GR34311B - METHOD FOR THE PRODUCTION OF GASOLINE. - Google Patents
METHOD FOR THE PRODUCTION OF GASOLINE.Info
- Publication number
- GR34311B GR34311B GR670134311A GR670134311A GR34311B GR 34311 B GR34311 B GR 34311B GR 670134311 A GR670134311 A GR 670134311A GR 670134311 A GR670134311 A GR 670134311A GR 34311 B GR34311 B GR 34311B
- Authority
- GR
- Greece
- Prior art keywords
- gasoline
- aromatics
- recovery
- boiling point
- hydrogen
- Prior art date
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
-
- 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
- C10G69/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process
- C10G69/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only
- C10G69/04—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one step of catalytic cracking in the absence of hydrogen
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)
- Lift Valve (AREA)
- Mechanically-Actuated Valves (AREA)
- Catalysts (AREA)
Abstract
ία μέθοδος διά την παραγωγήν βενζίνης υψηλού οκτανίου από μίαν τροφοδοσίαν πυριμάχου πετρελαίου έχοντος μέσον όρον σημείου ζέσεως υπεράνω της περιοχής ζέσεως της βενζίνης και κάτω της περιοχής ζέσεωςτου βαρέος πετρελαίου του κύκλου και περιέχοντοςτουλάχιστον 45 όγκους τοις εκατόν αρωματικών εκ τωνοποίων ο μεγαλύτερος απλούς αρωματικός τύπος είναι J-12, χαρακτηριζομένη από: α) κατεργασίαν με υδρογόνον του ειρημένου πυριμάχου πετρελαίου παρουσία ενός καταλύτο β) ανάκτησιν του παραγομένου κανονικώς υγρού, κατειργασμένου με υδρογόνον προϊόντος περιέχοντος κατ' ελάχιστον 40 όγκους τοις εκατόν αρωματικά τις τα οποία ο μεγαλύτερος απλούς τύπος αρωματικού είναι J- γ) πυρόλυσιν μέρους τουλάχιστοντου υδρογονοκατειργασμένουπροϊόντοςπαρουσία ενός καταλύτου της πυρολύσεω δ) ανάκτησιν από το εκ τηςπυρολύσεως παραγόμενον προϊόν μιας βενζίνης εχούσης ένα F-I αριθμόν καθαρών οκτανίων τουλάχιστον 95και περιεχούσης τουλάχιστον 45 τοις εκατόν κατ' όγκον αρωματικά από τα οποία ο μεγαλύτερος απλούς αρωματικός τύπος είναι J- ε) και την κεχωρισμένων ανάκτησιν από του πυρολυθέντος προϊόντος ενός δευτέρου πυριμάχου πετρελαίου έχοντος ένα μέσον όρον σημείου ζέσεως υπεράνω της περιοχής ζέσεως της βενζίνης και περιέχοντος το J-12 ως τον μεγαλύτερον απλούν αρωματικόν τύποA process for producing high-octane gasoline from a refractory oil supply having an average boiling point above the gasoline boiling zone and below the heavy cycle boiling zone of the cycle and containing at least 45 volumes of aromatics greater than one hundred 12, characterized by: (a) hydrogen treatment of said refractory oil in the presence of a catalyst (b) recovery of the normally produced, hydrogen-treated product containing at least 40 per cent by volume of aromatics of which the largest simple aromatic type is J; (c) cracking of at least part of a hydrogen-treated product in the presence of a cracking catalyst (d) recovery from the cracked product of a petrol having an F-I number of pure octane of at least 95 and containing at least 45 per cent by volume of aromatics, of which the largest simple aromatic formula is J; (e) and the separated recovery from the cracked product of a second refractory oil having an average boiling point above the boiling point of gasoline and containing J-12 as the largest single aromatic type
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US57421466A | 1966-08-22 | 1966-08-22 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GR34311B true GR34311B (en) | 1968-04-15 |
Family
ID=24295173
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GR670134311A GR34311B (en) | 1966-08-22 | 1967-08-16 | METHOD FOR THE PRODUCTION OF GASOLINE. |
Country Status (17)
| Country | Link |
|---|---|
| US (1) | US3479279A (en) |
| AT (1) | AT285006B (en) |
| BE (1) | BE710004A (en) |
| BR (1) | BR6792376D0 (en) |
| CH (1) | CH505885A (en) |
| DE (1) | DE1645822B1 (en) |
| DK (1) | DK128284B (en) |
| ES (1) | ES344256A1 (en) |
| FI (1) | FI48609C (en) |
| GB (1) | GB1188692A (en) |
| GR (1) | GR34311B (en) |
| IL (1) | IL28518A (en) |
| NL (1) | NL6711527A (en) |
| NO (1) | NO120152B (en) |
| OA (1) | OA02489A (en) |
| SE (1) | SE341435B (en) |
| YU (1) | YU33885B (en) |
Families Citing this family (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2726222B2 (en) * | 1977-06-10 | 1980-02-07 | Reinhard Mohn Gmbh, 4830 Guetersloh | Method and device for drying paints, varnishes or adhesives on print carriers, in particular on print carriers made of paper or cardboard |
| US4372841A (en) * | 1979-12-31 | 1983-02-08 | Exxon Research And Engineering Co. | Process for reducing coke formation in heavy feed catalytic cracking |
| US4370220A (en) * | 1979-12-31 | 1983-01-25 | Exxon Research And Engineering Co. | Process for reducing coke formation in heavy feed catalytic cracking |
| US4372840A (en) * | 1979-12-31 | 1983-02-08 | Exxon Research And Engineering Co. | Process for reducing coke formation in heavy feed catalytic cracking |
| US4409093A (en) * | 1981-05-04 | 1983-10-11 | Exxon Research And Engineering Co. | Process for reducing coke formation in heavy feed catalytic cracking |
| EP0066018B1 (en) * | 1981-06-01 | 1986-03-12 | Exxon Research And Engineering Company | Method of reducing coke formation in heavy hydrocarbon feed catalytic cracking |
| US4504380A (en) * | 1983-08-23 | 1985-03-12 | Exxon Research And Engineering Co. | Passivation of metal contaminants in cat cracking |
| US5770043A (en) * | 1994-08-17 | 1998-06-23 | Exxon Research And Engineering Company | Integrated staged catalytic cracking and hydroprocessing process |
| US5770044A (en) * | 1994-08-17 | 1998-06-23 | Exxon Research And Engineering Company | Integrated staged catalytic cracking and hydroprocessing process (JHT-9614) |
| US20010042701A1 (en) | 2000-04-17 | 2001-11-22 | Stuntz Gordon F. | Cycle oil conversion process |
| US6565739B2 (en) * | 2000-04-17 | 2003-05-20 | Exxonmobil Research And Engineering Company | Two stage FCC process incorporating interstage hydroprocessing |
| US20010042700A1 (en) * | 2000-04-17 | 2001-11-22 | Swan, George A. | Naphtha and cycle oil conversion process |
| US6569315B2 (en) * | 2000-04-17 | 2003-05-27 | Exxonmobil Research And Engineering Company | Cycle oil conversion process |
| US6569316B2 (en) | 2000-04-17 | 2003-05-27 | Exxonmobil Research And Engineering Company | Cycle oil conversion process incorporating shape-selective zeolite catalysts |
| US20010042702A1 (en) | 2000-04-17 | 2001-11-22 | Stuntz Gordon F. | Cycle oil conversion process |
| BRPI1012237A2 (en) * | 2009-03-27 | 2016-03-29 | Jx Nippon Oil & Energy Corp | method for the production of aromatic hydrocarbons |
| US20170241308A1 (en) * | 2016-02-24 | 2017-08-24 | Ford Global Technologies, Llc | Oil maintenance strategy for electrified vehicles |
Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2370533A (en) * | 1942-11-23 | 1945-02-27 | Shell Dev | Cracking and reforming of hydrocarbons |
| US2431243A (en) * | 1946-12-02 | 1947-11-18 | Shell Dev | Conversion of hydrocarbon oils |
| FR1320310A (en) * | 1960-04-25 | 1963-03-08 | Universal Oil Prod Co | Process for converting hydrocarbon oils |
| US3168461A (en) * | 1960-11-10 | 1965-02-02 | Sinclair Research Inc | Catalytic cracking of mineral hydrocarbon oil |
| GB1009102A (en) * | 1961-12-23 | 1965-11-03 | British Petroleum Co | Improvements relating to the alkylation of alkanes with olefins |
| US3204006A (en) * | 1962-05-14 | 1965-08-31 | Universal Oil Prod Co | Hydrotreatment of hydrocarbon stocks and separation of aromatic components |
| US3203889A (en) * | 1962-11-01 | 1965-08-31 | Universal Oil Prod Co | Catalytic hydrocracking process with the preliminary hydrogenation of the aromatic containing feed oil |
| US3219574A (en) * | 1963-09-03 | 1965-11-23 | Sun Oil Co | Conversion of catalytic gas oil to lower boiling hydrocarbons |
| US3245900A (en) * | 1963-12-26 | 1966-04-12 | Chevron Res | Hydrocarbon conversion process |
-
1966
- 1966-08-22 US US574214A patent/US3479279A/en not_active Expired - Lifetime
-
1967
- 1967-08-16 GR GR670134311A patent/GR34311B/en unknown
- 1967-08-17 IL IL28518A patent/IL28518A/en unknown
- 1967-08-18 AT AT763367A patent/AT285006B/en not_active IP Right Cessation
- 1967-08-19 ES ES344256A patent/ES344256A1/en not_active Expired
- 1967-08-19 DE DE1967U0014166 patent/DE1645822B1/en active Pending
- 1967-08-21 OA OA53033A patent/OA02489A/en unknown
- 1967-08-21 SE SE11675/67A patent/SE341435B/xx unknown
- 1967-08-21 DK DK422667AA patent/DK128284B/en unknown
- 1967-08-21 NO NO169438A patent/NO120152B/no unknown
- 1967-08-21 GB GB38413/67A patent/GB1188692A/en not_active Expired
- 1967-08-22 NL NL6711527A patent/NL6711527A/xx unknown
- 1967-08-22 CH CH1175967A patent/CH505885A/en not_active IP Right Cessation
- 1967-08-22 FI FI672254A patent/FI48609C/en active
- 1967-08-22 BR BR192376/67A patent/BR6792376D0/en unknown
- 1967-08-22 YU YU1649/67A patent/YU33885B/en unknown
-
1968
- 1968-01-29 BE BE710004D patent/BE710004A/xx unknown
Also Published As
| Publication number | Publication date |
|---|---|
| DK128284B (en) | 1974-04-01 |
| NO120152B (en) | 1970-09-07 |
| FI48609C (en) | 1974-11-11 |
| CH505885A (en) | 1971-04-15 |
| NL6711527A (en) | 1968-02-23 |
| IL28518A (en) | 1971-01-28 |
| DE1645822B1 (en) | 1972-05-31 |
| GB1188692A (en) | 1970-04-22 |
| AT285006B (en) | 1970-10-12 |
| BR6792376D0 (en) | 1973-12-26 |
| YU164967A (en) | 1977-12-31 |
| BE710004A (en) | 1968-05-30 |
| OA02489A (en) | 1970-05-05 |
| SE341435B (en) | 1971-12-27 |
| US3479279A (en) | 1969-11-18 |
| FI48609B (en) | 1974-07-31 |
| ES344256A1 (en) | 1968-09-16 |
| YU33885B (en) | 1978-06-30 |
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