CA2422534A1 - Products produced from rapid thermal processing of heavy hydrocarbon feedstocks - Google Patents
Products produced from rapid thermal processing of heavy hydrocarbon feedstocks Download PDFInfo
- Publication number
- CA2422534A1 CA2422534A1 CA002422534A CA2422534A CA2422534A1 CA 2422534 A1 CA2422534 A1 CA 2422534A1 CA 002422534 A CA002422534 A CA 002422534A CA 2422534 A CA2422534 A CA 2422534A CA 2422534 A1 CA2422534 A1 CA 2422534A1
- Authority
- CA
- Canada
- Prior art keywords
- feedstock
- heat carrier
- heavy hydrocarbon
- liquid product
- simulated distillation
- 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.)
- Granted
Links
Classifications
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- 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
- C10G9/28—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid material
- C10G9/32—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid material according to the "fluidised-bed" technique
-
- 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
- C10G31/00—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for
- C10G31/06—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for by heating, cooling, or pressure treatment
-
- 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
- C10G9/28—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid material
-
- 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
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/201—Impurities
- C10G2300/205—Metal content
-
- 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
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/30—Physical properties of feedstocks or products
-
- 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
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/30—Physical properties of feedstocks or products
- C10G2300/301—Boiling range
-
- 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
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/30—Physical properties of feedstocks or products
- C10G2300/302—Viscosity
-
- 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
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/30—Physical properties of feedstocks or products
- C10G2300/308—Gravity, density, e.g. API
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)
- Fats And Perfumes (AREA)
Abstract
The present invention is directed to the upgrading of heavy hydrocarbon feedstock that utilizes a short residence pyrolytic reactor operating under conditions that cracks and chemically upgrades the feedstock. The process of the present invention provides for the preparation of a partially upgraded feedstock exhibiting reduced viscosity and increased API gravity. This proce ss selectively removes metals, salts, water and nitrogen from the feedstock, while at the same time maximizes the yield of the liquid product, and minimizes coke and gas production. Furthermore, this process reduces the viscosity of the feedstock in order to permit pipeline transport, if desired , of the upgraded feedstock with little or no addition of diluents. The method for upgrading a heavy hydrocarbon feedstock comprises introducing a particulate heat carrier into an upflow reactor, introducing the heavy hydrocarbon feedstock into the upflow reactor at a location above that of th e particulate heat carrier so that a loading ratio of the particulate heat carrier to feedstock is from about 15:1 to about 200:1, allowing the heavy hydrocarbon feedstock to interact with the heat carrier with a residence tim e of less than about 1 second, to produce a product stream, separating the product stream from the particulate heat carrier, regenerating the particula te heat carrier, and collecting a gaseous and liquid product from the product stream. This invention also pertains to the products produced by the method.
Claims (5)
1. An upgraded heavy oil characterized by the following properties:
i) an API gravity from about 13 to about 23;
ii) a density at 15°C from about 0.92 g/ml to about 0.98 g/ml;
iii) a viscosity at 40°C, cSt, from about 15 to about 300;
iv) a reduced Vanadium content of about 60 to about 100 ppm; and v) a reduced Nickel content of about 10 to about 50 ppm.
i) an API gravity from about 13 to about 23;
ii) a density at 15°C from about 0.92 g/ml to about 0.98 g/ml;
iii) a viscosity at 40°C, cSt, from about 15 to about 300;
iv) a reduced Vanadium content of about 60 to about 100 ppm; and v) a reduced Nickel content of about 10 to about 50 ppm.
2. An upgraded bitumen characterized by the following properties:
i) an API gravity from about 10 to about 21;
ii) a density at 15°C from about 0.93 g/ml to about 1.0 g/ml;
iii) a viscosity at 40°C, cSt, from about 15 to about 300;
iv) a reduced Vanadium content of about 60 to about 100 ppm; and v) a reduced Nickel content of about 10 to about 50 ppm.
i) an API gravity from about 10 to about 21;
ii) a density at 15°C from about 0.93 g/ml to about 1.0 g/ml;
iii) a viscosity at 40°C, cSt, from about 15 to about 300;
iv) a reduced Vanadium content of about 60 to about 100 ppm; and v) a reduced Nickel content of about 10 to about 50 ppm.
3. A liquid product characterized in having at least one of the following properties:
i) less than 50% of the components evolving at temperatures above 538°C
during simulated distillation;
ii) from about 60% to about 95% of the product evolving below 538°
during simulated distillation;
iii) from about 1.0% to about 10% of the liquid product evolve below 193°C
during simulated distillation;
iv) from about 2% to about 6% of the liquid product evolve between 193-232°C during simulated distillation;
v) from about 10% to about 25% of the liquid product evolve between 232-327°C during simulated distillation;
vi) from about 6% to about 15% of the liquid product evolve between 327-360°C during simulated distillation; and vii) from about 34.5% to about 60% of the liquid product evolve between 360-538°C during simulated distillation.
i) less than 50% of the components evolving at temperatures above 538°C
during simulated distillation;
ii) from about 60% to about 95% of the product evolving below 538°
during simulated distillation;
iii) from about 1.0% to about 10% of the liquid product evolve below 193°C
during simulated distillation;
iv) from about 2% to about 6% of the liquid product evolve between 193-232°C during simulated distillation;
v) from about 10% to about 25% of the liquid product evolve between 232-327°C during simulated distillation;
vi) from about 6% to about 15% of the liquid product evolve between 327-360°C during simulated distillation; and vii) from about 34.5% to about 60% of the liquid product evolve between 360-538°C during simulated distillation.
4. A VGO characterised with a measured analine point from about 110°F
to about 130°F, and a calculated analine point from about 125°F to about 170°F.
to about 130°F, and a calculated analine point from about 125°F to about 170°F.
5. The VGO of claim 4, further characterized by having a hydrocarbon profile comprising about 38% mono-aromatics.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US23335400P | 2000-09-18 | 2000-09-18 | |
| US60/233,354 | 2000-09-18 | ||
| PCT/CA2001/001316 WO2002024835A2 (en) | 2000-09-18 | 2001-09-18 | Products produced from rapid thermal processing of heavy hydrocarbon feedstocks |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2422534A1 true CA2422534A1 (en) | 2002-03-28 |
| CA2422534C CA2422534C (en) | 2012-05-22 |
Family
ID=22876886
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA2422534A Expired - Fee Related CA2422534C (en) | 2000-09-18 | 2001-09-18 | Products produced from rapid thermal processing of heavy hydrocarbon feedstocks |
Country Status (13)
| Country | Link |
|---|---|
| US (1) | US7270743B2 (en) |
| EP (2) | EP2275513A3 (en) |
| AR (1) | AR033838A1 (en) |
| AT (1) | ATE532842T1 (en) |
| AU (1) | AU2001291563A1 (en) |
| BR (1) | BR0113937A (en) |
| CA (1) | CA2422534C (en) |
| DK (1) | DK1332199T3 (en) |
| ES (1) | ES2395116T3 (en) |
| MX (1) | MXPA03002341A (en) |
| NO (1) | NO330786B1 (en) |
| PT (1) | PT1332199E (en) |
| WO (1) | WO2002024835A2 (en) |
Families Citing this family (46)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8105482B1 (en) * | 1999-04-07 | 2012-01-31 | Ivanhoe Energy, Inc. | Rapid thermal processing of heavy hydrocarbon feedstocks |
| US8062503B2 (en) * | 2001-09-18 | 2011-11-22 | Ivanhoe Energy Inc. | Products produced from rapid thermal processing of heavy hydrocarbon feedstocks |
| US7270743B2 (en) | 2000-09-18 | 2007-09-18 | Ivanhoe Energy, Inc. | Products produced form rapid thermal processing of heavy hydrocarbon feedstocks |
| US7572362B2 (en) * | 2002-10-11 | 2009-08-11 | Ivanhoe Energy, Inc. | Modified thermal processing of heavy hydrocarbon feedstocks |
| US7572365B2 (en) * | 2002-10-11 | 2009-08-11 | Ivanhoe Energy, Inc. | Modified thermal processing of heavy hydrocarbon feedstocks |
| EP2007744B1 (en) | 2006-04-03 | 2017-05-17 | Pharmatherm Chemicals Inc. | Thermal extraction method for producing a taxane extract |
| DK2069467T3 (en) | 2006-10-06 | 2014-10-20 | Vary Petrochem Llc | Various compositions and methods of use |
| US8062512B2 (en) * | 2006-10-06 | 2011-11-22 | Vary Petrochem, Llc | Processes for bitumen separation |
| US7758746B2 (en) | 2006-10-06 | 2010-07-20 | Vary Petrochem, Llc | Separating compositions and methods of use |
| CA2624746C (en) | 2007-03-12 | 2015-02-24 | Robert Graham | Methods and systems for producing reduced resid and bottomless products from heavy hydrocarbon feedstocks |
| US8858783B2 (en) * | 2009-09-22 | 2014-10-14 | Neo-Petro, Llc | Hydrocarbon synthesizer |
| US20110094937A1 (en) * | 2009-10-27 | 2011-04-28 | Kellogg Brown & Root Llc | Residuum Oil Supercritical Extraction Process |
| US20110284359A1 (en) | 2010-05-20 | 2011-11-24 | Uop Llc | Processes for controlling afterburn in a reheater and for controlling loss of entrained solid particles in combustion product flue gas |
| US8499702B2 (en) | 2010-07-15 | 2013-08-06 | Ensyn Renewables, Inc. | Char-handling processes in a pyrolysis system |
| CA2714842C (en) * | 2010-09-22 | 2012-05-29 | Imperial Oil Resources Limited | Controlling bitumen quality in solvent-assisted bitumen extraction |
| CN103347601B (en) | 2010-11-05 | 2015-04-22 | 国际热化学恢复股份有限公司 | Solids circulation system and method for capture and conversion of reactive solid |
| CA2823332A1 (en) | 2010-12-29 | 2012-07-05 | Ivanhoe Energy Inc. | Method, system, and apparatus for lift gas distribution |
| CN103442794A (en) | 2010-12-29 | 2013-12-11 | 艾芬豪能源有限公司 | Improved reactor feed nozzle |
| EA201390989A1 (en) | 2010-12-30 | 2014-06-30 | Айванхо Энерджи Инк. | METHOD, SYSTEM AND DEVICE FOR SEPARATION IN TREATMENT OF INITIAL RAW MATERIALS |
| US9011646B2 (en) | 2011-01-28 | 2015-04-21 | Mccutchen Co. | Mechanical pyrolysis in a shear retort |
| US9441887B2 (en) | 2011-02-22 | 2016-09-13 | Ensyn Renewables, Inc. | Heat removal and recovery in biomass pyrolysis |
| CN102116144A (en) * | 2011-03-08 | 2011-07-06 | 西南石油大学 | Integrated method for thin oil blending, viscosity reduction, extraction and transportation of thickened oil |
| EP2865735B1 (en) | 2011-03-29 | 2018-02-21 | Fuelina Technologies, LLC | Method and apparatus for making a hybrid fuel |
| US9062525B2 (en) | 2011-07-07 | 2015-06-23 | Single Buoy Moorings, Inc. | Offshore heavy oil production |
| US9347005B2 (en) | 2011-09-13 | 2016-05-24 | Ensyn Renewables, Inc. | Methods and apparatuses for rapid thermal processing of carbonaceous material |
| US10400175B2 (en) | 2011-09-22 | 2019-09-03 | Ensyn Renewables, Inc. | Apparatuses and methods for controlling heat for rapid thermal processing of carbonaceous material |
| US10041667B2 (en) | 2011-09-22 | 2018-08-07 | Ensyn Renewables, Inc. | Apparatuses for controlling heat for rapid thermal processing of carbonaceous material and methods for the same |
| US9044727B2 (en) * | 2011-09-22 | 2015-06-02 | Ensyn Renewables, Inc. | Apparatuses and methods for controlling heat for rapid thermal processing of carbonaceous material |
| AU2012315914B2 (en) | 2011-09-27 | 2015-07-09 | Thermochem Recovery International, Inc. | System and method for syngas clean-up |
| US9109177B2 (en) | 2011-12-12 | 2015-08-18 | Ensyn Renewables, Inc. | Systems and methods for renewable fuel |
| US9670413B2 (en) | 2012-06-28 | 2017-06-06 | Ensyn Renewables, Inc. | Methods and apparatuses for thermally converting biomass |
| BR112015003952B1 (en) | 2012-08-24 | 2021-11-23 | Ensyn Renewables, Inc | METHOD FOR PROCESSING AN OIL FRACTION RAW MATERIAL AND A DEVOLATILIZED LIQUID PRODUCT IN A REFINERY SYSTEM |
| US10633606B2 (en) | 2012-12-10 | 2020-04-28 | Ensyn Renewables, Inc. | Systems and methods for renewable fuel |
| US9707532B1 (en) | 2013-03-04 | 2017-07-18 | Ivanhoe Htl Petroleum Ltd. | HTL reactor geometry |
| MX2013002908A (en) * | 2013-03-14 | 2014-09-18 | Fluidoil Ltd | Gravitational collision enhanced upgrading of heavy oils. |
| EA037733B1 (en) | 2014-12-03 | 2021-05-14 | Дрексел Юниверсити | Direct incorporation of natural gas into hydrocarbon liquid fuels |
| US10337726B2 (en) | 2015-08-21 | 2019-07-02 | Ensyn Renewables, Inc. | Liquid biomass heating system |
| ES2940894T3 (en) | 2016-02-16 | 2023-05-12 | Thermochem Recovery Int Inc | Two-stage integrated power product gas generation system and method |
| CN109153929B (en) | 2016-03-25 | 2019-12-20 | 国际热化学恢复股份有限公司 | Three-stage energy integrated product gas generation system and method |
| US10364398B2 (en) | 2016-08-30 | 2019-07-30 | Thermochem Recovery International, Inc. | Method of producing product gas from multiple carbonaceous feedstock streams mixed with a reduced-pressure mixing gas |
| CN110366448B (en) | 2016-12-29 | 2023-05-02 | 安辛可再生能源有限公司 | Demetallization of liquid biomass |
| CA2963436C (en) | 2017-04-06 | 2022-09-20 | Iftikhar Huq | Partial upgrading of bitumen |
| US9920926B1 (en) | 2017-07-10 | 2018-03-20 | Thermochem Recovery International, Inc. | Pulse combustion heat exchanger system and method |
| US10099200B1 (en) | 2017-10-24 | 2018-10-16 | Thermochem Recovery International, Inc. | Liquid fuel production system having parallel product gas generation |
| US11555157B2 (en) | 2020-03-10 | 2023-01-17 | Thermochem Recovery International, Inc. | System and method for liquid fuel production from carbonaceous materials using recycled conditioned syngas |
| US11466223B2 (en) | 2020-09-04 | 2022-10-11 | Thermochem Recovery International, Inc. | Two-stage syngas production with separate char and product gas inputs into the second stage |
Family Cites Families (94)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2735804A (en) | 1956-02-21 | Stack | ||
| US2573906A (en) | 1944-12-18 | 1951-11-06 | Universal Oil Prod Co | Multistage catalytic conversion of bituminous solids |
| US3039955A (en) | 1958-08-21 | 1962-06-19 | United Eng & Constructors Inc | Pyrolysis process |
| CA932686A (en) | 1970-03-02 | 1973-08-28 | Crown Zellerbach Corporation | Process for pyrolytically degrading bark |
| US3853498A (en) | 1972-06-28 | 1974-12-10 | R Bailie | Production of high energy fuel gas from municipal wastes |
| JPS5139644B2 (en) | 1972-11-30 | 1976-10-29 | ||
| US3929619A (en) | 1973-07-19 | 1975-12-30 | Exxon Research Engineering Co | Hydrocracking process with tri-metallic catalyst |
| US4039390A (en) | 1973-09-13 | 1977-08-02 | Occidental Petroleum Corporation | Feed system for pyrolysis reactors |
| CA1050736A (en) | 1974-05-24 | 1979-03-20 | Occidental Petroleum Corporation | Mixing of particulate materials |
| US4153514A (en) | 1975-02-27 | 1979-05-08 | Occidental Petroleum Corporation | Pyrolysis process for solid wastes |
| DE2508707C2 (en) | 1975-02-28 | 1982-09-23 | Metallgesellschaft Ag, 6000 Frankfurt | Process for the treatment of vapors resulting from the smoldering of oil shale |
| US4049540A (en) | 1975-03-08 | 1977-09-20 | Chiyoda Chemical Engineering & Construction Co. Ltd. | Process for the thermal cracking of heavy oils with a fluidized particulate heat carrier |
| US4083751A (en) | 1975-08-11 | 1978-04-11 | Occidental Petroleum Corporation | Continuous feed pyrolysis chamber for decomposing solid waste |
| US4211606A (en) | 1975-08-19 | 1980-07-08 | Chikul Olga S | Method for thermal processing bitumen-containing materials and device for realization of same |
| US4322222A (en) | 1975-11-10 | 1982-03-30 | Occidental Petroleum Corporation | Process for the gasification of carbonaceous materials |
| US4069107A (en) | 1976-05-03 | 1978-01-17 | Edward Koppelman | Continuous thermal reactor system and method |
| US4085030A (en) | 1976-06-25 | 1978-04-18 | Occidental Petroleum Corporation | Pyrolysis of carbonaceous materials with solvent quench recovery |
| US4102773A (en) | 1976-06-25 | 1978-07-25 | Occidental Petroleum Corporation | Pyrolysis with cyclone burner |
| US4064018A (en) | 1976-06-25 | 1977-12-20 | Occidental Petroleum Corporation | Internally circulating fast fluidized bed flash pyrolysis reactor |
| CA1108545A (en) | 1976-06-25 | 1981-09-08 | Charles K. Choi | Process and apparatus for rapid pyrolysis of carbonaceous materials |
| US4141794A (en) | 1976-06-25 | 1979-02-27 | Occidental Petroleum Corporation | Grid-wall pyrolysis reactor |
| US4080285A (en) * | 1976-07-12 | 1978-03-21 | Gulf Research & Development Company | Thermal cracking of shale oil |
| US4097362A (en) | 1976-07-12 | 1978-06-27 | Gulf Research & Development Company | Method for enhancing distillate liquid yield from an ethylene cracking process |
| US4057490A (en) | 1976-07-12 | 1977-11-08 | Gulf Research & Development Company | Thermal cracking process employing crushed oil shale as fuel |
| US4147593A (en) | 1976-07-21 | 1979-04-03 | Occidental Petroleum Corporation | Flash pyrolysis of organic solid waste employing ash recycle |
| US4087347A (en) | 1976-09-20 | 1978-05-02 | Chevron Research Company | Shale retorting process |
| US4090285A (en) | 1977-02-14 | 1978-05-23 | Bochat Elbert E | Process and product for fitting a brake shoe to a brake drum |
| CA1097245A (en) | 1977-11-22 | 1981-03-10 | Chandra P. Khulbe | Thermal hydrocracking of heavy hydrocarbon oils with heavy oil recycle |
| US4298453A (en) | 1977-12-27 | 1981-11-03 | Mobil Oil Corporation | Coal conversion |
| US4161442A (en) | 1978-01-05 | 1979-07-17 | Mobil Oil Corporation | Processing of tar sands |
| US4263128A (en) | 1978-02-06 | 1981-04-21 | Engelhard Minerals & Chemicals Corporation | Upgrading petroleum and residual fractions thereof |
| US4243514A (en) | 1979-05-14 | 1981-01-06 | Engelhard Minerals & Chemicals Corporation | Preparation of FCC charge from residual fractions |
| US4284494A (en) | 1978-05-01 | 1981-08-18 | Engelhard Minerals & Chemicals Corporation | Control of emissions in FCC regenerator flue gas |
| US4280876A (en) | 1978-10-27 | 1981-07-28 | Occidental Research Corporation | Coal pyrolysis process |
| US4604268A (en) | 1979-04-19 | 1986-08-05 | Kay Alan R | Methods of desulfurizing gases |
| US4260456A (en) | 1979-05-29 | 1981-04-07 | Tosco Corporation | Single retort manufacturing technique for producing valuable char and gases from coke |
| CA1156953A (en) | 1979-06-08 | 1983-11-15 | Michael A. Kessick | Lime addition to heavy crude oils prior to coking |
| US4232514A (en) | 1979-06-20 | 1980-11-11 | General Motors Corporation | Dump control for turbine engine gate valve actuator |
| US4328091A (en) | 1979-11-01 | 1982-05-04 | Engelhard Minerals & Chemicals Corporation | Selective vaporization process |
| US4311580A (en) | 1979-11-01 | 1982-01-19 | Engelhard Minerals & Chemicals Corporation | Selective vaporization process and dynamic control thereof |
| US4448589A (en) | 1980-01-23 | 1984-05-15 | Kansas State University Research Foundation | Pyrolytic conversion of carbonaceous solids to fuel gas in quartz sand fluidized beds |
| US4305809A (en) | 1980-03-06 | 1981-12-15 | Mobil Oil Corporation | Fixed sulfur petroleum coke fuel and method for its production |
| US4294686A (en) | 1980-03-11 | 1981-10-13 | Gulf Canada Limited | Process for upgrading heavy hydrocarbonaceous oils |
| US4446009A (en) | 1980-06-02 | 1984-05-01 | Engelhard Corporation | Selective vaporization process and apparatus |
| JPS5718783A (en) | 1980-07-09 | 1982-01-30 | Terukatsu Miyauchi | Pyrolysis of heavy oil |
| US4428862A (en) * | 1980-07-28 | 1984-01-31 | Union Oil Company Of California | Catalyst for simultaneous hydrotreating and hydrodewaxing of hydrocarbons |
| EP0072873B1 (en) | 1981-08-21 | 1986-02-26 | Kiyoshige Hayashi | Refining process for producing increased yield of distillation from heavy petroleum feedstocks |
| US4569753A (en) | 1981-09-01 | 1986-02-11 | Ashland Oil, Inc. | Oil upgrading by thermal and catalytic cracking |
| US4490234A (en) | 1982-02-22 | 1984-12-25 | Beckman Instruments, Inc. | Method for measuring ionic concentration utilizing an ion-sensing electrode |
| US4409416A (en) | 1982-03-01 | 1983-10-11 | Snell George J | Lignin cracking process using fast fluidized bed reactions |
| GB2117394B (en) | 1982-03-22 | 1986-05-21 | Engelhard Corp | Decarbonizing and demetallizing petroleum stocks |
| US4435272A (en) | 1982-04-16 | 1984-03-06 | Engelhard Corporation | Process for upgrading crude oil and residual fractions thereof by vaporizing the charge in a falling curtain of contact particles |
| US4427539A (en) | 1982-09-07 | 1984-01-24 | Ashland Oil, Inc. | Demetallizing and decarbonizing heavy residual oil feeds |
| US4507195A (en) | 1983-05-16 | 1985-03-26 | Chevron Research Company | Coking contaminated oil shale or tar sand oil on retorted solid fines |
| JPS60248793A (en) | 1984-05-22 | 1985-12-09 | Fuji Standard Res Kk | Thermal decomposition of heavy oil |
| US4818373A (en) | 1984-10-19 | 1989-04-04 | Engelhard Corporation | Process for upgrading tar and bitumen |
| US4578183A (en) | 1984-11-30 | 1986-03-25 | Mobil Oil Corporation | Feed mixing technique for fluidized catalytic cracking of hydrocarbon oil |
| US4828681A (en) | 1984-12-24 | 1989-05-09 | Exxon Research & Engineering Company | Process of thermally cracking hydrocarbons using particulate solids as heat carrier |
| JPH0662958B2 (en) | 1985-02-28 | 1994-08-17 | 富士スタンダ−ドリサ−チ株式会社 | Pyrolysis of heavy oil |
| DE3663955D1 (en) | 1985-11-12 | 1989-07-20 | Inst Francais Du Petrole | Process and apparatus for the catalytic cracking of a hydrocarbon feedstock submitted to a pretreatment with solid particles having a poor activity |
| US4747938A (en) | 1986-04-17 | 1988-05-31 | The United States Of America As Represented By The United States Department Of Energy | Low temperature pyrolysis of coal or oil shale in the presence of calcium compounds |
| US4816136A (en) | 1986-05-27 | 1989-03-28 | Exxon Research And Engineering Company | Low severity fluid coking |
| US4693808A (en) | 1986-06-16 | 1987-09-15 | Shell Oil Company | Downflow fluidized catalytic cranking reactor process and apparatus with quick catalyst separation means in the bottom thereof |
| CA1283880C (en) | 1987-05-07 | 1991-05-07 | Dave A. Berg | Method and apparatus for rapid thermal processing |
| US4919898A (en) | 1987-08-11 | 1990-04-24 | Stone & Webster Engineering Corp. | Particulate solids cracking apparatus |
| US4814067A (en) | 1987-08-11 | 1989-03-21 | Stone & Webster Engineering Corporation | Particulate solids cracking apparatus and process |
| DE3828633A1 (en) | 1987-08-29 | 1989-03-09 | Asea Brown Boveri | Process for the utilisation (valorisation) of starting material containing halogenated hydrocarbons |
| US4985136A (en) | 1987-11-05 | 1991-01-15 | Bartholic David B | Ultra-short contact time fluidized catalytic cracking process |
| US4980045A (en) | 1988-08-02 | 1990-12-25 | Chevron Research Company | Heavy oil pretreatment process with reduced sulfur oxide emissions |
| US5092984A (en) | 1989-12-29 | 1992-03-03 | Institute Of Gas Technology | Pyrolysis of coal |
| US5792340A (en) | 1990-01-31 | 1998-08-11 | Ensyn Technologies, Inc. | Method and apparatus for a circulating bed transport fast pyrolysis reactor system |
| CA2009021C (en) * | 1990-01-31 | 2001-09-11 | Barry A. Freel | Method and apparatus for a circulating bed transport fast pyrolysis reactor system |
| US5626741A (en) * | 1990-03-26 | 1997-05-06 | Amoco Corporation | Catalytic cracking with quenching |
| US5077261A (en) | 1990-06-25 | 1991-12-31 | Phillips Petroleum Company | Sulfur absorbants |
| CA2022721C (en) * | 1990-08-03 | 1999-10-26 | Teresa Ignasiak | Process for converting heavy oil deposited on coal to distillable oil in a low severity process |
| US5136117A (en) | 1990-08-23 | 1992-08-04 | Battelle Memorial Institute | Monomeric recovery from polymeric materials |
| US5102854A (en) | 1991-03-08 | 1992-04-07 | Phillips Petroleum Company | Adsorbent compositions for the removal of hydrogen sulfide from fluid streams |
| US5120428A (en) * | 1991-06-06 | 1992-06-09 | Energy Mines & Resources Canada | Deashing of heavy hydrocarbon residues |
| US5370848A (en) | 1991-06-20 | 1994-12-06 | Phillips Petroleum Company | Sulfur absorbents |
| US5413702A (en) | 1992-02-21 | 1995-05-09 | Mobil Oil Corporation | High severity visbreaking of residual oil |
| US5296131A (en) | 1992-12-02 | 1994-03-22 | Mobil Oil Corporation | Process for short contact time cracking |
| US5264623A (en) | 1993-01-04 | 1993-11-23 | Energy Mines & Resources Canada | Method of producing calcium salts from biomass |
| US5370789A (en) | 1994-02-03 | 1994-12-06 | Energy Mines & Resources Canada | Ultrapyrolytic heavy oil upgrading in an internally circulating aerated bed |
| US5662868A (en) | 1994-09-22 | 1997-09-02 | Stone & Webster Engineering Corporation | Short residence time cracking apparatus and process |
| US5723040A (en) | 1994-09-22 | 1998-03-03 | Stone & Webster Engineering Corporation | Fluid catalytic cracking process and apparatus |
| US5626742A (en) * | 1995-05-02 | 1997-05-06 | Exxon Reseach & Engineering Company | Continuous in-situ process for upgrading heavy oil using aqueous base |
| US5952539A (en) | 1996-02-23 | 1999-09-14 | Exxon Chemical Patents Inc. | Dual process for obtaining olefins |
| US5858213A (en) * | 1996-07-30 | 1999-01-12 | Exxon Research And Engineering Company | Monitoring for coke formation during hydrocarbon feed processing |
| US5807478A (en) | 1997-05-16 | 1998-09-15 | Exxon Research And Engineering Company | Bitumen modification using fly ash derived from bitumen coke |
| US5904839A (en) | 1997-06-06 | 1999-05-18 | Exxon Research And Engineering Co. | Process for upgrading heavy oil using lime |
| US5928501A (en) | 1998-02-03 | 1999-07-27 | Texaco Inc. | Process for upgrading a hydrocarbon oil |
| DE69904212T2 (en) * | 1998-09-03 | 2003-08-28 | Dow Chemical Co | ONLINE SYNTHESIS AND REGENERATION OF A CATALYST FOR AUTOTHERMAL OXIDATION |
| ES2429508T3 (en) * | 1999-04-07 | 2013-11-15 | Ivanhoe Htl Petroleum Ltd | Fast thermal processing of bitumen raw materials |
| US7270743B2 (en) | 2000-09-18 | 2007-09-18 | Ivanhoe Energy, Inc. | Products produced form rapid thermal processing of heavy hydrocarbon feedstocks |
-
2001
- 2001-09-18 US US09/955,267 patent/US7270743B2/en not_active Expired - Fee Related
- 2001-09-18 PT PT01971568T patent/PT1332199E/en unknown
- 2001-09-18 AR ARP010104414A patent/AR033838A1/en not_active Application Discontinuation
- 2001-09-18 EP EP10075528A patent/EP2275513A3/en not_active Withdrawn
- 2001-09-18 DK DK01971568.9T patent/DK1332199T3/en active
- 2001-09-18 AT AT01971568T patent/ATE532842T1/en active
- 2001-09-18 CA CA2422534A patent/CA2422534C/en not_active Expired - Fee Related
- 2001-09-18 ES ES01971568T patent/ES2395116T3/en not_active Expired - Lifetime
- 2001-09-18 WO PCT/CA2001/001316 patent/WO2002024835A2/en active Application Filing
- 2001-09-18 MX MXPA03002341A patent/MXPA03002341A/en active IP Right Grant
- 2001-09-18 EP EP01971568A patent/EP1332199B8/en not_active Expired - Lifetime
- 2001-09-18 AU AU2001291563A patent/AU2001291563A1/en not_active Abandoned
- 2001-09-18 BR BR0113937-1A patent/BR0113937A/en not_active IP Right Cessation
-
2003
- 2003-03-17 NO NO20031230A patent/NO330786B1/en not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| ES2395116T3 (en) | 2013-02-08 |
| EP2275513A2 (en) | 2011-01-19 |
| AU2001291563A1 (en) | 2002-04-02 |
| WO2002024835A2 (en) | 2002-03-28 |
| AR033838A1 (en) | 2004-01-07 |
| NO20031230D0 (en) | 2003-03-17 |
| NO20031230L (en) | 2003-05-19 |
| US7270743B2 (en) | 2007-09-18 |
| EP1332199A2 (en) | 2003-08-06 |
| WO2002024835A3 (en) | 2002-10-31 |
| EP1332199B1 (en) | 2011-11-09 |
| EP2275513A3 (en) | 2011-04-13 |
| BR0113937A (en) | 2004-01-13 |
| PT1332199E (en) | 2012-02-06 |
| DK1332199T3 (en) | 2012-02-06 |
| CA2422534C (en) | 2012-05-22 |
| ATE532842T1 (en) | 2011-11-15 |
| MXPA03002341A (en) | 2003-10-06 |
| US20020100711A1 (en) | 2002-08-01 |
| NO330786B1 (en) | 2011-07-18 |
| EP1332199B8 (en) | 2012-03-14 |
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