Classifications

• • 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
  • E21B36/00—Heating, cooling or insulating arrangements for boreholes or wells, e.g. for use in permafrost zones
• • 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
  • E21B36/00—Heating, cooling or insulating arrangements for boreholes or wells, e.g. for use in permafrost zones
  • E21B36/006—Combined heating and pumping means
• • 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
  • E21B36/00—Heating, cooling or insulating arrangements for boreholes or wells, e.g. for use in permafrost zones
  • E21B36/003—Insulating arrangements
• • 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
  • E21B36/00—Heating, cooling or insulating arrangements for boreholes or wells, e.g. for use in permafrost zones
  • E21B36/04—Heating, cooling or insulating arrangements for boreholes or wells, e.g. for use in permafrost zones using electrical heaters
• • 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
  • E21B43/24—Enhanced recovery methods for obtaining hydrocarbons using heat, e.g. steam injection
• • 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
  • E21B43/24—Enhanced recovery methods for obtaining hydrocarbons using heat, e.g. steam injection
  • E21B43/2401—Enhanced recovery methods for obtaining hydrocarbons using heat, e.g. steam injection by means of electricity
• • 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
  • E21B43/24—Enhanced recovery methods for obtaining hydrocarbons using heat, e.g. steam injection
  • E21B43/2406—Steam assisted gravity drainage [SAGD]

Definitions

• the technical sector of the present invention is that of the heating devices of the hydrocarbon extraction ducts in a paraffinic or heavy crude oil well.
• this envelope is pierced with a number of orifices to provide access to the liquid.
• This pierced part is designated by the term strainer or drain along its length.
• a pipe of constant diameter and smaller than that of the casing is introduced into the previous casing in order to reach the bottom of the bore to pump the liquid to the surface.
• This pipe is therefore a pumping pipe.
• This pipe can be equipped with a downhole pump.
• a heat transfer solution consists in arranging resistive or inductive electric heating elements along the oil lift pipe. These elements can be installed either outside or inside the pipe. In the case of an installation outside, these electrical elements need to be installed against the wall of the pipe to promote the heat exchange between the resistors and the pipe. The risk is to have a high temperature of the resistances. There is then the problem of choice of the material of these resistors as well as connections.
• the purpose of the present invention is to provide a system for heating the upwell oil line in a well to prevent the deposition of paraffins or asphaltenes on the wall of the pipe during production, dissolve these deposits that may have appeared in the oil recovery line during a shutdown and before a restart of the well or maintain the viscosity of the oil at an acceptable level for the downhole pump.
• the subject of the invention is therefore a heating installation of the hydrocarbon extraction ducts through a well connecting the surface to an extraction zone, comprising a substantially cylindrical duct consolidating said drilling, a means for extracting hydrocarbons and means for circulating a hot fluid from the surface to the zone to be heated in the well, characterized in that the circulation means comprise in the pipe a first isolated heating pipe. thermally injection from the surface of the hot fluid to the desired depth and a second heating pipe surrounding the first pipe to return the hot fluid to the surface and in that the extraction means comprises a pumping pipe surrounding the first and second heating pipes for the extraction of hydrocarbons.
• the first and second heating pipes are connected at the surface to a hot fluid production station composed of a storage tank or expansion tank, a pump and a heater for heating. ensuring a continuous circulation of the hot fluid in said heating pipes with continuous control of temperature and flow.
• the hot fluid exiting the heater flows in the thermally insulated pipe to the end thereof and then rises to the surface between the thermally insulated pipe and the second heating pipe.
• the expansion vessel makes it possible to accommodate the increase in volume of the hot oil in the closed circuit and thus avoid any overpressure in the circuit.
• the first heating pipe is open at its distal end and the second heating pipe is closed at its distal end by a transverse wall.
• the first heating pipe is thermally insulated with a compression-resistant insulator, either because of its compressive strength properties or by the addition of spacers regularly arranged between the first and the second pipe. .
• the pumping line is connected to an extraction unit. surface.
• the pumping line is equipped with a downhole pump.
• the pumping line is open at its distal end and has perforations at least at its end portion.
• the first heating pipe consists of a first inner tube surrounded by a second concentric outer tube and an insulator housed in the space between the two tubes.
• the insulation consists of a microporous material and in that a reduced pressure is established in the space between the two tubes.
• the reduced pressure between the two tubes of the first pipe is between 1 and 100 mbar.
• the first heating pipe is provided with a heating electric wire disposed against the inner wall of the inner tube.
• An advantage of the invention lies in the realization of a closed circuit allowing the supply of heat in the pumping line, to its end in the well, before the downhole pump.
• the hot fluid may be chosen from fluids used in heating installations, for example an industrial thermal oil or water.
• the hot fluid exiting the heater flows in the first thermally insulated pipe to the end thereof and then rises to the surface between the first thermally insulated pipe and the second heating pipe. During this ascent, the heat energy contained in the hot fluid is dissipated by conducto-convection in the oil produced in the pumping line and in the pumping line itself.
• the temperature of the hot fluid is maximum at the surface in heater outlet. Thermal losses and therefore the decrease of the fluid temperature are low during the descent into the thermally insulated pipe. During the rise of the hot fluid to the surface, the heat exchange with the pump pipe is important to allow the exchange of heat and the fluid temperature decreases sharply.
• the heat is supplied to the pumping line and the crude oil produced in this pipe will maintain the temperature of the oil when rising to the surface and prevent the appearance of paraffins or asphaltenes in the pumping line.
• the temperature of appearance of the paraffins can be between 25 ° C and 70 ° C depending on the hydrocarbons.
• Another advantage of the invention lies in the mastery of the heat input at the section of the pumping line to be heated, in order to maintain the temperature of the oil produced while ensuring a continuity of production.
• the flow rate and temperature of the hot fluid are surface-controlled and can vary depending on the minimum acceptable oil temperature in the pump line.
• Another advantage of the invention lies in the fact that there is no mixing of the hot fluid and the recovered hydrocarbons thus allowing the elimination of a hydrocarbon separation station.
• Another advantage of the invention lies in the absence of pollution of the deposit since the hot fluid does not contaminate this deposit.
• Another advantage of the invention lies in the use of an industrial thermal oil as heat transfer fluid.
• the volume of oil required in the closed loop formed by the first and the second pipe is between 500 liters to 3000 liters.
• Such a thermal oil standard in the industry, will have an optimized composition to be heated to the desired temperature, typically 80 ° C or up to 200 ° C and will allow the use of surface equipment, pump and heater, standard in industry and less complex.
• heating a hydrocarbon mixture at temperatures of the order of 200 ° C has the risk of creating solid deposits on the heating elements of the boiler can cause a decrease in heating power see the rise in temperature of the heating element concerned and its degradation.
• the method of heating a thermal oil will be simpler since the composition thereof is uniform and it will be selected so as not to create deposits at the desired temperature.
• Another advantage of the invention lies in the use of even polluting fluid.
• the installation according to the invention allows a control and a surface adjustment of the temperature of the hot fluid, the injection rate of this hot fluid as a function of the need for heating in the pumping line. Thus, it prevents or eliminates any accumulation of paraffin in the pipe at its vertical portion and / or at its horizontal portion.
• Another advantage of the invention is that after a modification of the wellhead, this installation is independent of the other standard well production equipment and can therefore be installed and removed according to the needs of the well leaving the equipment in place. standards of production of well bottoms and also of surface.
• Another advantage of the invention lies in the fact that the pipes for the closed-loop circulation of the hot fluid can be made from coiled tubing known as "coiled tubing".
• the thermally insulated double wall pipe can be produced from two coiled pipes and inserted into the second larger diameter pipe, which can be coiled tubing as well.
• This triple pipe can be wrapped around a wheel for transportation and installed in a single operation by a unit of "coiled tubing" in the well. Special pieces are installed at each end of the coiled tubing to isolate or communicate the annular rings as required by closed loop circulation.
• FIG. 1 illustrates an installation for heating hydrocarbon extraction ducts according to the invention, from a well
• FIG. 2 is a section along AA of FIG. 1,
• An oil well is most generally composed of two essential parts, an outer casing (designated by the English word casing) responsible for consolidating the inner wall of the well in the ground and an inner pipe (designated by the English word tubing) allowing the oil recovery on the surface.
• an outer casing designated by the English word casing
• an inner pipe designated by the English word tubing
• Figure 1 illustrates the entire vertical portion of the wellbore.
• FIG. 1 there is shown a substantially vertical crude oil extraction shaft having an outer portion and a depth portion corresponding to the well itself.
• the heating installation 1 therefore comprises a drilled vertical well 2 -consolidated by a metallic pipe 3 cylindrical. This well is in relation with a deep field 12 in its extension.
• This hydrocarbon extraction facility 1 through the well 2 connects the surface to an extraction zone at the reservoir 12 located at the bottom of the well. It comprises the substantially cylindrical pipe 3 consolidating said drilling, a hydrocarbon extraction means 4 and means 5 for circulating a hot fluid in a closed loop from the surface to the section of the pipe 7 to be heated from the well 2 and then again on the surface.
• hydrocarbon pumping line 7 to the surface and heating pipes 8 and 11 for circulating a hot fluid from the surface and along the section of the pumping line to heat.
• the extraction means 4 thus consist of an extraction unit 6 comprising the pumping line 7 connecting this unit to the hydrocarbon reservoir to the level of the deep deposit 12 and a downhole pump (no shown) for the extraction of hydrocarbons.
• the closed-loop circulation means 5 comprise in line 3 a first heat-insulated heating pipe 8 for injecting from the surface of the hot fluid to the deposit.
• This heating pipe 8 is connected to a unit 9 for heating and injecting the hot fluid continuously, for example by means of a pump 10.
• This first heating pipe 8 is surrounded by a second heating pipe 11 to return the hot fluid to the unit 9.
• the heating pipes 8 and 11 together with the hot fluid production unit 9 constitute a closed circulation circuit. continuous of this hot fluid.
• the hot fluid production unit 9 consists of a storage tank 22 or expansion tank, a pump 10 and a heater 23 to ensure continuous circulation of the hot fluid in said heating pipes with continuous control of temperature and flow.
• the hot fluid circuit is closed at the level of the distal end of the second duct 11 by a transverse wall 18 while the first duct 8 is open at its distal end 17.
• the distal end 17 opens in the vicinity of the wall 18 and at a distance of it.
• the length of the pipes 8 and 11 in the casing 3 is a function of the zone in which the paraffins accumulate against the wall of the pipe 7.
• This zone is generally located in the upper part of the pipe which is the zone at where the hydrocarbons have been significantly cooled. This zone is generally located from the surface to the depth at which paraffin deposits appear, ie 200 to 2000 meters deep.
• the hot fluid is injected by the pump 10 into the pipe 8 to its distal end 17, then this hot fluid rises to the unit 9 via the pipe 11. It is therefore easy to control the temperature hot fluid leaving the heater 23 and the necessary flow rate of the pump 10.
• FIG. 2 shows a section AA of FIG. 1 on which the envelope 3 has been taken up.
• the first pipe 8 consists of a first inner tube 16 surrounded by a second concentric outer tube 17 and an insulator 20 housed in the space between these two tubes.
• FIGS. 1 and 2 do not have a scale and are only shown for illustrative purposes.
• Insulator 20 may be a powdery material commonly used in this field.
• This reduced pressure can be between 1 and 100 mbar.
• the fact of using a hot fluid confers a double action.
• the heat makes it possible to prevent the appearance and deposition of solid fractions such as paraffins and asphaltenes and to melt the fractions already solidified or deposited during a restart of the well, for example.
• the depth of the well can reach several hundred meters (100 to 2000 m), it is essential to bring heat to the deposit, to have a pipe 8 highly thermally insulated.
• Line 8 is made according to the technique known as the English word "pipe in pipe”. Between the two tubes 16 and 17 is disposed the insulator 20 as explained above.
• the first tube 16 internal, ensures the transport of the hot fluid.
• This tube 16 is mechanically protected by the second tube 17 of larger diameter concentric with this first tube 16 and thermally by the insulator 20.
• a microporous material can be used as insulation between the tubes 16 and 17.
• This microporous material of the type described in patent FR-2746891, is advantageously obtained by compressing a powder for example fumed silica.
• Such a compressed microporous material advantageously has a density of between 180 and 400 kg / m 3 .
• the insulating thermal capacities of such a material are significantly improved when it is placed in the ring under low pressure between the two tubes 16 and 17.
• an insulator 20 by providing a multilayer super-insulation consisting of reflective screens interposing layers of powder as described in patent FR-2862122.
• the screens are constituted by a reflective sheet, for example aluminum, on which the powder is deposited, wound spirally on itself.
• the powder has a particle size substantially equal to 40 ⁇ m, pores whose size is of the order of magnitude of the average free path of the molecules of the gas in which this powder is placed and a density of between 50 and 150 kg / m 3 .
• the insulating thermal capacities of such a material are significantly improved when it is placed in the ring under low pressure between the two tubes 16 and 17, between 10 ⁇ 2 and 1 mbar
• This insulation having no sufficient compressive strength properties, requires the addition of spacers regularly between the tubes 16 and 17.
• the material used to make these spacers must have a good insulating behavior.
• Such a material may advantageously be a microporous material as described above.
• the heating pipe 8 as described above in connection with FIGS. 1 and 2 allows a heat input sufficient to make the hydrocarbons sufficiently fluid with a boiler of 5 to 500 K.
• the installation 1 according to the invention makes it possible to ensure continuous operation and to avoid deposits of deposits on the pumping line. This makes it possible to increase the production of crude oil by 20 to 100% and to avoid any pollution of the deposits.
• a pipe 8 according to the invention may consist of an outer tube 17 of 33 mm outside diameter with a thickness of 2 mm and a tube internal 16 13 mm outside diameter with a thickness of 2 mm and is able to transport 20 kW at 200 ° C over an overall distance of 1000 meters.
• a pipe 8 consisting of an outer tube 17 with a diameter of 60 mm and a thickness of 5 mm and an inner tube 16 with a diameter of 33 mm and a thickness of 4 mm will easily transport 200 kW to 200 ° C over an overall distance of 2000 meters.
• the length of the pipes 8 and 11 is a function of the section of the pipe 7 in which the paraffins accumulates against the wall. This section is usually located in the upper section of the pipe, which is the area where the hydrocarbons have undergone significant cooling but can also spread deep. This section is usually between 100m and 2000m deep.
• the length of the pipes 8 and 11 may also vary from the surface to the end of the pipe 7 depending on the power required to maintain the temperature of the oil produced.
• the pipes 8 and 11 may extend beyond the end of the pipe 7, in the casing 3 to have a thermal action on the pipes. perforations of the strainer or drain, at the end of the envelope 3 as well as on the deposit.
• the hot fluid is injected by the pump 10 into the pipe 8 to its distal end 17, then this hot fluid rises to the unit 9 via the pipe 11. It is therefore easy to control the temperature hot fluid and the necessary flow rate of the pump 10.
• FIGS. 1 and 2 it can still be seen that the heating pipes 8 and 11 are inserted in their vertical part in the pipe 7 for pumping hydrocarbons.

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• Life Sciences & Earth Sciences (AREA)
• Engineering & Computer Science (AREA)
• Geology (AREA)
• Mining & Mineral Resources (AREA)
• Physics & Mathematics (AREA)
• Environmental & Geological Engineering (AREA)
• Fluid Mechanics (AREA)
• General Life Sciences & Earth Sciences (AREA)
• Geochemistry & Mineralogy (AREA)
• Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
• Pipeline Systems (AREA)
• Extraction Or Liquid Replacement (AREA)

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• 2017
  • 2017-05-29 FR FR1770549A patent/FR3066778B1/fr not_active Expired - Fee Related
• 2018
  • 2018-05-28 CA CA3063274A patent/CA3063274A1/fr active Pending
  • 2018-05-28 US US16/618,223 patent/US10995588B2/en active Active
  • 2018-05-28 WO PCT/FR2018/000144 patent/WO2018220293A1/fr unknown
  • 2018-05-28 EP EP18734273.8A patent/EP3631155B1/de active Active

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