lower boiling fraction is reformed at 750 p.s.i.g. and 571 DEG C. to give 26 per cent wt. C3 and lighter. The two products when blended give a gasoline of octane number iso-octane + 0.30 ml. TEL/USG (research). Specification 742,769 is referred to.
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BE552865D BE552865A (en) | 1955-11-24 | ||
GB33704/55A GB800666A (en) | 1955-11-24 | 1955-11-24 | Improvements relating to motor fuels |
DEB42474A DE1026461B (en) | 1955-11-24 | 1956-11-14 | Process for the production of gasoline |
US622337A US2897132A (en) | 1955-11-24 | 1956-11-15 | Thermal reforming of a catalytic reformate |
FR1189873D FR1189873A (en) | 1955-11-24 | 1956-11-22 | Manufacturing process of gasoline for the operation of internal combustion engines |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB33704/55A GB800666A (en) | 1955-11-24 | 1955-11-24 | Improvements relating to motor fuels |
Publications (1)
Publication Number | Publication Date |
---|---|
GB800666A true GB800666A (en) | 1958-08-27 |
Family
ID=10356379
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB33704/55A Expired GB800666A (en) | 1955-11-24 | 1955-11-24 | Improvements relating to motor fuels |
Country Status (5)
Country | Link |
---|---|
US (1) | US2897132A (en) |
BE (1) | BE552865A (en) |
DE (1) | DE1026461B (en) |
FR (1) | FR1189873A (en) |
GB (1) | GB800666A (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE554073A (en) * | 1956-01-11 | |||
US3017344A (en) * | 1958-05-05 | 1962-01-16 | Texaco Inc | Serial reforming of hydrocarbons |
DE1102943B (en) * | 1958-05-20 | 1961-03-23 | British Petroleum Co | Process to increase the volatility of platforms |
DE1102944B (en) * | 1958-05-20 | 1961-03-23 | British Petroleum Co | Process to increase the volatility of platforms |
BE578938A (en) * | 1958-05-23 | 1959-09-16 | ||
US2999804A (en) * | 1958-12-09 | 1961-09-12 | Houdry Process Corp | Reforming gasoline |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2249461A (en) * | 1937-08-17 | 1941-07-15 | Standard Oil Co | Manufacture of antiknock gasoline |
US2490287A (en) * | 1946-09-19 | 1949-12-06 | Standard Oil Dev Co | Upgrading of naphtha |
US2659692A (en) * | 1949-02-26 | 1953-11-17 | Universal Oil Prod Co | Catalytic reforming of hydrocarbons in two stages utilizing a platinum-alumina-halogen catalyst composite |
US2866745A (en) * | 1951-12-15 | 1958-12-30 | Houdry Process Corp | Multistage hydrocarbon reforming process |
US2740751A (en) * | 1952-02-23 | 1956-04-03 | Universal Oil Prod Co | Reforming of both straight run and cracked gasolines to provide high octane fuels |
FR1090846A (en) * | 1953-11-16 | 1955-04-04 | Universal Oil Prod Co | Process for the catalytic reformation of petroleum hydrocarbons |
-
0
- BE BE552865D patent/BE552865A/xx unknown
-
1955
- 1955-11-24 GB GB33704/55A patent/GB800666A/en not_active Expired
-
1956
- 1956-11-14 DE DEB42474A patent/DE1026461B/en active Pending
- 1956-11-15 US US622337A patent/US2897132A/en not_active Expired - Lifetime
- 1956-11-22 FR FR1189873D patent/FR1189873A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
FR1189873A (en) | 1959-10-07 |
DE1026461B (en) | 1958-03-20 |
BE552865A (en) | |
US2897132A (en) | 1959-07-28 |
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