GB1160258A - Preparation of Motor Fuels Having and Octane Number Above 100 - Google Patents
Preparation of Motor Fuels Having and Octane Number Above 100Info
- Publication number
- GB1160258A GB1160258A GB53155/66A GB5315566A GB1160258A GB 1160258 A GB1160258 A GB 1160258A GB 53155/66 A GB53155/66 A GB 53155/66A GB 5315566 A GB5315566 A GB 5315566A GB 1160258 A GB1160258 A GB 1160258A
- Authority
- GB
- United Kingdom
- Prior art keywords
- heartcut
- reforming
- octane number
- full range
- clear
- 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
- C10G35/00—Reforming naphtha
- C10G35/04—Catalytic reforming
- C10G35/06—Catalytic reforming characterised by the catalyst used
- C10G35/085—Catalytic reforming characterised by the catalyst used containing platinum group metals 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
- 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
-
- 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)
Abstract
1,160,258. Reforming. AIR PRODUCTS & CHEMICALS Inc. 28 Nov., 1966 [1 March, 1966], No. 53155/66. Heading C5E. A method for increasing the octane number of a liquid hydrocarbon by treatment over a platinum catalyst comprises fractionating a primary full range reformate of liquid hydrocarbons of 85 to 93 octane (F1 clear) to provide a heartcut having an initial boiling point of at least 70 C. and an end boiling point below 170 C., whereby normal hexane and lower boiling paraffins and polycyclic aromatics are substantially excluded, reforming said heartcut over supported platinum catalyst at severe conditions and blending the reformed heartcut with the remaining liquid forerun and bottoms components of the fractionated primary full range reformate to obtain a full range gasoline having an F1 clear octane number greater than 100. Conditions for the severe reforming may be hydrogen to hydrocarbon mol ratio 3 to 8. S.V. 1 to 3 v./v./hr., pressure 15 to 30 atmospheres, and temperature 480 to 550 C.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US530989A US3374167A (en) | 1966-03-01 | 1966-03-01 | Preparation of motor fuels having an octane number above 100 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1160258A true GB1160258A (en) | 1969-08-06 |
Family
ID=24115810
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB53155/66A Expired GB1160258A (en) | 1966-03-01 | 1966-11-28 | Preparation of Motor Fuels Having and Octane Number Above 100 |
Country Status (4)
Country | Link |
---|---|
US (1) | US3374167A (en) |
DE (1) | DE1545224B2 (en) |
FR (1) | FR1504192A (en) |
GB (1) | GB1160258A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
USRE31647E (en) * | 1980-03-17 | 1984-08-14 | Mobil Oil Corporation | Startup procedure for reforming catalysts |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3516924A (en) * | 1968-04-19 | 1970-06-23 | Universal Oil Prod Co | Catalytic reforming process |
US3664949A (en) * | 1969-11-10 | 1972-05-23 | Standard Oil Co | Platinum reforming with a mordenite containing support using two reactors |
US3883418A (en) * | 1973-01-02 | 1975-05-13 | Phillips Petroleum Co | Lead free motor fuel production |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2905621A (en) * | 1956-03-02 | 1959-09-22 | Phillips Petroleum Co | Two stage reforming with noble metal catalyst |
-
1966
- 1966-03-01 US US530989A patent/US3374167A/en not_active Expired - Lifetime
- 1966-11-28 GB GB53155/66A patent/GB1160258A/en not_active Expired
- 1966-12-02 DE DE19661545224 patent/DE1545224B2/en not_active Withdrawn
- 1966-12-08 FR FR86685A patent/FR1504192A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
USRE31647E (en) * | 1980-03-17 | 1984-08-14 | Mobil Oil Corporation | Startup procedure for reforming catalysts |
Also Published As
Publication number | Publication date |
---|---|
DE1545224A1 (en) | 1969-07-10 |
DE1545224B2 (en) | 1976-04-15 |
US3374167A (en) | 1968-03-19 |
FR1504192A (en) | 1967-12-01 |
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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 |