ES8401122A1 - A combination process for upgrading residual oils. - Google Patents
A combination process for upgrading residual oils.Info
- Publication number
- ES8401122A1 ES8401122A1 ES512277A ES512277A ES8401122A1 ES 8401122 A1 ES8401122 A1 ES 8401122A1 ES 512277 A ES512277 A ES 512277A ES 512277 A ES512277 A ES 512277A ES 8401122 A1 ES8401122 A1 ES 8401122A1
- Authority
- ES
- Spain
- Prior art keywords
- visbreaking
- high boiling
- combination process
- processing
- fluidized
- 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
- 238000000034 method Methods 0.000 title abstract 2
- 239000003921 oil Substances 0.000 title abstract 2
- 238000009835 boiling Methods 0.000 abstract 3
- 239000000356 contaminant Substances 0.000 abstract 3
- 239000002184 metal Substances 0.000 abstract 3
- 239000007787 solid Substances 0.000 abstract 3
- 229910021536 Zeolite Inorganic materials 0.000 abstract 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 abstract 2
- 239000010457 zeolite Substances 0.000 abstract 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract 1
- 229910052799 carbon Inorganic materials 0.000 abstract 1
- 239000003054 catalyst Substances 0.000 abstract 1
- 238000004523 catalytic cracking Methods 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 abstract 1
- 150000001875 compounds Chemical class 0.000 abstract 1
- 238000005336 cracking Methods 0.000 abstract 1
- 239000003546 flue gas Substances 0.000 abstract 1
- 239000007789 gas Substances 0.000 abstract 1
- 239000011159 matrix material Substances 0.000 abstract 1
- 238000011027 product recovery Methods 0.000 abstract 1
- 230000001172 regenerating effect Effects 0.000 abstract 1
- 238000000926 separation method Methods 0.000 abstract 1
- 239000002594 sorbent Substances 0.000 abstract 1
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
- C10G51/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only
- C10G51/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only
- C10G51/04—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only including only thermal and catalytic cracking steps
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (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)
- Fats And Perfumes (AREA)
- Catalysts (AREA)
Abstract
A combination process is described for upgrading residual oils (2) and high boiling portions thereof comprising metal contaminants and high boiling Conradson carbon forming compounds comprising a thermal visbreaking operation (7) with fluidizable inert solids followed by a fluidized zeolite catalytic cracking operation 12 processing demetallized products (8) (10) of the visbreaking operation, regenerating solid particulate of each operation under conditions to provide CO rich flue gases relied upon to generate steam used in each of the fluidized solids conversion operation and downstream product separation arrangements, separating the wet gas product stream of each operation in a common product recovery arrangement (22) and processing the high boiling feed product of visbreaking comprising up to 100 ppm Ni + V metal contaminant over a recycled crystalline zeolite cracking catalyst distributed in a sorbent matrix material comprising a high lever of Ni + V metal contaminant.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/US1981/000648 WO1982004062A1 (en) | 1981-05-13 | 1981-05-13 | A combination process for upgrading residual oils |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| ES512277A0 ES512277A0 (en) | 1983-11-16 |
| ES8401122A1 true ES8401122A1 (en) | 1983-11-16 |
Family
ID=22161226
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ES512277A Expired ES8401122A1 (en) | 1981-05-13 | 1982-05-13 | A combination process for upgrading residual oils. |
Country Status (8)
| Country | Link |
|---|---|
| EP (2) | EP0078797A1 (en) |
| AU (2) | AU549952B2 (en) |
| CA (1) | CA1185914A (en) |
| DE (1) | DE3267379D1 (en) |
| ES (1) | ES8401122A1 (en) |
| IL (1) | IL67653A (en) |
| MX (1) | MX160803A (en) |
| WO (1) | WO1982004062A1 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4569753A (en) * | 1981-09-01 | 1986-02-11 | Ashland Oil, Inc. | Oil upgrading by thermal and catalytic cracking |
| RU2518481C1 (en) * | 2013-05-21 | 2014-06-10 | Открытое акционерное общество "Всероссийский научно-исследовательский институт по переработке нефти" (ОАО "ВНИИ НП") | Method of obtaining high-octane base gasoline |
| CN112604718B (en) * | 2020-12-24 | 2022-06-24 | 新疆大全新能源股份有限公司 | A kind of recovery process of residual liquid in high-boiling cracking reaction |
Family Cites Families (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2526881A (en) * | 1948-05-17 | 1950-10-24 | Shell Dev | Catalytic conversion of hydrocarbons to produce alkyl naphthalenes |
| US2688401A (en) * | 1949-09-29 | 1954-09-07 | Standard Oil Co | Flotation of active catalyst from spent catalyst |
| US2766184A (en) * | 1952-02-01 | 1956-10-09 | Exxon Research Engineering Co | Combination oil refining process |
| FR1363813A (en) * | 1963-07-22 | 1964-06-12 | Shell Int Research | Method and apparatus for recovering energy from waste gases from a catalytic cracking unit |
| US3303123A (en) * | 1964-10-16 | 1967-02-07 | Phillips Petroleum Co | Catalytic cracking of residuum oils containing metal contaminants in several stages |
| US3767566A (en) * | 1970-01-26 | 1973-10-23 | Standard Oil Co | Catalytic petroleum conversion process |
| US3763034A (en) * | 1972-02-03 | 1973-10-02 | Exxon Research Engineering Co | Process for the preparation of high octane gasoline fractions |
| CA1093050A (en) * | 1975-12-19 | 1981-01-06 | Iacovos A. Vasalos | Catalytic cracking with reduced emission of noxious gases |
| US4200520A (en) * | 1978-01-30 | 1980-04-29 | Exxon Research & Engineering Co. | Catalytic cracking process |
| US4263128A (en) * | 1978-02-06 | 1981-04-21 | Engelhard Minerals & Chemicals Corporation | Upgrading petroleum and residual fractions thereof |
| CA1127581A (en) * | 1978-02-06 | 1982-07-13 | David B. Bartholic | Preparation of fcc charge from residual fractions |
| US4243514A (en) * | 1979-05-14 | 1981-01-06 | Engelhard Minerals & Chemicals Corporation | Preparation of FCC charge from residual fractions |
| US4274942A (en) * | 1979-04-04 | 1981-06-23 | Engelhard Minerals & Chemicals Corporation | Control of emissions in FCC regenerator flue gas |
| US4260475A (en) * | 1979-11-01 | 1981-04-07 | Chevron Research Company | Hydrocarbon cracking process |
| US4276150A (en) * | 1979-11-05 | 1981-06-30 | Standard Oil Company (Indiana) | Fluid catalytic cracking of heavy petroleum fractions |
-
1981
- 1981-05-13 AU AU74121/81A patent/AU549952B2/en not_active Ceased
- 1981-05-13 MX MX191998A patent/MX160803A/en unknown
- 1981-05-13 EP EP81901837A patent/EP0078797A1/en not_active Withdrawn
- 1981-05-13 WO PCT/US1981/000648 patent/WO1982004062A1/en not_active Ceased
-
1982
- 1982-05-12 DE DE8282302428T patent/DE3267379D1/en not_active Expired
- 1982-05-12 EP EP82302428A patent/EP0066387B1/en not_active Expired
- 1982-05-13 ES ES512277A patent/ES8401122A1/en not_active Expired
- 1982-05-13 CA CA000402926A patent/CA1185914A/en not_active Expired
-
1983
- 1983-01-10 IL IL67653A patent/IL67653A/en unknown
-
1985
- 1985-12-17 AU AU51374/85A patent/AU568964B2/en not_active Ceased
Also Published As
| Publication number | Publication date |
|---|---|
| ES512277A0 (en) | 1983-11-16 |
| CA1185914A (en) | 1985-04-23 |
| IL67653A (en) | 1986-07-31 |
| EP0066387A1 (en) | 1982-12-08 |
| EP0066387B1 (en) | 1985-11-13 |
| WO1982004062A1 (en) | 1982-11-25 |
| DE3267379D1 (en) | 1985-12-19 |
| AU549952B2 (en) | 1986-02-20 |
| MX160803A (en) | 1990-05-25 |
| AU7412181A (en) | 1982-12-07 |
| AU568964B2 (en) | 1988-01-14 |
| AU5137485A (en) | 1986-04-17 |
| EP0078797A1 (en) | 1983-05-18 |
| IL67653A0 (en) | 1983-05-15 |
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