ES372921A1 - Conversion and desulfurization of hydrocarbonaceous black oils - Google Patents
Conversion and desulfurization of hydrocarbonaceous black oilsInfo
- Publication number
- ES372921A1 ES372921A1 ES372921A ES372921A ES372921A1 ES 372921 A1 ES372921 A1 ES 372921A1 ES 372921 A ES372921 A ES 372921A ES 372921 A ES372921 A ES 372921A ES 372921 A1 ES372921 A1 ES 372921A1
- Authority
- ES
- Spain
- Prior art keywords
- zone
- reaction zone
- liquid phase
- catalytic reaction
- originate
- 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
- 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
- C10G69/06—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 thermal cracking in the absence of hydrogen
-
- 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
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)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
A process for the conversion and desulfurization of a hydrocarbon, sulphidated filler material of which at least about 10.0% boils above a temperature of about 566ºC to give low-boiling hydrocarbon products, the process comprising : a) heating said charge to a temperature between approximately 260 and 399ºC; b) contacting said heated filler material with a catalytic compound in a catalytic reaction zone, and reacting therein said filler material with hydrogen at a pressure greater than 68 gauge atmospheres; c) separating the resulting effluent from the reaction zone in a first separation zone, at substantially the same pressure as that maintained in said catalytic reaction zone, to originate a first vapor phase and a first liquid phase; d) separating the first vapor phase in the second separation zone urn, at substantially the same pressure as that maintained in said first separation zone, to originate a second hydrogen-rich vapor phase and a second liquid phase; e) fractionating at least a portion of said first liquid phase in a non-catalytic reaction zone; f) introducing the effluent resulting from said non-catalytic reaction zone into a fractionation zone; g) extracting from said fractionation zone a heavy hydrocarbon stream boiling substantially above a temperature of about 343ºC, and introducing said stream into a third separation zone; and h) separating said heavy hydrocarbon stream therein, at a reduced pressure comprised between a sub-atmospheric pressure and about 3.4 gauge atmospheres, to originate a third liquid phase containing distilled hydrocarbons and a residue concentrate. (Machine-translation by Google Translate, not legally binding)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US77124868A | 1968-10-28 | 1968-10-28 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| ES372921A1 true ES372921A1 (en) | 1971-11-16 |
Family
ID=25091198
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ES372921A Expired ES372921A1 (en) | 1968-10-28 | 1969-10-27 | Conversion and desulfurization of hydrocarbonaceous black oils |
Country Status (14)
| Country | Link |
|---|---|
| US (1) | US3594309A (en) |
| JP (1) | JPS4830441B1 (en) |
| AT (1) | AT303941B (en) |
| BR (1) | BR6913678D0 (en) |
| CS (1) | CS166719B2 (en) |
| DK (1) | DK133474B (en) |
| ES (1) | ES372921A1 (en) |
| FR (1) | FR2021705A1 (en) |
| GB (1) | GB1276864A (en) |
| NL (1) | NL6916218A (en) |
| NO (1) | NO126919B (en) |
| OA (1) | OA03157A (en) |
| SE (1) | SE369197B (en) |
| SU (1) | SU374838A3 (en) |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4606812A (en) * | 1980-04-15 | 1986-08-19 | Chemroll Enterprises, Inc. | Hydrotreating of carbonaceous materials |
| US4446004A (en) * | 1982-12-23 | 1984-05-01 | Mobil Oil Corporation | Process for upgrading vacuum resids to premium liquid products |
| US4604185A (en) * | 1985-07-02 | 1986-08-05 | Conoco Inc. | Co-processing of straight run vacuum resid and cracked residua |
| US4661238A (en) * | 1985-09-05 | 1987-04-28 | Uop Inc. | Combination process for the conversion of a distillate hydrocarbon to maximize middle distillate production |
| US4721557A (en) * | 1986-10-08 | 1988-01-26 | Uop Inc. | Combination process for the conversion of a residual asphaltene-containing hydrocarbonaceous stream to maximize middle distillate production |
| US4715947A (en) * | 1986-11-24 | 1987-12-29 | Uop Inc. | Combination process for the conversion of a residual asphaltene-containing hydrocarbonaceous stream to maximize middle distillate production |
| US4792390A (en) * | 1987-09-21 | 1988-12-20 | Uop Inc. | Combination process for the conversion of a distillate hydrocarbon to produce middle distillate product |
| US4961839A (en) * | 1988-05-23 | 1990-10-09 | Uop | High conversion hydrocracking process |
| US7938953B2 (en) * | 2008-05-20 | 2011-05-10 | Institute Francais Du Petrole | Selective heavy gas oil recycle for optimal integration of heavy oil conversion and vacuum gas oil treating |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR659583A (en) * | 1927-09-01 | 1929-07-01 | Ig Farbenindustrie Ag | Process for the production of high value hydrocarbons |
| FR1313068A (en) * | 1959-06-04 | 1962-12-28 | Inst Francais Du Petrole | Continuous process of hydrotreating petroleum products |
| FR1386576A (en) * | 1963-07-02 | 1965-01-22 | Gulf Research Development Co | Process for treating a mixture of hydrocarbons |
| US3324028A (en) * | 1964-04-22 | 1967-06-06 | Gulf Research Development Co | Preparation of low sulfur content heavy fuel oils |
| US3371029A (en) * | 1966-11-30 | 1968-02-27 | Universal Oil Prod Co | Mixed-phase conversion product separation process |
| US3371030A (en) * | 1966-12-30 | 1968-02-27 | Universal Oil Prod Co | Black oil conversion product separation process |
-
1968
- 1968-10-28 US US771248A patent/US3594309A/en not_active Expired - Lifetime
-
1969
- 1969-10-21 GB GB51469/69A patent/GB1276864A/en not_active Expired
- 1969-10-27 DK DK567769AA patent/DK133474B/en unknown
- 1969-10-27 BR BR213678/69A patent/BR6913678D0/en unknown
- 1969-10-27 FR FR6936720A patent/FR2021705A1/fr not_active Withdrawn
- 1969-10-27 SE SE14655/69A patent/SE369197B/xx unknown
- 1969-10-27 ES ES372921A patent/ES372921A1/en not_active Expired
- 1969-10-27 NO NO04237/69A patent/NO126919B/no unknown
- 1969-10-28 AT AT1016369A patent/AT303941B/en not_active IP Right Cessation
- 1969-10-28 OA OA53765A patent/OA03157A/en unknown
- 1969-10-28 NL NL6916218A patent/NL6916218A/xx unknown
- 1969-10-28 JP JP44085774A patent/JPS4830441B1/ja active Pending
- 1969-10-28 SU SU1374015A patent/SU374838A3/ru active
- 1969-10-29 CS CS7146A patent/CS166719B2/cs unknown
Also Published As
| Publication number | Publication date |
|---|---|
| DE1954002A1 (en) | 1970-05-21 |
| NO126919B (en) | 1973-04-09 |
| BR6913678D0 (en) | 1973-01-23 |
| SU374838A3 (en) | 1973-03-20 |
| DK133474C (en) | 1976-11-01 |
| CS166719B2 (en) | 1976-03-29 |
| SE369197B (en) | 1974-08-12 |
| FR2021705A1 (en) | 1970-07-24 |
| GB1276864A (en) | 1972-06-07 |
| OA03157A (en) | 1970-12-15 |
| DK133474B (en) | 1976-05-24 |
| JPS4830441B1 (en) | 1973-09-20 |
| AT303941B (en) | 1972-12-11 |
| US3594309A (en) | 1971-07-20 |
| NL6916218A (en) | 1970-05-01 |
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