Patent Application
20060201715
This disclosure relates generally to the field of recovery of subterranean resources, and more particularly to a system and method for drilling normally to sub-normally pressured formations.
Reservoirs are subterranean formations of rock containing oil, gas, and/or water. Unconventional reservoirs include coal formations, shale formations and low permeability formations containing gas and, in some cases, water. A coal bed, for example, may contain natural gas and water.
Coal bed methane (CBM) is often produced using vertical wells drilled from the surface into a coal bed. Vertical wells drain a very small radius of methane gas in low permeability formations. As a result, after gas in the vicinity of the vertical well has been produced, further production from the coal seam through the vertical well is limited.
To enhance production through vertical wells, the wells have been fractured using conventional and/or other stimulation techniques. Horizontal patterns have also been formed in coal seams to increase and/or accelerate gas production.
The invention encompasses a system and method for drilling normally to sub-normally pressured formations. In one embodiment, the method includes drilling a substantially horizontal well bore in a normally to sub-normally pressured formation. The normally to sub-normally pressured formation is an unconventional reservoir. The well bore is drilled over-balanced with a drilling fluid including a fluid loss agent. The fluid loss agent is operable to form a filter cake on the well bore during drilling.
More specifically, in accordance with a particular embodiment, the unconventional reservoir may comprise a fractured formation, a coal bed and/or a shale. The fluid loss agent may comprise a non-invasive or low-invasive fluid such as micelles, aphrons or other agent operable to form a filter cake to limit fluid loss from the well bore to the formation. The drilling fluid may comprise a heavy fluid having a density of 9.5 pounds per gallon or greater, 10 pounds per gallon or greater and/or a density substantially equal to or greater than that of the cuttings generated during drilling of the well bore.
Technical advantages of certain embodiments include providing a system and method for drilling a normally to sub-normally pressured formation. In a particular embodiment, a fluid loss agent may be used to form a filter cake around the well bore to enhance well bore stability. For example, the filter cake may seal the well bore and prevent fluid loss to the formation that could destabilize the formation and lower productivity of the formation. In addition, the filter cake may allow a positive pressure differential to be maintained between the well bore and the formation during drilling to stabilize the well bore.
Another technical advantage of certain embodiments may include the use of a dense drilling fluid to enhance well bore stability and/or improve cutting removal efficiency. In a particular embodiment, a dense drilling fluid having a density greater than 9.5 pounds per gallon, may be used. In other embodiments, the density of the drilling fluid may be 10 pounds per gallon or greater and/or have a density substantially the same or greater than the cuttings in order to improve cuttings removal.
Other technical advantages will be readily apparent to one skilled in the art from the following figures, description, and claims. Moreover, while specific advantages have been enumerated above, various embodiments may include all, some, or none of the enumerated advantages.
Like reference symbols in the various drawings indicate like elements.
In the illustrated embodiment, subterranean zone 30 is an unconventional reservoir, such as a coal seam, tight shale or low permeability formations. Subterranean zone 30 may be accessed to remove and/or produce water, hydrocarbons, and other fluids, to sequester carbon dioxide or other pollutants, and/or for other operations. Subterranean zone 30 may, in one embodiment, be naturally fractured.
For ease of reference and purposes of example, subterranean zone 30 will be referred to as coal seam 30. The coal seam 30 may be a normally to sub-normally pressured formation. For a normally pressured formation, the pressure in the formation is equal or substantially equal to that of the water gradient at the depth of the formation. For a sub-normally pressured formation, the pressure in the formation is less than that of the water gradient at the depth of the formation. For example, a sub-normally pressured coal seam 30 may have a pressure that is 5 or more percent less than that of the water gradient at the depth of the coal seam 30.
The well bore 40 can define a first portion 42 that extends from the surface 20, a second portion 44 at least partially coinciding with the coal seam 30 and a curved or radiused portion 46 interconnecting the portions 42 and 44. In one instance, the first portion 42 may be drilled to extend past the curved portion 46 to define a sump and/or to provide access to additional coal seams 30, for example, by drilling additional curved portions 46 and second portions 44. Additionally, although the first portion 42 is illustrated as being substantially vertical, the first portion 42 may be formed at any angle relative to the surface. For example, the first portion 42 may be slanted to reduce the radius of the curved portion 46, to accommodate surface 20 geometric characteristics or other concerns such as nearby well bores. For example, the first portion 42 may be angled to accommodate an adjacent well bore 40 drilled from the same surface area or same drilling pad. The first portion 42 of well bore 40 may be lined with a suitable casing 48. The casing 48 may also extend into or through the curved section 46, and in some instances, into the second portion 44.
The second portion 44 may be substantially horizontal and/or in the seam of coal seam 30, may track the depth of the coal seam 30, may undulate in the coal seam 30 or be otherwise suitably disposed in or about the coal seam 30. The second portion 44 of the well bore 40 may include a well bore pattern with a plurality of lateral or other horizontal well bores, as it discussed in more detail with respect to
Although
Articulated well bore 40 is drilled using drill string 50 that includes a suitable down-hole motor and drill bit 52. The drill string 50 may be driven by a rotary rig, top drive rig and/or coiled tubing rig. Accordingly, the drill string 50 may be coiled tubing, sectioned drill pipe or other suitable tubing. Other down hole drill and/or steering systems may be used. During the process of drilling well bore 40, drilling fluid or mud is pumped down drill string 50, as illustrated by arrows 60, and circulated out of drill string 50 in the vicinity of drill bit 52, as illustrated by arrows 62. The drilling fluid flows into the annulus between drill string 50 and well bore walls 49 where the drilling fluid is used to remove formation cuttings and coal fines. The cuttings and coal fines (hereinafter referred to as “debris”) are entrained in the drilling fluid, which circulates up through the annulus between the drill string 40 and the well bore walls 49, as illustrated by arrows 63, until it reaches surface 20, where the debris is removed from the drilling fluid and the fluid is re-circulated through well bore 40.
In certain embodiments, the drilling fluid may comprise water and one or more weighting agents, fluid loss agents, and/or viscosity agents. The weighting agents may be used to increase the density of the drilling fluid and thus the hydrostatic fluid pressure exerted on the coal seam 30 during drilling of the well bore 40. The drilling operation produces a column of drilling fluid in the well bore 40 having a vertical height equal to the depth of the well bore 40 and produces a hydrostatic pressure on well bore 40 relating to the density of the drilling fluid and the vertical height of the column of fluid. In one embodiment, the well bore 40 is drilled over-balanced with the hydrostatic fluid pressure in well bore 40 exceeding the pressure in the coal seam 30. For normally and sub-normally pressured coal seams 30, the well bore 40 may be drilled with a drilling fluid having a density selected to be approximately equal to or greater than the density of the formation cuttings. In one instance, the well bore 40 may be drilled with a drilling fluid having a density of 9.5 pounds per gallon or higher, 10 pounds per gallon or higher, or a density close to or matching that of the coal cuttings, which may be 11.2 pounds per gallon. In this embodiment, the coal cuttings may be buoyant or nearly buoyant in the drilling fluid and efficiently removed from the well bore 40. This would allow for extremely high rates of drilling and high hole cleaning efficiency, greater than could be achieved with drilling fluid having a lower density than the cuttings.
In one embodiment, a salt such as sodium chloride or calcium chloride may be used as a weighting agent. In particular, sodium chloride may provide a brine having a density of up to 9.9 pounds per gallon. Calcium chloride may provide a brine having a density up to 11.7 pounds per gallon. In other embodiments, potassium formate may be used as a weighting agent. Potassium formate may provide a drilling fluid having a density up to 14 pounds per gallon. Other suitable weighting agents may be used.
The density, or specific gravity, of the drilling fluid may be determined based on bore hole stability needs, fracture gradient of the coal seam 30, and/or cutting removal needs. In this and other embodiments, bore hole stability needs may be initially determined based on the formation stress, formation pressure, and/or formation strength of the coal seam 30. For example, drilling fluid density may be increased when the coal seam 30 has less rock stability, while the density of the drilling fluid may be reduced when the coal seam 30 has a greater rock stability. Other suitable criteria may be used in initially or otherwise determining the density of the drilling fluid.
The fluid loss agent may form a filter cake 100 along the walls of the well bore 40. Filter cake 100 may prevent or significantly restrict drilling fluids from flowing into coal seam 30 from the well bore 40. The filter cake 100 may also provide a pressure boundary or seal between coal seam 30 and well bore 40 which may allow hydrostatic pressure in the well bore 40 to be used to control stability of the well bore 40 to prevent collapse during drilling. For example, during drilling, the filter cake 100 may aid well bore stability by allowing the hydrostatic pressure to act against the walls of the well bore 40 and/or by preventing drilling fluid from entering the coal seam 30 and destabilizing the seam around the well bore 40.
The depth of the filter cake 100 may be dependent upon many factors including the composition of the drilling fluid, the fluid loss agent, and/or the properties of the formation. The fluid loss agent may be selected or otherwise designed in connection with the drilling fluid based on rock mechanics, pressure and other characteristics of the coal seam 30 to form a filter cake that reduces or minimizes fluid loss during drilling and/or reduces or minimizes skin damage to the well bore 40.
The filter cake 100 may be formed with low-loss, ultra low-loss, non-invasive, low-invasive or other suitable drilling fluids. In one embodiment, fluid loss agent may comprise solid micelles that form microscopic spheres, rods, and/or plates in solutions. The micelles may comprise polymers with a range of water and oil solubilities. The micelles form a low permeability seal over pore throats of the coal seam 30 to greatly limit further fluid invasion or otherwise seal the coal seam boundary. In a particular embodiment, the fluid loss agent may comprise FLC 2000 available from IMPACT SOLUTIONS GROUP which may create a shallow filter cake 100 having a depth of invasion into the formation approximately two to four centimeters with a structural integrity operable to seal the well bore 40. In some instances, the fluid invasion rate of FLC 2000 may be 0.17 cubic meters of fluid lost to the formation per square meter of exposed formation in a day (m3/m2·day), as compared to 0.6 m3/m2·day for other conventional drilling fluids. FLC 2000 may provide a high return permeability after drilling during production. Starch and/or other fluid loss agents may be used in connection with the FLC 2000. In a particular embodiment, starch may be used to increase the sealing effect of the filter cake 100 formed by the FLC 2000. In another embodiment, aphrons, for example may be used as the fluid loss agent.
The viscosity agents may increase lifting capacity of the drilling fluid. In a particular embodiment, the viscosity agents may comprise carboxyl methyl cellulose (CMC), hydroxyl ethyl cellulose (HEC), polyanionic cellulose (PAC), and/or xanthan gum (XG polymer). Other suitable viscosity agents may be used. In addition, the viscosity agents may be omitted when not needed.
During drilling, the first portion 42 of the well bore 40 may be drilled overbalanced with a dense drilling fluid, but without the fluid loss and viscosity agents. The density of the drilling fluid may initially be between 8.3 and 9.0 pounds per gallon. After casing the first portion 42 of the well bore 40, and, in one embodiment, prior to entering the coal seam 30, the fluid loss and viscosity agents may be added to the drilling fluid. In the embodiment in which FLC 2000 is used as the fluid loss agent, FLC 2000 may initially be added to the drilling fluid in concentrations of up to 6-10 kilograms per cubic meter. If additional stability is needed, the concentration of FLC 2000 may be increased up to about 15 kilograms per cubic meter. Similarly, the density of the drilling fluid may be increased up to, for example, 9.5 pounds per gallon or greater to control bore hole 40 stability and/or assist in cuttings removal. For example, the density of the drilling fluid may be increased up to the density of the coal to suspend the cuttings in the drilling fluid and increase hole cleaning efficiency. However, the density of the drilling fluid may be limited due to the fracture gradient of the coal seam 30. In this case, additional viscofiers may be used. Additionally, the velocity and/or pump rate of the drilling fluid may be increased in the bore hole 40 to assist with cutting cleanout and removal
In certain embodiments, artificial lift apparatus 74 may comprise a pump coupled to tubing string 72 that is operable to draw fluid from well bore 40 through tubing string 72 to surface 20 and reduce the pressure within well bore 40. In the illustrated embodiment, artificial lift apparatus 74 comprises a fluid injector, which may inject gas, liquid, or foam into well bore 40. Any suitable type of injection fluid may be used in conjunction with system 70. Examples of injection fluid may include, for example: (1) production gas, such as natural gas, (2) water, (3) air, and (4) any combination of production gas, water, air and/or treating foam. In particular embodiments, production gas, water, air, or any combination of these may be provided from a source outside of well bore 40. In other embodiments, gas recovered from well bore 40 may be used as the injection fluid by re-circulating the gas back into well bore 40. Rod, positive displacement and other pumps may be used. In these and other embodiments, as illustrated in
The fluid extraction system 70 may also include a liner 75. The liner 75 may have a plurality of apertures and may be loose in the well bore or otherwise uncemented. The apertures may be holes, slots, or openings of any other suitable size and shape. The apertures may allow water and gas to enter into the liner 75 from the coal seal 30 for production to the surface. The liner 75 may have apertures when installed or may be perforated after installation. For example, the liner 75 may comprise a drill or other string perforated after another use in well bore 40.
The size and/or shape of apertures in the liner 75 may in one embodiment be determined based on rock mechanics of the coal seam. In this embodiment, for example, a representative formation sample may be taken and tested in a tri-axial cell with pressures on all sides. During testing, pressure may be adjusted to simulate pressure in down-hole conditions. For example, pressure may be changed to simulate drilling conditions by increasing hydrostatic pressure on one side of the sample. Pressure may also be adjusted to simulate production conditions. During testing, water may be flowed through the formation sample to determine changes in permeability of the coal at the well bore in different conditions. The tests may provide permeability, solids flow and solids bridging information which may be used in sizing the apertures, determining the periodicity of the apertures, and determining the shape of the apertures. Based on testing, if the coal fails in blocks without generating a large number of fines that can flow into the well bore, large perforations and/or high clearance liners with a loose fit may be used. High clearance liners may comprise liners one or more casing sizes smaller than a conventional liner for the hole size. The apertures may, in a particular embodiment, for example, be holes that are ½ inch in size.
In operation of the illustrated embodiment, fluid injector 74 injects a fluid, such as water or natural gas, into tubing string 72, as illustrated by arrows 76. The injection fluid travels through tubing string 72 and is injected into the liner 75 in the well bore 40, as illustrated by arrows 78. As the injection fluid flows through the liner 75 and annulus between liner 75 and tubing string 72, the injection fluid mixes with water, debris, and resources, such as natural gas, in well bore 40. Thus, the flow of injection fluid removes water and coal fines in conjunction with the resources. The mixture 80 of injection fluid, water, debris, and resources is collected at a separator (not illustrated) that separates the resource from the injection fluid carrying the resource. Tubing string 72 and fuel injector 74 may be omitted in some embodiments. For example, if coal fines or other debris are not produced from the coal seam 30 into the liner 75, fluid injection may be omitted.
In certain embodiments, the separated fluid is re-circulated into well bore 40. In a particular embodiment, liquid, such as water, may be injected into well bore 40. Because liquid has a higher viscosity than air, liquid may pick up any potential obstructive material, such as debris in well bore 40, and remove such obstructive material from well bore 40. In another particular embodiment, gas may be injected into well bore 40. Although certain types of injection fluids are described, any combination of air, water, and/or gas that are provided from an outside source and/or re-circulated from the separator may be injected back into well bore 40.
Also in certain embodiments, after drilling is completed, the drilling fluid may be left in well bore 40 while drill string 50 is removed and tubing string 72 and liner 75 are inserted. The drilling fluid, and possibly other fluids flowing from the coal seam 30, may be pumped or gas lifted (for example, using a fluid injector) to surface 20 to reduce, or “draw down,” the pressure within well bore 40. As pressure is drawn down below reservoir pressure, fluid from the coal seam 30 may begin to flow into the well bore 40. This flow may wash out the filter cake 100 when non-invasive or other suitable drilling fluids are used. In other embodiments, the filter cake 100 or a portion thereof may remain. In response to the initial reduction in pressure and/or friction reduction in pressure, the well bore 40 may collapse, as described below.
Collapse may, in certain embodiments, improve the efficiency of gas production from coal seam 30 by, for example, increasing the localized permeability of the coal seam 30. The localized permeability is a permeability of all or part of an area around, otherwise about, or local to the well bore 40. The localized permeability may be enhanced, in one embodiment, by spalling or cleaving the subterranean zone 30 around the well bore and/or otherwise collapsing the well bore 40. Cleaving refers to splitting or separating portions of the subterranean zone 30. Spalling refers to breaking portions of the subterranean zone 30 into fragments and may be localized collapsed, fracturing, splitting and/or shearing. The increased localized permeability provides more drainage surface area without hydraulically fracturing the coal seam 30. Hydraulic fracturing comprises pumping a fracturing fluid down-hole under high pressure, for example, 1000 psi, 5000 psi, 10,000 psi or more.
Collapse may occur before or after production begins. Collapse may be beneficial in situations where coal seam 30 has low permeability, such as below 3 millidarcies. However, coal seams 30 having other levels of permeability may also benefit from collapse. In certain embodiments, the drilling fluid may be removed before the pressure drop in well bore 40. In other embodiments, the pressure within well bore 40 may be reduced by removing the drilling fluid.
As previously described, use of a fluid loss agent, or non-invasive fluid, may create a relatively shallow invasion filter cake 100, resulting in a relatively low amount of drilling fluid lost into the cleats 102 of the coal seam 30. In certain embodiments, a filter cake 100 may have an invasion depth 110 between two and four centimeters thick. A thin filter cake 100 may be advantageous when it will not cause a permanent blockage but is strong enough to form a seal between coal seam 30 and well bore 40 to facilitate stability of the well bore 40 during drilling.
During collapse, a shear plane 120 may be formed along the sides of the well bore 40. The shear planes 120 may extend into the coal seam 30 and form high permeability pathways connected to cleats 102. In some embodiments, multiple shear planes 120 may be formed during spalling. Each shear plane 120 may extend about the well bore 40.
Collapse may generate an area of high permeability within and around the pre-existing walls 49 of the well bore 40. This enhancement and localized permeability may permit a substantially improved flow of gas or other resources from the coal seam 30 into liner 75 than would have occurred without collapse. In an embodiment where the well bore 40 includes a multi-lateral pattern, the main horizontal bore and lateral bores may each be lined with liner 75 and collapsed by reducing hydrostatic pressure in the well bores.
Referring to
Proceeding to step 206, the vertical portion 42 of the well bore 40 is drilled and cased. At step 208, and, in one embodiment, prior to drilling into the coal seam 30, one or more fluid loss agents are added to the drilling fluid. In one embodiment, the fluid loss agents include at least one of aphrons and micelles. As previously described, the fluid loss agents may form a filter cake 100 on the walls 49 of the well bore 40. The filter cake 100 may stabilize the well bore 40 during drilling and may, in one embodiment, reduce differential sticking and provide lubrication to reduce friction of the drill string 50 in the well bore 40. The fluid loss agents may, for example, comprise FLC 2000, other micelle, and/or aphrons.
At step 210, one or more viscosity agents may be added to the drilling fluid. As previously described, the viscosity agents may comprise, for example, CMC, HEC, PAC and/or XG polymer. The viscosity agents may increase the viscosity of the drilling fluid and may thereby enhance cutting removal from the well bore 40.
Proceeding to step 212, the radiused portion 46 and horizontal portion 44 of the well bore 40 are drilled over-balance using the drilling fluid with the fluid loss agents and/or viscosity agents. Step 212 leads to decisional step 214 where during ongoing drilling operations, the No branch leads to decisional step 216. At decisional step 216, well bore 40 stability is determined. Well bore 40 stability may be determined based on, for example, the size and/or amount of cuttings being returned to the surface 20 during drilling. Large and/or a large number of cuttings may indicate instability of the well bore 40.
If the well bore is not stable, the No branch of decisional step 216 leads to step 218. At step 218, density of the drilling fluid may be increased to increase pressure on the walls 49 of the well bore 40 and stabilize the well bore 40. In one embodiment, care may be taken to avoid increasing drilling fluid density up to or beyond the fracture gradient of the coal seam 30. Also, at step 220, additional fluid loss agents may be added to the drilling fluid to enhance the filter cake 100 and reduce loss of drilling fluid into the coal seam 30. In a particular embodiment, starch may be added to enhance the sealability of the filter cake 100. In another embodiment, the additional amounts of fluid loss agents (aphrons, micelles, or other fluid loss agents) may be added to enhance the filter cake 100. Also, at step 221, the flow rate of the drilling fluid can be adjusted.
Step 221 leads to decisional step 222. The Yes branch of decisional step 216 also leads to step 222. At decisional step 222, it is determined if cuttings are building up in the well bore 40. Cutting buildup may be determined by the volume of cuttings recovered at the surface from the drilling fluid. For example, a low volume of cuttings may indicate buildup in the well bore 40. If cuttings are building up in the well bore 40, the Yes branch of decisional step 222 leads to step 224. At step 224, the density of the drilling fluid may be increased to enhance the ability of the drilling fluid to remove cuttings from the well bore 40. The density of the drilling fluid may be increased to a specific gravity toward, up to, at, near or above that of the coal cuttings in order to increase buoyancy of cuttings in the drilling fluid and increase cutting removal. As previously described, in one embodiment, care may be taken to avoid reaching the fracture gradient of the coal seam 30 and causing fractures in the seam. Next, at step 226, additional viscosity agents may be added to enhance cutting removal. At step 227, the flow of drilling fluid may be adjusted. In one instance, the flow can be increased to increase cuttings removal.
Step 227 returns to step 212. The No branch of decisional step 222 also returns to step 212. At step 212, drilling of the radiused and/or horizontal portions 46 and 44 of the well bore 40 is continued with adjustments for fluid density, fluid loss, and/or viscosity made as need for well bore stability and cuttings removal of the well bore 40. Upon completion of the well bore 40, the Yes branch of decisional step 214 leads to the end of the process.
The surface bore 310 may be horizontally offset from the first portion 42 of the well bore 40 proximate the coal seam 30 a sufficient distance to permit the curved portion 46 and any desired length of second portion 44 to be drilled before intersecting the cavity 312. The amount of the offset can be selected so the radius of the curved portion 46 can be large. A large radius of curvature reduces friction in the well bore 40 during drilling operations, and as a result, increases the reach of the drill string (as limited by friction) over well bores drilled with tighter radiuses.
Cavity 312 is formed proximate the coal seam 30. As used herein, proximate is intended to encompass the case where the cavity 312 is partly or wholly within the coal seam 30. The cavity 312 can be formed though the surface bore 310, for example, with an under reamer device, by hydrojetting, or other cavity forming device. Many cavity forming devices will form a cavity 312 with a substantially cylindrical portion, whereas natural occurring cracks or crevices are not cylindrical. The cavity 312 can be an enlarged cavity having a transverse dimension greater than the transverse dimension of the surface bore 310. Alternately the cavity 312 can have a transverse dimension equal to or smaller than the transverse dimension of the surface bore 310. The vertical dimension of the cavity 312, may be smaller than the vertical thickness of the coal seam 30, approximately the same as the vertical thickness of the coal seam 30, or may be larger than the vertical thickness of the coal seam 30.
The well bore 40 is drilled similarly to that described above, but the surface bore 310 and the cavity 312 are typically (although not necessarily) formed first. Also, the drilling of well bore 40 is controlled so that the bore intersects the cavity 312. In certain embodiments, the cavity 312 provides an enlarged target for intersection, and reduces the precision to which drilling well bore 40 must be controlled. After the cavity 312 has been successfully intersected, drilling may continue through the cavity 312 and into the coal seam 30. As discussed above, drilling fluid or mud is circulated down through the interior of drilling string 50 and up the annulus between drilling string 50 and well bore walls 49 where the drilling fluid is used to remove debris. While drilling the well bore 40, additional fluids, for example additional drilling fluid with the same or different characteristics and/or amounts and types of weighting agents, fluid loss agents, and/or viscosity agents as that pumped down the drilling string 50, or other suitable fluids, can be pumped down the surface bore 310 into the annulus between the drilling string 50 and the well bore walls 49. The additional fluids can be flowed to increase the flow rate in the annulus and aid in removing debris that may otherwise traversing the curved portion 42 and traveling up the first portion 42 to the surface 20.
As above, the well bore 40 may be a single bore without laterals, or may include a well bore pattern with a plurality of lateral or other horizontal well bores. If desired, all or part of the well bore pattern can be lined. For example, liners may be provided in the lateral or other horizontal well bores and tied back to casing or liners in the well bore 40. Where the well bore 40 includes a well bore pattern, the cavity 312 can act as a junction for multiple lined bores. If two or more of the liners communicate with the cavity 312, production from the bores can centrally collected in the cavity 312 and withdrawn.
In certain embodiments, the cavity 312 can be provided with a apertured liner 320 positioned to communicate with the surface bore 310. The apertured liner 320 can be provided in the cavity 312 prior to gravel packing. Alternatively, the cavity 312 can be gravel packed and the apertured liner 320 provided with a conical or other suitable tip 322 and subsequently driven through the gravel 318 into position in the cavity 312.
In this embodiment, the inlet 324 of a pump, such as a sucker rod pump, electric submersible pump, or other type of pump, is installed in the surface bore 310 to withdraw fluids collected in the cavity 312 to the surface 20 through a pump string 326. The pump inlet 324 can be positioned within the surface bore 310 or within the apertured liner 320 in the cavity 312. Other artificial lift techniques or the natural flow from the formation can be used in combination with or as an alternative to a pump.
In operation of the illustrative embodiment, water, debris, and resources, such as gas from the coal seam 30, flow along the well bore 40. The water and debris collect and the cavity 312, and, if provided, also in the sump 314. The water is removed from the cavity 312 to the surface 20 by the inlet 324 of the pump, or by other artificial lift or natural flow from the formation. Gas may flow through the well bore 40 to the surface 20, through the surface bore 310 (in the annulus between the pump string 326 and the wall of the surface bore 310) to the surface 20, or through both.
Although the present disclosure has been described with several embodiments, various changes and modifications may be suggested to one skilled in the art. It is intended that the present invention encompasses such changes and modifications as fall within the scope of the appended claims.
This application is a continuation-in-part of, and therefore claims priority from, U.S. patent application Ser. No. 11/035,537 filed on Jan. 14, 2005, which is a continuation-in-part of, and therefore claims priority from, U.S. patent application Ser. No. 10/723,322, filed on Nov. 26, 2003. This application incorporates by reference the two applications noted above, as well as the application entitled Well Bore Cleaning filed May 31, 2005.
| Number | Date | Country | |
|---|---|---|---|
| Parent | 11035537 | Jan 2005 | US |
| Child | 11141459 | May 2005 | US |
| Parent | 10723322 | Nov 2003 | US |
| Child | 11035537 | Jan 2005 | US |
