MX9701616A - Process for the thermal cracking of a residual hydrocarbon oil. - Google Patents
Process for the thermal cracking of a residual hydrocarbon oil.Info
- Publication number
- MX9701616A MX9701616A MX9701616A MX9701616A MX9701616A MX 9701616 A MX9701616 A MX 9701616A MX 9701616 A MX9701616 A MX 9701616A MX 9701616 A MX9701616 A MX 9701616A MX 9701616 A MX9701616 A MX 9701616A
- Authority
- MX
- Mexico
- Prior art keywords
- hydrocarbon oil
- degree
- soaker
- percent
- final
- Prior art date
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
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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Process for the thermal cracking of a residual hydrocarbon oil wherein a final 520 degree C+ conversion of at least 35 percent by weight is attained, which process comprises the steps of: (a) heating the residual hydrocarbon oil feed in a furnace to a temperature in the range of from 400 to 510 degree C for sufficient time to achieve 30 to 45 percent of the final 520 degree C+ conversion; (b) feeding the partially converted, hot hydrocarbon oil produced in step (a) and a hot hydrogen-containing gas into a soaker, said hydrogen-containing gas having a sufficiently high temperature to maintain the temperature of the hydrocarbon oil in the soaker by means of direct heat exchange at a value in the range of from 420 to 650 degree C, in which soaker the remainder up to 100 percent of the final 520 degree C+ conversion takes place; and (c) recovering a gaseous fraction containing the hydrogen-containing gas and a cracked residue from the soaker.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP94202527 | 1994-09-05 | ||
| PCT/EP1995/003504 WO1996007716A1 (en) | 1994-09-05 | 1995-09-04 | Process for the thermal cracking of a residual hydrocarbon oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| MX9701616A true MX9701616A (en) | 1997-06-28 |
Family
ID=8217160
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| MX9701616A MX9701616A (en) | 1994-09-05 | 1995-09-04 | Process for the thermal cracking of a residual hydrocarbon oil. |
Country Status (13)
| Country | Link |
|---|---|
| EP (1) | EP0779916B1 (en) |
| JP (1) | JP3764480B2 (en) |
| CN (1) | CN1122705C (en) |
| AU (1) | AU694799B2 (en) |
| BR (1) | BR9508692A (en) |
| CA (1) | CA2199045C (en) |
| DE (1) | DE69506565T2 (en) |
| DK (1) | DK0779916T3 (en) |
| FI (1) | FI119843B (en) |
| MX (1) | MX9701616A (en) |
| NO (1) | NO317941B1 (en) |
| WO (1) | WO1996007716A1 (en) |
| ZA (1) | ZA957400B (en) |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4495791B2 (en) * | 1998-07-03 | 2010-07-07 | 日揮株式会社 | Combined cycle power generation system |
| CN1090668C (en) * | 1999-09-10 | 2002-09-11 | 中国石油化工集团公司北京化工研究院 | Coking inhibiting method for ethylene cracker |
| CN101400766B (en) * | 2006-03-29 | 2013-07-24 | 国际壳牌研究有限公司 | Improved process for producing lower olefins from heavy hydrocarbon feedstock utilizing two vapor/liquid separators |
| US8202480B2 (en) | 2009-06-25 | 2012-06-19 | Uop Llc | Apparatus for separating pitch from slurry hydrocracked vacuum gas oil |
| US8540870B2 (en) | 2009-06-25 | 2013-09-24 | Uop Llc | Process for separating pitch from slurry hydrocracked vacuum gas oil |
| US8231775B2 (en) | 2009-06-25 | 2012-07-31 | Uop Llc | Pitch composition |
| EP2792729A1 (en) | 2013-04-17 | 2014-10-22 | XTLgroup bv | Process for hydroprocessing a liquid feed comprising hydrocarbons into fuel components |
| CN108723064A (en) * | 2018-05-28 | 2018-11-02 | 四川锐源能环科技有限公司 | A kind of oil-containing solid waste harmless resource treatment technology equipment |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3714282A (en) * | 1970-07-09 | 1973-01-30 | Monsanto Co | Production of propylene and aromatic compounds from liquid feed streams |
| NL8201243A (en) * | 1982-03-25 | 1983-10-17 | Shell Int Research | PROCESS FOR THE PREPARATION OF LOW ASPHALTANE HYDROCARBON MIXTURE. |
| EP0125709B1 (en) * | 1983-04-18 | 1989-08-02 | Shell Internationale Researchmaatschappij B.V. | A process for the production of low-asphaltenes hydrocarbon mixtures |
| US4569752A (en) * | 1983-12-14 | 1986-02-11 | Exxon Research And Engineering Co. | Combination coking and hydroconversion process |
| CA1312033C (en) * | 1987-09-16 | 1992-12-29 | Clarence M. Eidt, Jr. | Combination coking and hydroconversion process |
| GB8803156D0 (en) * | 1988-02-11 | 1988-03-09 | Shell Int Research | Process for thermal cracking of residual hydrocarbon oils |
-
1995
- 1995-09-04 AU AU35226/95A patent/AU694799B2/en not_active Ceased
- 1995-09-04 EP EP95932000A patent/EP0779916B1/en not_active Expired - Lifetime
- 1995-09-04 BR BR9508692A patent/BR9508692A/en not_active IP Right Cessation
- 1995-09-04 MX MX9701616A patent/MX9701616A/en not_active IP Right Cessation
- 1995-09-04 DK DK95932000T patent/DK0779916T3/en active
- 1995-09-04 CN CN95194908A patent/CN1122705C/en not_active Expired - Fee Related
- 1995-09-04 CA CA002199045A patent/CA2199045C/en not_active Expired - Fee Related
- 1995-09-04 ZA ZA957400A patent/ZA957400B/en unknown
- 1995-09-04 DE DE69506565T patent/DE69506565T2/en not_active Expired - Fee Related
- 1995-09-04 JP JP50921696A patent/JP3764480B2/en not_active Expired - Fee Related
- 1995-09-04 WO PCT/EP1995/003504 patent/WO1996007716A1/en active IP Right Grant
-
1997
- 1997-03-03 FI FI970908A patent/FI119843B/en active IP Right Grant
- 1997-03-03 NO NO19970975A patent/NO317941B1/en not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| DE69506565D1 (en) | 1999-01-21 |
| NO317941B1 (en) | 2005-01-10 |
| FI119843B (en) | 2009-04-15 |
| BR9508692A (en) | 1998-01-06 |
| NO970975L (en) | 1997-05-05 |
| EP0779916B1 (en) | 1998-12-09 |
| DE69506565T2 (en) | 1999-06-17 |
| CN1122705C (en) | 2003-10-01 |
| NO970975D0 (en) | 1997-03-03 |
| ZA957400B (en) | 1996-04-17 |
| JPH10505126A (en) | 1998-05-19 |
| FI970908A0 (en) | 1997-03-03 |
| DK0779916T3 (en) | 1999-07-19 |
| WO1996007716A1 (en) | 1996-03-14 |
| FI970908A (en) | 1997-03-03 |
| AU694799B2 (en) | 1998-07-30 |
| JP3764480B2 (en) | 2006-04-05 |
| CN1157006A (en) | 1997-08-13 |
| AU3522695A (en) | 1996-03-27 |
| CA2199045A1 (en) | 1996-03-14 |
| EP0779916A1 (en) | 1997-06-25 |
| CA2199045C (en) | 2007-02-20 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FG | Grant or registration | ||
| MM | Annulment or lapse due to non-payment of fees |