CA2012071A1 - Upgrading oil emulsions with carbon monoxide or synthesis gas - Google Patents
Upgrading oil emulsions with carbon monoxide or synthesis gasInfo
- Publication number
- CA2012071A1 CA2012071A1 CA2012071A CA2012071A CA2012071A1 CA 2012071 A1 CA2012071 A1 CA 2012071A1 CA 2012071 A CA2012071 A CA 2012071A CA 2012071 A CA2012071 A CA 2012071A CA 2012071 A1 CA2012071 A1 CA 2012071A1
- Authority
- CA
- Canada
- Prior art keywords
- carbon monoxide
- hydrogen
- temperature range
- carbon dioxide
- cracking
- 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
-
- 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
- C10G9/007—Visbreaking
Abstract
ABSTRACT OF THE DISCLOSURE
Several procedures are provided herein which reduce the viscosity and density of heavy oils to make them amenable for transportation by pipeline from the field to refineries for further processing. The procedure involves contacting a water emulsion of a heavy oil with carbon monoxide at a pressure range and a temperature range such that a water gas shift reaction takes place to convert the steam and carbon monoxide to hydrogen and carbon dioxide. Simultaneously, a thermal rearrangement takes place, thereby reducing the viscosity and density of the oil without any significant thermal cracking. Under one procedure, at a low temperature range, e.g., below 400°C., there is substantially no cracking and minimal molecular changes.
Under another procedure, at a higher temperature range, e.g., up to 460°C., significant cracking and molecular changes take place.
Nevertheless under both procedures there is a net production of hydrogen and carbon dioxide, and both hydrogen and carbon dioxide are separated, and may be used in other processes.
Several procedures are provided herein which reduce the viscosity and density of heavy oils to make them amenable for transportation by pipeline from the field to refineries for further processing. The procedure involves contacting a water emulsion of a heavy oil with carbon monoxide at a pressure range and a temperature range such that a water gas shift reaction takes place to convert the steam and carbon monoxide to hydrogen and carbon dioxide. Simultaneously, a thermal rearrangement takes place, thereby reducing the viscosity and density of the oil without any significant thermal cracking. Under one procedure, at a low temperature range, e.g., below 400°C., there is substantially no cracking and minimal molecular changes.
Under another procedure, at a higher temperature range, e.g., up to 460°C., significant cracking and molecular changes take place.
Nevertheless under both procedures there is a net production of hydrogen and carbon dioxide, and both hydrogen and carbon dioxide are separated, and may be used in other processes.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA002012071A CA2012071C (en) | 1990-03-13 | 1990-03-13 | Upgrading oil emulsions with carbon monoxide or synthesis gas |
US07/578,262 US5104516A (en) | 1990-03-13 | 1990-09-06 | Upgrading oil emulsions with carbon monoxide or synthesis gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA002012071A CA2012071C (en) | 1990-03-13 | 1990-03-13 | Upgrading oil emulsions with carbon monoxide or synthesis gas |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2012071A1 true CA2012071A1 (en) | 1991-09-13 |
CA2012071C CA2012071C (en) | 1994-03-08 |
Family
ID=4144514
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA002012071A Expired - Lifetime CA2012071C (en) | 1990-03-13 | 1990-03-13 | Upgrading oil emulsions with carbon monoxide or synthesis gas |
Country Status (2)
Country | Link |
---|---|
US (1) | US5104516A (en) |
CA (1) | CA2012071C (en) |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4032045A1 (en) * | 1990-10-09 | 1992-04-23 | Uhde Gmbh | Partial oxidn. of bitumen oil emulsions - using oxygen@ or air, useful for prodn. of synthesis gas and hydrogen@ |
US5868923A (en) * | 1991-05-02 | 1999-02-09 | Texaco Inc | Hydroconversion process |
US5322617A (en) * | 1992-08-07 | 1994-06-21 | Her Majesty The Queen In Right Of Canada As Represented By The Minister Of Energy, Mines And Resources | Upgrading oil emulsions with carbon monoxide or synthesis gas |
US6059957A (en) * | 1996-09-16 | 2000-05-09 | Texaco Inc. | Methods for adding value to heavy oil |
US5935419A (en) * | 1996-09-16 | 1999-08-10 | Texaco Inc. | Methods for adding value to heavy oil utilizing a soluble metal catalyst |
AU3798300A (en) * | 1999-04-07 | 2000-11-14 | Ensyn Group, Inc. | Rapid thermal processing of heavy hydrocarbon feedstocks |
US6491053B1 (en) | 1999-05-24 | 2002-12-10 | William H. Briggeman | Method and system for reducing the viscosity of crude oil |
US6644334B2 (en) | 2000-05-05 | 2003-11-11 | William H. Briggeman | Method and system for reducing the viscosity of crude oil employing engine exhaust gas |
US7790018B2 (en) * | 2005-05-11 | 2010-09-07 | Saudia Arabian Oil Company | Methods for making higher value products from sulfur containing crude oil |
US8322430B2 (en) * | 2005-06-03 | 2012-12-04 | Shell Oil Company | Pipes, systems, and methods for transporting fluids |
CA2705199A1 (en) * | 2007-11-19 | 2009-05-28 | Shell Internationale Research Maatschappij B.V. | Producing oil and/or gas with emulsion comprising miscible solvent |
WO2009117191A1 (en) * | 2008-03-20 | 2009-09-24 | Exxonmobil Upstream Research Company | Viscous oil recovery using emulsions |
US20130193040A1 (en) * | 2011-08-08 | 2013-08-01 | Ah-Hyung Alissa Park | Systems for automated capture and recovery of oil from oil-contaminated water and solids |
CA2963436C (en) | 2017-04-06 | 2022-09-20 | Iftikhar Huq | Partial upgrading of bitumen |
CN115820333B (en) * | 2021-09-17 | 2024-01-26 | 山东大学 | Recycling recycling method of waste lubricating oil sludge |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3929429A (en) * | 1974-09-26 | 1975-12-30 | Texaco Inc | Fuel gas from solid carbonaceous fuels |
US4007019A (en) * | 1975-12-22 | 1977-02-08 | Texaco Inc. | Production of clean synthesis or fuel gas |
US4007018A (en) * | 1975-12-22 | 1977-02-08 | Texaco Inc. | Production of clean synthesis or fuel gas |
US4309274A (en) * | 1979-05-14 | 1982-01-05 | Engelhard Minerals & Chemicals Corporation | Preparation of FCC charge from residual fractions |
US4542114A (en) * | 1982-08-03 | 1985-09-17 | Air Products And Chemicals, Inc. | Process for the recovery and recycle of effluent gas from the regeneration of particulate matter with oxygen and carbon dioxide |
US4504377A (en) * | 1983-12-09 | 1985-03-12 | Mobil Oil Corporation | Production of stable low viscosity heating oil |
-
1990
- 1990-03-13 CA CA002012071A patent/CA2012071C/en not_active Expired - Lifetime
- 1990-09-06 US US07/578,262 patent/US5104516A/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
US5104516A (en) | 1992-04-14 |
CA2012071C (en) | 1994-03-08 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
EEER | Examination request | ||
MKEX | Expiry |