ES398415A1 - Effluent cooling in a hydrocracking and hydrodesulfurizing process - Google Patents
Effluent cooling in a hydrocracking and hydrodesulfurizing processInfo
- Publication number
- ES398415A1 ES398415A1 ES398415A ES398415A ES398415A1 ES 398415 A1 ES398415 A1 ES 398415A1 ES 398415 A ES398415 A ES 398415A ES 398415 A ES398415 A ES 398415A ES 398415 A1 ES398415 A1 ES 398415A1
- Authority
- ES
- Spain
- Prior art keywords
- hydrocracking
- effluent
- substantially constant
- fraction
- hydrocracked
- 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
- 238000004517 catalytic hydrocracking Methods 0.000 title abstract 2
- 238000001816 cooling Methods 0.000 title 1
- 238000000034 method Methods 0.000 title 1
- 238000006243 chemical reaction Methods 0.000 abstract 3
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 abstract 2
- 238000009835 boiling Methods 0.000 abstract 2
- 239000005864 Sulphur Substances 0.000 abstract 1
- 125000003118 aryl group Chemical group 0.000 abstract 1
- 238000006477 desulfuration reaction Methods 0.000 abstract 1
- 230000023556 desulfurization Effects 0.000 abstract 1
- 239000000463 material Substances 0.000 abstract 1
- 239000000203 mixture Substances 0.000 abstract 1
- 239000003208 petroleum Substances 0.000 abstract 1
- 229910052717 sulfur Inorganic materials 0.000 abstract 1
- 239000011593 sulfur 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
- 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
- C10G65/12—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including cracking steps and other hydrotreatment steps
-
- 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/107—Atmospheric residues having a boiling point of at least about 538 °C
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)
- Catalysts (AREA)
Abstract
A residue-containing petroleum fraction, 50 percent boiling above 1,000 DEG F, is hydrocracked and then hydrodesulfurized. During the onstream period, the conversion level of material boiling above 1,000 DEG F is maintained substantially constant while the sulfur content of the hydrocracked effluent increases. The sulphur content of a product fraction is maintained substantially constant by gradually increasing the hydrodesulfurization temperature. The effluent from the hydrocracking reaction is cooled by adding an aromatic-rich fraction and the cooled mixture is passed to the desulfurization reaction.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US10225170A | 1970-12-28 | 1970-12-28 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| ES398415A1 true ES398415A1 (en) | 1974-10-01 |
Family
ID=22288915
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ES398415A Expired ES398415A1 (en) | 1970-12-28 | 1971-12-28 | Effluent cooling in a hydrocracking and hydrodesulfurizing process |
Country Status (11)
| Country | Link |
|---|---|
| US (1) | US3716476A (en) |
| JP (1) | JPS5129164B1 (en) |
| AU (1) | AU452024B2 (en) |
| BE (1) | BE777428A (en) |
| CA (1) | CA968291A (en) |
| DE (1) | DE2164449B2 (en) |
| ES (1) | ES398415A1 (en) |
| FR (1) | FR2120022B1 (en) |
| GB (1) | GB1324580A (en) |
| IT (1) | IT951966B (en) |
| NL (1) | NL7117858A (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02110715U (en) * | 1989-02-22 | 1990-09-05 | ||
| FI934623A0 (en) * | 1992-02-21 | 1993-10-20 | Idemitsu Kosan Co | FOERFARANDE FOER HYDROGENERANDE BEHANDLING AV TUNG KOLVAETEOLJA |
| US5885440A (en) * | 1996-10-01 | 1999-03-23 | Uop Llc | Hydrocracking process with integrated effluent hydrotreating zone |
| DE19832087A1 (en) * | 1998-07-16 | 2000-01-20 | Basf Ag | Process for the conversion of organic compounds with boron oxide-containing, macroporous supported catalysts |
| CN104650970B (en) * | 2013-11-20 | 2016-08-17 | 中国石油化工股份有限公司 | A kind of hydrocracking method reducing light fraction product sulfur content |
| CN104650972B (en) * | 2013-11-20 | 2016-08-17 | 中国石油化工股份有限公司 | Reduce the method for hydrogen cracking of light fraction product sulfur content |
Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3254017A (en) * | 1963-08-23 | 1966-05-31 | Exxon Research Engineering Co | Process for hydrocracking heavy oils in two stages |
| US3297563A (en) * | 1964-08-17 | 1967-01-10 | Union Oil Co | Treatment of heavy oils in two stages of hydrotreating |
| US3322665A (en) * | 1965-05-18 | 1967-05-30 | Hydrocarbon Research Inc | High conversion hydrogenation of heavy gas oil |
| US3360457A (en) * | 1965-07-01 | 1967-12-26 | Texaco Inc | Hydrocracking process |
| GB1193213A (en) * | 1967-04-25 | 1970-05-28 | Atlantic Richfield Co | Petroleum Purification |
| US3472759A (en) * | 1967-04-25 | 1969-10-14 | Atlantic Richfield Co | Process for removal of sulfur and metals from petroleum materials |
| US3472758A (en) * | 1967-08-02 | 1969-10-14 | Universal Oil Prod Co | Multiple-stage hydrocarbon hydrocracking process |
| US3562144A (en) * | 1968-06-24 | 1971-02-09 | Texaco Inc | Hydrocracking process |
| US3540997A (en) * | 1968-09-27 | 1970-11-17 | Texaco Inc | Production of motor and jet fuels |
-
1970
- 1970-12-28 US US00102251A patent/US3716476A/en not_active Expired - Lifetime
-
1971
- 1971-12-20 GB GB5916571A patent/GB1324580A/en not_active Expired
- 1971-12-24 DE DE2164449A patent/DE2164449B2/en not_active Ceased
- 1971-12-24 CA CA131,166A patent/CA968291A/en not_active Expired
- 1971-12-27 FR FR7146721A patent/FR2120022B1/fr not_active Expired
- 1971-12-27 IT IT32977/71A patent/IT951966B/en active
- 1971-12-27 NL NL7117858A patent/NL7117858A/xx unknown
- 1971-12-28 BE BE777428A patent/BE777428A/en unknown
- 1971-12-28 ES ES398415A patent/ES398415A1/en not_active Expired
- 1971-12-28 JP JP47003733A patent/JPS5129164B1/ja active Pending
- 1971-12-30 AU AU37495/71A patent/AU452024B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| NL7117858A (en) | 1972-06-30 |
| GB1324580A (en) | 1973-07-25 |
| US3716476A (en) | 1973-02-13 |
| CA968291A (en) | 1975-05-27 |
| IT951966B (en) | 1973-07-10 |
| DE2164449A1 (en) | 1972-07-27 |
| FR2120022A1 (en) | 1972-08-11 |
| DE2164449B2 (en) | 1973-09-20 |
| BE777428A (en) | 1972-06-28 |
| JPS5129164B1 (en) | 1976-08-24 |
| FR2120022B1 (en) | 1976-03-26 |
| AU452024B2 (en) | 1974-08-22 |
| AU3749571A (en) | 1973-07-05 |
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