WO2014046767A1 - Pumping and vaporization system for enhanced oil recovery applications - Google Patents

Pumping and vaporization system for enhanced oil recovery applications Download PDF

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Publication number
WO2014046767A1
WO2014046767A1 PCT/US2013/049852 US2013049852W WO2014046767A1 WO 2014046767 A1 WO2014046767 A1 WO 2014046767A1 US 2013049852 W US2013049852 W US 2013049852W WO 2014046767 A1 WO2014046767 A1 WO 2014046767A1
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Prior art keywords
pump
liquid cryogen
gas
feeding
coolant
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Ceased
Application number
PCT/US2013/049852
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French (fr)
Inventor
Joseph NAUMOVITZ
Andreas Opfermann
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Linde GmbH
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Linde GmbH
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Filing date
Publication date
Application filed by Linde GmbH filed Critical Linde GmbH
Priority to ROA201500183A priority Critical patent/RO130699A2/en
Priority to BR112015005678A priority patent/BR112015005678A2/en
Priority to CA2883934A priority patent/CA2883934A1/en
Priority to MX2015003299A priority patent/MX2015003299A/en
Publication of WO2014046767A1 publication Critical patent/WO2014046767A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C9/00—Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure
    • F17C9/02—Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure with change of state, e.g. vaporisation
    • E—FIXED CONSTRUCTIONS
    • E21—EARTH OR ROCK DRILLING; MINING
    • E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/16—Enhanced recovery methods for obtaining hydrocarbons
    • E21B43/166—Injecting a gaseous medium; Injecting a gaseous medium and a liquid medium
    • E21B43/168—Injecting a gaseous medium
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C9/00—Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure
    • F17C9/02—Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure with change of state, e.g. vaporisation
    • F17C9/04—Recovery of thermal energy
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2221/00—Handled fluid, in particular type of fluid
    • F17C2221/01—Pure fluids
    • F17C2221/013—Carbon dioxide
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2221/00—Handled fluid, in particular type of fluid
    • F17C2221/01—Pure fluids
    • F17C2221/014—Nitrogen
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/01—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
    • F17C2223/0146—Two-phase
    • F17C2223/0153—Liquefied gas, e.g. LPG, GPL
    • F17C2223/0161—Liquefied gas, e.g. LPG, GPL cryogenic, e.g. LNG, GNL, PLNG
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/03—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the pressure level
    • F17C2223/033—Small pressure, e.g. for liquefied gas
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2225/00—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel
    • F17C2225/01—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel characterised by the phase
    • F17C2225/0107—Single phase
    • F17C2225/0115—Single phase dense or supercritical, i.e. at high pressure and high density
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2225/00—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel
    • F17C2225/01—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel characterised by the phase
    • F17C2225/0107—Single phase
    • F17C2225/0123—Single phase gaseous, e.g. CNG, GNC
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2225/00—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel
    • F17C2225/03—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel characterised by the pressure level
    • F17C2225/036—Very high pressure, i.e. above 80 bars
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/01—Propulsion of the fluid
    • F17C2227/0128—Propulsion of the fluid with pumps or compressors
    • F17C2227/0135—Pumps
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/03—Heat exchange with the fluid
    • F17C2227/0302—Heat exchange with the fluid by heating
    • F17C2227/0309—Heat exchange with the fluid by heating using another fluid
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/03—Heat exchange with the fluid
    • F17C2227/0302—Heat exchange with the fluid by heating
    • F17C2227/0309—Heat exchange with the fluid by heating using another fluid
    • F17C2227/0311—Air heating
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/03—Heat exchange with the fluid
    • F17C2227/0302—Heat exchange with the fluid by heating
    • F17C2227/0309—Heat exchange with the fluid by heating using another fluid
    • F17C2227/0323—Heat exchange with the fluid by heating using another fluid in a closed loop
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/03—Heat exchange with the fluid
    • F17C2227/0302—Heat exchange with the fluid by heating
    • F17C2227/0327—Heat exchange with the fluid by heating with recovery of heat
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/03—Heat exchange with the fluid
    • F17C2227/0367—Localisation of heat exchange
    • F17C2227/0388—Localisation of heat exchange separate
    • F17C2227/0393—Localisation of heat exchange separate using a vaporiser
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2265/00—Effects achieved by gas storage or gas handling
    • F17C2265/05—Regasification
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2270/00—Applications
    • F17C2270/01—Applications for fluid transport or storage
    • F17C2270/0142—Applications for fluid transport or storage placed underground
    • F17C2270/0144—Type of cavity
    • F17C2270/0155—Type of cavity by using natural cavities

Definitions

  • the present invention is able to overcome this limitation by using a system that can pump and vaporize either liquid nitrogen or liquid carbon dioxide to their gaseous state to a location where an operator has need for either of these gases such as for enhanced oil recovery operations.
  • the invention provides for a system for providing a gas selected from the group consisting of nitrogen and carbon dioxide for use in enhanced oil recovery operations comprising a source of said gas and a storage vessel for said gas, utilizing an interchangeable pump, and a single (non-interchangeable) vaporizer system capable providing either gas at a specified delivery pressure and temperature.
  • the invention operates to provide a high pressure gas to an end user for use in enhanced oil recovery operations.
  • the invention starts with Iiquid carbon dioxide and/or nitrogen, using a pump set to increase the supply pressure and direct the Iiquid to an air fan vaporizer.
  • the Iiquid carbon dioxide or nitrogen is typically drawn from a storage tank by the pump.
  • the carbon dioxide and/or nitrogen air vaporizer will vaporize the liquid and will provide higher pressure gas to the location where the end user can employ the higher pressure gas in enhanced oil recovery operations or it is simply fed to a storage unit.
  • the components of the system are fluidly connected by the appropriate piping.
  • the invention utilizes equipment in part that can be used for more than one type of Iiquid cryogen and vaporized form thereof without having to have its settings changed at all or substantially at all in the event that a different Iiquid cryogen is used. So for example, an operator might desire that carbon dioxide be employed in an enhanced oil recovery operation first and followed up by the addition of nitrogen after a period of time.
  • the present invention can provide both without the operator of the gas provisioning system making any or any substantial changes to the settings of the vaporizer and coolant exchanger.
  • a method for producing a gas for use in an enhanced oil recovery operation comprising the steps: a) Feeding a liquid cryogen to a pump; b) Feeding the liquid cryogen from the pump to a vaporizer whereby the liquid cryogen vaporizes to form a gas and wherein said vaporizer is capable of vaporizing a different liquid cryogen without any or any substantial adjustment to its settings; c) Feeding the gas to a coolant exchanger, wherein said coolant exchanger is capable of cooling a different gas without any or any substantial adjustment to its settings; and d) Feeding the gas to the enhanced oil recovery operation,
  • the liquid cryogen that may be vaporized is selected from the group consisting of nitrogen and carbon dioxide and may also consist of a mixture of nitrogen and carbon dioxide.
  • the pump is typically a high pressure pump that is capable of pressurizing the liquid cryogen to a pressure of about 100 to 500 psia.
  • the pump may be assisted by a booster between the source of the liquid cryogen and the pump.
  • the liquid cryogen is fed to a vaporizer where the pressure is increased to 1400 to 5000 psia and the liquid cryogen becomes a gas.
  • the vaporizer directs the gas to a coolant exchanger where the high pressure gas is fed to an operation such as enhanced oil recovery operations or to storage for other uses onsite.
  • the coolant exchanger is in a thermal exchange relationship with a combustion engine which is powered by a hydrocarbon such as diesel fuel or natural gas. The combustion engine will provide hot engine coolant to the coolant exchanger while the coolant exchanger provides cooled engine coolant to the combustion engine therefore allowing for efficient operation of the combustion engine.
  • the combustion engine is used to provide power to a hydraulic pump which will draw fluid from a hydraulic fluid reservoir and direct it to hydraulic drivers.
  • the hydraulic drivers convert pressure energy from the hydraulic fluid Into mechanical energy. This mechanical energy is transmitted to the booster pump, the high pressure pump and the vaporizer fan.
  • a method for providing high pressure gas to an enhanced oil recovery operation comprising the steps: a) Feeding liquid cryogen to a pump; b) Feeding the liquid cryogen from the pump to a vaporizer whereby the liquid cryogen vaporizes to form a gas and wherein said vaporizer is capable of vaporizing a different liquid cryogen without any or any substantial adjustment to its settings; c) Feeding the gas to a coolant exchanger, wherein said coolant exchanger is capable of cooling a different gas without any or any substantial adjustment to its settings; and d) Feeding the gas to the enhanced oil recovery operation.
  • the phrase "wherein said vaporizer is capable of vaporizing a different liquid cryogen without any or any substantial adjustment to its settings” means that the vaporizer that is used to vaporize a liquid cryogen to gas can be used to vaporize a second, different liquid cryogen to gas without any or any substantial changes made to its settings under which it vaporizes a liquid cryogen.
  • the phrase "wherein said coolant exchanger is capable of cooling a different liquid cryogen without any or any substantial adjustment to its settings" means that the coolant exchanger that is used to cool a gas can be used to cool a second, different gas without any or any substantial changes made to its settings under which it cools a gas.
  • Figure 1 is a schematic of the system configured for providing high pressure nitrogen gas per the invention.
  • Figure 2 is a schematic of the system configured for providing supercritical carbon dioxide per the invention.
  • FIG. 1 a schematic of the invention is shown for pressurizing and vaporizing liquid nitrogen for use in enhanced oil recovery operations.
  • the liquid nitrogen is fed through line 1 to a liquid storage tank A.
  • the storage tank A can be capable of storing either the liquid nitrogen or liquid carbon dioxide which are typically stored at two different temperatures: liquid nitrogen in the range of - 320 to -270 °F (-198 to -168°C) and liquid carbon dioxide in the range of - 85 to -45 °F (-65 to -43°C).
  • storage tank A consists of a single tank or a series of separate tanks that are manifolded together to form a common liquid nitrogen supply.
  • the storage tank A is able to control pressure in the tank by venting through line 2 any gas present in the storage tank.
  • a pressure building system is included to vaporize a portion of the liquid in order to maintain pressure during operations.
  • the storage tank A can be any storage tank that is used to store Isquid cryogenic materials.
  • a booster pump B will receive a feed of the liquid nitrogen through line 3 from storage tank A.
  • the liquid nitrogen will be fed at a pressure between 100 and 500 psia through line 4 into a high pressure reciprocating pump system C.
  • This pump system is driven by a hydraulic driver D.
  • This driver is common to both nitrogen and carbon dioxide pumping modes.
  • the high pressure liquid nitrogen will be fed through line 5 at a pressure between 1400 and 5000 psia to a nitrogen air vaporizer E and nitrogen coolant exchanger F,
  • the nitrogen air vaporizer E and coolant exchanger F will vaporize the liquid nitrogen and produce a gas in the pressure range of 1400 to 5000 psia and in the temperature range of 40 to 80 °F (4 to 27oC).
  • the resulting gaseous nitrogen is fed through line 6 directly to an enhanced oil recovery operation where it can be used in downhole operations. Alternatively, the gaseous nitrogen can be fed to a storage unit (not shown) for later use in the enhanced oil recovery operation.
  • the pumping and vaporization system is driven by a combustion engine G which can be either diesel or natural gas driven.
  • An engine coolant is used to transfer heat through line 7 to the coolant exchanger F.
  • Engine coolant from the coolant exchanger F is fed to the combustion engine G through line 8.
  • the pumps and vaporizer fans are driven by means of a hydraulic fluid in the following manner.
  • a hydraulic fluid is fed through line 9 from the hydraulic fluid reservoir L to hydraulic pump H.
  • Line 10 provides pressurized hydraulic fluid to hydraulic driver K and through lines 10A and 10B to hydraulic drivers I and J respectively.
  • Low pressure hydraulic fluid is returned to the hydraulic fluid reservoir L through lines 10C, 1 1 and 12.
  • Figure 2 provides a schematic of the invention is configured for pressurizing and vaporizing liquid carbon dioxide for use in enhanced oil recovery operations.
  • the same number and letter designations are employed in Figure 2 as are employed in Figure 1 with the exception that carbon dioxide is being employed in the process of the invention in Figure 2 while nitrogen is being employed in Figure 1.
  • the booster pump B and the cold end cylinders C of the high pressure pump are replaced with materials compatible for pumping liquid carbon dioxide.
  • the system operates in the same manner as the description for Figure 1 to produce supercritical carbon dioxide in the pressure range of 1400 to 5000 psia and in the temperature range of 40 to 80 °F (4 to 27oC).

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  • General Engineering & Computer Science (AREA)
  • Mining & Mineral Resources (AREA)
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  • Life Sciences & Earth Sciences (AREA)
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  • Physics & Mathematics (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Environmental & Geological Engineering (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Lubrication Of Internal Combustion Engines (AREA)

Description

PUMPING AND VAPORIZATION SYSTEM FOR ENHANCED OIL RECOVERY APPLICATIONS
CROSS REFERENCE TO RELATED APPLICATIONS
[0001] The present application claims priority from US provisional application serial number 61/702,310 filed September 18, 2012.
BACKGROUND OF THE INVENTION
[0002] The development of enhanced oil recovery projects is complex requiring the methodology to be tailored to each specific oil reservoir. To improve the success of these projects it is often necessary to conduct pilot injection tests to measure well injectivity, areal sweep and conformance, gravity override, viscous fingering, and loss of mobility control. The conditions of the oil reservoir will help to determine whether carbon dioxide or nitrogen is the appropriate fluid for enhanced oil recovery (EOR).
[0003] The carbon dioxide or nitrogen that is necessary for EOR must be supplied at higher pressures and requires pumping and vaporization systems. Typically these pumping and vaporization systems are separate systems such that one system provides high pressure carbon dioxide and a second system provides high pressure nitrogen. However, much of the required usage for these gases is for less than one year and each type of system requires significant capital investment.
[0004] The present invention is able to overcome this limitation by using a system that can pump and vaporize either liquid nitrogen or liquid carbon dioxide to their gaseous state to a location where an operator has need for either of these gases such as for enhanced oil recovery operations.
SUMMARY OF THE INVENTION
[0005] The invention provides for a system for providing a gas selected from the group consisting of nitrogen and carbon dioxide for use in enhanced oil recovery operations comprising a source of said gas and a storage vessel for said gas, utilizing an interchangeable pump, and a single (non-interchangeable) vaporizer system capable providing either gas at a specified delivery pressure and temperature.
[0006] The invention operates to provide a high pressure gas to an end user for use in enhanced oil recovery operations. The invention starts with Iiquid carbon dioxide and/or nitrogen, using a pump set to increase the supply pressure and direct the Iiquid to an air fan vaporizer. The Iiquid carbon dioxide or nitrogen is typically drawn from a storage tank by the pump. The carbon dioxide and/or nitrogen air vaporizer will vaporize the liquid and will provide higher pressure gas to the location where the end user can employ the higher pressure gas in enhanced oil recovery operations or it is simply fed to a storage unit. The components of the system are fluidly connected by the appropriate piping.
[0007] The invention utilizes equipment in part that can be used for more than one type of Iiquid cryogen and vaporized form thereof without having to have its settings changed at all or substantially at all in the event that a different Iiquid cryogen is used. So for example, an operator might desire that carbon dioxide be employed in an enhanced oil recovery operation first and followed up by the addition of nitrogen after a period of time. The present invention can provide both without the operator of the gas provisioning system making any or any substantial changes to the settings of the vaporizer and coolant exchanger. [0008] In one embodiment of the invention, there is disclosed a method for producing a gas for use in an enhanced oil recovery operation comprising the steps: a) Feeding a liquid cryogen to a pump; b) Feeding the liquid cryogen from the pump to a vaporizer whereby the liquid cryogen vaporizes to form a gas and wherein said vaporizer is capable of vaporizing a different liquid cryogen without any or any substantial adjustment to its settings; c) Feeding the gas to a coolant exchanger, wherein said coolant exchanger is capable of cooling a different gas without any or any substantial adjustment to its settings; and d) Feeding the gas to the enhanced oil recovery operation,
[0009] The liquid cryogen that may be vaporized is selected from the group consisting of nitrogen and carbon dioxide and may also consist of a mixture of nitrogen and carbon dioxide.
[0010] The pump is typically a high pressure pump that is capable of pressurizing the liquid cryogen to a pressure of about 100 to 500 psia. The pump may be assisted by a booster between the source of the liquid cryogen and the pump.
[0011] The liquid cryogen is fed to a vaporizer where the pressure is increased to 1400 to 5000 psia and the liquid cryogen becomes a gas. [0012] The vaporizer directs the gas to a coolant exchanger where the high pressure gas is fed to an operation such as enhanced oil recovery operations or to storage for other uses onsite. The coolant exchanger is in a thermal exchange relationship with a combustion engine which is powered by a hydrocarbon such as diesel fuel or natural gas. The combustion engine will provide hot engine coolant to the coolant exchanger while the coolant exchanger provides cooled engine coolant to the combustion engine therefore allowing for efficient operation of the combustion engine.
[0013] The combustion engine is used to provide power to a hydraulic pump which will draw fluid from a hydraulic fluid reservoir and direct it to hydraulic drivers. The hydraulic drivers convert pressure energy from the hydraulic fluid Into mechanical energy. This mechanical energy is transmitted to the booster pump, the high pressure pump and the vaporizer fan.
[0014] In an alternative embodiment of the invention, there is disclosed a method for providing high pressure gas to an enhanced oil recovery operation comprising the steps: a) Feeding liquid cryogen to a pump; b) Feeding the liquid cryogen from the pump to a vaporizer whereby the liquid cryogen vaporizes to form a gas and wherein said vaporizer is capable of vaporizing a different liquid cryogen without any or any substantial adjustment to its settings; c) Feeding the gas to a coolant exchanger, wherein said coolant exchanger is capable of cooling a different gas without any or any substantial adjustment to its settings; and d) Feeding the gas to the enhanced oil recovery operation.
[0015] For purposes of the present invention, the phrase "wherein said vaporizer is capable of vaporizing a different liquid cryogen without any or any substantial adjustment to its settings" means that the vaporizer that is used to vaporize a liquid cryogen to gas can be used to vaporize a second, different liquid cryogen to gas without any or any substantial changes made to its settings under which it vaporizes a liquid cryogen.
[0016] For purposes of the present invention, the phrase "wherein said coolant exchanger is capable of cooling a different liquid cryogen without any or any substantial adjustment to its settings" means that the coolant exchanger that is used to cool a gas can be used to cool a second, different gas without any or any substantial changes made to its settings under which it cools a gas.
BRIEF DESCRIPTION OF THE DRAWINGS
[0017] Figure 1 is a schematic of the system configured for providing high pressure nitrogen gas per the invention.
[0018] Figure 2 is a schematic of the system configured for providing supercritical carbon dioxide per the invention.
DETAILED DESCRIPTION OF THE INVENTION
[0019] Turning to figure 1 , a schematic of the invention is shown for pressurizing and vaporizing liquid nitrogen for use in enhanced oil recovery operations. The liquid nitrogen is fed through line 1 to a liquid storage tank A. The storage tank A can be capable of storing either the liquid nitrogen or liquid carbon dioxide which are typically stored at two different temperatures: liquid nitrogen in the range of - 320 to -270 °F (-198 to -168°C) and liquid carbon dioxide in the range of - 85 to -45 °F (-65 to -43°C). Depending on the application, storage tank A consists of a single tank or a series of separate tanks that are manifolded together to form a common liquid nitrogen supply. The storage tank A is able to control pressure in the tank by venting through line 2 any gas present in the storage tank. A pressure building system is included to vaporize a portion of the liquid in order to maintain pressure during operations. The storage tank A can be any storage tank that is used to store Isquid cryogenic materials.
[0020] A booster pump B will receive a feed of the liquid nitrogen through line 3 from storage tank A. The liquid nitrogen will be fed at a pressure between 100 and 500 psia through line 4 into a high pressure reciprocating pump system C. This pump system is driven by a hydraulic driver D. This driver is common to both nitrogen and carbon dioxide pumping modes. The high pressure liquid nitrogen will be fed through line 5 at a pressure between 1400 and 5000 psia to a nitrogen air vaporizer E and nitrogen coolant exchanger F, The nitrogen air vaporizer E and coolant exchanger F will vaporize the liquid nitrogen and produce a gas in the pressure range of 1400 to 5000 psia and in the temperature range of 40 to 80 °F (4 to 27ºC). The resulting gaseous nitrogen is fed through line 6 directly to an enhanced oil recovery operation where it can be used in downhole operations. Alternatively, the gaseous nitrogen can be fed to a storage unit (not shown) for later use in the enhanced oil recovery operation.
[0021] The pumping and vaporization system is driven by a combustion engine G which can be either diesel or natural gas driven. An engine coolant is used to transfer heat through line 7 to the coolant exchanger F. Engine coolant from the coolant exchanger F is fed to the combustion engine G through line 8. [0022] The pumps and vaporizer fans are driven by means of a hydraulic fluid in the following manner. A hydraulic fluid is fed through line 9 from the hydraulic fluid reservoir L to hydraulic pump H. Line 10 provides pressurized hydraulic fluid to hydraulic driver K and through lines 10A and 10B to hydraulic drivers I and J respectively. Low pressure hydraulic fluid is returned to the hydraulic fluid reservoir L through lines 10C, 1 1 and 12.
[0023] Figure 2 provides a schematic of the invention is configured for pressurizing and vaporizing liquid carbon dioxide for use in enhanced oil recovery operations. The same number and letter designations are employed in Figure 2 as are employed in Figure 1 with the exception that carbon dioxide is being employed in the process of the invention in Figure 2 while nitrogen is being employed in Figure 1.
[0024] To service carbon dioxide, the booster pump B and the cold end cylinders C of the high pressure pump are replaced with materials compatible for pumping liquid carbon dioxide. The system operates in the same manner as the description for Figure 1 to produce supercritical carbon dioxide in the pressure range of 1400 to 5000 psia and in the temperature range of 40 to 80 °F (4 to 27ºC).
[0025] While this invention has been described with respect to particular embodiments thereof, it is apparent that numerous other forms and modifications of the invention will be obvious to those skilled in the art. The appended claims in this invention generally should be construed to cover all such obvious forms and modifications which are within the true spirit and scope of the invention.

Claims

Having thus described the invention, what I claim is:
1. A method for producing a gas for use in an enhanced oil recovery operation comprising the steps: a) Feeding a liquid cryogen to a pump; b) Feeding said liquid cryogen from said pump to a vaporizer whereby said liquid cryogen vaporizes to form a gas and wherein said vaporizer is capable of vaporizing a different liquid cryogen without any or any substantial adjustment to its settings; c) Feeding said gas to a coolant exchanger, wherein said coolant exchanger is capable of cooling a different gas without any or any substantial adjustment to its settings; and d) Feeding said gas to said enhanced oil recovery operation.
2. The method as claimed in claim 1 wherein said liquid cryogen is selected from the group consisting of nitrogen, carbon dioxide and mixtures of nitrogen and carbon dioxide.
3. The method as claimed in claim 1 wherein said pump is a high pressure pump.
4. The method as claimed in claim 1 wherein said liquid cryogen is at a pressure of 100 to 500 psia.
5. The method as claimed in claim 1 wherein said liquid cryogen is vaporized to a pressure of 1400 to 5000 psia,
6. The method as claimed in claim 1 further comprising feeding said liquid cryogen to a booster prior to feeding to said pump,
7. The method as claimed in claim 1 wherein said coolant exchanger is in a thermal exchange relationship with a combustion engine.
8. The method as claimed in claim 1 wherein said engine provides hot engine coolant to the coolant exchanger and the coolant exchanger provides cooled engine coolant to the combustion engine.
9. The method as claimed in claim 1 wherein said combustion engine provides power to a hydraulic pump.
10. The method as claimed in claim 1 wherein said hydraulic pump provides hydraulic fluid to a hydraulic driver connected to said pump.
11 . A method for providing high pressure gas to an enhanced oil recovery operation comprising the steps: a) Feeding liquid cryogen to a pump; b) Feeding said liquid cryogen from said pump to a vaporizer whereby said liquid cryogen vaporizes to form a gas and wherein said vaporizer is capable of vaporizing a different liquid cryogen without any or any substantial adjustment to its settings; c) Feeding said gas to a coolant exchanger, wherein said coolant exchanger is capable of cooling a different gas without any or any substantial adjustment to its settings; and d) Feeding said gas to said enhanced oil recovery operation.
12. The method as claimed in claim 1 1 wherein said liquid cryogen is selected from the group consisting of nitrogen, carbon dioxide and mixtures of nitrogen and carbon dioxide.
13. The method as claimed in claim 1 1 wherein said pump is a high pressure pump.
14. The method as claimed in claim 1 1 wherein said liquid cryogen is at a pressure of 100 to 500 psia.
15. The method as claimed in claim 1 1 wherein said liquid cryogen is vaporized to a pressure of 1400 to 5000 psia.
16. The method as claimed in claim 1 1 further comprising feeding said liquid cryogen to a booster prior to feeding to said pump.
17. The method as claimed in claim 1 1 wherein said coolant exchanger is in a thermal exchange relationship with a combustion engine.
18. The method as claimed in claim 1 1 wherein said engine provides hot engine coolant to the coolant exchanger and the coolant exchanger provides cooled engine coolant to the combustion engine.
19. The method as claimed in claim 1 1 wherein said combustion engine provides power to a hydraulic pump,
20. The method as claimed in claim 1 1 wherein said hydraulic pump provides hydraulic fluid to a hydraulic driver connected to said pump.
PCT/US2013/049852 2012-09-18 2013-07-10 Pumping and vaporization system for enhanced oil recovery applications Ceased WO2014046767A1 (en)

Priority Applications (4)

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ROA201500183A RO130699A2 (en) 2012-09-18 2013-07-10 Pumping and vaporization system for improved oil recovery applications
BR112015005678A BR112015005678A2 (en) 2012-09-18 2013-07-10 vaporization and pumping system for improved oil recovery applications
CA2883934A CA2883934A1 (en) 2012-09-18 2013-07-10 Pumping and vaporization system for enhanced oil recovery applications
MX2015003299A MX2015003299A (en) 2012-09-18 2013-07-10 Pumping and vaporization system for enhanced oil recovery applications.

Applications Claiming Priority (4)

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US201261702310P 2012-09-18 2012-09-18
US61/702,310 2012-09-18
US13/753,634 US20140075964A1 (en) 2012-09-18 2013-01-30 Pumping and vaporization system for enhanced oil recovery applications
US13/753,634 2013-01-30

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CN104482402B (en) * 2014-11-27 2016-08-31 三一重型能源装备有限公司 A kind of liquid nitrogen pump vehicle
US9932799B2 (en) 2015-05-20 2018-04-03 Canadian Oilfield Cryogenics Inc. Tractor and high pressure nitrogen pumping unit
CN111895267B (en) * 2020-07-27 2022-03-01 一汽解放汽车有限公司 A vehicle-mounted gas cylinder pressurization control system and its control method

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MX2015003299A (en) 2015-07-14
ECSP15015383A (en) 2015-12-31

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