CA2353109A1 - Process for removing solvent from an underflow stream from the last separation step in an oil sands froth treatment process - Google Patents
Process for removing solvent from an underflow stream from the last separation step in an oil sands froth treatment process Download PDFInfo
- Publication number
- CA2353109A1 CA2353109A1 CA002353109A CA2353109A CA2353109A1 CA 2353109 A1 CA2353109 A1 CA 2353109A1 CA 002353109 A CA002353109 A CA 002353109A CA 2353109 A CA2353109 A CA 2353109A CA 2353109 A1 CA2353109 A1 CA 2353109A1
- Authority
- CA
- Canada
- Prior art keywords
- solvent
- stream
- oil sands
- solids
- last separation
- 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
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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
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/04—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by extraction
- C10G1/047—Hot water or cold water extraction processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/0208—Separation of non-miscible liquids by sedimentation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/0208—Separation of non-miscible liquids by sedimentation
- B01D17/0211—Separation of non-miscible liquids by sedimentation with baffles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/04—Breaking emulsions
- B01D17/041—Breaking emulsions with moving devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/0018—Separation of suspended solid particles from liquids by sedimentation provided with a pump mounted in or on a settling tank
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/0039—Settling tanks provided with contact surfaces, e.g. baffles, particles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/0039—Settling tanks provided with contact surfaces, e.g. baffles, particles
- B01D21/0042—Baffles or guide plates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/009—Heating or cooling mechanisms specially adapted for settling tanks
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/24—Feed or discharge mechanisms for settling tanks
- B01D21/2433—Discharge mechanisms for floating particles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/24—Feed or discharge mechanisms for settling tanks
- B01D21/2444—Discharge mechanisms for the classified liquid
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0033—Other features
- B01D5/0036—Multiple-effect condensation; Fractional condensation
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B9/00—General arrangement of separating plant, e.g. flow sheets
- B03B9/02—General arrangement of separating plant, e.g. flow sheets specially adapted for oil-sand, oil-chalk, oil-shales, ozokerite, bitumen, or the like
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/08—Subsequent treatment of concentrated product
- B03D1/10—Removing adhering liquid from separated materials
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/12—Agent recovery
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/048—Purification of waste water by evaporation
-
- 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
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/04—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by extraction
- C10G1/045—Separation of insoluble materials
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/0208—Separation of non-miscible liquids by sedimentation
- B01D17/0214—Separation of non-miscible liquids by sedimentation with removal of one of the phases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/04—Breaking emulsions
- B01D17/042—Breaking emulsions by changing the temperature
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/04—Breaking emulsions
- B01D17/044—Breaking emulsions by changing the pressure
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/04—Breaking emulsions
- B01D17/045—Breaking emulsions with coalescers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/04—Breaking emulsions
- B01D17/047—Breaking emulsions with separation aids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/04—Breaking emulsions
- B01D17/048—Breaking emulsions by changing the state of aggregation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/0005—Degasification of liquids with one or more auxiliary substances
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/10—Treatment of water, waste water, or sewage by heating by distillation or evaporation by direct contact with a particulate solid or with a fluid, as a heat transfer medium
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Thermal Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Physics & Mathematics (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Wood Science & Technology (AREA)
- Water Supply & Treatment (AREA)
- Dispersion Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Hydrology & Water Resources (AREA)
- Geology (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Degasification And Air Bubble Elimination (AREA)
Abstract
A process is described for treating an underflow stream containing water, solvent, asphaltenes and solids, from one of the last separation steps in a paraffinic solvent process for separating bitumen from an oil sands froth, wherein a) the stream is introduced to a solvent recovery vessel that is substantially free of internals wherein the temperature and pressure are such that the solvent is normally a vapour, b) a pool of liquid and solids is maintained in the lower part of the vessel at a controlled level for sufficient time to allow the solvent to vapourize, c) the pool is agitated to the point where the asphaltenes are dispersed, submerged and prevented from re-agglomerating and the solids are maintained in suspension, d) the solvent is recovered as an overhead vapour stream, and e) the solvent depleted remainder of the stream is removed from the bottom of the vessel as a liquid slurry.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA002353109A CA2353109C (en) | 2001-07-16 | 2001-07-16 | Process for removing solvent from an underflow stream from the last separation step in an oil sands froth treatment process |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA002353109A CA2353109C (en) | 2001-07-16 | 2001-07-16 | Process for removing solvent from an underflow stream from the last separation step in an oil sands froth treatment process |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2353109A1 true CA2353109A1 (en) | 2003-01-16 |
CA2353109C CA2353109C (en) | 2005-12-06 |
Family
ID=4169477
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA002353109A Expired - Lifetime CA2353109C (en) | 2001-07-16 | 2001-07-16 | Process for removing solvent from an underflow stream from the last separation step in an oil sands froth treatment process |
Country Status (1)
Country | Link |
---|---|
CA (1) | CA2353109C (en) |
Cited By (30)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20080185350A1 (en) * | 2007-02-05 | 2008-08-07 | Koch-Glitsch, Lp | Method and apparatus for separating oil sand particulates from a three-phase stream |
US20100282642A1 (en) * | 2009-05-07 | 2010-11-11 | Total E&P Canada, Ltd. | Tailings solvent recovery unit |
US8349269B2 (en) | 2007-06-27 | 2013-01-08 | H R D Corporation | High shear system and process for the production of acetic anhydride |
CN103143435A (en) * | 2013-02-19 | 2013-06-12 | 蔡宏武 | Complete set of electricity and water-saving water supply and drainage unit suitable for concentration plant |
US8592351B2 (en) | 2008-03-20 | 2013-11-26 | Exxonmobil Upstream Research Company | Enhancing emulsion stability |
US8591724B2 (en) | 2009-07-14 | 2013-11-26 | Exxonmobil Upstream Research Company | Feed delivery system for a solid-liquid separation vessel |
US8597504B2 (en) | 2008-06-27 | 2013-12-03 | Arun K. Sharma | Optimizing feed mixer performance in a paraffinic froth treatment process |
US8701470B2 (en) | 2009-01-23 | 2014-04-22 | Exxonmobil Upstream Research Company | Method and system for determining particle size distribution and filterable solids in a bitumen-containing fluid |
US8852429B2 (en) | 2010-02-22 | 2014-10-07 | Titanium Corporation Inc. | Method for processing froth treatment tailings |
US8949038B2 (en) | 2010-09-22 | 2015-02-03 | Exxonmobil Upstream Research Company | Controlling bitumen quality in solvent-assisted bitumen extraction |
US8974661B2 (en) | 2010-12-30 | 2015-03-10 | Exxonmobil Upstream Research Company | Methods for separation of bitumen from oil sands |
US9207019B2 (en) | 2011-04-15 | 2015-12-08 | Fort Hills Energy L.P. | Heat recovery for bitumen froth treatment plant integration with sealed closed-loop cooling circuit |
US9222929B2 (en) | 2009-12-07 | 2015-12-29 | Exxonmobil Upstream Research Company | Solvent surveillance in solvent-based heavy oil recovery processes |
US9283499B2 (en) | 2011-03-29 | 2016-03-15 | Exxonmobil Upstream Research Company | Feedwell system for a separation vessel |
US9314713B2 (en) | 2010-05-12 | 2016-04-19 | Titanium Corporation | Apparatus and method for recovering a hydrocarbon diluent from tailings |
US9475994B2 (en) | 2011-05-03 | 2016-10-25 | Exxonmobil Upstream Research Company | Enhancing fine capture in paraffinic froth treatment process |
US9546323B2 (en) | 2011-01-27 | 2017-01-17 | Fort Hills Energy L.P. | Process for integration of paraffinic froth treatment hub and a bitumen ore mining and extraction facility |
US9550190B2 (en) | 2011-11-08 | 2017-01-24 | Exxonmobil Upstream Research Company | Dewatering oil sand tailings |
US9587176B2 (en) | 2011-02-25 | 2017-03-07 | Fort Hills Energy L.P. | Process for treating high paraffin diluted bitumen |
US9587177B2 (en) | 2011-05-04 | 2017-03-07 | Fort Hills Energy L.P. | Enhanced turndown process for a bitumen froth treatment operation |
US9676684B2 (en) | 2011-03-01 | 2017-06-13 | Fort Hills Energy L.P. | Process and unit for solvent recovery from solvent diluted tailings derived from bitumen froth treatment |
US9719022B2 (en) | 2009-04-09 | 2017-08-01 | Titanium Corporation Inc. | Methods for separating a feed material derived from a process for recovering bitumen from oil sands |
US9791170B2 (en) | 2011-03-22 | 2017-10-17 | Fort Hills Energy L.P. | Process for direct steam injection heating of oil sands slurry streams such as bitumen froth |
US10041005B2 (en) | 2011-03-04 | 2018-08-07 | Fort Hills Energy L.P. | Process and system for solvent addition to bitumen froth |
CN108636122A (en) * | 2018-06-22 | 2018-10-12 | 南京航空航天大学 | Pressure drops arranging system and the working method such as a kind of more membrane components and compressor |
US10226717B2 (en) | 2011-04-28 | 2019-03-12 | Fort Hills Energy L.P. | Method of recovering solvent from tailings by flashing under choked flow conditions |
US10508241B2 (en) | 2017-06-05 | 2019-12-17 | Syncrude Canada Ltd. | Recovery of hydrocarbon diluent from tailings |
US10954448B2 (en) | 2017-08-18 | 2021-03-23 | Canadian Natural Resources Limited | High temperature paraffinic froth treatment process |
US11261383B2 (en) | 2011-05-18 | 2022-03-01 | Fort Hills Energy L.P. | Enhanced temperature control of bitumen froth treatment process |
CN114787290A (en) * | 2019-11-28 | 2022-07-22 | 班恩化工公司 | Process for purifying indigo white salt solutions using inert gases |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA2455011C (en) | 2004-01-09 | 2011-04-05 | Suncor Energy Inc. | Bituminous froth inline steam injection processing |
CA2595336C (en) | 2007-07-31 | 2009-09-15 | Imperial Oil Resources Limited | Reducing foulant carry-over or build-up in a paraffinic froth treatment process |
US8357291B2 (en) | 2008-02-11 | 2013-01-22 | Exxonmobil Upstream Research Company | Upgrading bitumen in a paraffinic froth treatment process |
CA2645267C (en) | 2008-11-26 | 2013-04-16 | Imperial Oil Resources Limited | Solvent for extracting bitumen from oil sands |
CA2644821C (en) | 2008-11-26 | 2013-02-19 | Imperial Oil Resources Limited | A method for using native bitumen markers to improve solvent-assisted bitumen extraction |
CA2693640C (en) | 2010-02-17 | 2013-10-01 | Exxonmobil Upstream Research Company | Solvent separation in a solvent-dominated recovery process |
CA2696638C (en) | 2010-03-16 | 2012-08-07 | Exxonmobil Upstream Research Company | Use of a solvent-external emulsion for in situ oil recovery |
CA2705643C (en) | 2010-05-26 | 2016-11-01 | Imperial Oil Resources Limited | Optimization of solvent-dominated recovery |
US8739869B2 (en) | 2010-11-19 | 2014-06-03 | Exxonmobil Upstream Research Company | Systems and methods for enhanced waterfloods |
US8657000B2 (en) | 2010-11-19 | 2014-02-25 | Exxonmobil Upstream Research Company | Systems and methods for enhanced waterfloods |
US8656996B2 (en) | 2010-11-19 | 2014-02-25 | Exxonmobil Upstream Research Company | Systems and methods for enhanced waterfloods |
-
2001
- 2001-07-16 CA CA002353109A patent/CA2353109C/en not_active Expired - Lifetime
Cited By (41)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20080185350A1 (en) * | 2007-02-05 | 2008-08-07 | Koch-Glitsch, Lp | Method and apparatus for separating oil sand particulates from a three-phase stream |
US8592620B2 (en) | 2007-06-27 | 2013-11-26 | H R D Corporation | High shear system and process for the production of acetic anhydride |
US8349269B2 (en) | 2007-06-27 | 2013-01-08 | H R D Corporation | High shear system and process for the production of acetic anhydride |
US8592351B2 (en) | 2008-03-20 | 2013-11-26 | Exxonmobil Upstream Research Company | Enhancing emulsion stability |
US8597504B2 (en) | 2008-06-27 | 2013-12-03 | Arun K. Sharma | Optimizing feed mixer performance in a paraffinic froth treatment process |
US8701470B2 (en) | 2009-01-23 | 2014-04-22 | Exxonmobil Upstream Research Company | Method and system for determining particle size distribution and filterable solids in a bitumen-containing fluid |
US9719022B2 (en) | 2009-04-09 | 2017-08-01 | Titanium Corporation Inc. | Methods for separating a feed material derived from a process for recovering bitumen from oil sands |
US20100282642A1 (en) * | 2009-05-07 | 2010-11-11 | Total E&P Canada, Ltd. | Tailings solvent recovery unit |
US8197676B2 (en) | 2009-05-07 | 2012-06-12 | Total E&P Canada Ltd | Method for tailings solvent recovery |
US8741107B2 (en) | 2009-05-07 | 2014-06-03 | Total E & P Canada Ltd. | Tailings solvent recovery unit |
US9089797B2 (en) | 2009-07-14 | 2015-07-28 | Exxonmobil Upstream Research Company | Feed delivery system for a solid-liquid separation vessel |
US8591724B2 (en) | 2009-07-14 | 2013-11-26 | Exxonmobil Upstream Research Company | Feed delivery system for a solid-liquid separation vessel |
US9222929B2 (en) | 2009-12-07 | 2015-12-29 | Exxonmobil Upstream Research Company | Solvent surveillance in solvent-based heavy oil recovery processes |
US8852429B2 (en) | 2010-02-22 | 2014-10-07 | Titanium Corporation Inc. | Method for processing froth treatment tailings |
US9314713B2 (en) | 2010-05-12 | 2016-04-19 | Titanium Corporation | Apparatus and method for recovering a hydrocarbon diluent from tailings |
US8949038B2 (en) | 2010-09-22 | 2015-02-03 | Exxonmobil Upstream Research Company | Controlling bitumen quality in solvent-assisted bitumen extraction |
US8974661B2 (en) | 2010-12-30 | 2015-03-10 | Exxonmobil Upstream Research Company | Methods for separation of bitumen from oil sands |
US9546323B2 (en) | 2011-01-27 | 2017-01-17 | Fort Hills Energy L.P. | Process for integration of paraffinic froth treatment hub and a bitumen ore mining and extraction facility |
US10125325B2 (en) | 2011-02-25 | 2018-11-13 | Fort Hills Energy L.P. | Process for treating high paraffin diluted bitumen |
US9587176B2 (en) | 2011-02-25 | 2017-03-07 | Fort Hills Energy L.P. | Process for treating high paraffin diluted bitumen |
US9676684B2 (en) | 2011-03-01 | 2017-06-13 | Fort Hills Energy L.P. | Process and unit for solvent recovery from solvent diluted tailings derived from bitumen froth treatment |
US10041005B2 (en) | 2011-03-04 | 2018-08-07 | Fort Hills Energy L.P. | Process and system for solvent addition to bitumen froth |
US10988695B2 (en) | 2011-03-04 | 2021-04-27 | Fort Hills Energy L.P. | Process and system for solvent addition to bitumen froth |
US9791170B2 (en) | 2011-03-22 | 2017-10-17 | Fort Hills Energy L.P. | Process for direct steam injection heating of oil sands slurry streams such as bitumen froth |
US9283499B2 (en) | 2011-03-29 | 2016-03-15 | Exxonmobil Upstream Research Company | Feedwell system for a separation vessel |
US9207019B2 (en) | 2011-04-15 | 2015-12-08 | Fort Hills Energy L.P. | Heat recovery for bitumen froth treatment plant integration with sealed closed-loop cooling circuit |
US10226717B2 (en) | 2011-04-28 | 2019-03-12 | Fort Hills Energy L.P. | Method of recovering solvent from tailings by flashing under choked flow conditions |
US9475994B2 (en) | 2011-05-03 | 2016-10-25 | Exxonmobil Upstream Research Company | Enhancing fine capture in paraffinic froth treatment process |
US9587177B2 (en) | 2011-05-04 | 2017-03-07 | Fort Hills Energy L.P. | Enhanced turndown process for a bitumen froth treatment operation |
US11261383B2 (en) | 2011-05-18 | 2022-03-01 | Fort Hills Energy L.P. | Enhanced temperature control of bitumen froth treatment process |
US9550190B2 (en) | 2011-11-08 | 2017-01-24 | Exxonmobil Upstream Research Company | Dewatering oil sand tailings |
CN103143435A (en) * | 2013-02-19 | 2013-06-12 | 蔡宏武 | Complete set of electricity and water-saving water supply and drainage unit suitable for concentration plant |
CN103143435B (en) * | 2013-02-19 | 2014-09-10 | 蔡宏武 | Complete set of electricity and water-saving water supply and drainage unit suitable for concentration plant |
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