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The present invention relates to techniques for monitoring pressure at a downhole location within an oil, gas or other hydrocarbon wellbore. More particularly, the present invention is directed to a safety valve apparatus for downhole pressure transmission systems.
The accurate measurement of downhole fluid pressure and temperature in a borehole has long been recognized as being important in the production of oil, gas, and/or geothermal energy. Accurate pressure and temperature measurements are important in maximizing the efficiency of a well and may indicate problems in oil recovery operations. Both secondary hydrocarbon recovery operations and geothermal operations typically require pressure and temperature information to determine various factors considered useful in predicting the success of the operation, and in obtaining the maximum recovery of energy from the borehole.
In secondary hydrocarbon recovery operations, accurate borehole pressure specifically give an indication of well productivity potential, and allow the operator to predict the amount of fluid that should be required to fill the formation before oil or gas can be expected to be forced out from the formation into the borehole and then recovered to the surface. The accurate measurement of pressure and temperature changes in well fluids from each of various boreholes extending into a formation may indicate the location of injection fluid fronts, as well as the efficiency with which the fluid front is sweeping the formation. In geothermal wells, accurate pressure and temperature information is critical to efficient production due to the potential damage which occurs if reinjected fluids cool the formation or changes in fluid dynamics cause well bore plugging.
Techniques have been devised for providing a periodic measurement of downhole conditions by lowering sensors into the borehole at desired times, although such periodic measurement techniques are both inconvenient and expensive due to the time and expense normally required to insert instrumentation into the borehole. Any such periodic measurement technique is limited in that it provides only a representation of borehole conditions at specific times, and does not provide the desired information over a substantial length of time which is typically desired by the operator.
Permanent installation techniques have been devised for continually monitoring pressure in a borehole in a manner which overcomes the inherent problems associated with periodic measurement. One such prior art technique employs a downhole pressure transducer and a temperature sensor having electronic scanning ability for converting detected downhole pressures and temperatures into electronic data, which then are transmitted to the surface on a conductor line. The conductor line is normally attached to the outside of the tubing in the wellbore, and the transducer and temperature sensor are conveniently mounted on the lower end of the production tubing. This system has shortcomings, however, in part because of the expense and high maintenance required for the electronics positioned in the hostile wellbore environment over an extended period of time. The high temperatures, pressures and/or corrosive fluids in the wellbore substantially increase the expense and decrease the reliability of the downhole electronics. Downhole pressure transducers and temperature sensors which output electronic data for transmission to the surface are generally considered delicate systems, and thus are not favored in the hostile environments which normally accompany a downhole wellbore.
Overcoming these problems, a system for downhole pressure measurement was devised utilizing a small diameter capillary tube or microtube connected to a downhole pressure chamber. The pressure chamber is in fluid communication with the fluid pressure in the well. The small diameter tubing transmits the pressure from the downhole location to the surface where pressure measurement using conventional or electronic pressure gauges is possible in a friendlier environment. These systems are sometimes referred to as Pressure Telemetry Systems or Molecular Telemetry Systems. Typically a monitoring gas, such as helium or nitrogen, used. U.S. Pat. No. 3,895,527, issued to McArthur, incorporated herein by reference for all purposes, discloses a system for remotely measuring pressure in a borehole which utilizes a small diameter tube which has one end exposed to borehole pressure and has its other end connected to a pressure gauge or other detector at the surface.
The concept of measuring downhole pressure according to a system which uses such a small diameter tube is also disclosed in U.S. Pat. No. 3,898,877, issued to McArthur, and an improved version of such a system is disclosed in U.S. Pat. No. 4,010,642, also issued to McArthur, both of which are incorporated herein by reference for all purposes. The teachings of this latter patent have rendered this technology particularly well suited for more reliably measuring pressure in a borehole, since the lower end of the tube extends into a chamber having at least a desired volume. Further methods are found in U.S. Pat. No. 4,505,155 to Jackson, incorporated herein by reference for all purposes. U.S. Pat. No. 4,018,088 to McArthur teaches use of a downhole high pressure float valve in the chamber. Accurate downhole temperature readings in conjunction with pressure readings utilizing small diameter tubing pressure transmission are taught in U.S. Pat. Nos. 4,976,142 and 5,163,321, both issued to Perales and both incorporated herein for all purposes. Additional improvements have been made resulting in retrievable pressure telemetry systems, purging and system check techniques, simultaneous temperature measurement, advanced temperature and pressure measurement techniques, expandable chambers, continuous capillary tubing, capillary gas weight calculation to correct for truer bottom hole pressures, use of helium as the monitoring gas, concentric chambers, automatic purge systems and others. Pressure telemetry systems are commercially available from Halliburton Energy Services under the tradename EZ-Gauge.
One problem with the pressure telemetry systems is the lack of a device to stop hydrocarbon flow up the small diameter conduit in the case of failure of the system due to a leak of the monitoring gas or due to a catastrophic wellhead event. The continuous conduit of molecules to the surface is perfectly safe during normal operation, but can become a concern after catastrophic events. If the wellhead is severely damaged, such as after it is hit by a truck or other surface equipment, by a natural or man-made disaster, such as an iceberg, tsunami, hurricane, tornado, avalanche, earthquake, mudslide or military ordnance, the conduit can become a potential path for hydrocarbon to travel from the wellbore to the surface. Due to the extremely small diameter of the conduit, the surface leak will be small or even non-existent if the conduit becomes plugged, but the potential does exist for a leak. Whether the failure of the system is due to a catastrophic event or a leak in the conduit, wellbore fluid flows into the conduit where it can foul the small diameter tubing of the conduit.
Disadvantages of the prior art are overcome by the present invention, and improved methods and apparatus are hereinafter disclosed for reducing or eliminating the possibility of a surface leak after a catastrophic wellhead event and preventing movement of wellbore fluid into the small diameter tubing of a pressure telemetry system.
Safety valve apparatus for a pressure telemetry system, or a pressure monitoring system utilizing a small diameter tubing conveying pressure from a downhole pressure chamber to the surface, the system pressurized with a monitoring gas, is presented. A pressure measuring apparatus for continuously measuring pressure of a wellbore fluid in a wellbore at a downhole location has a conduit positioned in the wellbore and having a flow path extending from the surface to a downhole housing. The downhole housing defines a monitoring-gas chamber, the housing in fluid communication with the flow path in the conduit and with the wellbore. A pressurized monitoring-gas source is used for pressuring the flow path in the conduit and at least a portion of the monitoring-gas chamber with a selected monitoring gas.
In one embodiment, a check valve assembly is placed along the fluid flow path having a check valve housing defining a check valve chamber. An operating member is disposed within the check valve chamber and is movable between an open position wherein fluid communication between the wellbore and the surface along the flow path of the conduit is allowed and a sealed position wherein fluid communication between the wellbore and the surface along the flow path of the conduit is prevented. The operating member moves to the sealed position by floating on an activating fluid. The operating member must be of low effective specific gravity to float on wellbore hydrocarbon fluids, either liquid or gas. Consequently, in one preferred embodiment, the check valve operating member is a hollow dart which retains the monitoring gas inside the hollow portion, thereby effectively reducing its specific gravity such that it will float on the activating fluid. The activating fluid is a fluid can be hydrocarbon wellbore liquid or gas, completion, stimulation or other injected liquids or gases or an activating liquid or gas stored in a separate chamber in fluid communication with the check valve chamber. Preferably, the dart comprises at least a portion with a standoff member to assist in preventing the dart from sticking to the check valve chamber wall. The assembly may have a retaining member for limiting movement of the operating member away from the sealed position and may utilize a biasing mechanism to bias the member toward the open or closed position. The biasing mechanism can be gravity, a spring or other devices.
In another embodiment, the check valve assembly has a semi-permeable membrane creating a barrier across the check valve chamber. The semi-permeable membrane is substantially permeable to the monitoring gas and substantially impermeable to the activating fluid. For example, the semi-permeable membrane can be highly permeable to helium while being substantially impermeable to hydrocarbon gas. The sealing operating member of the valve is moved to the sealed position when the membrane is contacted by the activating fluid. A pressure differential is created across the semi-permeable membrane when it is contacted on one side by the activating fluid, such as hydrocarbon gas, and on the other side only by the monitoring gas. This pressure differential causes the membrane to expand or contract, depending on the particular design, and thereby move the operating member into the sealed position. In a particular design a membrane “balloon” is provided, which contracts upon contact by the activating fluid. As the balloon contracts, the operating member is forced into sealing contact with the chamber sealing surface.
In another embodiment, the check valve assembly operating member is moved to the sealed position by a swellable material, the swellable material substantially swelling when exposed to an activating fluid. The swellable material is positioned within the check valve assembly chamber and, when swollen, forces the operating member into the sealed position. Preferably the swellable material reduces to at or near its original unswelled size when the activating fluid is removed, such as by purging the system.
These and further objects, features, and advantages of the present invention will become apparent from the following detailed description, wherein references made to the figures in the accompanying drawings.
The accompanying drawings are incorporated into and form a part of the specification to illustrate several examples of the present inventions. These drawings together with the description serve to explain the principles of the inventions. The drawings are only for the purpose of illustrating preferred and alternative examples of how the inventions can be made and used and are not to be construed as limiting the inventions to only the illustrated and described examples. The various advantages and features of the present inventions will be apparent from a consideration of the drawings in which:
The present invention has utility for reducing or eliminating the possibility of a surface leak after a catastrophic wellhead or other event in a wellbore having a pressure telemetry system utilizing a small diameter tubing extending from the surface of the well to a downhole test location. The downhole fluid pressure to be monitored may be monitored in flowing, pumping or static wells, and the downhole fluid may be equal or greater than hydrostatic pressure. For purposes of this of this description, the terms “up,” “down,” “uphole,” “downhole,” “top,” and “bottom” and the like are for reference purposes only. The device can be used in a horizontal or deviated well, and practitioners will recognize that some of the parts of the device can be rotated or reversed in orientation or order.
The small diameter conduit 18 extends from the surface to a downhole location where monitoring-gas housing 19 is located. The conduit 18 may be run inside of the production tubing 13, outside the tubing 13, as shown, or independently on a wireline or conduit spool or outside the casing. The lower end of the conduit 18 is in fluid communication with the chamber 16. Suitable small diameter tubing may vary in diameter according to the specific parameters of the well and well conditions, but is typically 0.125″ or 0.250″ in outer diameter with an 0.035″ or 0.152″ internal diameter, respectively. Temperature monitoring equipment (not shown) may also be utilized, such as a thermocouple or fiber optic line, inside or outside the conduit and thermal sensors. As those skilled in the art appreciate, small diameter tubing in the range as specified above is commonly referred to as microtubing.
A safety check valve assembly 30 is provided at the top of the monitoring-gas chamber 16. The assembly can alternately be provided above or below the assembly. In another alternative, the assembly can be provided anywhere along the flow path 23 of the conduit 18 above the pressure monitoring housing 19. The check valve assembly 30 has a housing 32 defining a check valve chamber 34. The check valve chamber 34 is in fluid communication, in this case, through ports 35, with the monitoring-gas chamber 16. The check valve chamber 34 is in fluid communication, via the ports 35 and monitoring-gas chamber 16, with the activating fluid 42, in this case wellbore fluid 27. The check valve chamber 34 is also in fluid communication through port 42 to the flow path 23 of conduit 18. The check valve assembly includes an operating member 36 disposed within the check valve chamber 34 and movable between an open position 38, seen in
In
In
In
If the check valve assembly 30 operates to block fluid flow to the surface, that is, the operating member moves to the closed position 40, the pressure telemetry system can be re-pressurized and placed back into service by purging the system. During purging, monitoring gas 29 is pressurized into the conduit 18 and through flow path 23. As the pressure of the monitoring gas 29 exceeds that of the activating fluid below the operating member 36, the operating member 36 is forced down out of the closed position 40 and the interface 44 of the activating fluid 42 and monitoring gas 29 is similarly forced downward. The monitoring-gas chamber and check valve assembly will return to the configuration shown in
To float on the activating fluid, the operating member, obviously, must have an effective specific gravity of less than the activating fluid. Since the activating fluid is often hydrocarbon liquid or gas, the effective specific gravity of the operating member must be very light. Typical wellbore fluids, such as hydrocarbon liquids and gases, have very low specific gravities. Hydrocarbon liquid, for example, may have a specific gravity in the range of about 0.8, while hydrocarbon gases have an even lower specific gravity. Although the operating member in
In this arrangement, if the wellbore fluid pressure exceeds the monitoring gas pressure, the wellbore fluid 27 forces the activating fluid 42 through communication tubing 58 into monitoring-gas chamber 16. The activating fluid 42 rises through the monitoring-gas chamber 16, into the check valve chamber 34 and contacts the operating member 36, moving the member 36 into the closed position. This arrangement has the advantage that the activating fluid 42 is pre-selected, having chosen characteristics, and is cleaner than typical wellbore fluid.
The dart 55 has a sealing face 50 which cooperates with a sealing surface in the check valve chamber. The sealing face 50 can be conical, as shown, spherical, flat or any desired shape. To prevent the dart 55 from sticking to the check valve housing inner wall, the dart 55 is preferably designed with an offset 62 formed by a standoff member 64. In
The dart can be made of any material, but is preferably made of a lightweight material capable of surviving in the downhole environment. Preferably the dart, or other shaped operating member, is made of PEEK. Alternate materials include, but are not limited to, polyethersulfone, acrylics, Vivac (tradename), polyethylenes, polypropylene, polysulfones, polyurethane and polyphenylene oxide. The dart or other operating member can be made partially or entirely of metal, ceramic or other substances. Metal may be desirable to form the sealing face of the operating member. The additional weight, and higher effective specific gravity, may require a greater hollow portion for retaining a greater volume of monitoring gas or use of the dual-chamber design. Similarly, if the activating fluid is a gas, the effective specific gravity of the operating member must be further reduced.
The membrane 88 is preferably provided with “slack” such that the membrane can easily elongate to move the operating member into the closed position. In the embodiment in
The retaining member 37 is provided with flow passages 89 therethrough. The retaining member 37 can be a disc with passages or a simple bar across the chamber 34. In the embodiment shown in
In
Other arrangements of the membrane balloon are possible. The balloon can be attached to the chamber wall or retaining member in various arrangements. Further, the biasing mechanism can be positioned inside or outside the balloon. Another biasing mechanism 90 can be supplied by using a stiffer membrane which can be folded, similar to an accordion. Other variations and arrangements will present themselves to those skilled in the art.
An example of a swellable material is a 50 duro nitrile with a low CAN content, or a soft EPDM. These substances will swell in the presence of hydrocarbons, so the activating fluid can be wellbore fluids. Further possible swellable materials include, but are not limited to, hydrogenated nitrile, polychloroprene, butyl, polyurethane and silicon, for instance, which swell in benzene. Similarly brake fluid will cause swelling of fluorocarbon, hifluor and flourosilicon, for example. Diesel will cause swelling of ethylene propylene, polyurethane, butyl, butadiene, isoprene and silicon, for example. Other swellable materials and activating fluids will present themselves to those skilled in the art.
The embodiments shown and described above are only exemplary. Many details are often found in the art such as screen or expansion cone configurations and materials. Therefore, many such details are neither shown nor described. It is not claimed that all of the details, parts, elements, or steps described and shown were invented herein. Even though, numerous characteristics and advantages of the present inventions have been set forth in the foregoing description, together with details of the structure and function of the inventions, the disclosure is illustrative only, and changes may be made in the detail, especially in matters of shape, size and arrangement of the parts within the principles of the inventions to the full extent indicated by the broad general meaning of the terms used in the attached claims.
The restrictive description and drawings of the specific examples above do not point out what an infringement of this patent would be, but are to provide at least one explanation of how to make and use the inventions. The limits of the inventions and the bounds of the patent protection are measured by and defined in the following claims.
Number | Name | Date | Kind |
---|---|---|---|
3633414 | Field et al. | Jan 1972 | A |
3744307 | Harper et al. | Jul 1973 | A |
3895527 | McArthur | Jul 1975 | A |
3898877 | McArthur | Aug 1975 | A |
3985027 | Tricon | Oct 1976 | A |
4010642 | McArthur | Mar 1977 | A |
4018088 | McArthur | Apr 1977 | A |
4505155 | Jackson | Mar 1985 | A |
4678035 | Goldschild | Jul 1987 | A |
4976142 | Perales | Dec 1990 | A |
5163321 | Perales | Nov 1992 | A |
5184508 | Desbrandes | Feb 1993 | A |
Number | Date | Country | |
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20070012434 A1 | Jan 2007 | US |