WO2014113793A1 - Systems and methods for treating produced water - Google Patents
Systems and methods for treating produced water Download PDFInfo
- Publication number
- WO2014113793A1 WO2014113793A1 PCT/US2014/012336 US2014012336W WO2014113793A1 WO 2014113793 A1 WO2014113793 A1 WO 2014113793A1 US 2014012336 W US2014012336 W US 2014012336W WO 2014113793 A1 WO2014113793 A1 WO 2014113793A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- energy
- water
- produced water
- heat energy
- oil
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K17/00—Using steam or condensate extracted or exhausted from steam engine plant
- F01K17/04—Using steam or condensate extracted or exhausted from steam engine plant for specific purposes other than heating
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K25/00—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for
- F01K25/08—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours
- F01K25/10—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours the vapours being cold, e.g. ammonia, carbon dioxide, ether
-
- 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
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- 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
- C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
-
- 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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
-
- 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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
-
- 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
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/469—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis
- C02F1/4693—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis electrodialysis
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/009—Apparatus with independent power supply, e.g. solar cells, windpower, fuel cells
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/10—Energy recovery
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/20—Controlling water pollution; Waste water treatment
- Y02A20/208—Off-grid powered water treatment
- Y02A20/212—Solar-powered wastewater sewage treatment, e.g. spray evaporation
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
Definitions
- One or more aspects relate generally to energy production, and more particularly to systems and methods for treating water used in oil and gas extraction.
- oil and gas are routinely extracted from underground sources.
- Conventional oil and gas extraction is a water intensive process.
- Produced water is typically unfit for discharge into local water sources and may be injected into underground wells for disposal. Alternatively, produced water may be treated to render it suitable for a variety of uses.
- integrated systems and methods for energy production are disclosed.
- a method for treating produced water may comprise recovering heat energy from the produced water, and using the recovered heat energy to directly drive treatment of the produced water.
- recovering heat energy from the produced water comprises converting heat energy to mechanical energy.
- the mechanical energy may be used to separate oil and/or contaminants from the produced water.
- Recovering heat energy from the produced water may further comprise converting the mechanical energy to electrical energy.
- Recovering heat energy from the produced water may comprise using a heat engine in fluid communication with a generator to convert the recovered heat energy to electrical energy.
- Recovering heat energy from the produced water may comprise using a thermoelectric generator to convert the recovered heat energy to electrical energy.
- the method may further comprise delivering excess recovered heat energy to an energy network.
- An energy network may be used to supplement the recovered heat energy or as a backup source of power.
- the heat energy may be recovered prior to separating oil from the produced water.
- the heat energy may be recovered during treatment of the produced water.
- a system for providing energy to treat produced water may comprise a source of produced water having heat energy, a water treatment subsystem having an energy requirement and fluidly connected downstream of the source of produced water, and an energy recovery subsystem configured to convert a portion of the heat energy from the produced water to mechanical and/or electrical energy, and to supply at least a portion of the energy requirement of the water treatment system.
- the energy recovery subsystem may comprise a generator disposed in communication with a turbine to generate electrical energy.
- the turbine may comprise a two-phase turbine.
- the water treatment subsystem may comprise an oil- water separator and at least one of a microfiltration unit, an activated carbon media unit, a reverse osmosis unit, and an electrodialysis unit.
- the energy recovery subsystem may comprise a heat engine configured to operate in accordance with a trilateral thermodynamic energy conversion cycle.
- FIG. 1 presents a schematic of a conventional water cycle during oil and gas extraction operations in accordance with one or more embodiments
- FIG. 2 presents a schematic of a produced water treatment process in accordance with one or more embodiments
- FIG. 3 presents a schematic of a produced water treatment process in accordance with one or more embodiments
- FIG. 4 presents an energy flow diagram of systems and methods in accordance with one or more embodiments
- FIG. 5 presents an example of heat recovery using a working fluid to exchange and recover heat in accordance with one or more embodiments
- FIG. 6 presents a schematic of a generator suitable for transforming heat energy transferred from a well fluid to electrical energy in accordance with one or more embodiments
- FIG. 7 presents an energy flow diagram of systems and methods in accordance with one or more embodiments.
- FIG. 8 presents a schematic of a thermoelectric generator in accordance with one or more embodiments.
- heat may be extracted from water associated with geothermal applications as well as from various industrial or refinery water streams.
- heat may be recovered from process streams associated with metal casting or the manufacture of cement, iron, steel, aluminum and glass. The recovered energy may then be used to treat the water from which the heat was extracted. The following discussion regarding energy recovery and its use in water treatment may therefore be applied to any source of water to be treated.
- injected water may be used to drive oil or gas to the surface at a well head.
- a typical water to oil ratio may be about 5-10: 1 but may vary greatly.
- Temperatures at the depth under the earth's surface where oil and gas yielding formations exist are generally high, which causes the water to become heated.
- the produced water may be at a temperature in the range of about 100 °F to about 750 °F. In some specific non-limiting embodiments, the produced water may be at about 170 °F.
- a second step 120 of the water cycle the water portion and oil portion of the produced water are separated by various unit operations, as discussed in greater detail below with reference to FIG. 2.
- portions of the separated water stream may undergo different treatment operations depending on their intended use. If the water is intended for reinjection to permanent well disposal or for waterflooding, then further treatment may be minimal.
- a portion of the produced water is reinjected for waterflooding to enhance water production. Alternatively, minimally treated produced water may be injected in an underground well for disposal (not shown). If the intended use requires an improved water quality, such as for irrigation, then a more robust water treatment may be required as discussed in greater detail below with reference to FIG. 3.
- FIG. 2 presents a non-limiting schematic of a method for oil and gas separation from produced water in accordance with one or more embodiments.
- the produced water 210 may enter an oil/water separation train 200 and may first undergo treatment in a gravity separation device 230 to separate the oil from the water.
- a gravity separation device 230 to separate the oil from the water.
- gravity separation devices may operate based on the specific gravity differences between oil and water. Given time, the less dense oil will form an oil layer 240 that floats on top of the denser water layer 230. Likewise, particulate matter will sink to the bottom of the water layer and will be drained out as part of a sludge 250. Hydrocarbons in a vapor phase may, in some embodiments, be directed through a vapor outlet towards a vapor collection vessel (not shown). The oil 240 and water layers 230 may then be directed to different outlets, with the oil layer collected as a commodity, and the water layer directed toward further separation and treatment. Passage through a single separation device may not complete the separation of oil and water to a satisfactory degree.
- the water mixture effluent from device 230 may continue on to another oil water separation unit, for example, an inclined plate separator 260.
- an inclined plate separator smaller oil droplets that remained in the water layer coalesce on the inclined plates 265 into larger droplets and separate from the water layer to form an oil layer 240 separate from the water layer 230. The two layers may then be directed to different outlets.
- the oil layer 240 produced by the inclined plate separator 260 may be removed from the train 200, and collected as a commodity.
- the remaining water mixture may continue on to another separation device, for example, an induced gas flotation device 270 and/or a membrane filter 290.
- an induced gas flotation device gas or air is introduced into the water mixture, coalescing entrained oil particles and bringing them to the surface where they are separated from the water mixture, and reserved as a commodity.
- TDS total dissolved solids
- FIG. 3 presents a schematic of a method for further treatment of a water mixture after oil separation in accordance with one or more embodiments.
- the water treatment train 300 of the non-limiting embodiment presented may include microfiltration 310, activated carbon media 320, and/or a desalination process such as reverse osmosis or electrodialysis 330 unit operations.
- Microfiltration 310 typically refers to filtration with a membrane pore size ranging from 0.1 to 10 microns. However, other filtration techniques, whether they involve larger or smaller pore sizes, may be substituted for microfiltration.
- Another method for filtering which may be employed in the water treatment train 300 involves activated carbon media 320, e.g., activated carbon, to remove contaminants through chemical adsorption.
- Reverse osmosis 330 may separate contaminants by applying pressure to push a water stream through a selective membrane. Additional or alternative steps in the water treatment train 300 not shown could include coagulation and flocculation, water softening, air stripping, or any other process generally known in the art for treating water. Various combinations of such unit operations may be used for treatment.
- the result of this water treatment train 300 may be a concentrate flow 340 which comprises a reject stream that includes the impurities, and a product flow 350 which comprises purified water of a quality that may be suitable for a variety of uses.
- the product flow 350 may be appropriate for a number of end uses which fall within established water quality regulations.
- the product flow may be used to recharge aquifers, or for agricultural and irrigation purposes.
- heat energy from well fluids or other sources of water to be treated may be harnessed to power oil/water separation and other water treatment processes. Treatment of produced water may be driven by heat energy captured from the produced water. Such integration may beneficially allow water treatment and overall oil or gas extraction operations to be performed in a more efficient manner.
- the temperature of the produced water may vary, such as may depend on geographical location, depth of extraction, and other factors. In some embodiments, the temperature may be relatively low, for example, between about -10 and 200 °F.
- FIG. 4 presents a non-limiting schematic of an integrated system and method in accordance with one or more embodiments.
- System 400 includes oil and gas recovery 440 and water treatment 450 operations.
- System 400 may also include an energy recovery system 460, electric generator(s) 470, and/or an energy supply 420 as discussed below.
- the energy recovery system 460 may convert heat energy 480 from well fluids 475 to mechanical energy 485 and/or electrical energy 490.
- Mechanical energy 485 and electrical energy 490 may be used to operate unit operations of not only the oil/water separation processes 440 but also the further water treatment processes 450.
- the heated well fluid, or heated produced water 475 may be directed to a heat exchanger which may be part of the energy recovery system 460.
- the transfer of heat from the well fluids 475 can occur at any point or multiple points along its path.
- One or more heat energy recovery units may be used.
- the heat energy may be recovered prior to or during oil/water separation. Heat energy may be recovered during a downstream water treatment process.
- cooling may generally be required prior to surface discharge and upstream of any membrane filtration or biological treatment used for water treatment.
- the heat from the well fluids may be transferred to a working fluid in a heat exchanger as part of the energy recovery system 460 in accordance with one or more embodiments.
- a heat exchanger may be implemented which are capable of operating at the involved process conditions.
- the inlet temperature to the heat exchanger may be about 40 to 100 °F.
- the outlet temperature from the heat exchanger may be about 45 to 110 °F.
- the heated working fluid may then be vaporized to drive a turbine, or other mechanical transfer device, thus converting the heat energy to mechanical energy in some non-limiting embodiments. Any mechanical transfer device may be used.
- a turbine may be used.
- the turbine should generally be suitable for operation at the involved process temperatures as discussed herein.
- the turbine may be a Euler turbine or a variable phase turbine.
- the turbine may be a two-phase turbine commercially available from Energent Corporation (CA).
- CA Energent Corporation
- a screw expander or other mechanical transfer device may be used.
- the mechanical energy of the turbine may then be used directly or to generate electrical energy via a generator 470.
- the mechanical energy may be used for driving pump(s) 430, oil/water separator 440 or water treatment process 450.
- Other applicable methods for energy extraction may be recognized by those of ordinary skill in the art.
- the electrical energy 490 thus produced may then be used to directly supply or supplement the electrical energy requirements of the unit operations 440 and/or 450. If the produced electricity 490 exceeds system
- the difference may be supplied to grid 420.
- the difference may be supplied from the grid 420.
- the turbine may be used to generate electricity.
- the turbine may be used to provide mechanical energy to a water treatment process, for example, to directly move a pump, a mixer or other device.
- the energy recovery system may transfer mechanical energy to an oil water separator and/or a water treatment process.
- a rotating shaft may be implemented such that shaft energy may be used directly in an oil separator, for example, to run a mixer, or a flotation unit.
- FIG. 5 presents a non-limiting schematic illustrating a system 500 for the exchange of heat from a well fluid to a working fluid to generate mechanical energy that may be used to operate a mechanical system or provide electricity in accordance with one or more embodiments.
- Heated fluid from a production well 510 passes through a heat exchanger 520 and transfers a portion of its heat to a working fluid 540, for example a refrigerant.
- the heated working fluid vaporizes to turn a turbine 550.
- the mechanical energy of the turbine 550 is transformed into electrical energy in a generator 560.
- the embodiment depicted in FIG. 5 may operate based on an organic Rankine cycle or alternative thermodynamic energy conversion cycles such as, for example, a trilateral cycle, a variable phase cycle, or a Kalina cycle.
- the trilateral cycle for example, is a thermodynamic cycle involving a substantially perfect temperature matching between the heat source and the working fluid to minimize irreversibility associated with the process and to maximize its efficiency.
- the expansion of liquid may start in the saturated liquid phase forming a mixture of gas and liquid as a result.
- Alternative working fluids or heat cycles may be substituted for those in FIG. 5.
- FIG. 6 presents a non-limiting schematic of a generator 600 suitable for transforming heat energy transferred from a well fluid to electrical energy in accordance with one or more embodiments.
- Generator 600 may convert heat energy to mechanical energy, which may be subsequently converted to electrical energy.
- a working fluid as described above, may evaporate in evaporator 610 after heat is transferred to it from extracted produced water. The evaporated fluid may perform work on a turbine 620, the mechanical energy of which may be used to produce electricity. The working fluid may then be condensed in condenser 640 before beginning the cycle again.
- thermoelectric conversion process may be used instead of a heat engine.
- FIG. 7 presents a non-limiting schematic of one such embodiment of an oil and gas recovery operation.
- System 700 includes a thermoelectric conversion process 760 and an energy supply 720.
- a thermoelectric conversion process 760 uses heat 785 from well fluid 795 to produce electricity 790.
- the thermoelectric conversion process 760 may involve a thermoelectric generator described below with reference to FIG. 8.
- the electricity 790 may then be used to power the operations of the system 700, either driving the pump 730, powering the oil/water separations 740, or powering the water treatment process 750. If more power is produced than required by the system, the balance of the energy may be transferred to the energy supply 720, e.g. the grid. If the system requires more energy than that produced by the thermoelectric conversion process 760, then the energy supply 730 will supply the difference.
- FIG. 8 presents a schematic of a thermoelectric generator in accordance with one or more embodiments. Recaptured heat from the produced water may be used to operate a thermoelectric generator 800.
- generator 800 heat is absorbed by a substrate 810 connected to thermoelectric couples 820.
- the thermoelectric couples 820 of thermoelectric semiconductors may be connected electrically in series and thermally in parallel to make a thermoelectric generator.
- the flow of heat may generally drive the free electrons to produce electrical power from heat.
- energy may be harnessed from produced water and used to drive oil/water separation as well as treatment of the produced water.
- Recovered energy may be mechanical energy used directly to drive pumps used for water treatment. In other embodiments, mechanical energy may be converted to electrical energy directly used to drive motors used for water treatment. In some embodiments, a thermoelectric generator may be used to convert the recovered heat energy to electrical energy. Recovered energy may be more or less than that required for conveyance and treatment of the produced water. Excess energy may be delivered to an electric energy network which may provide supplemental energy when needed or otherwise serve as a backup source of power. The heat energy from the produced water may be recovered prior to separating oil from the produced water. In other embodiments, the heat energy may be recovered during treatment of the produced water.
- the systems and methods may generally be described as having an energy recovery component or subsystem, followed by a water treatment component or subsystem.
- Table illustrates a prophetic example of the electric energy that can be recovered as an oil field is developed and produced water increases.
- the last row on the Table indicates the Tons of C02 that will be avoided with the technology as a result of displacing the use of a fossil fuel to generate electric power with a renewable energy source such as natural water heat.
- the results from the pilot energy recovery unit indicate that the systems are sensitive to the influent temperature to the unit. There is therefore an incentive to harvest the heat before it is dissipated.
- an existing system or method may be modified to utilize or incorporate any one or more aspects of the disclosure.
- embodiments may involve configuring an existing energy extraction system or method to include the integration described herein.
- an existing system or process may be retrofitted to involve use of heat from produced water to drive treatment of the produced water in accordance with one or more embodiments.
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA2898715A CA2898715A1 (en) | 2013-01-21 | 2014-01-21 | Systems and methods for treating produced water |
MX2015009319A MX2015009319A (en) | 2014-01-21 | 2014-01-21 | Systems and methods for treating produced water. |
US14/796,665 US10450207B2 (en) | 2013-01-21 | 2015-07-10 | Systems and methods for treating produced water |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201361754691P | 2013-01-21 | 2013-01-21 | |
US61/754,691 | 2013-01-21 |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US14/796,665 Continuation-In-Part US10450207B2 (en) | 2013-01-21 | 2015-07-10 | Systems and methods for treating produced water |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2014113793A1 true WO2014113793A1 (en) | 2014-07-24 |
Family
ID=51210136
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US2014/012336 WO2014113793A1 (en) | 2013-01-21 | 2014-01-21 | Systems and methods for treating produced water |
Country Status (3)
Country | Link |
---|---|
CA (1) | CA2898715A1 (en) |
PE (1) | PE20151699A1 (en) |
WO (1) | WO2014113793A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108395042A (en) * | 2018-03-12 | 2018-08-14 | 青海天怡复合材料开发有限公司 | A kind of GRP pipe manufacture sewage-treatment plant |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4557112A (en) * | 1981-12-18 | 1985-12-10 | Solmecs Corporation | Method and apparatus for converting thermal energy |
US20070144785A1 (en) * | 2005-02-14 | 2007-06-28 | Smith Kevin W | Separating mixtures of oil and water |
US20070261844A1 (en) * | 2006-05-10 | 2007-11-15 | Raytheon Company | Method and apparatus for capture and sequester of carbon dioxide and extraction of energy from large land masses during and after extraction of hydrocarbon fuels or contaminants using energy and critical fluids |
US20090301087A1 (en) * | 2008-06-10 | 2009-12-10 | Borissov Alexandre A | System and method for producing power from thermal energy stored in a fluid produced during heavy oil extraction |
US20100236595A1 (en) * | 2005-06-28 | 2010-09-23 | Bell Lon E | Thermoelectric power generator for variable thermal power source |
US20100282593A1 (en) * | 2007-11-02 | 2010-11-11 | Speirs Brian C | Recovery of high water from produced water arising from a thermal hydrocarbon recovery operation using vaccum technologies |
US20100294719A1 (en) * | 2009-05-19 | 2010-11-25 | Polizzotti David M | Process for treatment of produced water |
-
2014
- 2014-01-21 PE PE2015001358A patent/PE20151699A1/en not_active Application Discontinuation
- 2014-01-21 CA CA2898715A patent/CA2898715A1/en not_active Abandoned
- 2014-01-21 WO PCT/US2014/012336 patent/WO2014113793A1/en active Application Filing
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4557112A (en) * | 1981-12-18 | 1985-12-10 | Solmecs Corporation | Method and apparatus for converting thermal energy |
US20070144785A1 (en) * | 2005-02-14 | 2007-06-28 | Smith Kevin W | Separating mixtures of oil and water |
US20100236595A1 (en) * | 2005-06-28 | 2010-09-23 | Bell Lon E | Thermoelectric power generator for variable thermal power source |
US20070261844A1 (en) * | 2006-05-10 | 2007-11-15 | Raytheon Company | Method and apparatus for capture and sequester of carbon dioxide and extraction of energy from large land masses during and after extraction of hydrocarbon fuels or contaminants using energy and critical fluids |
US20100282593A1 (en) * | 2007-11-02 | 2010-11-11 | Speirs Brian C | Recovery of high water from produced water arising from a thermal hydrocarbon recovery operation using vaccum technologies |
US20090301087A1 (en) * | 2008-06-10 | 2009-12-10 | Borissov Alexandre A | System and method for producing power from thermal energy stored in a fluid produced during heavy oil extraction |
US20100294719A1 (en) * | 2009-05-19 | 2010-11-25 | Polizzotti David M | Process for treatment of produced water |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108395042A (en) * | 2018-03-12 | 2018-08-14 | 青海天怡复合材料开发有限公司 | A kind of GRP pipe manufacture sewage-treatment plant |
Also Published As
Publication number | Publication date |
---|---|
PE20151699A1 (en) | 2015-12-04 |
CA2898715A1 (en) | 2014-07-24 |
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