GB1338612A - Aromatic gasoline production - Google Patents
Aromatic gasoline productionInfo
- Publication number
- GB1338612A GB1338612A GB5968970A GB5968970A GB1338612A GB 1338612 A GB1338612 A GB 1338612A GB 5968970 A GB5968970 A GB 5968970A GB 5968970 A GB5968970 A GB 5968970A GB 1338612 A GB1338612 A GB 1338612A
- Authority
- GB
- United Kingdom
- Prior art keywords
- stream
- gasoline
- hydrocarbons
- reforming
- line
- 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- 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
- 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
- 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
- C10G63/00—Treatment of naphtha by at least one reforming process and at least one other conversion process
- C10G63/02—Treatment of naphtha by at least one reforming process and at least one other conversion process plural serial stages only
- C10G63/04—Treatment of naphtha by at least one reforming process and at least one other conversion process plural serial stages only including at least one cracking 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L1/00—Liquid carbonaceous fuels
-
- 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/02—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
- C10L1/023—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only 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
1338612 Cracking and reforming naphtha UNIVERSAL OIL PRODUCTS CO 16 Dec 1970 [17 Dec 1969] 59689/70 Heading C5E An aromatic gasoline and saturated and unsaturated hydrocarbons having three or four carbon atoms in the molecule are made from a feedstock comprising both alkanes and naphthenes boiling in the range 82 to 204 C. by first reforming the feed under conditions to convert more than 80% of the naphthenes but less than 40% of the alkanes to aromatics, then separating the product into an aromatic gasoline stream and a saturated hydrocarbon stream by solvent extraction and finally cracking the saturated stream in a fluidized bed of catalyst without added hydrogen. The hydrocarbons of three or four carbon atoms may be used to make alkylate gasoline, or hydrolysed to alcohols or converted to amines, esters, ethers or ketones, all of which can be used as gasoline components. Suitable feedstocks are straight-run gasoline, natural gasolines, and thermally or catalytically cracked gasolines, and may be of full boiling range, or higher-boiling fractions only. Catalysts for the reforming step comprise carriers such as alumina, faujasite, mordenite or combinations of these and a reactive metal component such as Fe, Co, Ni, Ru, Rh, Pd, Os, Ir, Pt or Re and may also contain a combined halogen. The catalyst may be fluidized or otherwise moving, but is preferably in a fixed bed. Catalysts for the cracking step are silica-alumina, silica-magnesia, silica-zirconia and zeolites, natural or synthetic, and may be compounded by ion-exchange or impregnation with alkali metals, alkaline-earth metals, rare-earth metals or metals of Group VIII. As shown, feed in line 20 and hydrogen in line 21 pass to reforming at 15. The reformate is fractionated at 16 to give a hydrogen-rich gas stream 23, a stream 24 of hydrocarbons up to C 4 , a stream 25 of C 5 and C 6 hydrocarbons and a stream 26 of heavier hydrocarbons. Stream 26 is or streams 25 and 26 are extracted by a solvent at 17, and the aromatic extract taken off at 28. The raffinate in line 27 is cracked at 18 and fractionated at 19 to give cracked gasoline 31 and light hydrocarbons (C 3 and C 4 ) 30. The cracked gasoline can be recycled by line 33.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US88585969A | 1969-12-17 | 1969-12-17 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB1338612A true GB1338612A (en) | 1973-11-28 |
Family
ID=25387844
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB5968970A Expired GB1338612A (en) | 1969-12-17 | 1970-12-16 | Aromatic gasoline production |
Country Status (16)
| Country | Link |
|---|---|
| US (1) | US3714023A (en) |
| AR (1) | AR212954A1 (en) |
| CA (1) | CA943484A (en) |
| CS (1) | CS153570B2 (en) |
| DE (1) | DE2061945C3 (en) |
| DK (1) | DK137765B (en) |
| EG (1) | EG10506A (en) |
| ES (1) | ES386517A1 (en) |
| FR (1) | FR2070902B1 (en) |
| GB (1) | GB1338612A (en) |
| IL (1) | IL35865A (en) |
| NL (1) | NL7018328A (en) |
| PL (1) | PL81513B1 (en) |
| TR (1) | TR17194A (en) |
| YU (1) | YU35270B (en) |
| ZA (1) | ZA708450B (en) |
Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3650943A (en) * | 1970-07-10 | 1972-03-21 | Universal Oil Prod Co | High octane unleaded gasoline production |
| US3873439A (en) * | 1973-02-26 | 1975-03-25 | Universal Oil Prod Co | Process for the simultaneous production of an aromatic concentrate and isobutane |
| US3928175A (en) * | 1973-05-24 | 1975-12-23 | Mobil Oil Corp | Upgrading crude oil by combination processing |
| US4067798A (en) * | 1976-02-26 | 1978-01-10 | Standard Oil Company (Indiana) | Catalytic cracking process |
| US4053388A (en) * | 1976-12-06 | 1977-10-11 | Moore-Mccormack Energy, Inc. | Process for preparing aromatics from naphtha |
| US5292976A (en) * | 1993-04-27 | 1994-03-08 | Mobil Oil Corporation | Process for the selective conversion of naphtha to aromatics and olefins |
| KR102723620B1 (en) | 2018-01-08 | 2024-10-31 | 스위프트 퓨얼스, 엘엘씨 | Method for improving gasoline octane for long-chain paraffin feed streams |
| US10941357B2 (en) | 2018-04-16 | 2021-03-09 | Swift Fuels, Llc | Process for converting C2—C5 hydrocarbons to gasoline and diesel fuel blendstocks |
| CA3179173A1 (en) | 2020-03-31 | 2021-10-07 | Chris D'acosta | Process for converting c2-c5 hydrocarbons to gasoline and diesel fuel blendstocks |
| US11965136B2 (en) * | 2021-01-15 | 2024-04-23 | Saudi Arabian Oil Company | Cyclization and fluid catalytic cracking systems and methods for upgrading naphtha |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2908629A (en) * | 1955-05-31 | 1959-10-13 | Sun Oil Co | High octane gasoline manufacture |
| US3060116A (en) * | 1959-11-06 | 1962-10-23 | Socony Mobil Oil Co Inc | Combination reforming and cracking process |
-
1969
- 1969-12-17 US US00885859A patent/US3714023A/en not_active Expired - Lifetime
-
1970
- 1970-12-14 ZA ZA708450A patent/ZA708450B/en unknown
- 1970-12-15 EG EG529/70A patent/EG10506A/en active
- 1970-12-15 YU YU3060/70A patent/YU35270B/en unknown
- 1970-12-16 PL PL1970145034A patent/PL81513B1/pl unknown
- 1970-12-16 DK DK639570AA patent/DK137765B/en unknown
- 1970-12-16 IL IL35865A patent/IL35865A/en unknown
- 1970-12-16 TR TR17194A patent/TR17194A/en unknown
- 1970-12-16 GB GB5968970A patent/GB1338612A/en not_active Expired
- 1970-12-16 ES ES386517A patent/ES386517A1/en not_active Expired
- 1970-12-16 NL NL7018328A patent/NL7018328A/xx not_active Application Discontinuation
- 1970-12-16 DE DE2061945A patent/DE2061945C3/en not_active Expired
- 1970-12-16 CA CA100,822A patent/CA943484A/en not_active Expired
- 1970-12-16 CS CS850470A patent/CS153570B2/cs unknown
- 1970-12-17 FR FR7045554A patent/FR2070902B1/fr not_active Expired
- 1970-12-17 AR AR233025A patent/AR212954A1/en active
Also Published As
| Publication number | Publication date |
|---|---|
| IL35865A0 (en) | 1971-02-25 |
| DE2061945A1 (en) | 1971-06-24 |
| ES386517A1 (en) | 1973-03-16 |
| FR2070902B1 (en) | 1973-12-07 |
| ZA708450B (en) | 1971-11-24 |
| CA943484A (en) | 1974-03-12 |
| DK137765C (en) | 1978-10-09 |
| CS153570B2 (en) | 1974-02-25 |
| YU35270B (en) | 1980-10-31 |
| US3714023A (en) | 1973-01-30 |
| IL35865A (en) | 1973-11-28 |
| DE2061945B2 (en) | 1973-11-29 |
| DE2061945C3 (en) | 1974-06-27 |
| AR212954A1 (en) | 1978-11-30 |
| FR2070902A1 (en) | 1971-09-17 |
| PL81513B1 (en) | 1975-08-30 |
| YU306070A (en) | 1980-04-30 |
| EG10506A (en) | 1977-03-31 |
| DK137765B (en) | 1978-05-01 |
| TR17194A (en) | 1974-04-25 |
| NL7018328A (en) | 1971-06-21 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US2380279A (en) | Production of aromatics | |
| US2910426A (en) | Process for producing high energy fuels | |
| US11427773B2 (en) | Catalytic cracking process for producing isobutane and/or light aromatics in high yield | |
| US2289716A (en) | Catalytic motor fuel production | |
| JP7248400B2 (en) | A catalytic cracking process that produces a large amount of gasoline with a low olefin content and a high octane number | |
| GB1383229A (en) | Production of gaseous olefins from petroleum residue feedstocks | |
| US11807818B2 (en) | Integrated FCC and aromatic recovery complex to boost BTX and light olefin production | |
| US4192734A (en) | Production of high quality fuel oils | |
| GB1338612A (en) | Aromatic gasoline production | |
| CN109705913B (en) | A method and system for producing high-octane gasoline and light olefins | |
| US3719586A (en) | Naphtha conversion process including hydrocracking and hydroreforming | |
| US2352025A (en) | Conversion of hydrocarbon oils | |
| US2429875A (en) | Production of gasoline and diesel fuel by catalytic cracking and solvent extraction | |
| US3799864A (en) | Fluid catalytic cracking process | |
| US2242504A (en) | Catalytic conversion of hydrocarbons | |
| JPH0649869B2 (en) | Catalytic cracking method for paraffinic raw materials with zeolite beta | |
| GB766404A (en) | A process for the production of gasoline and related lighter products by means of hydrogenation and catalytic cracking | |
| US2304187A (en) | Manufacture of balanced motor fuel and aviation safety fuel | |
| CA3016531A1 (en) | Method and catalyst for producing high octane components | |
| US5314612A (en) | Fluid catalytic cracking process for producing low emissions fuels | |
| JPH05222382A (en) | Method for improving the quality of hydrocarbonaceous feedstocks and apparatus for use therein | |
| CN109679680B (en) | Catalytic conversion method of light distillate oil | |
| US2974099A (en) | Catalytic conversion of heavy naphtha fractions | |
| US2252928A (en) | Hydrocarbon conversion | |
| CN105622316B (en) | A kind of method for transformation of Fischer-Tropsch synthesis oil raw material |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PS | Patent sealed [section 19, patents act 1949] | ||
| PCNP | Patent ceased through non-payment of renewal fee |