GB1420248A - Multiple-stage production of low sulphur fuel oil - Google Patents
Multiple-stage production of low sulphur fuel oilInfo
- Publication number
- GB1420248A GB1420248A GB2249373A GB2249373A GB1420248A GB 1420248 A GB1420248 A GB 1420248A GB 2249373 A GB2249373 A GB 2249373A GB 2249373 A GB2249373 A GB 2249373A GB 1420248 A GB1420248 A GB 1420248A
- Authority
- GB
- United Kingdom
- Prior art keywords
- phase
- separated
- oil
- stream
- liquid phase
- 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
- C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
- C10G49/007—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 in the presence of hydrogen from a special source or of a special composition or having been purified by a special treatment
-
- 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
- C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
- C10G49/22—Separation of effluents
-
- 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
- C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
- C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
- C10G65/04—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps
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
1420248 Hydrodesulphurization of heavy oils UOP Inc 11 May 1973 [12 May 1972] 22493/73 Heading C5E A black oil charge stock 1 is catalytically reacted with hydrogen at 3 and the effluent 4 is separated at 5, at substantially the same temperature and pressure, into a first liquid phase 6 and a first vaporous phase 7. Hydrogen sulphide is removed-at 12 from at least a portion 11 of the first vaporous phase to produce a hydrogen-rich stream 13 with which the liquid phase 6 is reacted in a second catalytic reaction zone 14. The effluent 19 from the zone 14 is separated at 20 to produce a second vaporous phase 2, of which at least a portion is recycled to the zone 3, and a second liquid phase 21. As shown the first vaporous phase 7 can be separated at 10 into a third vaporous phase 11 and a third liquid phase 15 from which a vent gas stream is separated at 16 leaving a recycle stream 9 and a product stream 18 comprising mainly heptane to light fuel oil. A water stream 8 can be incorporated in the feed to the second reactor 14 and is recovered from the cold separator 10. The feedstocks treated can be crude oils, atmospheric or vacuum residues, heavy cycle oil, tar sand oil or heavy gas oil. The catalytic hydrogenation in both zones 3 and 20 can be carried out at 200-3000 p.s.i.g. and 600-900 F. using a catalyst, such as Cr, Mo, W or the Group VIII metals as the metal, oxide or sulphide on a support, such as alumina, alumina-silica, mordenite, faujasite or zeolite A or U, which can comprise halogen, zinc and/or bismuth components.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US25278772A | 1972-05-12 | 1972-05-12 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB1420248A true GB1420248A (en) | 1976-01-07 |
Family
ID=22957547
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB2249373A Expired GB1420248A (en) | 1972-05-12 | 1973-05-11 | Multiple-stage production of low sulphur fuel oil |
Country Status (21)
| Country | Link |
|---|---|
| JP (1) | JPS536643B2 (en) |
| AR (1) | AR230292A1 (en) |
| AU (1) | AU475817B2 (en) |
| BR (1) | BR7303460D0 (en) |
| CA (1) | CA1008007A (en) |
| CS (1) | CS178886B2 (en) |
| DK (1) | DK145349C (en) |
| ES (1) | ES414199A1 (en) |
| FI (1) | FI59262C (en) |
| FR (1) | FR2184684B1 (en) |
| GB (1) | GB1420248A (en) |
| HU (1) | HU169802B (en) |
| IL (1) | IL42096A (en) |
| IN (1) | IN140155B (en) |
| NL (1) | NL173657C (en) |
| PH (1) | PH10317A (en) |
| PL (1) | PL89221B1 (en) |
| RO (1) | RO74154A (en) |
| SE (1) | SE395468B (en) |
| SU (1) | SU490295A3 (en) |
| ZA (1) | ZA732760B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2700077C1 (en) * | 2018-05-30 | 2019-09-12 | Публичное акционерное общество "Татнефть" имени В.Д. Шашина | Method of oil cleaning from hydrogen sulphide and installation for implementation thereof |
| RU2790067C1 (en) * | 2022-04-20 | 2023-02-14 | Закрытое акционерное общество "Алойл" | Oil preparation method and desorption column for its implementation |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0128250A1 (en) * | 1983-06-08 | 1984-12-19 | Mobil Oil Corporation | Catalytic dewaxing process |
| JPH01294796A (en) * | 1988-05-23 | 1989-11-28 | Agency Of Ind Science & Technol | Multistage hydrocracking method of fossil fuel oil |
| JPH0391591A (en) * | 1989-09-05 | 1991-04-17 | Cosmo Oil Co Ltd | Hydrotreatment of heavy hydrocarbon oil |
| JPH06299168A (en) * | 1993-02-15 | 1994-10-25 | Shell Internatl Res Maatschappij Bv | Hydrotreatment |
| US5968347A (en) * | 1994-11-25 | 1999-10-19 | Kvaerner Process Technology Limited | Multi-step hydrodesulfurization process |
| FR2940313B1 (en) * | 2008-12-18 | 2011-10-28 | Inst Francais Du Petrole | HYDROCRACKING PROCESS INCLUDING PERMUTABLE REACTORS WITH LOADS CONTAINING 200PPM WEIGHT-2% WEIGHT OF ASPHALTENES |
-
1973
- 1973-04-18 CA CA169,059A patent/CA1008007A/en not_active Expired
- 1973-04-24 ZA ZA732760A patent/ZA732760B/en unknown
- 1973-04-25 IL IL42096A patent/IL42096A/en unknown
- 1973-04-26 IN IN975/CAL/73A patent/IN140155B/en unknown
- 1973-04-28 ES ES414199A patent/ES414199A1/en not_active Expired
- 1973-04-30 AU AU54966/73A patent/AU475817B2/en not_active Expired
- 1973-05-07 NL NLAANVRAGE7306335,A patent/NL173657C/en not_active IP Right Cessation
- 1973-05-08 AR AR247909A patent/AR230292A1/en active
- 1973-05-09 FI FI1483/73A patent/FI59262C/en active
- 1973-05-09 JP JP5083073A patent/JPS536643B2/ja not_active Expired
- 1973-05-10 HU HUUI204A patent/HU169802B/hu unknown
- 1973-05-10 FR FR7316944A patent/FR2184684B1/fr not_active Expired
- 1973-05-10 PL PL1973162457A patent/PL89221B1/pl unknown
- 1973-05-11 SE SE7306688A patent/SE395468B/en unknown
- 1973-05-11 CS CS7300003381A patent/CS178886B2/en unknown
- 1973-05-11 GB GB2249373A patent/GB1420248A/en not_active Expired
- 1973-05-11 PH PH14618A patent/PH10317A/en unknown
- 1973-05-11 SU SU1920833A patent/SU490295A3/en active
- 1973-05-11 DK DK262673A patent/DK145349C/en not_active IP Right Cessation
- 1973-05-11 BR BR3460/73A patent/BR7303460D0/en unknown
- 1973-05-11 RO RO7374750A patent/RO74154A/en unknown
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2700077C1 (en) * | 2018-05-30 | 2019-09-12 | Публичное акционерное общество "Татнефть" имени В.Д. Шашина | Method of oil cleaning from hydrogen sulphide and installation for implementation thereof |
| RU2790067C1 (en) * | 2022-04-20 | 2023-02-14 | Закрытое акционерное общество "Алойл" | Oil preparation method and desorption column for its implementation |
Also Published As
| Publication number | Publication date |
|---|---|
| SE395468B (en) | 1977-08-15 |
| FI59262C (en) | 1981-07-10 |
| PH10317A (en) | 1976-11-25 |
| JPS4961204A (en) | 1974-06-13 |
| ES414199A1 (en) | 1976-02-01 |
| FR2184684A1 (en) | 1973-12-28 |
| DK145349B (en) | 1982-11-01 |
| DK145349C (en) | 1983-05-16 |
| DE2323146B2 (en) | 1977-03-17 |
| IN140155B (en) | 1976-09-18 |
| AR230292A1 (en) | 1984-03-01 |
| BR7303460D0 (en) | 1974-07-18 |
| ZA732760B (en) | 1974-03-27 |
| FI59262B (en) | 1981-03-31 |
| NL173657B (en) | 1983-09-16 |
| AU5496673A (en) | 1974-10-31 |
| CS178886B2 (en) | 1977-10-31 |
| RO74154A (en) | 1981-03-30 |
| DE2323146A1 (en) | 1973-11-22 |
| JPS536643B2 (en) | 1978-03-10 |
| FR2184684B1 (en) | 1978-03-17 |
| NL7306335A (en) | 1973-11-14 |
| PL89221B1 (en) | 1976-11-30 |
| AU475817B2 (en) | 1976-09-02 |
| CA1008007A (en) | 1977-04-05 |
| SU490295A3 (en) | 1975-10-30 |
| IL42096A (en) | 1975-11-25 |
| NL173657C (en) | 1984-02-16 |
| IL42096A0 (en) | 1973-06-29 |
| HU169802B (en) | 1977-02-28 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US3898299A (en) | Production of gaseous olefins from petroleum residue feedstocks | |
| US2952626A (en) | Mixed-phase hydrofining of hydrocarbon oils | |
| US5522983A (en) | Hydrocarbon hydroconversion process | |
| US3114701A (en) | Catalytic hydrodenitrification process | |
| US3532617A (en) | Hydroconversion of coal with combination of catalysts | |
| US3679577A (en) | Molten salt hydrofining process | |
| US3766054A (en) | Demetalation of hydrocarbon charge stocks | |
| GB1437527A (en) | Conversion of black oil to low-sulphur fuel oil | |
| US3932269A (en) | Hydrogenation of hydrocarbon residuum | |
| GB1420248A (en) | Multiple-stage production of low sulphur fuel oil | |
| US3472759A (en) | Process for removal of sulfur and metals from petroleum materials | |
| KR19990022632A (en) | Reverse Step Method in Hydroprocessing Reactor System | |
| GB913571A (en) | Hydroconversion of hydrocarbons | |
| US3011971A (en) | Hydrodesulfurizing dissimilar hydrocarbons | |
| US3094481A (en) | Hydrofining process with temperature control | |
| US3172836A (en) | Hydrocarbon conversion process | |
| US3691063A (en) | Residual fuel oil hydrocracking process | |
| US2370707A (en) | Treatment of hydrocarbons | |
| GB1323257A (en) | Catalytic hydrogen contact process | |
| GB1435350A (en) | Desulphurization and hydrogenative conversion of black oils | |
| US2865841A (en) | Hydrocracking with a catalyst comprising aluminum, or aluminum chloride, titanium tetrachloride, and hydrogen chloride | |
| US3248317A (en) | Combination of hydrogen producing and hydrogen consuming units | |
| GB1404170A (en) | Multiple stage production of fuel oil | |
| Mochida et al. | Hydrodesulfurization of petroleum coke deposited on iron ores | |
| US1990708A (en) | Production of valuable hydrocarbons |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PS | Patent sealed [section 19, patents act 1949] | ||
| PCNP | Patent ceased through non-payment of renewal fee |