ECSP12011824A - HEAVY OIL IMPROVEMENT EQUIPMENT AND HEAVY OIL IMPROVEMENT METHOD - Google Patents
HEAVY OIL IMPROVEMENT EQUIPMENT AND HEAVY OIL IMPROVEMENT METHODInfo
- Publication number
- ECSP12011824A ECSP12011824A ECSP12011824A ECSP12011824A EC SP12011824 A ECSP12011824 A EC SP12011824A EC SP12011824 A ECSP12011824 A EC SP12011824A EC SP12011824 A ECSP12011824 A EC SP12011824A
- Authority
- EC
- Ecuador
- Prior art keywords
- heavy oil
- supercritical water
- fraction
- residual
- reactor
- 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
- C10G9/00—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
-
- 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
- C10G9/00—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G9/34—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts
- C10G9/36—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts with heated gases or vapours
-
- 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
- C10G2300/80—Additives
- C10G2300/805—Water
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)
Abstract
Se proporcionan un aparato para mejorar el petróleo pesado y un método de mejoramiento, en donde el grado avanzado del craqueo térmico del petróleo pesado puede ser controlado cuando el petróleo pesado es mejorado mediante el uso de agua supercrítica. Un reactor 1 es mantenido a una temperatura y presión igual o mayor que los puntos críticos del agua. En el reactor, un petróleo pesado y el agua supercrítica son puestos en contacto uno con otro, y el petróleo pesado es separado en una primera fase compuesta de una fracción de petróleo pesado residual, obtenido mediante el craqueo térmico y el agua supercrítica disuelta en la fracción de petróleo pesado residual, y una segunda fase compuesta por el agua supercrítica y una fracción de petróleo liviano extraída hacia el agua supercrítica, mientras avanza el craqueo térmico del petróleo pesado. Una unidad de detección de interface 75 detecta la altura de la posición de una interfaz entre la primera y la segunda fase en el reactor. Una unidad de control 7 controla la cantidad desechada del fluido mezclado de la fracción de petróleo pesado residual y el agua supercrítica, sobre la base del volumen de la altura de la posición de la primera fase encontrada, tal que un tiempo de residencia del fluido mezclado de la fracción de petróleo pesado residual y el agua supercrítica disuelta en la fracción de petróleo pesado residual, se convierta en un primer tiempo de residencia, el cual ha sido ajustado por anticipado. (FIG. 2)An apparatus for improving heavy oil and an improvement method are provided, wherein the advanced degree of thermal cracking of heavy oil can be controlled when heavy oil is improved by the use of supercritical water. A reactor 1 is maintained at a temperature and pressure equal to or greater than the critical points of the water. In the reactor, a heavy oil and supercritical water are brought into contact with each other, and the heavy oil is separated in a first phase composed of a fraction of residual heavy oil, obtained by thermal cracking and the supercritical water dissolved in the fraction of residual heavy oil, and a second phase composed of supercritical water and a fraction of light oil extracted into supercritical water, while thermal cracking of heavy oil progresses. An interface detection unit 75 detects the height of the position of an interface between the first and the second phase in the reactor. A control unit 7 controls the discarded amount of the mixed fluid of the residual heavy oil fraction and the supercritical water, based on the volume of the height of the position of the first phase found, such that a residence time of the mixed fluid of the fraction of residual heavy oil and the supercritical water dissolved in the fraction of residual heavy oil, it becomes a first residence time, which has been adjusted in advance. (FIG. 2)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2009241766A JP2011088964A (en) | 2009-10-20 | 2009-10-20 | Apparatus and method for modifying heavy oil |
| PCT/JP2009/006855 WO2011048642A1 (en) | 2009-10-20 | 2009-12-14 | Device for reforming heavy oil and method of reforming heavy oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| ECSP12011824A true ECSP12011824A (en) | 2012-07-31 |
Family
ID=43899896
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ECSP12011824 ECSP12011824A (en) | 2009-10-20 | 2012-04-20 | HEAVY OIL IMPROVEMENT EQUIPMENT AND HEAVY OIL IMPROVEMENT METHOD |
Country Status (6)
| Country | Link |
|---|---|
| JP (1) | JP2011088964A (en) |
| CA (1) | CA2774062C (en) |
| CO (1) | CO6511243A2 (en) |
| EA (1) | EA022662B1 (en) |
| EC (1) | ECSP12011824A (en) |
| WO (1) | WO2011048642A1 (en) |
Families Citing this family (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8894846B2 (en) | 2010-12-23 | 2014-11-25 | Stephen Lee Yarbro | Using supercritical fluids to refine hydrocarbons |
| CA2772095C (en) * | 2011-04-19 | 2015-05-05 | Jgc Corporation | Method for producing upgraded oil, and apparatus for producing upgraded oil |
| US9783742B2 (en) | 2013-02-28 | 2017-10-10 | Aduro Energy, Inc. | System and method for controlling and optimizing the hydrothermal upgrading of heavy crude oil and bitumen |
| US9644455B2 (en) | 2013-02-28 | 2017-05-09 | Aduro Energy Inc. | System and method for controlling and optimizing the hydrothermal upgrading of heavy crude oil and bitumen |
| US10900327B2 (en) | 2013-02-28 | 2021-01-26 | Aduro Energy, Inc. | System and method for hydrothermal upgrading of fatty acid feedstock |
| US10144874B2 (en) | 2013-03-15 | 2018-12-04 | Terrapower, Llc | Method and system for performing thermochemical conversion of a carbonaceous feedstock to a reaction product |
| US9771527B2 (en) | 2013-12-18 | 2017-09-26 | Saudi Arabian Oil Company | Production of upgraded petroleum by supercritical water |
| RU2687072C2 (en) * | 2014-03-18 | 2019-05-07 | Адуро Энерджи, Инк. | System and method for monitoring and optimizing hydrothermal process of refining heavy crude oil and bitumen |
| WO2016200365A1 (en) * | 2015-06-08 | 2016-12-15 | Schlumberger Canada Limited | Automated method and apparatus for measuring saturate, aromatic, resin, and asphaltene fractions using microfluidics and spectroscopy |
| US10577546B2 (en) * | 2017-01-04 | 2020-03-03 | Saudi Arabian Oil Company | Systems and processes for deasphalting oil |
| CN110461810B (en) | 2017-03-24 | 2022-05-13 | 泰拉能源公司 | Method and system for recycling pyrolysis tail gas by conversion to formic acid |
| US10787610B2 (en) | 2017-04-11 | 2020-09-29 | Terrapower, Llc | Flexible pyrolysis system and method |
| US11414606B1 (en) | 2018-11-08 | 2022-08-16 | Aduro Energy, Inc. | System and method for producing hydrothermal renewable diesel and saturated fatty acids |
| US10920158B2 (en) | 2019-06-14 | 2021-02-16 | Saudi Arabian Oil Company | Supercritical water process to produce bottom free hydrocarbons |
| CN111701276B (en) * | 2020-08-19 | 2021-01-05 | 白婷婷 | Supercritical carbon dioxide extraction kettle |
| US11905470B1 (en) | 2023-04-03 | 2024-02-20 | Saudi Arabian Oil Company | Methods for reducing coke formation in heavy oil upgrading using supercritical water |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0626909A (en) * | 1992-07-10 | 1994-02-04 | Japan Tobacco Inc | Method and device for controlling contact interface position in pressure vessel |
| JP3459749B2 (en) * | 1997-05-21 | 2003-10-27 | オルガノ株式会社 | Supercritical water reactor |
| JP3791363B2 (en) * | 2001-08-07 | 2006-06-28 | 株式会社日立製作所 | Lightening of heavy oil |
| JP2007051224A (en) * | 2005-08-18 | 2007-03-01 | Chubu Electric Power Co Inc | Method and apparatus for modifying heavy oil |
| JP4171062B2 (en) * | 2008-02-25 | 2008-10-22 | 株式会社日立製作所 | Processing method for heavy oil |
-
2009
- 2009-10-20 JP JP2009241766A patent/JP2011088964A/en not_active Withdrawn
- 2009-12-14 EA EA201270444A patent/EA022662B1/en not_active IP Right Cessation
- 2009-12-14 WO PCT/JP2009/006855 patent/WO2011048642A1/en active Application Filing
- 2009-12-14 CA CA2774062A patent/CA2774062C/en active Active
-
2012
- 2012-03-15 CO CO12044979A patent/CO6511243A2/en active IP Right Grant
- 2012-04-20 EC ECSP12011824 patent/ECSP12011824A/en unknown
Also Published As
| Publication number | Publication date |
|---|---|
| JP2011088964A (en) | 2011-05-06 |
| CA2774062C (en) | 2014-06-17 |
| EA022662B1 (en) | 2016-02-29 |
| WO2011048642A1 (en) | 2011-04-28 |
| EA201270444A1 (en) | 2012-09-28 |
| CO6511243A2 (en) | 2012-08-31 |
| CA2774062A1 (en) | 2011-04-28 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| ECSP12011824A (en) | HEAVY OIL IMPROVEMENT EQUIPMENT AND HEAVY OIL IMPROVEMENT METHOD | |
| AR104394A1 (en) | PROCEDURE FOR THE USE OF THE INTERNAL ENERGY OF A FLUID OF AN ACUÍFERO IN A GEOTHERMAL INSTALLATION | |
| AR111136A1 (en) | PROCEDURE FOR ASSISTED OIL RECOVERY USING A (CO) HYDRAATED CRYSTALLINE POLYMER OF SULPHONIC ACID 2-ACRYLAMIDE-2-METHYLPROPANE | |
| AR089956A1 (en) | PETROLEUM RECOVERY PROCESS | |
| AR077836A1 (en) | METHODS TO DILATE DILATABLE ELEMENTS IN A WELL SECTION WITH THE USE OF A WATER EMULSION IN OIL | |
| BR112012014201A2 (en) | system and method of flooding with water from reservoirs at sea | |
| AR093383A1 (en) | WATERPROOF BASED DRILLING FLUID WITH CYCLODEXTRINE AS A SKIS STABILIZER | |
| AR087013A1 (en) | PLACEMENT IN THE FUND OF THE WATERPROOF OF POLYMEROS IN WATER | |
| AR103486A1 (en) | CONTROL SYSTEM AND METHOD OF FLOW RETURN OPERATIONS FOR BITUMINOUS SKIS FACILITIES | |
| BR112015023625A2 (en) | controlled unrated filling device and method | |
| AR106771A1 (en) | WEAK GEL SYSTEM FOR CHEMICAL ENHANCED OIL RECOVERY | |
| AR094475A1 (en) | LOW TEMPERATURE SWITCH FOR WELL FLUIDS WITH ITS VISCOSITY INCREASED BY A POLYACRYLAMIDE | |
| ES2721153T3 (en) | Procedure and system to insert an insertion element into a panel product | |
| AR103562A1 (en) | SYSTEM AND METHOD FOR HYDRAULIC FRACTURING WITH NANOPARTICLES | |
| AR092740A1 (en) | FORMULATION OF A TENSIOACTIVE FOR THE RELEASE OF UNDERGROUND FOSSIL FLUIDS | |
| BR112014029677A2 (en) | sieve arrangement and method for producing a fluid composition from an underground formation | |
| CO6761355A2 (en) | Method and related process of high pressure hydrocarbon fracturing on demand | |
| AR108113A1 (en) | IMPROVED OIL RECOVERY WITH MISCIBLE SOLVENT | |
| PH12017501174A1 (en) | A displacement system and method for a submersible electrical system | |
| DK201670938A1 (en) | Method and apparatus for retrieving a tubing from a well | |
| BR102012011913A2 (en) | subsea wellhead assembly and method to provide a positive indication of wellhead | |
| BR102014014759A8 (en) | oil-in-water emulsion, method for modifying the wetting capacity of water-to-oil wet sandstone rock, and use of an emulsion | |
| GB2537734A (en) | Hydrocarbon production and storage facility | |
| AR087073A1 (en) | COMPRESSION WATER INJECTION AND EXTRACTION FLOCULATION UNIT FOR SOLID CONTROL AND MANAGEMENT OF DRILLING FLUIDS, AND RELATED METHODS | |
| CO6210832A2 (en) | A MODIFIED PROCESS FOR THE RECOVERY OF HYDROCARBON USING COMBUSTION IN SITU |