The present invention relates to plunger lift apparatus for the lifting of formation liquids in a hydrocarbon well. The plunger comprises a thermal actuated valve encased in the plunger which reacts to downhole heat to open and close apertures, thereby slowing a rate of travel of the plunger apparatus to protect the apparatus at the bottom and top of the well.
A plunger lift is an apparatus that is used to increase the productivity of oil and gas wells. As today's companies implement cost containment and resource allocation measures in response to lower product prices, the use of a plunger lift production method should be considered because it can be one of the most economical methods of production. Large returns are possible from a relatively small capital expenditure. This is particularly true for marginal wells.
The cost-effectiveness of plunger lift methodology can be characterized by at least three features: low initial costs, low annual maintenance costs, and the ability to better utilize other field assets. The benefits of these features are lower overall costs and lower unit production costs.
A typical plunger lift application can cost less than $5,000 per installation as compared to $20,000 to $40,000 for beam lift. Plunger lift costs typically do not increase with well depth and annual maintenance costs can range from $500 to $1,000 versus $5,000 to $10,000 for beam lift.
Other benefits can include: better utilization of an operator's time, reduction of environmental liability concerns from not venting hydrocarbons into the atmosphere (blowing), and applications are not typically limited by depth. Although systems have been successfully installed on wells as deep as 26,000 feet, even greater depths may be achieved.
There are five common applications for plunger lifts: 1). gas well liquid unloading; 2). oil production with associated gas; 3). gas wells with coiled tubing; 4). control scale and paraffin; and 5). intermittent gas lift.
In the early stages of a well's life, liquid loading is usually not a problem. When rates are high, the well liquids are carried out of the tubing by the high velocity gas. As a well declines, a critical velocity is reached below which the heavier liquids do not make it to the surface and start to fall back to the bottom exerting back pressure on the formation, thus loading up the well. A plunger system is a method of unloading gas in high ratio oil wells without interrupting production. In operation, the plunger travels to the bottom of the well where the loading fluid is picked up by the plunger and is brought to the surface removing all liquids in the tubing. The plunger also keeps the tubing free of paraffin, salt or scale build-up. A plunger lift system works by cycling a well open and closed. During the open time a plunger interfaces between a liquid slug and gas. The gas below the plunger will push the plunger and liquid to the surface. This removal of the liquid from the tubing bore allows an additional volume of gas to flow from a producing well. A plunger lift requires sufficient gas presence within the well to be functional in driving the system. Oil wells making no gas are thus not plunger lift candidates.
As flow rate and pressures decline in a well, lifting efficiency can decline. Before long the well could begin to “load up”. This is a condition whereby the gas being produced by the formation can no longer carry the liquid being produced to the surface. There are two reasons this occurs. First, as liquid comes in contact with the wall of the production string of tubing, friction occurs. The velocity of the liquid is slowed and some of the liquid adheres to the tubing wall, creating a film of liquid on the tubing wall. This liquid may not reach the surface. Secondly, as the flow velocity continues to slow the gas phase may no longer support liquid in either slug form or droplet form. This liquid along with the liquid film on the sides of the tubing, may fall back to the bottom of the well. In a very aggravated situation, there could be liquid in the bottom of the well with only a small amount of gas being produced at the surface. The produced gas must bubble through the liquid at the bottom of the well and then flow to the surface. Because of the low velocity, very little liquid, if any, is carried to the surface by the gas. A plunger lift will act to remove the accumulated liquid, thereby improving well efficiency.
A typical installation plunger lift system 100 can be seen in
Surface control equipment usually consists of motor valve(s) 14, sensors 6, pressure recorders 16, etc., and an electronic controller 15 which opens and closes the well at the surface. Well flow ‘F’ proceeds downstream when surface controller 15 opens well head flow valves. Controllers operate on time, or pressure, to open or close the surface valves based on operator-determined requirements for production. Modern electronic controllers incorporate features that are user friendly, easy to program, addressing the shortcomings of mechanical controllers and early electronic controllers. Additional features include: battery life extension through solar panel recharging, computer memory program retention in the event of battery failure and built-in lightning protection. For complex operating conditions, controllers can be purchased that have multiple valve capability to fully automate the production process.
Standard downhole bypass plungers typically have vertical corridors built into them to allow fluids to pass through the plunger during a descent. These corridors are closed when the plunger strikes the bottom of the well and during plunger ascent. When the corridors are open, the plunger falls quickly against flow. Bypass plungers may be used with strong gas wells, flowing wells, and wells that make a lot of fluid. The size of the vertical corridors of a standard bypass plunger cannot typically be varied during the fall or rise of the plunger. Onr type of a standard non bypass plunger operates by pushing its way through fluids, wherein the fluids must flow between the small area between the tubing and the outside of the plunger. Such plungers, without flow through vertical corridors will fall much slower than a plunger with open vertical corridors. When rising near the surface, a plunger with slightly open vertical corridors will slow down signifying that it is losing its seal.
Fall rates of about 1000 to about 2000 feet per minute (fpm) through gas have been experienced. Foss and Gaul reported a 2000 fpm plunger fall rate and incorporated this value into their calculations. Bypass type plungers fall at rates of about 3000 to about 3500 fpm. Abercrombie found that this rate may be too aggressive for general applications, and used a 1000 fpm value in his calculations. If pad, wobble washer or blade plungers are being used, the fall rate can generally be as low as 175 fpm through gas.
Plunger fall rates through liquid range from 17 fpm to 250 fpm. Foss and Gaul used 172 fpm in their calculations.
Plunger rise rates average between about 750 to about 2000 fpm. A common rise rate used is 1000 fpm. In general, the lower the upward velocity, the more efficient the application will be. The drawback to low upward velocity is the possibility of a plunger stalling. If a good seal exists between the plunger and tubing, an operator can attempt to bring the plunger up at speeds less than 1000 fpm. Lower speeds will allow the operator to maintain the well at a lower average casing pressure, and this will maximize reservoir drawdown. The disclosed device can help to slow the plunger's rise, thus optimizing well operation, and minimizing plunger stall.
Since plungers weigh several pounds, they can act as a projectile when traveling at a fall rate of up to about 3500 fpm, or about 30–45 miles per hour (mph). The impact force of a ten-pound projectile, for example, traveling at over 30 mph can clearly impart damage to downhole equipment that it slams against in order to stop while falling downhole. The same problem can exist for rising plungers.
Not only can the disclosed plunger automatically slows down at the bottom (or top) portion of its travel, it can do so without impact. The present invention provides a thermal actuated valve that motivates fluid to flow in or around the plunger as fluid temperature increases or decreases. Thus the plunger's apertures and speeds can be controllable in relation to ambient temperatures.
A wax-filled canister or equivalent can expand internally downhole and move a piston to motivate a valve in a fluid passage corridor in a plunger. When the corridor is closed, the plunger can no longer efficiently pass downhole fluids through it as it falls. Therefore, the temperature of the downhole fluids acts to provide a breaking action on the descending plunger. Production operators can save money with a reduction of broken downhole plunger stops, plungers and the reduction of downtime. An alternate embodiment uses a thermal actuator(s) to expand an outer casing of the plunger, thereby slowing the speed of the plunger.
An aspect of the present invention is to open/close plunger bypass apertures without impact at a top or a bottom of a well.
Another aspect of the present invention is to provide an automatic brake for a downhole plunger during its falling or rising mode.
Another aspect of the present invention is to use a thermal actuator as the trigger to close a fluid passage corridor in the plunger when the thermal actuator senses an increase in ambient temperature, and to open as the actuator senses a temperature drop.
Another aspect of the present invention is to use a thermal actuator to expand the outer casing of a plunger, thereby slowing its rate of travel. While the expandable plunger is falling, liquid and gas are passing around the O.D. of the plunger. As the plunger nears the bottom of the well where the temperature is increased, the plunger's thermal actuator(s) motivates a valve causing an expansion of the sealing surface of the plunger, making the gap between the tubing and the plunger smaller and allowing for less liquid and gas to pass. Thus plunger fall rate slows.
The present invention uses the known technology of expanding waxes in a closed container to move a piston upon the expansion of the wax (or equivalent) fluid in the container. Once the plunger nears the bottom of the well the actuator will sense a pre-determined actuator temperature and motivate the piston to fully expand the plunger sealing surface, making full contact with the tubing or casing, creating a tight friction seal, thereby forcing the plunger and liquid load to the surface. In one example, the actuator is preset at about 160° F. but any temperature desired may be the set point. Once the plunger has arrived into the lubricator, where cool gas flows around the plunger the thermal actuator(s) will sense a cooling thereby contracting the sealing surface, thus allowing the plunger to fall back to the bottom of the well starting the cycle over.
Other aspects of this invention will appear from the following description and appended claims, reference being made to the accompanying drawings forming a part of this specification wherein like reference characters designate corresponding parts in the several views.
In one embodiment of the present invention, the thermal actuator is filled with an expandable material such as Thermoloid® (Therm-Omega-Tech, Inc.), which changes phase from a solid to a liquid and expands as the temperature increases. Other expandable phase change materials may be used. Since the expandable material can be incompressible and encased in a rigid housing, only the piston can move. When the expandable material cools, the volume contracts and allows the piston to retract if a return force is acting on the piston. The piston will not normally retract unless a return force is present.
The phase change and resultant motion occurs over a narrow temperature range. Such a property can allow precise control of a device at a specific temperature with no significant effect outside a chosen control range.
A temperature actuated valve is encased in a downhole plunger. Temperature change alone can be used to operate the device; e.g., open or close the valve. Push-out pads can be used to open and close valve feet. Because the expandable material can operate in the solid and liquid or gas phase, each of which are typically incompressible, load changes on the piston (within design limits) can have little or no effect on operating temperature. Vapor-filled or liquid to vapor phase change devices can be used, but may be more sensitive to load changes (changing the load on these devices, e.g., changing spring tension, is used to change the operating temperature range).
Since the operating temperature of solid-liquid phase change actuators is determined by various properties of the expandable material (e.g., melting and solidification temperatures), the operating temperature can be extremely stable, repeatable and accurate.
Commercially available thermal actuators are useful in the present invention. Reliable choices are those that can be used in pressure or vacuum, liquid or gas, and can be made from most machineable materials. Custom mounting configurations may be desired. For maximum stroke, a typical temperature change can range from about 10° F. to about 20° F. while start to stroke temperatures can range from about −30° F. to about 300° F. A wide choice of temperature ranges are available. In one embodiment the temperature ranges from about −40° F. to about 325° F.
Before explaining the disclosed embodiment of the present invention in detail, it is to be understood that the invention is not limited in its application to the details of the particular arrangement shown, since the invention is capable of other embodiments.
Also, the terminology used herein is for the purpose of description and not of limitation.
When the plunger falls to the bottom of a well a thermal actuated valve will close by sensing heat. It will open at the top of a well when it senses cool temperature gas flowing around the plunger.
Plunger mandrel 20 is shown with solid ring 22 sidewall geometry. Solid sidewall rings 22 can be made of various materials such as steel, poly materials, Teflon®, stainless steel, etc. Plunger mandrel 80 is shown with shifting ring 81 sidewall geometry. Shifting rings 81 allows for continuous contact against the tubing to produce an effective seal with wiping action to ensure that all scale, salt or paraffin is removed from the tubing wall. Shifting rings 81 are individually separated at each upper surface and lower surface by air gap 82. Plunger mandrel 60 has spring-loaded interlocking pads 61 in one or more sections. Interlocking pads 61 expand and contract to compensate for any irregularities in the tubing thus creating a tight friction seal. Plunger mandrel 70 incorporates a spiral-wound, flexible nylon brush 71 surface to create a seal and allow the plunger to travel despite the presence of sand, coal fines, tubing irregularities, etc.
The plungers each have a threaded connector 266. A thermal actuated canister 265 screws onto a threaded connector 266 via threaded collar 2660. Under normal conditions during the free fall of the plunger, holes 267 are open, and fluid flows into holes 267 and through internal orifice H. Under high temperature conditions as the plunger reaches (thousands of feet) downhole, holes 267 are automatically and proportionally shut according to temperature. When the holes 267 are fully shut, then the fluids can only flow between the plunger and the casing 9 (this is the case for a non-flowing well in a shut-in state). In this manner, the plunger's rate of fall is reduced.
Referring next to
A sheath 308 (preferably a rubber insulation) houses the elements 303, 304, 305, 306, 307 inside cavity 309 of the canister 265. A metal cup 311 holds thermal actuator 307 and serves as a thermal mass.
Sheath 308 can be sized to keep the downhole heat away from thermal actuator 307 until the plunger nears bottom. At the bottom, ambient heat heats sheath 308 which heats thermal actuator 307, closing the bypass valve for the plunger's journey up the tubing. Near the top, ambient gas cools thermal actuator 307, so it proportionally opens allowing gas to escape up through the plunger, losing the gas seal, thus slowing the plunger down. Sheath 308 keeps the heat away from the actuator on the way to the bottom of the well so the valve stays open. Then sheath 308 holds the heat in to keep the actuator closed until it reaches the top of the well. Insulation may or may not be used depending on the application and type of plunger. The size of sheath 308 can be tailored to slow the heat transfer in the plunger before it reaches bottom, and partially open at top to slow the travel time.
Referring next to
In
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Slots 512 allow fluid to flow directly against thermal actuators 507, 509 without any insulation. The thermal actuators are selected for different actuation temperatures or setpoints, for example 140° F., 150° F., etc. A plug 511 with threads 5111 allows “in-the-filed” replacement of different actuation temperature actuators to get the best results. In this example pistons 508, 510 move about ¼ inch each, resulting in a total displacement of the valve stem 503 of about half an inch. Other distances are possible if desired. With differing actuation temperatures, valve 502 can first be half closed for part of its travel, and then fully closed at the bottom of the well; on the rise just the opposite would occur. Once closed, actuator 505 locks the stem by inserting piston 506 in groove 504.
Referring next to
For flowing wells, the two (or more) setpoint thermal actuator systems are typically used to make sure that no full closure of the valve occurs until the plunger reaches bottom. If a valve closes before the plunger reaches bottom of a flowing well, the plunger can change direction, going up propelled by gas flow without any liquid above the plunger. The disclosed method uses multiple setpoints to partially close valve 502, and to not totally close the valve on the way down.
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A central shaft 1018 has cam extensions 1019. Thermal actuator 1012 has a piston 1013 which, upon reaching setpoint temperature, pushes a shaft 1018 upward, thereby causing cam extensions 1019 to push outbound the wedges 1017 which in turn push outbound pads 1002. Sleeves 1053 hold wedges 1019 in place. A spring 1011 returns shaft 1018 to the passive mode shown in
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Pusher actuator 2202 can be set at, for example, about 160° F. to push a piston 2205 up. A piston head 2206 engages a slide valve 2207 up, thereby closing holes 2204 with a valve gate segment 2208 which comprises a top rim seat 2209 which seats against plunger 750. A retaining ring 2210 remains stationary to secure the thermal actuator 2202 in place.
When the piston 2205 and piston head 2206 are actuated up as shown in
Snap rings 2211, 2214 secure a spring guide 2212 and a spring 2213. Spring guide 2212 draws spring 2213 up in
Holes 2215 (see
Thermal actuator 2203 is usually set at about ambient ground level temperature, perhaps at about 70° F. When actuated, a locking piston 2220 pushes off a spring 2221, thereby forcing thermal actuator 2203 down as seen in
An Allen screw lead hole 3225 is used to lock a cap 3226 in place. Locking ball holes 3227 are known in the art to house a ball and a locking ring. Indentations 4444 function to give the balls 2217 a snap action to unlock.
Referring next to
It is understood in the art that a “pad” type plunger is an external bypass plunger, wherein upon a thermal actuated extension of the pads essentially closes the valve so as to create a tight seal against the downhole tubing for the rising of the plunger. Pads are known as blades or any member which extends away from a central mandrel to decrease the gap between the tubing and the plunger.
Although the present invention has been described with reference to disclosed embodiments, numerous modifications and variations can be made and still the result will come within the scope of the invention. No limitation with respect to the specific embodiments disclosed herein is intended or should be inferred. Each apparatus embodiment described herein has numerous equivalents.
This application is a non-provisional application claiming the benefits of provisional application No. 60/549,814 filed Mar. 3, 2004.
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