CA2589798C - Methods of stimulating a subterranean formation comprising multiple production intervals - Google Patents
Methods of stimulating a subterranean formation comprising multiple production intervals Download PDFInfo
- Publication number
- CA2589798C CA2589798C CA002589798A CA2589798A CA2589798C CA 2589798 C CA2589798 C CA 2589798C CA 002589798 A CA002589798 A CA 002589798A CA 2589798 A CA2589798 A CA 2589798A CA 2589798 C CA2589798 C CA 2589798C
- Authority
- CA
- Canada
- Prior art keywords
- particulates
- fluid
- well bore
- casing
- jetting
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
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- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 claims description 5
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- 229910010293 ceramic material Inorganic materials 0.000 claims description 5
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- 239000000377 silicon dioxide Substances 0.000 claims description 5
- 239000002023 wood Substances 0.000 claims description 5
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims description 4
- 229920002732 Polyanhydride Polymers 0.000 claims description 4
- 125000005396 acrylic acid ester group Chemical group 0.000 claims description 4
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- 229920006237 degradable polymer Polymers 0.000 claims description 4
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- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 claims description 3
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- 239000007849 furan resin Substances 0.000 claims description 3
- 229920000647 polyepoxide Polymers 0.000 claims description 3
- QNIRRHUUOQAEPB-UHFFFAOYSA-N 2-(prop-2-enoylamino)butane-2-sulfonic acid Chemical class CCC(C)(S(O)(=O)=O)NC(=O)C=C QNIRRHUUOQAEPB-UHFFFAOYSA-N 0.000 claims description 2
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- XYOMMVNZIAGSMW-UHFFFAOYSA-N (prop-2-enoylamino)methyl propane-1-sulfonate Chemical compound CCCS(=O)(=O)OCNC(=O)C=C XYOMMVNZIAGSMW-UHFFFAOYSA-N 0.000 claims 1
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Classifications
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH DRILLING; MINING
- E21B—EARTH DRILLING, e.g. DEEP 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
- E21B43/11—Perforators; Permeators
- E21B43/114—Perforators using direct fluid action on the wall to be perforated, e.g. abrasive jets
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH DRILLING; MINING
- E21B—EARTH DRILLING, e.g. DEEP 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
- E21B43/25—Methods for stimulating production
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH DRILLING; MINING
- E21B—EARTH DRILLING, e.g. DEEP 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
- E21B43/25—Methods for stimulating production
- E21B43/26—Methods for stimulating production by forming crevices or fractures
Abstract
A method of stimulating a production interval adjacent a well bore having a casing disposed therein, that comprises introducing a carrier fluid comprising first particulates into the well bore, packing the first particulates into a plurality of perforations in the casing, perforating at least one remedial perforation in the casing adjacent to the production interval, and stimulating the production interval through the at least one remedial perforation. Also provided are methods of stimulating multiple production intervals adjacent a well bore.
Description
METHODS OF STIMULATING A SUBTERRANEAN FORMATION COMPRISING
MULTIPLE PRODUCTION INTERVALS
BACKGROUND
The present invention relates to subterranean stimulation operations and, more particularly, to methods of stimulating a subterranean formation comprising multiple production intervals.
To produce hydrocarbons (e.g., oil, gas, etc) from a subterranean formation, well bores may be drilled that penetrate the hydrocarbon-containing portions of the subterranean formation. The portion of the subterranean formation from which hydrocarbons may be produced is commonly referred to as a "production interval." In some instances, a subterranean formation penetrated by the well bore may have multiple production intervals at various depths in the well bore.
Generally, after a well bore has been drilled to a desired depth completion operations may be performed. Completion operations may involve the insertion of casing into a well bore, and thereafter the casing, if desired, may be cemented into place. So that hydrocarbons may be produced from the subterranean formation, one or more perforations may be created that penetrate through the casing, through the cement, and into the production interval. At some point in the completion operation, a stimulation operation may be performed to enhance hydrocarbon production from the well bore. Stimulation operations may involve hydraulic fracturing, acidizing, fracture acidizing, or other suitable stimulation operations. Once the stimulation operation has been completed and after any intermediate steps, the well bore may be placed into production. Generally, the produced hydrocarbons flow from the production intervals, through the perforations that connect the production intervals with the well bore, into the well bore, and to the surface.
Stimulation operations such as these may be problematic in subterranean formations comprising multiple production intervals. In particular, problems may result in stimulation operations where the well bore penetrates multiple perforated and depleted intervals due to the variation of fracture gradients between these intervals.
The most depleted intervals typically have the lowest fracture gradients among the multiple production intervals.
When a stimulation operation is simultaneously conducted on all of the production intervals, the treatment fluid may preferentially enter the most depleted intervals.
Therefore, the stimulation operation may not achieve desirable results in those production intervals having relatively higher fracture gradients. Packers and/or bridge plugs may be used to isolate the particular production interval before the stimulation operations, but this may be problematic due to the existence of open perforations in the well bore and the potential sticking of these mechanical isolation devices.
Another method conventionally used to combat problems encountered during the stimulation of a subterranean formation having multiple production intervals has been to perfonn a remedial cementing operation prior to the stimulation operation to plug the open perforations in the well bore, thereby hopefully preventing the undesired entry of the stimulation fluid into the most depleted intervals of the well bore. Once the pre-existing perforations are plugged with cement, a particular production interval may be perforated and then stimulated. While these remedial cementing operations may plug some of the pre-existing perforations and thus reduce the entry of the stimulation fluid into undesired portions of the formation, remedial cementing operations may not be completely effective in plugging all the pre-existing perforations in the well, requiring multiple remedial cementing operations to ensure complete plugging of all the pre-existing perforations. Further, remedial cementing operations may damage near well bore areas of the subterranean formation and/or require further remedial operations to remove undesired cement from the well bore before the well may be placed back into production.
SUMMARY
The present invention relates to subterranean stimulation operations and, more particularly, to methods of stimulating a. subterranean formation comprising multiple production intervals.
In one embodiment, the present invention provides a method of stimulating a production interval adjacent a well bore having a casing disposed therein, the method comprising: introducing a carrier fluid comprising first particulates into the well bore;
packing the first particulates into a plurality of perforations in the casing;
perforating at least one remedial perforation in the casing adjacent to the production interval, subsequent to the packing the first particulates; and stimulating the production interval through the at least one remedial perforation.
MULTIPLE PRODUCTION INTERVALS
BACKGROUND
The present invention relates to subterranean stimulation operations and, more particularly, to methods of stimulating a subterranean formation comprising multiple production intervals.
To produce hydrocarbons (e.g., oil, gas, etc) from a subterranean formation, well bores may be drilled that penetrate the hydrocarbon-containing portions of the subterranean formation. The portion of the subterranean formation from which hydrocarbons may be produced is commonly referred to as a "production interval." In some instances, a subterranean formation penetrated by the well bore may have multiple production intervals at various depths in the well bore.
Generally, after a well bore has been drilled to a desired depth completion operations may be performed. Completion operations may involve the insertion of casing into a well bore, and thereafter the casing, if desired, may be cemented into place. So that hydrocarbons may be produced from the subterranean formation, one or more perforations may be created that penetrate through the casing, through the cement, and into the production interval. At some point in the completion operation, a stimulation operation may be performed to enhance hydrocarbon production from the well bore. Stimulation operations may involve hydraulic fracturing, acidizing, fracture acidizing, or other suitable stimulation operations. Once the stimulation operation has been completed and after any intermediate steps, the well bore may be placed into production. Generally, the produced hydrocarbons flow from the production intervals, through the perforations that connect the production intervals with the well bore, into the well bore, and to the surface.
Stimulation operations such as these may be problematic in subterranean formations comprising multiple production intervals. In particular, problems may result in stimulation operations where the well bore penetrates multiple perforated and depleted intervals due to the variation of fracture gradients between these intervals.
The most depleted intervals typically have the lowest fracture gradients among the multiple production intervals.
When a stimulation operation is simultaneously conducted on all of the production intervals, the treatment fluid may preferentially enter the most depleted intervals.
Therefore, the stimulation operation may not achieve desirable results in those production intervals having relatively higher fracture gradients. Packers and/or bridge plugs may be used to isolate the particular production interval before the stimulation operations, but this may be problematic due to the existence of open perforations in the well bore and the potential sticking of these mechanical isolation devices.
Another method conventionally used to combat problems encountered during the stimulation of a subterranean formation having multiple production intervals has been to perfonn a remedial cementing operation prior to the stimulation operation to plug the open perforations in the well bore, thereby hopefully preventing the undesired entry of the stimulation fluid into the most depleted intervals of the well bore. Once the pre-existing perforations are plugged with cement, a particular production interval may be perforated and then stimulated. While these remedial cementing operations may plug some of the pre-existing perforations and thus reduce the entry of the stimulation fluid into undesired portions of the formation, remedial cementing operations may not be completely effective in plugging all the pre-existing perforations in the well, requiring multiple remedial cementing operations to ensure complete plugging of all the pre-existing perforations. Further, remedial cementing operations may damage near well bore areas of the subterranean formation and/or require further remedial operations to remove undesired cement from the well bore before the well may be placed back into production.
SUMMARY
The present invention relates to subterranean stimulation operations and, more particularly, to methods of stimulating a. subterranean formation comprising multiple production intervals.
In one embodiment, the present invention provides a method of stimulating a production interval adjacent a well bore having a casing disposed therein, the method comprising: introducing a carrier fluid comprising first particulates into the well bore;
packing the first particulates into a plurality of perforations in the casing;
perforating at least one remedial perforation in the casing adjacent to the production interval, subsequent to the packing the first particulates; and stimulating the production interval through the at least one remedial perforation.
In another embodiment, the present invention provides a method of stimulating a production interval adjacent a well bore having a casing disposed therein, the method comprising: introducing a carrier fluid comprising first particulates into the well bore;
packing the first particulates into a plurality of perforations in the casing;
providing a hydraulic jetting tool having at least one port, the hydrajetting tool attached to a work string;
positioning the hydraulic jetting tool in the well bore adjacent the production interval; jetting a jetting fluid through the at least one nozzle in the hydraulic jetting tool against the casing in the well bore so as to create at least one remedial perforation in the casing;
and stimulating the production interval through the at least one remedial perforation.
In yet another embodiment, the present invention provides a method of stimulating multiple production intervals adjacent a well bore having a casing disposed therein, the method comprising: introducing a carrier fluid comprising first particulates into the well bore; packing the first particulates into a plurality of perforations in the casing;
perforating at least one remedial perforation in the casing adjacent to a production interval, subsequent to the packing the first particulates; introducing a stimulation fluid into the well bore and into the at least one remedial perforation so as to contact the production interval;
and repeating the acts of perforating at least one remedial perforation and introducing the stimulation fluid for each of the remaining production intervals.
The features and advantages of the present invention will be readily apparent to those skilled in the art upon a reading of the description of the specific embodiments that follows.
DRAWINGS
A more complete understanding of the present disclosure and advantages thereof may be acquired by referring to the following description taken in conjunction with the accompanying drawings, wherein:
Figure 1 illustrates a cross-sectional side view of a vertical well bore that penetrates multiple production intervals in accordance with one embodiment of the present invention.
Figure 2 illustrates a cross-sectional side view of the well bore shown in Figure 1 having a conduit disposed therein in accordance with one embodiment of the present invention.
packing the first particulates into a plurality of perforations in the casing;
providing a hydraulic jetting tool having at least one port, the hydrajetting tool attached to a work string;
positioning the hydraulic jetting tool in the well bore adjacent the production interval; jetting a jetting fluid through the at least one nozzle in the hydraulic jetting tool against the casing in the well bore so as to create at least one remedial perforation in the casing;
and stimulating the production interval through the at least one remedial perforation.
In yet another embodiment, the present invention provides a method of stimulating multiple production intervals adjacent a well bore having a casing disposed therein, the method comprising: introducing a carrier fluid comprising first particulates into the well bore; packing the first particulates into a plurality of perforations in the casing;
perforating at least one remedial perforation in the casing adjacent to a production interval, subsequent to the packing the first particulates; introducing a stimulation fluid into the well bore and into the at least one remedial perforation so as to contact the production interval;
and repeating the acts of perforating at least one remedial perforation and introducing the stimulation fluid for each of the remaining production intervals.
The features and advantages of the present invention will be readily apparent to those skilled in the art upon a reading of the description of the specific embodiments that follows.
DRAWINGS
A more complete understanding of the present disclosure and advantages thereof may be acquired by referring to the following description taken in conjunction with the accompanying drawings, wherein:
Figure 1 illustrates a cross-sectional side view of a vertical well bore that penetrates multiple production intervals in accordance with one embodiment of the present invention.
Figure 2 illustrates a cross-sectional side view of the well bore shown in Figure 1 having a conduit disposed therein in accordance with one embodiment of the present invention.
Figure 3 illustrates a cross-sectional side view of a perforation after having a particulate pack placed therein in accordance with one embodiment of the present invention.
Figure 4 illustrates a cross-sectional side view of the well bore shown in Figures 1-2 having a hydraulic jetting tool disposed therein after creation of remedial perforations in the casing.
Figure 5 illustrates a cross-sectional side view of the well bore shown in Figures 1, 2, and 4 after creation of fractures in an interval of the subterranean formation.
Figure 6 illustrates a cross-sectional side view of the well bore shown in Figures 1, 2, 4, and 5 having a hydraulic jetting tool in position for perforating a second interval of the well bore.
While the present invention is susceptible to various modifications and alternative forms, specific exemplary embodiments thereof have been shown by way of example in the drawings and are herein described in detail. It should be understood, however, that the description herein of specific embodiments is not intended to limit or define the invention to the particular forms disclosed, but on the contrary, the intention is to cover all modifications, equivalents, and alternatives falling within the spirit and scope of the invention as defined by the appended claims.
DESCRIPTION
The present invention relates to subterranean stimulation operations and, more particularly, to methods of stimulating a subterranean formation comprising multiple production intervals. While the methods of the present invention are useful in a variety of applications, they may be particularly useful for stimulation operations in coal-bed-methane wells, high-permeability reservoirs suffering from near-well-bore compaction, or any well containing multiple perforated intervals that need stimulation. Among other things, the methods of the present invention allow for the closing of perforations in certain intervals of a well bore so that a desired interval or intervals of the subterranean formation may be stimulated.
Referring to Figure 1, a cross-sectional side view of a well bore in accordance with an embodiment of the present invention is shown. The well bore is generally indicated at 100. While well bore 100 is depicted as a generally vertical well bore, the methods of the present invention may be performed in generally horizontal, inclined, or otherwise formed portions of well bores. In addition, well bore 100 may include multilaterals, wherein well bore 100 may be a primary well bore having one or more branch well bores extending therefrom, or well bore 100 may be a branch well bore extending laterally from a primary well bore. Well bore 100 penetrates subterranean formation 102 and has casing 104 disposed therein. Casing 104 may or may not be cemented in well bore 100 by a cement sheath (not shown). While Figure 1 depicts well bore 100 as a cased well bore at least a portion of well bore 100 may be left openhole. Generally, subterranean formation 102 contains multiple production intervals, including lowermost or first production interval 106, second production interval 108, third production interval 110, and fourth production interval 112. The intervals of casing 104 adjacent to production intervals 106, 108, 110, 112 are perforated by plurality of perforations 114, wherein plurality of perforations 114 penetrate through casing 104, through the cement sheath (if present), and into production intervals 106, 108, 110, 112. The intervals of casing 104 adjacent to production intervals 106, 108, 110, 112 are first casing interval 107, second casing interval 109, third casing interval 111, and fourth casing interval 113, respectively.
Referring now to Figure 2, conduit 118 is shown disposed in well bore 100. Conduit 118 may be coiled tubing, jointed pipe, or any other suitable conduit for the delivery of fluids during subterranean operations. Annulus 120 is defined between casing 104 and conduit 118.
As shown in Figure 2, in accordance with one embodiment of the methods of the present invention, a carrier fluid may be introduced into well bore 100 by pumping the carrier fluid down conduit 118. In another embodiment, carrier fluid may be introduced into well bore 100 by pumping the carrier fluid down annulus 120. The carrier fluid should contain first particulates. The carrier fluid and the first particulates will be discussed further below.
The first particulates in the carrier fluid should be allowed to pack into plurality of perforations 114, thereby forming particulate packs 124 in each of the plurality of perforations 114. Any suitable method may be used to introduce the carrier fluid into well bore 100 so that particulate packs 124 are formed. Generally, the carrier fluid may be introduced into well bore 100 so that downhole pressures are sufficient for the carrier fluid to squeeze into production intervals 106, 108, 110, 112, but the downhole pressures are below the respective fracture gradients until plurality of perforations 114 are effectively packed with particulates. Surface pumping pressures may be monitored to determine when particulate packs 124 have formed in each of the plurality of perforations 114. For example, when the surface pumping pressures of the carrier fluid increase above a pressure necessary for the downhole pressures to exceed the fracture gradients of production intervals 106, 108, 110, 112 without fracturing of such intervals, particulate packs 124 should have formed in each of the plurality of perforations 114. In certain embodiments, back pressure should be held on annulus 120, among other things so that the carrier fluid enters plurality of perforations 114 and is squeezed into the matrix of subterranean formation 102, so that carrier fluid is spread across plurality of perforations 114, and so that carrier fluid maintains sufficient velocity for proppant suspension without exceeding fracturing pressures. In one embodiment, back pressure is applied on annulus 120 by limiting the return of the carrier fluid up through annulus 120 by utilizing a choke mechanism at the surface (not shown). As the carrier fluid enters plurality of perforations 114 and is squeezed into the matrix of subterranean formation 102, the first particulates in the carrier fluid should bridge in plurality of perforations 114 and thus pack into plurality of perforations 114 forming particulate packs 124 therein. One of ordinary skill in the art will recognize other suitable methods for squeezing the carrier fluid into the matrix of subterranean formation 102.
Referring now to Figure 3, a cross-sectional side view of particulate pack 124 in perforation 114 is shown, in accordance with one embodiment of the methods of the present invention. Perforation 114 penetrates through first casing interval 107 and into first production interval 106. As discussed above, first particulates are packed into perforation 114, thereby forming particulate pack 124.
In certain embodiments, once particulate packs 124 have been formed in plurality of perforations 114, particulate packs 124 may be contacted with a second carrier fluid that contains second particulates. Generally, the second particulates are of a smaller size than the first particulates so that the second particulates may plug at least a portion of the interstitial spaces between the first particulates in particulate packs 124.
In one certain embodiment, the second carrier fluid containing the second particulates may be introduced into well bore 100 as the pad fluid for a stimulation operation performed on first production interval 106. The second carrier fluid and second particulates will be discussed in more detail below. The second carrier fluid may be introduced into well bore 100 by any suitable manner, for example, by pumping the second carrier fluid down conduit 118.
Generally, the second carrier fluid may be introduced into well bore 100 so that downhole pressures are sufficient for the second carrier fluid to squeeze into particulate packs 124 and into production intervals 106, 108, 110, 112, but the downhole pressures are below production intervals' 106, 108, 110, 112 respective fracture gradients. In certain embodiments, back pressure should be held on annulus 120 so that the second carrier fluid is squeezed into particulate packs 124 and thus into the matrix of subterranean formation 102, plugging at least portion of the interstitial spaces between the first particulates in particulate packs 124, thereby forming a filter cake at the surface of particulate packs 124. When a filter cake has formed at the surface of particulate packs 124, the leak off rate of the second carrier fluid into the matrix of subterranean formation 102 through particulate packs 124 should be reduced, as indicated by the rate of pressure fall off during shut-in immediately after pumping the second carrier fluid.
Referring now to Figure 4, once particulate packs 124 are formed by the introduction of the carrier fluid into well bore 100 and, if desired, second carrier fluid is introduced into well bore 100, the methods of the present invention may further comprise perforating at least one remedial perforation 132 in casing 104 adjacent to a production interval (e.g., production interval 106). These perforations are referred to as "remedial"
because they are created after an initial completion process has been performed in the well.
Further, the at least one remedial perforation 132 may be created in one or more previously perforated intervals of casing 104 (e.g., casing intervals 107, 109, 111,.
113) and/or one or more previously unperforated intervals of casing 104. The at least one remedial perforation 132 may penetrate through casing 104 and into a portion of subterranean formation 102 adjacent thereto. For example, the at least one remedial perforation 132 may penetrate through first casing interval 107 and into first production interval 106.
As illustrated in Figure 4, hydraulic jetting tool 126 is shown disposed in well bore 100. Hydraulic jetting tool 126 contains at least one port 127. Hydraulic jetting tool 126 may be any suitable assembly for use in subterranean operations through which a fluid may be jetted at high pressures, including those described in U.S. Patent Number 5,765,642. In one embodiment, hydraulic jetting tool 126 is attached to work string 128, in the form of piping or coiled tubing, which lowers hydraulic jetting tool 126 into well bore 100 and supplies it with jetting fluid. Optional valve subassembly 129 may be attached to the end of hydraulic jetting tool 126 to cause the flow of the fluid (referred to herein as "jetting fluid") to discharge through at least one port 127 in hydraulic jetting tool 126. Annulus 130 is defined between casing 104 and work string 128. In one embodiment, hydraulic jetting tool 126 is positioned in well bore 100 adjacent to casing 104 in a location (such as first casing interval 107) that is adjacent to a production interval (such as first production interval 106).
Hydraulic jetting tool 126 then operates to form at least one remedial perforation 132 by jetting the jetting fluid through at least one port 127 and against first casing interval 107. At least one remedial perforation 132 may penetrate through the first casing interval 107 and into first production interval 106 adjacent thereto. The jetting fluid may contain a base fluid (e.g., water) and abrasives (e.g., sand). In one embodiment, sand is present in the jetting fluid in an amount of about 1 pound per gallon of the base fluid. While the above description describes the use of hydraulic jetting tool 126 to create at least one remedial perforation 132 in first casing interval 107, any suitable method may be used create at least one remedial perforation 132 in first casing interval 107. Suitable methods include all perforating methods known to those of ordinary skill in the art, but are not limited to, bullet perforating, jet perforating, and hydraulic jetting.
In accordance with the methods of the present invention, once at least one remedial perforation 132 has been created in casing 104 at the desired location (e.g., first casing interval 107 adjacent to first production interval 106), the subterranean formation 102 (e.g., first production interval 106) may be stimulated through the at least one remedial perforation 132. Referring now to Figure 5, the stimulation of first production interval may be commenced using hydraulic jetting tool 126 shown disposed in well bore 100, in accordance with one embodiment of the present invention. In these embodiments, once at least one remedial perforation 132 has been created in first casing interval 107 using hydraulic jetting tool 126, the stimulation fluid may be pumped into well bore 100, down annulus 130, and into at least one remedial perforation 132 at a pressure sufficient to create or enhance at least one fracture 134 in subterranean formation 100, e.g., first production interval 106, along at least one remedial perforation 132. While Figure 5 depicts at least one fracture 134 as a longitudinal fracture that is approximately longitudinal or parallel to the axis of well bore 100, those of ordinary skill in the art will recognize that the direction and orientation of the at least one fracture 134 is dependent on a number of factors, including rock mechanical stress, reservoir pressure, and perforation orientation. In certain embodiments, a jetting fluid may be pumped down through work string 128 and jetted through at least one port 127, through the at least one remedial perforation 132, and against first production interval 106, wherein hydraulic jetting tool 126 is positioned adjacent to at least one remedial perforation 132. In certain embodiments, the step of jetting the jetting fluid against first production interval 106 may occur simultaneously with the pumping of the stimulation fluid into well bore 100, down annulus 130, and into at least one remedial perforation 132, so as to create or enhance at least one fracture 134 in first production interval 106 along at least one remedial perforation 132. Proppant may be included in the stimulation fluid and/or the jetting fluid as desired so as to support at least one fracture 134 and prevent it from fully closing after hydraulic pressure is released. Suitable methods of fracturing a subterranean formation utilizing a hydraulic jetting tool are described in U.S. Patent Number 5,765,642.
While the above description describes the use of hydraulic jetting tool 126 to create or enhance at least one fracture 134, any suitable method of stimulation may be used to stimulate the desired interval of subterranean formation 102, including, but are not limited to, hydraulic fracturing and fracture acidizing operations. In some embodiments, the stimulation of first production interval 106 comprises introducing a stimulation fluid into well bore 100 and into at least one remedial perforation 132 so as to contact first production interval 106. In another embodiment, stimulation fluid is introduced into well bore 100 so as to contact first production interval 106 at a pressure sufficient to create at least one fracture in first production interval 106.
In accordance with one embodiment of the present invention, once the desired interval of subterranean formation 102, such as first production interval 106, has been stimulated, sufficient sand may be introduced into well bore 100 via the stimulation fluid (e.g., annulus fluid, jetting fluid, or both) to form sand plug 136 in casing 104, as depicted in Figure 6. Once the hydraulic pressure is released, the sand should settle to form sand plug 136 adjacent to first casing interval 107 extending above at least one remedial perforation 132. In some embodiments, sand plug 136 may be adjacent to first casing interval 107 extending from an optional mechanical plug to above at least one remedial perforation 132. Sand plug 136 acts to isolate the stimulated section of subterranean formation 102, e.g., first production interval 106. One of ordinary skill in the art will recognize other suitable methods of isolating the stimulated section of subterranean formation 102 that may be suitable for use with the methods of the present invention.
Having perforated and stimulated a desired interval (such as first casing interval 107 and first production interval 106), in the manner described above, an operator may elect to repeat the above acts of perforating and stimulating for each of the remaining production intervals (such as production intervals 108, 110, 112). Referring now to Figure 6, for example, the operator may next elect to perforate at least one remedial perforation 138 in casing 104 adjacent to second production interval 108 and then stimulate second production interval through the at least one remedial perforation 138. In some embodiments, at least one remedial perforation 138 may be created in second casing interval 109 and a stimulation fluid may be introduced into well bore 100 and into the at least one remedial perforation 138 created therein so as to contact the second production interval 108 of subterranean formation 106. In some embodiments, as illustrated in Figure 6, hydraulic jetting tool 126 may be positioned adjacent to second casing interval 109 and used to create at least one remedial perforation 138 in second casing interval 109. Thereafter, in the manner described above, at least one fracture 140 may be created or enhanced along at least one remedial perforation 138. In certain embodiments of the present invention wherein an operator uses the methods of the present invention to stimulate multiple production intervals of subterranean formation 102 (such as production intervals 106, 108, 110, 112), the operator may elect to sequentially stimulate the production intervals intersected by well bore 100, beginning with the deepest production interval (e.g., first production interval 106), and sequentially stimulating the shallower desired intervals, such as production intervals 108, 110, 112.
In certain embodiments, clean-out fluids optionally may be introduced into well bore 100. Generally, clean-out fluids, where used, may be introduced into well bore 100 at any suitable time as desired by one of ordinary skill in the art, for example, to e.g., to clean out debris, cuttings, pipe dope, and other materials from well bore 100 and inside equipment, such as conduit 118 or hydraulic jetting tool 126 that may be disposed in well bore 100. For example, a clean out fluid may be used after completion of the stimulation operations so as to remove the sand plugs, such as sand plug 136 that may be in well bore 100. In some embodiments, the clean out fluid may be used after the carrier fluid has been introduced into well bore 100 so as to remove any of the first particulates that are loose in well bore 100.
Generally, the clean-out fluids should not be circulated into well bore 100 at sufficient rates and pressures to impact the integrity of particulate packs 124. Generally, the cleaning fluid may be any conventional fluid used to prepare a formation for stimulation, such as water-based or oil-based fluids. In some embodiments, these cleaning fluids may be energized fluids that contain a gas, such as nitrogen or air.
While the above-described steps describe the use of conduit 118 to introduce the carrier fluid and the second carrier fluid into well bore 100, any suitable methodology may be used to introduce such fluids into well bore 100. In some embodiments, work string 128 with hydraulic jetting tool 126 attached thereto and optional valve subassembly 129 attached to the end of hydraulic jetting tool 126 may be used in the above-described step of introducing the carrier fluid containing first particulates into well bore 100.
This may save at least one trip out of the well bore, between the steps of packing the first particulates into plurality of perforations 114 and perforating at least one remedial perforation 132 because the same downhole equipment may be used for both steps. For example, hydraulic jetting tool 126 may have a longitudinal fluid flow passageway extending therethrough and optional valve subassembly 129 may have a longitudinal fluid flow passageway extending therethough. When optional valve subassembly 129 is not activated, fluid flows down through work string 128, into hydraulic jetting tool 126, and out through optional valve subassembly 129. Accordingly, in some embodiments, the carrier fluid may be introduced into well bore 100 by pumping the carrier fluid down work string 128, into hydraulic jetting tool 126, and out into well bore 100 through optional valve subassembly 129. Similarly, second carrier fluid also may be introduced into well bore 100. When desired to perform the above-described remedial perforation and/or stimulation steps, optional valve subassembly 129 should be activated thereby causing the flow of fluid to discharge through at least one port 127.
The carrier fluid that may be used in accordance with the present invention, may include any suitable fluids that may be used to transport particulates in subterranean operations. Suitable fluids include ungelled aqueous fluids, aqueous gels, hydrocarbon-based gels, foams, emulsions, viscoelastic surfactant gels, and any other suitable fluid. Where the carrier fluid is an ungelled aqueous fluid, it should be introduced into the well bore at a sufficient rate to transport the first particulates. Suitable emulsions can be comprised of two immiscible liquids such as an aqueous liquid or gelled liquid and a hydrocarbon. Foams can be created by the addition of a gas, such as carbon dioxide or nitrogen. Suitable aqueous gels are generally comprised of water and one or more gelling agents. In exemplary embodiments, the carrier fluid is an aqueous gel comprised of water, a gelling agent for gelling the aqueous component and increasing its viscosity, and, optionally, a crosslinking agent for crosslinking the gel and further increasing the viscosity of the fluid.
The increased viscosity of the gelled, or gelled and crosslinked, aqueous gels, inter alia, reduces fluid loss and enhances the suspension properties thereof. An example of a suitable crosslinked aqueous gel is a borate fluid system utilized in the "Delta Frac "
fracturing service, commercially available from Halliburton Energy Services, Duncan Okalahoma.
Another example of a suitable crosslinked aqueous gel is a borate fluid system utilized in the "Seaquest " fracturing service, commercially available from Halliburton Energy Services, Duncan, Oklahoma. The water used to form the aqueous gel may be fresh water, saltwater, brine, or any other aqueous liquid that does not adversely react with the other components.
The density of the water can be increased to provide additional particle transport and suspension in the present invention.
As mentioned above, the carrier fluid contains first particulates. First particulates used in accordance with the present invention are generally particulate materials of a size such that the first particulates bridge plurality of perforations 114 in casing 104 and form proppant packs 124 therein. The first particulates used may have an average particle size in the range of from about 10 mesh to about 100 mesh. A wide variety of particulate materials may be used as the first particulates in accordance with the present invention including sand; bauxite; ceramic materials; glass materials; polymer materials; Teflon materials; nut shell pieces; seed shell pieces; cured resinous particulates comprising nut shell pieces; cured resinous particulates comprising seed shell pieces; fruit pit pieces; cured resinous particulates comprising fruit pit pieces; wood; composite particulates; and combinations thereof. Suitable composite particulates may comprise a binder and a filler material wherein suitable filler materials include silica, alumina, fumed carbon, carbon black, graphite, mica, titanium dioxide, meta-silicate, calcium silicate, kaolin, talc, zirconia, boron, fly ash, hollow glass microspheres, solid glass, and combinations thereof.
Generally, the first particulates may be present in the carrier fluid in an amount in an amount sufficient to form the desired proppant packs 124 in plurality of perforations 114. In some embodiments, the first particulates, may be present in the carrier fluid in an amount in the range of from about 2 pounds to about 12 pounds per gallon of the carrier fluid not inclusive of the first particulates.
Generally, the first particulates do not degrade in the presence of hydrocarbon fluids and other fluids present in portion of the subterranean formation; this allows the first particulates to maintain their integrity in the presence of produced hydrocarbon products, formation water, and other compositions normally produced from subterranean formations. However, in some embodiments of the present invention, the first particulates may comprise degradable materials. Degradable materials may be included in the first particulates, for example, so that proppant packs 124 may degrade over time. Such degradable materials are capable of undergoing an irreversible degradation downhole. The term "irreversible" as used herein means that the degradable material, once degraded downhole, should not recrystallize or reconsolidate, e.g., the degradable material should degrade in situ but should not recrystallize or reconsolidate in situ.
The degradable materials may degrade by any suitable mechanism.
Suitable degradable materials may be water-soluble, gas-soluble, oil-soluble, biodegradable, temperature degradable, solvent-degradable, acid-soluble, oxidizer-degradable, or a combination thereof. Suitable degradable materials include a variety of degradable materials suitable for use in subterranean operations and may comprise dehydrated materials, waxes, boric acid flakes, degradable polymers, calcium carbonate, paraffins, crosslinked polymer gels, combinations thereof, and the like. One example of a suitable degradable crosslinked polymer gel is "Max SealTM" fluid loss control additive, commercially available from Halliburton Energy Services, Duncan, Oklahoma. An example of a suitable degradable polymeric material is "BioBallsTM" perforation ball sealers, commercially available from Santrol Corporation, Fresno, Texas.
In some embodiments, the degradable material comprises an oil-soluble material. Where such oil-soluble materials are used, the oil-soluble materials may be degraded by the produced fluids, thus degrading particulate packs 124 so as to unblock plurality of perforations 114. Suitable oil-soluble materials include either natural or synthetic polymers, such as, for example, polyacrylics, polyamides, and polyolefins (such as polyethylene, polypropylene, polyisobutylene, and polystyrene).
Suitable examples of degradable polymers that may be used in accordance with the present invention include, but are not limited to, homopolymers, random, block, graft, and star- and hyper-branched polymers. Specific examples of suitable polymers include polysaccharides (such as dextran or cellulose); chitin; chitosan;
proteins; aliphatic polyesters; poly(lactide); poly(glycolide); poly(s-caprolactone);
poly(hydroxybutyrate);
poly(anhydrides); aliphatic polycarbonates; poly(ortho esters); poly(amino acids);
poly(ethylene oxide); polyphosphazenes; copolymers thereof, and combinations thereof.
Polyanhydrides are another type of particularly suitable degradable polymer useful in the present invention. Examples of suitable polyanhydrides include poly(adipic anhydride), poly(suberic anhydride), poly(sebacic anhydride), poly(dodecanedioic anhydride). Other suitable examples include but are not limited to poly(maleic anhydride) and poly(benzoic anhydride). One skilled in the art will recognize that plasticizers may be included in forming suitable polymeric degradable materials of the present invention. The plasticizers may be present in an amount sufficient to provide the desired characteristics, for example, more effective compatibilization of the melt blend components, improved processing characteristics during the blending and processing steps, and control and regulation of the sensitivity and degradation of the polymer by moisture.
Suitable dehydrated compounds are those materials that will degrade over time when rehydrated. For example, a particulate solid dehydrated salt or a particulate solid anhydrous borate material that degrades over time may be suitable. Specific examples of particulate solid anhydrous borate materials that may be used include but are not limited to anhydrous sodium tetraborate (also known as anhydrous borax), and anhydrous boric acid.
These anhydrous borate materials are only slightly soluble in water. However, with time and heat in a subterranean environment, the anhydrous borate materials react with the surrounding aqueous fluid and are hydrated. The resulting hydrated borate materials are substantially soluble in water as compared to anhydrous borate materials and as a result degrade in the aqueous fluid.
Blends of certain degradable materials and other compounds may also be suitable. One example of a suitable blend of materials is a mixture of poly(lactic acid) and sodium borate where the mixing of an acid and base could result in a neutral solution where this is desirable. Another example would include a blend of poly(lactic acid) and boric oxide.
In choosing the appropriate degradable material or materials, one should consider the degradation products that will result. The degradation products should not adversely affect subterranean operations or components. The choice of degradable material also can depend, at least in part, on the conditions of the well, e.g., well bore temperature.
For instance, lactides have been found to be suitable for lower temperature wells, including those within the range of 60 F to 150 F, and polylactides have been found to be suitable for well bore temperatures above this range. Poly(lactic acid) and dehydrated salts may be suitable for higher temperature wells. Also, in some embodiments a preferable result is achieved if the degradable material degrades slowly over time as opposed to instantaneously.
In some embodiments, it may be desirable when the degradable material does not substantially degrade until after the degradable material has been substantially placed in a desired location within a subterranean formation.
In certain embodiments of the present invention, the first particulates are coated with an adhesive substance. As used herein, the ten=n "adhesive substance" refers to a material that is capable of being coated onto a particulate and that exhibits a sticky or tacky character such that the proppant particulates that have adhesive thereon have a tendency to create clusters or aggregates. As used herein, the term "tacky," in all of its forms, generally refers to a substance having a nature such that it is (or may be activated to become) somewhat sticky to the touch. Generally, the first particulates may be coated with an adhesive substance so that the first particulates once placed within plurality of perforations 114 to form particulate packs 124 may consolidate into the first particulates into a hardened mass.
Adhesive substances suitable for use in the present invention include non-aqueous tackifying agents; aqueous tackifying agents; silyl-modified polyamides; and curable resin compositions that are capable of curing to form hardened substances.
Tackifying agents suitable for use in the consolidation fluids of the present invention comprise any compound that, when in liquid form or in a solvent solution, will form a non-hardening coating upon a particulate. A particularly preferred group of tackifying agents comprise polyamides that are liquids or in solution at the temperature of the subterranean formation such that they are, by themselves, non-hardening when introduced into the subterranean formation. A particularly preferred product is a condensation reaction product comprised of commercially available polyacids and a polyamine. Such commercial products include compounds such as mixtures of C36 dibasic acids containing some trimer and higher oligomers and also small amounts of monomer acids that are reacted with polyamines. Other polyacids include trimer acids, synthetic acids produced from fatty acids, maleic anhydride, acrylic acid, and the like. Such acid compounds are commercially available from companies such as Witco Corporation, Union Camp, Chemtall, and Emery Industries. The reaction products are available from, for example, Champion Technologies, Inc. and Witco Corporation. Additional compounds which may be used as tackifying compounds include liquids and solutions of, for example, polyesters, polycarbonates and polycarbamates, natural resins such as shellac and the like. Other suitable tackifying agents are described in U. S. Patent Numbers 5,853,048 and 5,833,000.
Tackifying agents suitable for use in the present invention may be either used such that they form a non-hardening coating or they may be combined with a multifunctional material capable of reacting with the tackifying compound to form a hardened coating. A
"hardened coating" as used herein means that the reaction of the tackifying compound with the multifunctional material will result in a substantially non-flowable reaction product that exhibits a higher compressive strength in a consolidated agglomerate than the tackifying compound alone with the particulates. In this instance, the tackifying agent may function similarly to a hardenable resin. Multifunctional materials suitable for use in the present invention include, but are not limited to, aldehydes such as formaldehyde, dialdehydes such as glutaraldehyde, hemiacetals or aldehyde releasing compounds, diacid halides, dihalides such as dichlorides and dibromides, polyacid anhydrides such as citric acid, epoxides, furfuraldehyde, glutaraldehyde or aldehyde condensates and the like, and combinations thereof. In some embodiments of the present invention, the multifunctional material may be mixed with the tackifying compound in an amount of from about 0.01 to about 50 percent by weight of the tackifying compound to effect formation of the reaction product.
In some preferable embodiments, the compound is present in an amount of from about 0.5 to about I
percent by weight of the tackifying compound. Suitable multifunctional materials are described in U.S. Patent Number 5,839,510. Other suitable tackifying agents are described in U.S. Patent Number 5,853,048.
Solvents suitable for use with the tackifying agents of the present invention include any solvent that is compatible with the tackifying agent and achieves the desired viscosity effect. The solvents that can be used in the present invention preferably include those having high flash points (most preferably above about 125 F). Examples of solvents suitable for use in the present invention include, but are not limited to, butylglycidyl ether, dipropylene glycol methyl ether, butyl bottom alcohol, dipropylene glycol dimethyl ether, diethyleneglycol methyl ether, ethyleneglycol butyl ether, methanol, butyl alcohol, isopropyl alcohol, diethyleneglycol butyl ether, propylene carbonate, d'limonene, 2-butoxy ethanol, butyl acetate, furfuryl acetate, butyl lactate, dimethyl sulfoxide, dimethyl formamide, fatty acid methyl esters, and combinations thereof. It is within the ability of one skilled in the art, with the benefit of this disclosure, to determine whether a solvent is needed to achieve a viscosity suitable to the subterranean conditions and, if so, how much.
Suitable aqueous tackifier agents are capable of forming at least a partial coating upon the surface of the first particulates. Generally, suitable aqueous tackifier agents are not significantly tacky when placed onto a particulate, but are capable of being "activated"
(that is destabilized, coalesced and/or reacted) to transform the compound into a sticky, tackifying compound at a desirable time. Such activation may occur before, during, or after the aqueous tackifier compound is placed in the subterranean formation. In some embodiments, a pretreatment may be frrst contacted with the surface of a particulate to prepare it to be coated with an aqueous tackifier compound. Suitable aqueous tackifying agents are generally charged polymers that comprise compounds that, when in an aqueous solvent or solution, will form a non-hardening coating (by itself or with an activator) and, when placed on a particulate, will increase the continuous critical resuspension velocity of the particulate when contacted by a stream of water.
Examples of aqueous tackifier agents suitable for use in the present invention include, but are not limited to, acrylic acid polymers, acrylic acid ester polymers, acrylic acid derivative polymers, acrylic acid homopolymers, acrylic acid ester homopolymers (such as poly(methyl acrylate); poly (butyl acrylate), and poly(2-ethylhexyl acrylate)), acrylic acid ester co-polymers, methacrylic acid derivative polymers, methacrylic acid homopolymers, methacrylic acid ester homopolymers (such as poly(methyl methacrylate), poly(butyl methacrylate), and poly(2- ethylhexyl methacryate)), aciylamido-methyl-propane sulfonate polymers, acrylamido-methyl-propane sulfonate derivative polymers, acrylamido-methyl-propane sulfonate co-polymers, and acrylic acid/acrylamido-methyl-propane sulfonate co-polymers and combinations thereof. Methods of determining suitable aqueous tackifier agents and additional disclosure on aqueous tackifier agents can be found in U.S.
Patent Application Number 10/864,061 and filed June 9, 2004 and U.S. Patent Application Number 10/864,618 and filed June 9, 2004.
Silyl-modified polyamide compounds suitable for use as an adhesive substance in the methods of the present invention may be described as substantially self-hardening compositions that are capable of at least partially adhering to particulates in the unhardened state, and that are further capable of self-hardening themselves to a substantially non-tacky state to which individual particulates such as formation fines will not adhere. Such silyl-modified polyamides may be based, for example, on the reaction product of a silating compound with a polyamide or a mixture of polyamides. The polyamide or mixture of polyamides may be one or more polyamide intermediate compounds obtained, for example, f'rom the reaction of a polyacid (e.g., diacid or higher) with a polyamine (e.g., diamine or higher) to form a polyamide polymer with the elimination of water. Other suitable silyl-modified polyamides and methods of making such compounds are described in U.S.
Patent Number 6,439,309.
Curable resin compositions suitable for use in the consolidation fluids of the present invention generally comprise any suitable resin that is capable of forming a hardened, consolidated mass. Many such resins are commonly used in subterranean consolidation operations, and some suitable resins include two component epoxy based resins, novolak resins, polyepoxide resins, phenol-aldehyde resins, urea-aldehyde resins, urethane resins, phenolic resins, furan resins, furan/furfuryl alcohol resins, phenolic/latex resins, phenol formaldehyde resins, polyester resins and hybrids and copolymers thereof, polyurethane resins and hybrids and copolymers thereof, acrylate resins, and mixtures thereof.
Some suitable resins, such as epoxy resins, may be cured with an internal catalyst or activator so that when pumped down hole, they may be cured using only time and temperature. Other suitable resins, such as furan resins generally require a time-delayed catalyst or an external catalyst to help activate the polymerization of the resins if the cure temperature is low (i.e., less than 250 F), but will cure under the effect of time and temperature if the formation temperature is above about 250 F, preferably above about 3 00 F. It is within the ability of one skilled in the art, with the bencfit of this disclosure, to select a suitable resin for use in embodiments of the present invention and to determine whether a catalyst is required to trigger curing.
Further, the curable resin composition further may contain a solvent. Any solvent that is compatible with the resin and achieves the desired viscosity effect is suitable for use in the present invention. Preferred solvents include those listed above in connection with tackifying compounds. It is within the ability of one skilled in the art, with the benefit of this disclosure, to determine whether and how much solvent is needed to achieve a suitable viscosity.
The second carrier fluid that may be used in accordance with the present invention, may include any suitable fluids that may be used to transport particulates in subterranean operations. Suitable fluids include ungelled aqueous fluids, aqueous gels, hydrocarbon-based gels, foams, emulsions, viscoelastic surfactant gels, and any other suitable fluid. Where the second carrier fluid is an ungelled aqueous fluid, it should be introduced into the well bore at a sufficient rate to transport the first particulates.
Suitable emulsions can be comprised of two immiscible liquids such as an aqueous liquid or gelled liquid and a hydrocarbon. Foams can be created by the addition of a gas, such as carbon dioxide or nitrogen. Suitable aqueous gels are generally comprised of water and one or more gelling agents. In exemplary embodiments, the second carrier fluid is an aqueous gel comprised of water, a gelling agent for gelling the aqueous component and increasing its viscosity, and, optionally, a crosslinking agent for crosslinking the gel and further increasing the viscosity of the fluid. The increased viscosity of the gelled, or gelled and crosslinked, aqueous gels, inter alia, reduces fluid loss and enhances the suspension properties thereof. An example of a suitable crosslinked aqueous gel is a borate fluid system utilized in the "Delta Frac "
fracturing service, commercially available from Halliburton Energy Services, Duncan Okalahoma. Another example of a suitable crosslinked aqueous gel is a borate fluid system utilized in the "Seaquest " fracturing service, commercially available from Halliburton Energy Services, Duncan, Oklahoma. The water used to form the aqueous gel may be fresh water, saltwater, brine, or any other aqueous liquid that does not adversely react with the other components. The density of the water can be increased to provide additional particle transport and suspension in the present invention.
As mentioned above, the second carrier fluid contains second particulates.
The second particulates used in accordance with the present invention are generally particulate materials having an average particle size small than the average particle size of the first particulates so that the second particulates may plug at least a portion of the interstitial spaces between the first particulates in particulate packs 124. In certain embodiments, the second particulates used may have an average particle size of less than about 100 mesh.
Examples of suitable particulate materials that may be used as the second particulates include, but are not limited to, silica flour, sand; bauxite; ceramic materials; glass materials;
polymer materials; Teflon materials; nut shell pieces; seed shell pieces;
cured resinous particulates comprising nut shell pieces; cured resinous particulates comprising seed shell pieces; fruit pit pieces; cured resinous particulates comprising fruit pit pieces; wood;
composite particulates; and combinations thereof. Suitable composite particulates may comprise a binder and a filler material wherein suitable filler materials include silica, alumina, fumed carbon, carbon black, graphite, mica, titanium dioxide, meta-silicate, calcium silicate, kaolin, talc, zirconia, boron, fly ash, hollow glass microspheres, solid glass, and combinations thereof. Generally, the second particulates should be included in the second carrier fluid in an amount sufficient to form the desired filter cake on the surface of proppant packs 124. In certain embodiments, the second particulates may be present in the second carrier fluid in an amount in the range of from about 30 pounds to about 100 pounds per 1,000 gallons of the second carrier fluid not inclusive of the second particulates. In certain embodiments, the second particulates may comprise degradable particulates of the type described above.
The stimulation and jetting fluids that may be used in accordance with the present invention, may include any suitable fluids that may be used in subterranean stimulation operations. In some embodiments, the stimulation fluid may have substantially the same composition as the jetting fluid. Suitable fluids include ungelled aqueous fluids, aqueous gels, hydrocarbon-based gels, foams, emulsions, viscoelastic surfactant gels, acidizing treatment fluids (e.g., acid blends) and any other suitable fluid.
In some embodiments, the stimulation fluid and/or jetting fluid may contain an acid.
Where the stimulation or jetting fluid is an ungelled aqueous fluid, it should be introduced into the well bore at a sufficient rate to transport proppant (where present). Suitable emulsions can be comprised of two immiscible liquids such as an aqueous gelled liquid and a liquefied, normally gaseous, fluid, such as carbon dioxide or nitrogen. Foams can be created by the addition of a gas, such as carbon dioxide or nitrogen. Suitable aqueous gels are generally comprised of water and one or more gelling agents. In exemplary embodiments, the jetting fluid and/or stimulation fluid is an aqueous gel comprised of water, a gelling agent for gelling the aqueous component and increasing its viscosity, and, optionally, a crosslinking agent for crosslinking the gel and further increasing the viscosity of the fluid. The increased viscosity of the gelled, or gelled and crosslinked, aqueous gels, inter alia, reduces fluid loss and enhances the suspension properties thereof. The water used to form the aqueous gel may be fresh water, saltwater, brine, or any other aqueous liquid that does not adversely react with the other components: The density of the water can be increased to provide additional particle transport and suspension in the present invention. One of ordinary skill in the art, with the benefit of this disclosure, will be able to determine the appropriate stimulation and/or jetting fluid for a particulate application.
Optionally, proppant may be included in the stimulation fluid, the jetting fluid, or both. Among other things, proppant may be included to prevent fractures formed in the subterranean formation from fully closing once the hydraulic pressure is released. A
variety of suitable proppant may be used, for example, sand; bauxite; ceramic materials; glass materials; polymer materials; Teflon materials; nut shell pieces; seed shell pieces; cured resinous particulates comprising nut shell pieces; cured resinous particulates comprising seed shell pieces; fruit pit pieces; cured resinous particulates comprising fruit pit pieces; wood;
composite particulates; and combinations thereof. Suitable composite particulates may comprise a binder and a filler material wherein suitable filler materials include silica, alumina, fumed carbon, carbon black, graphite, mica, titanium dioxide, meta-silicate, calcium silicate, kaolin, talc, zirconia, boron, fly ash, hollow glass microspheres, solid glass, and combinations thereof. One of ordinary skill in the art, with the benefit of this disclosure, should know the appropriate amount and type of proppant to include in the jetting fluid and/or stimulation fluid for a particular application.
In one embodiment, the present invention provides a method of stimulating a production interval adjacent a well bore having a casing disposed therein, the method comprising: introducing a carrier fluid comprising first particulates into the well bore;
packing the first particulates into a plurality of perforations in the casing;
perforating at least one remedial perforation in the casing adjacent to the production interval, subsequent to the packing the first particulates; and stimulating the production interval through the at least one remedial perforation.
In another embodiment, the present invention provides a method of stimulating a production interval adjacent a well bore having a casing disposed therein, the method comprising: introducing a carrier fluid comprising first particulates into the well bore;
packing the first particulates into a plurality of perforations in the casing;
providing a hydraulic jetting tool having at least one port, the hydrajetting tool attached to a work string;
positioning the hydraulic jetting tool in the well bore adjacent the production interval; jetting a jetting fluid through the at least one nozzle in the hydraulic jetting tool against the casing in the well bore so as to create at least one remedial perforation in the casing;
and stimulating the production interval through the at least one remedial perforation.
In yet another embodiment, the present invention provides a method of stimulating multiple production intervals adjacent a well bore having a casing disposed therein, the method comprising: introducing a carrier fluid comprising first particulates into the well bore; packing the first particulates into a plurality of perforations in the casing;
perforating at least one remedial perforation in the casing adjacent to a production interval, subsequent to the packing the first particulates; introducing a stimulation fluid into the well bore and into the at least one remedial perforation so as to contact the production interval;
and repeating the acts of perforating at least one remedial perforation and introducing the stimulation fluid for each of the remaining production intervals.
Therefore, the present invention is well adapted to carry out the objects and attain the ends and advantages mentioned as well as those which are inherent therein.
While numerous changes may be made by those skilled in the art, such changes are encompassed within the spirit of this invention as defined by the appended claims.
Figure 4 illustrates a cross-sectional side view of the well bore shown in Figures 1-2 having a hydraulic jetting tool disposed therein after creation of remedial perforations in the casing.
Figure 5 illustrates a cross-sectional side view of the well bore shown in Figures 1, 2, and 4 after creation of fractures in an interval of the subterranean formation.
Figure 6 illustrates a cross-sectional side view of the well bore shown in Figures 1, 2, 4, and 5 having a hydraulic jetting tool in position for perforating a second interval of the well bore.
While the present invention is susceptible to various modifications and alternative forms, specific exemplary embodiments thereof have been shown by way of example in the drawings and are herein described in detail. It should be understood, however, that the description herein of specific embodiments is not intended to limit or define the invention to the particular forms disclosed, but on the contrary, the intention is to cover all modifications, equivalents, and alternatives falling within the spirit and scope of the invention as defined by the appended claims.
DESCRIPTION
The present invention relates to subterranean stimulation operations and, more particularly, to methods of stimulating a subterranean formation comprising multiple production intervals. While the methods of the present invention are useful in a variety of applications, they may be particularly useful for stimulation operations in coal-bed-methane wells, high-permeability reservoirs suffering from near-well-bore compaction, or any well containing multiple perforated intervals that need stimulation. Among other things, the methods of the present invention allow for the closing of perforations in certain intervals of a well bore so that a desired interval or intervals of the subterranean formation may be stimulated.
Referring to Figure 1, a cross-sectional side view of a well bore in accordance with an embodiment of the present invention is shown. The well bore is generally indicated at 100. While well bore 100 is depicted as a generally vertical well bore, the methods of the present invention may be performed in generally horizontal, inclined, or otherwise formed portions of well bores. In addition, well bore 100 may include multilaterals, wherein well bore 100 may be a primary well bore having one or more branch well bores extending therefrom, or well bore 100 may be a branch well bore extending laterally from a primary well bore. Well bore 100 penetrates subterranean formation 102 and has casing 104 disposed therein. Casing 104 may or may not be cemented in well bore 100 by a cement sheath (not shown). While Figure 1 depicts well bore 100 as a cased well bore at least a portion of well bore 100 may be left openhole. Generally, subterranean formation 102 contains multiple production intervals, including lowermost or first production interval 106, second production interval 108, third production interval 110, and fourth production interval 112. The intervals of casing 104 adjacent to production intervals 106, 108, 110, 112 are perforated by plurality of perforations 114, wherein plurality of perforations 114 penetrate through casing 104, through the cement sheath (if present), and into production intervals 106, 108, 110, 112. The intervals of casing 104 adjacent to production intervals 106, 108, 110, 112 are first casing interval 107, second casing interval 109, third casing interval 111, and fourth casing interval 113, respectively.
Referring now to Figure 2, conduit 118 is shown disposed in well bore 100. Conduit 118 may be coiled tubing, jointed pipe, or any other suitable conduit for the delivery of fluids during subterranean operations. Annulus 120 is defined between casing 104 and conduit 118.
As shown in Figure 2, in accordance with one embodiment of the methods of the present invention, a carrier fluid may be introduced into well bore 100 by pumping the carrier fluid down conduit 118. In another embodiment, carrier fluid may be introduced into well bore 100 by pumping the carrier fluid down annulus 120. The carrier fluid should contain first particulates. The carrier fluid and the first particulates will be discussed further below.
The first particulates in the carrier fluid should be allowed to pack into plurality of perforations 114, thereby forming particulate packs 124 in each of the plurality of perforations 114. Any suitable method may be used to introduce the carrier fluid into well bore 100 so that particulate packs 124 are formed. Generally, the carrier fluid may be introduced into well bore 100 so that downhole pressures are sufficient for the carrier fluid to squeeze into production intervals 106, 108, 110, 112, but the downhole pressures are below the respective fracture gradients until plurality of perforations 114 are effectively packed with particulates. Surface pumping pressures may be monitored to determine when particulate packs 124 have formed in each of the plurality of perforations 114. For example, when the surface pumping pressures of the carrier fluid increase above a pressure necessary for the downhole pressures to exceed the fracture gradients of production intervals 106, 108, 110, 112 without fracturing of such intervals, particulate packs 124 should have formed in each of the plurality of perforations 114. In certain embodiments, back pressure should be held on annulus 120, among other things so that the carrier fluid enters plurality of perforations 114 and is squeezed into the matrix of subterranean formation 102, so that carrier fluid is spread across plurality of perforations 114, and so that carrier fluid maintains sufficient velocity for proppant suspension without exceeding fracturing pressures. In one embodiment, back pressure is applied on annulus 120 by limiting the return of the carrier fluid up through annulus 120 by utilizing a choke mechanism at the surface (not shown). As the carrier fluid enters plurality of perforations 114 and is squeezed into the matrix of subterranean formation 102, the first particulates in the carrier fluid should bridge in plurality of perforations 114 and thus pack into plurality of perforations 114 forming particulate packs 124 therein. One of ordinary skill in the art will recognize other suitable methods for squeezing the carrier fluid into the matrix of subterranean formation 102.
Referring now to Figure 3, a cross-sectional side view of particulate pack 124 in perforation 114 is shown, in accordance with one embodiment of the methods of the present invention. Perforation 114 penetrates through first casing interval 107 and into first production interval 106. As discussed above, first particulates are packed into perforation 114, thereby forming particulate pack 124.
In certain embodiments, once particulate packs 124 have been formed in plurality of perforations 114, particulate packs 124 may be contacted with a second carrier fluid that contains second particulates. Generally, the second particulates are of a smaller size than the first particulates so that the second particulates may plug at least a portion of the interstitial spaces between the first particulates in particulate packs 124.
In one certain embodiment, the second carrier fluid containing the second particulates may be introduced into well bore 100 as the pad fluid for a stimulation operation performed on first production interval 106. The second carrier fluid and second particulates will be discussed in more detail below. The second carrier fluid may be introduced into well bore 100 by any suitable manner, for example, by pumping the second carrier fluid down conduit 118.
Generally, the second carrier fluid may be introduced into well bore 100 so that downhole pressures are sufficient for the second carrier fluid to squeeze into particulate packs 124 and into production intervals 106, 108, 110, 112, but the downhole pressures are below production intervals' 106, 108, 110, 112 respective fracture gradients. In certain embodiments, back pressure should be held on annulus 120 so that the second carrier fluid is squeezed into particulate packs 124 and thus into the matrix of subterranean formation 102, plugging at least portion of the interstitial spaces between the first particulates in particulate packs 124, thereby forming a filter cake at the surface of particulate packs 124. When a filter cake has formed at the surface of particulate packs 124, the leak off rate of the second carrier fluid into the matrix of subterranean formation 102 through particulate packs 124 should be reduced, as indicated by the rate of pressure fall off during shut-in immediately after pumping the second carrier fluid.
Referring now to Figure 4, once particulate packs 124 are formed by the introduction of the carrier fluid into well bore 100 and, if desired, second carrier fluid is introduced into well bore 100, the methods of the present invention may further comprise perforating at least one remedial perforation 132 in casing 104 adjacent to a production interval (e.g., production interval 106). These perforations are referred to as "remedial"
because they are created after an initial completion process has been performed in the well.
Further, the at least one remedial perforation 132 may be created in one or more previously perforated intervals of casing 104 (e.g., casing intervals 107, 109, 111,.
113) and/or one or more previously unperforated intervals of casing 104. The at least one remedial perforation 132 may penetrate through casing 104 and into a portion of subterranean formation 102 adjacent thereto. For example, the at least one remedial perforation 132 may penetrate through first casing interval 107 and into first production interval 106.
As illustrated in Figure 4, hydraulic jetting tool 126 is shown disposed in well bore 100. Hydraulic jetting tool 126 contains at least one port 127. Hydraulic jetting tool 126 may be any suitable assembly for use in subterranean operations through which a fluid may be jetted at high pressures, including those described in U.S. Patent Number 5,765,642. In one embodiment, hydraulic jetting tool 126 is attached to work string 128, in the form of piping or coiled tubing, which lowers hydraulic jetting tool 126 into well bore 100 and supplies it with jetting fluid. Optional valve subassembly 129 may be attached to the end of hydraulic jetting tool 126 to cause the flow of the fluid (referred to herein as "jetting fluid") to discharge through at least one port 127 in hydraulic jetting tool 126. Annulus 130 is defined between casing 104 and work string 128. In one embodiment, hydraulic jetting tool 126 is positioned in well bore 100 adjacent to casing 104 in a location (such as first casing interval 107) that is adjacent to a production interval (such as first production interval 106).
Hydraulic jetting tool 126 then operates to form at least one remedial perforation 132 by jetting the jetting fluid through at least one port 127 and against first casing interval 107. At least one remedial perforation 132 may penetrate through the first casing interval 107 and into first production interval 106 adjacent thereto. The jetting fluid may contain a base fluid (e.g., water) and abrasives (e.g., sand). In one embodiment, sand is present in the jetting fluid in an amount of about 1 pound per gallon of the base fluid. While the above description describes the use of hydraulic jetting tool 126 to create at least one remedial perforation 132 in first casing interval 107, any suitable method may be used create at least one remedial perforation 132 in first casing interval 107. Suitable methods include all perforating methods known to those of ordinary skill in the art, but are not limited to, bullet perforating, jet perforating, and hydraulic jetting.
In accordance with the methods of the present invention, once at least one remedial perforation 132 has been created in casing 104 at the desired location (e.g., first casing interval 107 adjacent to first production interval 106), the subterranean formation 102 (e.g., first production interval 106) may be stimulated through the at least one remedial perforation 132. Referring now to Figure 5, the stimulation of first production interval may be commenced using hydraulic jetting tool 126 shown disposed in well bore 100, in accordance with one embodiment of the present invention. In these embodiments, once at least one remedial perforation 132 has been created in first casing interval 107 using hydraulic jetting tool 126, the stimulation fluid may be pumped into well bore 100, down annulus 130, and into at least one remedial perforation 132 at a pressure sufficient to create or enhance at least one fracture 134 in subterranean formation 100, e.g., first production interval 106, along at least one remedial perforation 132. While Figure 5 depicts at least one fracture 134 as a longitudinal fracture that is approximately longitudinal or parallel to the axis of well bore 100, those of ordinary skill in the art will recognize that the direction and orientation of the at least one fracture 134 is dependent on a number of factors, including rock mechanical stress, reservoir pressure, and perforation orientation. In certain embodiments, a jetting fluid may be pumped down through work string 128 and jetted through at least one port 127, through the at least one remedial perforation 132, and against first production interval 106, wherein hydraulic jetting tool 126 is positioned adjacent to at least one remedial perforation 132. In certain embodiments, the step of jetting the jetting fluid against first production interval 106 may occur simultaneously with the pumping of the stimulation fluid into well bore 100, down annulus 130, and into at least one remedial perforation 132, so as to create or enhance at least one fracture 134 in first production interval 106 along at least one remedial perforation 132. Proppant may be included in the stimulation fluid and/or the jetting fluid as desired so as to support at least one fracture 134 and prevent it from fully closing after hydraulic pressure is released. Suitable methods of fracturing a subterranean formation utilizing a hydraulic jetting tool are described in U.S. Patent Number 5,765,642.
While the above description describes the use of hydraulic jetting tool 126 to create or enhance at least one fracture 134, any suitable method of stimulation may be used to stimulate the desired interval of subterranean formation 102, including, but are not limited to, hydraulic fracturing and fracture acidizing operations. In some embodiments, the stimulation of first production interval 106 comprises introducing a stimulation fluid into well bore 100 and into at least one remedial perforation 132 so as to contact first production interval 106. In another embodiment, stimulation fluid is introduced into well bore 100 so as to contact first production interval 106 at a pressure sufficient to create at least one fracture in first production interval 106.
In accordance with one embodiment of the present invention, once the desired interval of subterranean formation 102, such as first production interval 106, has been stimulated, sufficient sand may be introduced into well bore 100 via the stimulation fluid (e.g., annulus fluid, jetting fluid, or both) to form sand plug 136 in casing 104, as depicted in Figure 6. Once the hydraulic pressure is released, the sand should settle to form sand plug 136 adjacent to first casing interval 107 extending above at least one remedial perforation 132. In some embodiments, sand plug 136 may be adjacent to first casing interval 107 extending from an optional mechanical plug to above at least one remedial perforation 132. Sand plug 136 acts to isolate the stimulated section of subterranean formation 102, e.g., first production interval 106. One of ordinary skill in the art will recognize other suitable methods of isolating the stimulated section of subterranean formation 102 that may be suitable for use with the methods of the present invention.
Having perforated and stimulated a desired interval (such as first casing interval 107 and first production interval 106), in the manner described above, an operator may elect to repeat the above acts of perforating and stimulating for each of the remaining production intervals (such as production intervals 108, 110, 112). Referring now to Figure 6, for example, the operator may next elect to perforate at least one remedial perforation 138 in casing 104 adjacent to second production interval 108 and then stimulate second production interval through the at least one remedial perforation 138. In some embodiments, at least one remedial perforation 138 may be created in second casing interval 109 and a stimulation fluid may be introduced into well bore 100 and into the at least one remedial perforation 138 created therein so as to contact the second production interval 108 of subterranean formation 106. In some embodiments, as illustrated in Figure 6, hydraulic jetting tool 126 may be positioned adjacent to second casing interval 109 and used to create at least one remedial perforation 138 in second casing interval 109. Thereafter, in the manner described above, at least one fracture 140 may be created or enhanced along at least one remedial perforation 138. In certain embodiments of the present invention wherein an operator uses the methods of the present invention to stimulate multiple production intervals of subterranean formation 102 (such as production intervals 106, 108, 110, 112), the operator may elect to sequentially stimulate the production intervals intersected by well bore 100, beginning with the deepest production interval (e.g., first production interval 106), and sequentially stimulating the shallower desired intervals, such as production intervals 108, 110, 112.
In certain embodiments, clean-out fluids optionally may be introduced into well bore 100. Generally, clean-out fluids, where used, may be introduced into well bore 100 at any suitable time as desired by one of ordinary skill in the art, for example, to e.g., to clean out debris, cuttings, pipe dope, and other materials from well bore 100 and inside equipment, such as conduit 118 or hydraulic jetting tool 126 that may be disposed in well bore 100. For example, a clean out fluid may be used after completion of the stimulation operations so as to remove the sand plugs, such as sand plug 136 that may be in well bore 100. In some embodiments, the clean out fluid may be used after the carrier fluid has been introduced into well bore 100 so as to remove any of the first particulates that are loose in well bore 100.
Generally, the clean-out fluids should not be circulated into well bore 100 at sufficient rates and pressures to impact the integrity of particulate packs 124. Generally, the cleaning fluid may be any conventional fluid used to prepare a formation for stimulation, such as water-based or oil-based fluids. In some embodiments, these cleaning fluids may be energized fluids that contain a gas, such as nitrogen or air.
While the above-described steps describe the use of conduit 118 to introduce the carrier fluid and the second carrier fluid into well bore 100, any suitable methodology may be used to introduce such fluids into well bore 100. In some embodiments, work string 128 with hydraulic jetting tool 126 attached thereto and optional valve subassembly 129 attached to the end of hydraulic jetting tool 126 may be used in the above-described step of introducing the carrier fluid containing first particulates into well bore 100.
This may save at least one trip out of the well bore, between the steps of packing the first particulates into plurality of perforations 114 and perforating at least one remedial perforation 132 because the same downhole equipment may be used for both steps. For example, hydraulic jetting tool 126 may have a longitudinal fluid flow passageway extending therethrough and optional valve subassembly 129 may have a longitudinal fluid flow passageway extending therethough. When optional valve subassembly 129 is not activated, fluid flows down through work string 128, into hydraulic jetting tool 126, and out through optional valve subassembly 129. Accordingly, in some embodiments, the carrier fluid may be introduced into well bore 100 by pumping the carrier fluid down work string 128, into hydraulic jetting tool 126, and out into well bore 100 through optional valve subassembly 129. Similarly, second carrier fluid also may be introduced into well bore 100. When desired to perform the above-described remedial perforation and/or stimulation steps, optional valve subassembly 129 should be activated thereby causing the flow of fluid to discharge through at least one port 127.
The carrier fluid that may be used in accordance with the present invention, may include any suitable fluids that may be used to transport particulates in subterranean operations. Suitable fluids include ungelled aqueous fluids, aqueous gels, hydrocarbon-based gels, foams, emulsions, viscoelastic surfactant gels, and any other suitable fluid. Where the carrier fluid is an ungelled aqueous fluid, it should be introduced into the well bore at a sufficient rate to transport the first particulates. Suitable emulsions can be comprised of two immiscible liquids such as an aqueous liquid or gelled liquid and a hydrocarbon. Foams can be created by the addition of a gas, such as carbon dioxide or nitrogen. Suitable aqueous gels are generally comprised of water and one or more gelling agents. In exemplary embodiments, the carrier fluid is an aqueous gel comprised of water, a gelling agent for gelling the aqueous component and increasing its viscosity, and, optionally, a crosslinking agent for crosslinking the gel and further increasing the viscosity of the fluid.
The increased viscosity of the gelled, or gelled and crosslinked, aqueous gels, inter alia, reduces fluid loss and enhances the suspension properties thereof. An example of a suitable crosslinked aqueous gel is a borate fluid system utilized in the "Delta Frac "
fracturing service, commercially available from Halliburton Energy Services, Duncan Okalahoma.
Another example of a suitable crosslinked aqueous gel is a borate fluid system utilized in the "Seaquest " fracturing service, commercially available from Halliburton Energy Services, Duncan, Oklahoma. The water used to form the aqueous gel may be fresh water, saltwater, brine, or any other aqueous liquid that does not adversely react with the other components.
The density of the water can be increased to provide additional particle transport and suspension in the present invention.
As mentioned above, the carrier fluid contains first particulates. First particulates used in accordance with the present invention are generally particulate materials of a size such that the first particulates bridge plurality of perforations 114 in casing 104 and form proppant packs 124 therein. The first particulates used may have an average particle size in the range of from about 10 mesh to about 100 mesh. A wide variety of particulate materials may be used as the first particulates in accordance with the present invention including sand; bauxite; ceramic materials; glass materials; polymer materials; Teflon materials; nut shell pieces; seed shell pieces; cured resinous particulates comprising nut shell pieces; cured resinous particulates comprising seed shell pieces; fruit pit pieces; cured resinous particulates comprising fruit pit pieces; wood; composite particulates; and combinations thereof. Suitable composite particulates may comprise a binder and a filler material wherein suitable filler materials include silica, alumina, fumed carbon, carbon black, graphite, mica, titanium dioxide, meta-silicate, calcium silicate, kaolin, talc, zirconia, boron, fly ash, hollow glass microspheres, solid glass, and combinations thereof.
Generally, the first particulates may be present in the carrier fluid in an amount in an amount sufficient to form the desired proppant packs 124 in plurality of perforations 114. In some embodiments, the first particulates, may be present in the carrier fluid in an amount in the range of from about 2 pounds to about 12 pounds per gallon of the carrier fluid not inclusive of the first particulates.
Generally, the first particulates do not degrade in the presence of hydrocarbon fluids and other fluids present in portion of the subterranean formation; this allows the first particulates to maintain their integrity in the presence of produced hydrocarbon products, formation water, and other compositions normally produced from subterranean formations. However, in some embodiments of the present invention, the first particulates may comprise degradable materials. Degradable materials may be included in the first particulates, for example, so that proppant packs 124 may degrade over time. Such degradable materials are capable of undergoing an irreversible degradation downhole. The term "irreversible" as used herein means that the degradable material, once degraded downhole, should not recrystallize or reconsolidate, e.g., the degradable material should degrade in situ but should not recrystallize or reconsolidate in situ.
The degradable materials may degrade by any suitable mechanism.
Suitable degradable materials may be water-soluble, gas-soluble, oil-soluble, biodegradable, temperature degradable, solvent-degradable, acid-soluble, oxidizer-degradable, or a combination thereof. Suitable degradable materials include a variety of degradable materials suitable for use in subterranean operations and may comprise dehydrated materials, waxes, boric acid flakes, degradable polymers, calcium carbonate, paraffins, crosslinked polymer gels, combinations thereof, and the like. One example of a suitable degradable crosslinked polymer gel is "Max SealTM" fluid loss control additive, commercially available from Halliburton Energy Services, Duncan, Oklahoma. An example of a suitable degradable polymeric material is "BioBallsTM" perforation ball sealers, commercially available from Santrol Corporation, Fresno, Texas.
In some embodiments, the degradable material comprises an oil-soluble material. Where such oil-soluble materials are used, the oil-soluble materials may be degraded by the produced fluids, thus degrading particulate packs 124 so as to unblock plurality of perforations 114. Suitable oil-soluble materials include either natural or synthetic polymers, such as, for example, polyacrylics, polyamides, and polyolefins (such as polyethylene, polypropylene, polyisobutylene, and polystyrene).
Suitable examples of degradable polymers that may be used in accordance with the present invention include, but are not limited to, homopolymers, random, block, graft, and star- and hyper-branched polymers. Specific examples of suitable polymers include polysaccharides (such as dextran or cellulose); chitin; chitosan;
proteins; aliphatic polyesters; poly(lactide); poly(glycolide); poly(s-caprolactone);
poly(hydroxybutyrate);
poly(anhydrides); aliphatic polycarbonates; poly(ortho esters); poly(amino acids);
poly(ethylene oxide); polyphosphazenes; copolymers thereof, and combinations thereof.
Polyanhydrides are another type of particularly suitable degradable polymer useful in the present invention. Examples of suitable polyanhydrides include poly(adipic anhydride), poly(suberic anhydride), poly(sebacic anhydride), poly(dodecanedioic anhydride). Other suitable examples include but are not limited to poly(maleic anhydride) and poly(benzoic anhydride). One skilled in the art will recognize that plasticizers may be included in forming suitable polymeric degradable materials of the present invention. The plasticizers may be present in an amount sufficient to provide the desired characteristics, for example, more effective compatibilization of the melt blend components, improved processing characteristics during the blending and processing steps, and control and regulation of the sensitivity and degradation of the polymer by moisture.
Suitable dehydrated compounds are those materials that will degrade over time when rehydrated. For example, a particulate solid dehydrated salt or a particulate solid anhydrous borate material that degrades over time may be suitable. Specific examples of particulate solid anhydrous borate materials that may be used include but are not limited to anhydrous sodium tetraborate (also known as anhydrous borax), and anhydrous boric acid.
These anhydrous borate materials are only slightly soluble in water. However, with time and heat in a subterranean environment, the anhydrous borate materials react with the surrounding aqueous fluid and are hydrated. The resulting hydrated borate materials are substantially soluble in water as compared to anhydrous borate materials and as a result degrade in the aqueous fluid.
Blends of certain degradable materials and other compounds may also be suitable. One example of a suitable blend of materials is a mixture of poly(lactic acid) and sodium borate where the mixing of an acid and base could result in a neutral solution where this is desirable. Another example would include a blend of poly(lactic acid) and boric oxide.
In choosing the appropriate degradable material or materials, one should consider the degradation products that will result. The degradation products should not adversely affect subterranean operations or components. The choice of degradable material also can depend, at least in part, on the conditions of the well, e.g., well bore temperature.
For instance, lactides have been found to be suitable for lower temperature wells, including those within the range of 60 F to 150 F, and polylactides have been found to be suitable for well bore temperatures above this range. Poly(lactic acid) and dehydrated salts may be suitable for higher temperature wells. Also, in some embodiments a preferable result is achieved if the degradable material degrades slowly over time as opposed to instantaneously.
In some embodiments, it may be desirable when the degradable material does not substantially degrade until after the degradable material has been substantially placed in a desired location within a subterranean formation.
In certain embodiments of the present invention, the first particulates are coated with an adhesive substance. As used herein, the ten=n "adhesive substance" refers to a material that is capable of being coated onto a particulate and that exhibits a sticky or tacky character such that the proppant particulates that have adhesive thereon have a tendency to create clusters or aggregates. As used herein, the term "tacky," in all of its forms, generally refers to a substance having a nature such that it is (or may be activated to become) somewhat sticky to the touch. Generally, the first particulates may be coated with an adhesive substance so that the first particulates once placed within plurality of perforations 114 to form particulate packs 124 may consolidate into the first particulates into a hardened mass.
Adhesive substances suitable for use in the present invention include non-aqueous tackifying agents; aqueous tackifying agents; silyl-modified polyamides; and curable resin compositions that are capable of curing to form hardened substances.
Tackifying agents suitable for use in the consolidation fluids of the present invention comprise any compound that, when in liquid form or in a solvent solution, will form a non-hardening coating upon a particulate. A particularly preferred group of tackifying agents comprise polyamides that are liquids or in solution at the temperature of the subterranean formation such that they are, by themselves, non-hardening when introduced into the subterranean formation. A particularly preferred product is a condensation reaction product comprised of commercially available polyacids and a polyamine. Such commercial products include compounds such as mixtures of C36 dibasic acids containing some trimer and higher oligomers and also small amounts of monomer acids that are reacted with polyamines. Other polyacids include trimer acids, synthetic acids produced from fatty acids, maleic anhydride, acrylic acid, and the like. Such acid compounds are commercially available from companies such as Witco Corporation, Union Camp, Chemtall, and Emery Industries. The reaction products are available from, for example, Champion Technologies, Inc. and Witco Corporation. Additional compounds which may be used as tackifying compounds include liquids and solutions of, for example, polyesters, polycarbonates and polycarbamates, natural resins such as shellac and the like. Other suitable tackifying agents are described in U. S. Patent Numbers 5,853,048 and 5,833,000.
Tackifying agents suitable for use in the present invention may be either used such that they form a non-hardening coating or they may be combined with a multifunctional material capable of reacting with the tackifying compound to form a hardened coating. A
"hardened coating" as used herein means that the reaction of the tackifying compound with the multifunctional material will result in a substantially non-flowable reaction product that exhibits a higher compressive strength in a consolidated agglomerate than the tackifying compound alone with the particulates. In this instance, the tackifying agent may function similarly to a hardenable resin. Multifunctional materials suitable for use in the present invention include, but are not limited to, aldehydes such as formaldehyde, dialdehydes such as glutaraldehyde, hemiacetals or aldehyde releasing compounds, diacid halides, dihalides such as dichlorides and dibromides, polyacid anhydrides such as citric acid, epoxides, furfuraldehyde, glutaraldehyde or aldehyde condensates and the like, and combinations thereof. In some embodiments of the present invention, the multifunctional material may be mixed with the tackifying compound in an amount of from about 0.01 to about 50 percent by weight of the tackifying compound to effect formation of the reaction product.
In some preferable embodiments, the compound is present in an amount of from about 0.5 to about I
percent by weight of the tackifying compound. Suitable multifunctional materials are described in U.S. Patent Number 5,839,510. Other suitable tackifying agents are described in U.S. Patent Number 5,853,048.
Solvents suitable for use with the tackifying agents of the present invention include any solvent that is compatible with the tackifying agent and achieves the desired viscosity effect. The solvents that can be used in the present invention preferably include those having high flash points (most preferably above about 125 F). Examples of solvents suitable for use in the present invention include, but are not limited to, butylglycidyl ether, dipropylene glycol methyl ether, butyl bottom alcohol, dipropylene glycol dimethyl ether, diethyleneglycol methyl ether, ethyleneglycol butyl ether, methanol, butyl alcohol, isopropyl alcohol, diethyleneglycol butyl ether, propylene carbonate, d'limonene, 2-butoxy ethanol, butyl acetate, furfuryl acetate, butyl lactate, dimethyl sulfoxide, dimethyl formamide, fatty acid methyl esters, and combinations thereof. It is within the ability of one skilled in the art, with the benefit of this disclosure, to determine whether a solvent is needed to achieve a viscosity suitable to the subterranean conditions and, if so, how much.
Suitable aqueous tackifier agents are capable of forming at least a partial coating upon the surface of the first particulates. Generally, suitable aqueous tackifier agents are not significantly tacky when placed onto a particulate, but are capable of being "activated"
(that is destabilized, coalesced and/or reacted) to transform the compound into a sticky, tackifying compound at a desirable time. Such activation may occur before, during, or after the aqueous tackifier compound is placed in the subterranean formation. In some embodiments, a pretreatment may be frrst contacted with the surface of a particulate to prepare it to be coated with an aqueous tackifier compound. Suitable aqueous tackifying agents are generally charged polymers that comprise compounds that, when in an aqueous solvent or solution, will form a non-hardening coating (by itself or with an activator) and, when placed on a particulate, will increase the continuous critical resuspension velocity of the particulate when contacted by a stream of water.
Examples of aqueous tackifier agents suitable for use in the present invention include, but are not limited to, acrylic acid polymers, acrylic acid ester polymers, acrylic acid derivative polymers, acrylic acid homopolymers, acrylic acid ester homopolymers (such as poly(methyl acrylate); poly (butyl acrylate), and poly(2-ethylhexyl acrylate)), acrylic acid ester co-polymers, methacrylic acid derivative polymers, methacrylic acid homopolymers, methacrylic acid ester homopolymers (such as poly(methyl methacrylate), poly(butyl methacrylate), and poly(2- ethylhexyl methacryate)), aciylamido-methyl-propane sulfonate polymers, acrylamido-methyl-propane sulfonate derivative polymers, acrylamido-methyl-propane sulfonate co-polymers, and acrylic acid/acrylamido-methyl-propane sulfonate co-polymers and combinations thereof. Methods of determining suitable aqueous tackifier agents and additional disclosure on aqueous tackifier agents can be found in U.S.
Patent Application Number 10/864,061 and filed June 9, 2004 and U.S. Patent Application Number 10/864,618 and filed June 9, 2004.
Silyl-modified polyamide compounds suitable for use as an adhesive substance in the methods of the present invention may be described as substantially self-hardening compositions that are capable of at least partially adhering to particulates in the unhardened state, and that are further capable of self-hardening themselves to a substantially non-tacky state to which individual particulates such as formation fines will not adhere. Such silyl-modified polyamides may be based, for example, on the reaction product of a silating compound with a polyamide or a mixture of polyamides. The polyamide or mixture of polyamides may be one or more polyamide intermediate compounds obtained, for example, f'rom the reaction of a polyacid (e.g., diacid or higher) with a polyamine (e.g., diamine or higher) to form a polyamide polymer with the elimination of water. Other suitable silyl-modified polyamides and methods of making such compounds are described in U.S.
Patent Number 6,439,309.
Curable resin compositions suitable for use in the consolidation fluids of the present invention generally comprise any suitable resin that is capable of forming a hardened, consolidated mass. Many such resins are commonly used in subterranean consolidation operations, and some suitable resins include two component epoxy based resins, novolak resins, polyepoxide resins, phenol-aldehyde resins, urea-aldehyde resins, urethane resins, phenolic resins, furan resins, furan/furfuryl alcohol resins, phenolic/latex resins, phenol formaldehyde resins, polyester resins and hybrids and copolymers thereof, polyurethane resins and hybrids and copolymers thereof, acrylate resins, and mixtures thereof.
Some suitable resins, such as epoxy resins, may be cured with an internal catalyst or activator so that when pumped down hole, they may be cured using only time and temperature. Other suitable resins, such as furan resins generally require a time-delayed catalyst or an external catalyst to help activate the polymerization of the resins if the cure temperature is low (i.e., less than 250 F), but will cure under the effect of time and temperature if the formation temperature is above about 250 F, preferably above about 3 00 F. It is within the ability of one skilled in the art, with the bencfit of this disclosure, to select a suitable resin for use in embodiments of the present invention and to determine whether a catalyst is required to trigger curing.
Further, the curable resin composition further may contain a solvent. Any solvent that is compatible with the resin and achieves the desired viscosity effect is suitable for use in the present invention. Preferred solvents include those listed above in connection with tackifying compounds. It is within the ability of one skilled in the art, with the benefit of this disclosure, to determine whether and how much solvent is needed to achieve a suitable viscosity.
The second carrier fluid that may be used in accordance with the present invention, may include any suitable fluids that may be used to transport particulates in subterranean operations. Suitable fluids include ungelled aqueous fluids, aqueous gels, hydrocarbon-based gels, foams, emulsions, viscoelastic surfactant gels, and any other suitable fluid. Where the second carrier fluid is an ungelled aqueous fluid, it should be introduced into the well bore at a sufficient rate to transport the first particulates.
Suitable emulsions can be comprised of two immiscible liquids such as an aqueous liquid or gelled liquid and a hydrocarbon. Foams can be created by the addition of a gas, such as carbon dioxide or nitrogen. Suitable aqueous gels are generally comprised of water and one or more gelling agents. In exemplary embodiments, the second carrier fluid is an aqueous gel comprised of water, a gelling agent for gelling the aqueous component and increasing its viscosity, and, optionally, a crosslinking agent for crosslinking the gel and further increasing the viscosity of the fluid. The increased viscosity of the gelled, or gelled and crosslinked, aqueous gels, inter alia, reduces fluid loss and enhances the suspension properties thereof. An example of a suitable crosslinked aqueous gel is a borate fluid system utilized in the "Delta Frac "
fracturing service, commercially available from Halliburton Energy Services, Duncan Okalahoma. Another example of a suitable crosslinked aqueous gel is a borate fluid system utilized in the "Seaquest " fracturing service, commercially available from Halliburton Energy Services, Duncan, Oklahoma. The water used to form the aqueous gel may be fresh water, saltwater, brine, or any other aqueous liquid that does not adversely react with the other components. The density of the water can be increased to provide additional particle transport and suspension in the present invention.
As mentioned above, the second carrier fluid contains second particulates.
The second particulates used in accordance with the present invention are generally particulate materials having an average particle size small than the average particle size of the first particulates so that the second particulates may plug at least a portion of the interstitial spaces between the first particulates in particulate packs 124. In certain embodiments, the second particulates used may have an average particle size of less than about 100 mesh.
Examples of suitable particulate materials that may be used as the second particulates include, but are not limited to, silica flour, sand; bauxite; ceramic materials; glass materials;
polymer materials; Teflon materials; nut shell pieces; seed shell pieces;
cured resinous particulates comprising nut shell pieces; cured resinous particulates comprising seed shell pieces; fruit pit pieces; cured resinous particulates comprising fruit pit pieces; wood;
composite particulates; and combinations thereof. Suitable composite particulates may comprise a binder and a filler material wherein suitable filler materials include silica, alumina, fumed carbon, carbon black, graphite, mica, titanium dioxide, meta-silicate, calcium silicate, kaolin, talc, zirconia, boron, fly ash, hollow glass microspheres, solid glass, and combinations thereof. Generally, the second particulates should be included in the second carrier fluid in an amount sufficient to form the desired filter cake on the surface of proppant packs 124. In certain embodiments, the second particulates may be present in the second carrier fluid in an amount in the range of from about 30 pounds to about 100 pounds per 1,000 gallons of the second carrier fluid not inclusive of the second particulates. In certain embodiments, the second particulates may comprise degradable particulates of the type described above.
The stimulation and jetting fluids that may be used in accordance with the present invention, may include any suitable fluids that may be used in subterranean stimulation operations. In some embodiments, the stimulation fluid may have substantially the same composition as the jetting fluid. Suitable fluids include ungelled aqueous fluids, aqueous gels, hydrocarbon-based gels, foams, emulsions, viscoelastic surfactant gels, acidizing treatment fluids (e.g., acid blends) and any other suitable fluid.
In some embodiments, the stimulation fluid and/or jetting fluid may contain an acid.
Where the stimulation or jetting fluid is an ungelled aqueous fluid, it should be introduced into the well bore at a sufficient rate to transport proppant (where present). Suitable emulsions can be comprised of two immiscible liquids such as an aqueous gelled liquid and a liquefied, normally gaseous, fluid, such as carbon dioxide or nitrogen. Foams can be created by the addition of a gas, such as carbon dioxide or nitrogen. Suitable aqueous gels are generally comprised of water and one or more gelling agents. In exemplary embodiments, the jetting fluid and/or stimulation fluid is an aqueous gel comprised of water, a gelling agent for gelling the aqueous component and increasing its viscosity, and, optionally, a crosslinking agent for crosslinking the gel and further increasing the viscosity of the fluid. The increased viscosity of the gelled, or gelled and crosslinked, aqueous gels, inter alia, reduces fluid loss and enhances the suspension properties thereof. The water used to form the aqueous gel may be fresh water, saltwater, brine, or any other aqueous liquid that does not adversely react with the other components: The density of the water can be increased to provide additional particle transport and suspension in the present invention. One of ordinary skill in the art, with the benefit of this disclosure, will be able to determine the appropriate stimulation and/or jetting fluid for a particulate application.
Optionally, proppant may be included in the stimulation fluid, the jetting fluid, or both. Among other things, proppant may be included to prevent fractures formed in the subterranean formation from fully closing once the hydraulic pressure is released. A
variety of suitable proppant may be used, for example, sand; bauxite; ceramic materials; glass materials; polymer materials; Teflon materials; nut shell pieces; seed shell pieces; cured resinous particulates comprising nut shell pieces; cured resinous particulates comprising seed shell pieces; fruit pit pieces; cured resinous particulates comprising fruit pit pieces; wood;
composite particulates; and combinations thereof. Suitable composite particulates may comprise a binder and a filler material wherein suitable filler materials include silica, alumina, fumed carbon, carbon black, graphite, mica, titanium dioxide, meta-silicate, calcium silicate, kaolin, talc, zirconia, boron, fly ash, hollow glass microspheres, solid glass, and combinations thereof. One of ordinary skill in the art, with the benefit of this disclosure, should know the appropriate amount and type of proppant to include in the jetting fluid and/or stimulation fluid for a particular application.
In one embodiment, the present invention provides a method of stimulating a production interval adjacent a well bore having a casing disposed therein, the method comprising: introducing a carrier fluid comprising first particulates into the well bore;
packing the first particulates into a plurality of perforations in the casing;
perforating at least one remedial perforation in the casing adjacent to the production interval, subsequent to the packing the first particulates; and stimulating the production interval through the at least one remedial perforation.
In another embodiment, the present invention provides a method of stimulating a production interval adjacent a well bore having a casing disposed therein, the method comprising: introducing a carrier fluid comprising first particulates into the well bore;
packing the first particulates into a plurality of perforations in the casing;
providing a hydraulic jetting tool having at least one port, the hydrajetting tool attached to a work string;
positioning the hydraulic jetting tool in the well bore adjacent the production interval; jetting a jetting fluid through the at least one nozzle in the hydraulic jetting tool against the casing in the well bore so as to create at least one remedial perforation in the casing;
and stimulating the production interval through the at least one remedial perforation.
In yet another embodiment, the present invention provides a method of stimulating multiple production intervals adjacent a well bore having a casing disposed therein, the method comprising: introducing a carrier fluid comprising first particulates into the well bore; packing the first particulates into a plurality of perforations in the casing;
perforating at least one remedial perforation in the casing adjacent to a production interval, subsequent to the packing the first particulates; introducing a stimulation fluid into the well bore and into the at least one remedial perforation so as to contact the production interval;
and repeating the acts of perforating at least one remedial perforation and introducing the stimulation fluid for each of the remaining production intervals.
Therefore, the present invention is well adapted to carry out the objects and attain the ends and advantages mentioned as well as those which are inherent therein.
While numerous changes may be made by those skilled in the art, such changes are encompassed within the spirit of this invention as defined by the appended claims.
Claims (59)
1. A method of stimulating a production interval adjacent a well bore having a casing disposed therein, the method comprising:
introducing a carrier fluid comprising first particulates into the well bore;
packing the first particulates into a plurality of perforations in the casing;
perforating at least one remedial perforation in the casing adjacent to a production interval, subsequent to the packing the first particulates; and stimulating the production interval through the at least one remedial perforation.
introducing a carrier fluid comprising first particulates into the well bore;
packing the first particulates into a plurality of perforations in the casing;
perforating at least one remedial perforation in the casing adjacent to a production interval, subsequent to the packing the first particulates; and stimulating the production interval through the at least one remedial perforation.
2. The method of claim 1 wherein the well bore is a primary well bore or a branch well bore extending from a primary well bore.
3. The method of claim 1 wherein the carrier fluid is selected from the group consisting of an ungelled aqueous fluid, an aqueous gel, a hydrocarbon-based gel, a foam, and a viscoelastic surfactant gel.
4. The method of claim 1 wherein the carrier fluid comprises an aqueous component and a gelling agent.
5. The method of claim 4 wherein the gelling agent is crosslinked using a crosslinking agent.
6. The method of claim 1 wherein the first particulates have an average particle size of from about 10 mesh to about 100 mesh.
7. The method of claim 1 wherein the first particulates are selected from the group consisting of sand, bauxite, ceramic materials, glass materials, polymer materials, TeflonĀ® materials, nut shell pieces, seed shell pieces, cured resinous particulates comprising nut shell pieces, cured resinous particulates comprising seed shell pieces, fruit pit pieces, cured resinous particulates comprising fruit pit pieces, wood, and composite particulates.
8. The method of claim 1 wherein the first particulates comprise a degradable material.
9. The method of claim 8 wherein the degradable material is selected from the group consisting of a water-soluble material, a gas- soluble material, an oil-soluble material, a biodegradable material, a temperature degradable material, a solvent-degradable material, an acid-soluble material, and an oxidizer-degradable material.
10. The method of claim 8 wherein the degradable material is selected from the group consisting of a dehydrated material, a wax, boric acid flakes, a degradable polymer, calcium carbonate, a paraffin, and a crosslinked polymer gel.
11. The method of claim 8 wherein the degradable material is selected from the group consisting of a polyacrylic, a polyamide, and a polyolefin.
12. The method of claim 8 wherein the degradable material is selected from the group consisting of a polysaccharide, a chitin, a chitosan, a protein, an aliphatic polyester, a poly(lactide), a poly(glycolide), a poly(.epsilon.-caprolactone), a poly(hydroxybutyrate), a poly(anhydride), an aliphatic polycarbonate, a poly(orthoester), a poly(amino acid), a poly(ethylene oxide), a polyphosphazene, and a polyanhydride.
13. The method of claim 1 wherein the first particulates are coated with an adhesive substance.
14. The method of claim 13 wherein the adhesive substance is selected from the group consisting of a non-aqueous tackifying agent, an aqueous tackifying agent, a silyl-modified polyamide, and a curable resin composition.
15. The method of claim 14 wherein the non-aqueous tackifying agent is selected from the group consisting of a polyamide, a polyester, a polycarbonate, polycarbamate, and a natural resin.
16. The method of claim 15 wherein the non-aqueous tackifying agent further comprises a multifunctional material.
17. The method of claim 14 wherein the aqueous tackifying agent is selected from the group consisting of an acrylic acid polymer, an acrylic acid ester polymer, an acrylic acid derivative polymer, an acrylic acid homopolymer, an acrylic acid ester homopolymer, an acrylamido-methyl-propane sulfonate polymer, an acrylamido-methyl-propane sulfonate derivative polymer, an acrylamido-methyl-propane sulfonate co-polymer, an acrylic acid/acrylamido-methyl-propane sulfonate co-polymer, and a copolymer thereof.
18. The method of claim 17 wherein the aqueous tackifying agent is made tacky through exposure to an activator, the activator is selected from the group consisting of an organic acid, an anhydride of an organic acid, an inorganic acid, an inorganic salt, a charged surfactant, and charged polymer.
19. The method of claim 14 wherein the curable resin composition is selected from the group consisting of a two component epoxy based resin, a novolak resin, a polyepoxide resin, a phenol-aldehyde resin, a urea-aldehyde resin, a urethane resin, a phenolic resin, a furan resin, a furan/furfuryl alcohol resin, a phenolic/latex resin, a phenol formaldehyde resin, a polyester resin, a hybrid polyester resin, copolymer polyester resin, a polyurethane resin, a hybrid polyurethane resin, a copolymer polyurethane resin, and an acrylate resin.
20. The method of claim 1 wherein the at least one remedial perforation is created in an interval of the casing that was previously perforated.
21. The method of claim 1 wherein the perforating comprises at least one of the following: bullet perforating, jet perforating, or hydraulic jetting.
22. The method of claim 1 wherein the perforating comprises:
positioning a hydraulic jetting tool adjacent to the casing in a location adjacent to the production interval, and jetting a jetting fluid through the hydraulic jetting tool against the casing.
positioning a hydraulic jetting tool adjacent to the casing in a location adjacent to the production interval, and jetting a jetting fluid through the hydraulic jetting tool against the casing.
23. The method of claim 22 wherein the jetting fluid comprises a base fluid and sand.
24. The method of claim 23 wherein the sand is present in the jetting fluid in an amount of about 1 pound per gallon of the base fluid.
25. The method of claim 1 wherein the stimulating comprises introducing a fluid into the well bore and into the at least one remedial perforation so as to contact the production interval.
26. The method of claim 25 wherein the fluid comprises at least one of the following: an ungelled aqueous fluid, an aqueous gel, a hydrocarbon-based gel, a foam, an emulsion, or a viscoelastic surfactant gel.
27. The method of claim 25 wherein the fluid comprises an acid.
28. The method of claim 25 wherein the fluid comprises proppant.
29. The method of claim 25 wherein the introducing the fluid comprises pumping the fluid into the well bore and into the at least one remedial perforation at a pressure sufficient to create or enhance at least one fracture in the production interval.
30. The method of claim 1 wherein the stimulating comprises jetting a jetting fluid through a hydraulic jetting tool and into the at least one remedial perforation, wherein the hydraulic jetting tool is attached to a work string, wherein the hydraulic jetting tool is positioned adjacent to the at least one remedial perforation.
31. The method of claim 30 wherein the jetting creates or enhances at least one fracture in the production interval.
32. The method of claim 30 wherein the stimulating comprises introducing a fluid into the well bore down an annulus defined between the casing and the work string.
33. The method of claim 32 the fluid is introduced into the well bore simultaneously with the jetting of the jetting fluid.
34. The method of claim 1 further comprising perforating at least one remedial perforation in the casing adjacent to a second production interval.
35. The method of claim 34 wherein the stimulating further comprises stimulating the second production interval through the at least one perforation in the casing adjacent to the second production interval.
36. The method of claim 1 further comprising repeating the acts of perforating and stimulating for each of the remaining production intervals.
37. The method of claim I further comprising introducing a clean-out fluid into the well bore.
38. The method of claim I wherein the first particulates form a particulate pack in each of the plurality of perforations.
39. The method of claim I further comprising contacting the particulate packs with a second carrier fluid comprising second particulates so that the second particulates plug at least a portion of the interstitial spaces between the first particulates in the particulate pack.
40. The method of claim 39 wherein the average particle size of the second particulates is smaller than the average particle size of the first particulates.
41. The method of claim 39 wherein the second carrier fluid is selected from the group consisting of an ungelled aqueous fluid, an aqueous gel, a hydrocarbon-based gel, a foam, and a viscoelastic surfactant gel.
42. The method of claim 39 wherein the second particulates are selected from a group consisting of silica flour, sand, bauxite, ceramic materials, glass materials, polymer materials, TeflonĀ® materials, nut shell pieces, seed shell pieces, cured resinous particulates comprising nut shell pieces, cured resinous particulates comprising seed shell pieces, fruit pit pieces, cured resinous particulates comprising fruit pit pieces, wood, and composite particulates.
43. The method of claim 39 wherein the second particulates comprise degradable materials.
44. A method of stimulating a production interval adjacent a well bore having a casing disposed therein, the method comprising:
introducing a carrier fluid comprising first particulates into the well bore;
packing the first particulates into a plurality of perforations in the casing;
providing a hydraulic jetting tool having at least one port, the hydrajetting tool attached to a work string;
positioning the hydraulic jetting tool in the well bore adjacent the production interval;
jetting ajetting fluid through the at least one nozzle in the hydraulic jetting tool against the casing in the well bore so as to create at least one remedial perforation in the casing; and stimulating the production interval through the at least one remedial perforation.
introducing a carrier fluid comprising first particulates into the well bore;
packing the first particulates into a plurality of perforations in the casing;
providing a hydraulic jetting tool having at least one port, the hydrajetting tool attached to a work string;
positioning the hydraulic jetting tool in the well bore adjacent the production interval;
jetting ajetting fluid through the at least one nozzle in the hydraulic jetting tool against the casing in the well bore so as to create at least one remedial perforation in the casing; and stimulating the production interval through the at least one remedial perforation.
45. The method of claim 44 wherein the first particulates have an average particle size in the range of from about 10 mesh to about 100 mesh.
46. The method of claim 44 wherein the first particulates are coated with an adhesive substance.
47. The method of claim 44 wherein the first particulates comprises a degradable material.
48. The method of claim 44 wherein the first particulates form a particulate pack in each of the plurality of perforations.
49. The method of claim 48 further comprising contacting the particulate pack in each of the plurality of perforations with a second carrier fluid comprising second particulates so that the second particulates plug at least a portion of the interstitial spaces between the first particulates in the particulate pack.
50. The method of claim 44 wherein the jetting fluid is selected from the group consisting of an ungelled aqueous fluid, an aqueous gel, a hydrocarbon-based gel, a foam, and a viscoelastic surfactant gel.
51. The method of claim 44 wherein the stimulating comprises introducing a stimulation fluid into an annulus so as to contact the at least one remedial perforation, the annulus is defined between the work string and the casing.
52. The method of claim 51 wherein the stimulation fluid is selected from the group consisting of an ungelled aqueous fluid, an aqueous gel, a hydrocarbon-based gel, a f'oam, and a viscoelastic surfactant gel.
53. The method of claim 51 wherein the stimulation fluid is introduced into the annulus at a pressure sufficient to create or enhance at least one fracture in the production interval.
54. The method of claim 51 wherein the stimulating comprises jetting a jetting fluid through the at least one nozzle in the hydraulic jetting tool, through the at least one remedial perforation, and against the production interval.
55. The method of claim 54 wherein the jetting the jetting fluid against the production interval and introducing the stimulation fluid into the annulus occur simultaneously.
56. The method of claim 54 wherein the jetting fluid is jetted against the production interval simultaneously with the introducing the stimulation fluid.
57. The method of claim 51 further comprising repeating the acts of positioning the hydraulic jetting tool, jetting the jetting fluid, and stimulating the production interval for each of the remaining production intervals.
58. A method of stimulating multiple production intervals adjacent a well bore having a casing disposed therein, the method comprising:
introducing a carrier fluid comprising first particulates into the well bore, packing the first particulates into a plurality of perforations in the casing, perforating at least one remedial perforation in the casing adjacent to a production interval, subsequent to the packing the first particulates, introducing a stimulation fluid into the well bore and into the at least one remedial perforation so as to contact the production interval, and repeating the acts of perforating at least one remedial perforation and introducing the stimulation fluid for each of the remaining production intervals.
introducing a carrier fluid comprising first particulates into the well bore, packing the first particulates into a plurality of perforations in the casing, perforating at least one remedial perforation in the casing adjacent to a production interval, subsequent to the packing the first particulates, introducing a stimulation fluid into the well bore and into the at least one remedial perforation so as to contact the production interval, and repeating the acts of perforating at least one remedial perforation and introducing the stimulation fluid for each of the remaining production intervals.
59. The method of claim 58 further comprising contacting the packed perforations with a second carrier fluid comprising second particulates so that second particulates plug at least a portion of the interstitial spaces between the first particulates packed into the plurality of perforations.
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US11/004,441 | 2004-12-03 | ||
PCT/GB2005/004009 WO2006059056A1 (en) | 2004-12-03 | 2005-10-18 | Methods of stimulating a subterranean formation comprising multiple production intervals |
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CA002589798A Expired - Fee Related CA2589798C (en) | 2004-12-03 | 2005-10-18 | Methods of stimulating a subterranean formation comprising multiple production intervals |
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AU (1) | AU2005311147B2 (en) |
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Families Citing this family (156)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7519268B2 (en) * | 1998-04-14 | 2009-04-14 | Nikon Corporation | Image recording apparatus, dynamic image processing apparatus, dynamic image reproduction apparatus, dynamic image recording apparatus, information recording / reproduction apparatus and methods employed therein, recording medium with computer program stored therein |
US8962535B2 (en) | 2003-05-16 | 2015-02-24 | Halliburton Energy Services, Inc. | Methods of diverting chelating agents in subterranean treatments |
US8091638B2 (en) | 2003-05-16 | 2012-01-10 | Halliburton Energy Services, Inc. | Methods useful for controlling fluid loss in subterranean formations |
US8631869B2 (en) | 2003-05-16 | 2014-01-21 | Leopoldo Sierra | Methods useful for controlling fluid loss in subterranean treatments |
US8251141B2 (en) | 2003-05-16 | 2012-08-28 | Halliburton Energy Services, Inc. | Methods useful for controlling fluid loss during sand control operations |
US8181703B2 (en) | 2003-05-16 | 2012-05-22 | Halliburton Energy Services, Inc. | Method useful for controlling fluid loss in subterranean formations |
DE20307912U1 (en) * | 2003-05-19 | 2003-09-25 | Jvk Filtration Systems Gmbh | Leakage indicator for a filter element of a filter press |
US7766099B2 (en) | 2003-08-26 | 2010-08-03 | Halliburton Energy Services, Inc. | Methods of drilling and consolidating subterranean formation particulates |
US8167045B2 (en) | 2003-08-26 | 2012-05-01 | Halliburton Energy Services, Inc. | Methods and compositions for stabilizing formation fines and sand |
US20050173116A1 (en) | 2004-02-10 | 2005-08-11 | Nguyen Philip D. | Resin compositions and methods of using resin compositions to control proppant flow-back |
US7211547B2 (en) | 2004-03-03 | 2007-05-01 | Halliburton Energy Services, Inc. | Resin compositions and methods of using such resin compositions in subterranean applications |
US20080060810A9 (en) * | 2004-05-25 | 2008-03-13 | Halliburton Energy Services, Inc. | Methods for treating a subterranean formation with a curable composition using a jetting tool |
US7299875B2 (en) | 2004-06-08 | 2007-11-27 | Halliburton Energy Services, Inc. | Methods for controlling particulate migration |
US7775278B2 (en) * | 2004-09-01 | 2010-08-17 | Schlumberger Technology Corporation | Degradable material assisted diversion or isolation |
US7275596B2 (en) | 2005-06-20 | 2007-10-02 | Schlumberger Technology Corporation | Method of using degradable fiber systems for stimulation |
US7380600B2 (en) * | 2004-09-01 | 2008-06-03 | Schlumberger Technology Corporation | Degradable material assisted diversion or isolation |
US7398825B2 (en) * | 2004-12-03 | 2008-07-15 | Halliburton Energy Services, Inc. | Methods of controlling sand and water production in subterranean zones |
US7748451B2 (en) * | 2004-12-08 | 2010-07-06 | Halliburton Energy Services, Inc. | Methods for improving low-quality proppant and method of using low-quality proppant in subterranean operations |
US7883740B2 (en) | 2004-12-12 | 2011-02-08 | Halliburton Energy Services, Inc. | Low-quality particulates and methods of making and using improved low-quality particulates |
US7673686B2 (en) | 2005-03-29 | 2010-03-09 | Halliburton Energy Services, Inc. | Method of stabilizing unconsolidated formation for sand control |
US7318474B2 (en) | 2005-07-11 | 2008-01-15 | Halliburton Energy Services, Inc. | Methods and compositions for controlling formation fines and reducing proppant flow-back |
US7296625B2 (en) * | 2005-08-02 | 2007-11-20 | Halliburton Energy Services, Inc. | Methods of forming packs in a plurality of perforations in a casing of a wellbore |
US20070044969A1 (en) * | 2005-08-31 | 2007-03-01 | Schlumberger Technology Corporation | Perforating a Well Formation |
US7926591B2 (en) | 2006-02-10 | 2011-04-19 | Halliburton Energy Services, Inc. | Aqueous-based emulsified consolidating agents suitable for use in drill-in applications |
US8613320B2 (en) | 2006-02-10 | 2013-12-24 | Halliburton Energy Services, Inc. | Compositions and applications of resins in treating subterranean formations |
US7819192B2 (en) | 2006-02-10 | 2010-10-26 | Halliburton Energy Services, Inc. | Consolidating agent emulsions and associated methods |
US7845413B2 (en) * | 2006-06-02 | 2010-12-07 | Schlumberger Technology Corporation | Method of pumping an oilfield fluid and split stream oilfield pumping systems |
US7571766B2 (en) * | 2006-09-29 | 2009-08-11 | Halliburton Energy Services, Inc. | Methods of fracturing a subterranean formation using a jetting tool and a viscoelastic surfactant fluid to minimize formation damage |
US7730950B2 (en) | 2007-01-19 | 2010-06-08 | Halliburton Energy Services, Inc. | Methods for treating intervals of a subterranean formation having variable permeability |
US7934557B2 (en) | 2007-02-15 | 2011-05-03 | Halliburton Energy Services, Inc. | Methods of completing wells for controlling water and particulate production |
US8726991B2 (en) * | 2007-03-02 | 2014-05-20 | Schlumberger Technology Corporation | Circulated degradable material assisted diversion |
US7647966B2 (en) | 2007-08-01 | 2010-01-19 | Halliburton Energy Services, Inc. | Method for drainage of heavy oil reservoir via horizontal wellbore |
US7673673B2 (en) * | 2007-08-03 | 2010-03-09 | Halliburton Energy Services, Inc. | Apparatus for isolating a jet forming aperture in a well bore servicing tool |
US8598094B2 (en) | 2007-11-30 | 2013-12-03 | Halliburton Energy Services, Inc. | Methods and compostions for preventing scale and diageneous reactions in subterranean formations |
US7832477B2 (en) * | 2007-12-28 | 2010-11-16 | Halliburton Energy Services, Inc. | Casing deformation and control for inclusion propagation |
DE102008004112A1 (en) * | 2008-01-11 | 2009-07-16 | Saertex Gmbh & Co. Kg | Semifinished textile product with at least one surface provided with an adhesive |
US7896075B2 (en) * | 2008-02-04 | 2011-03-01 | Halliburton Energy Services, Inc. | Subterranean treatment fluids with enhanced particulate transport or suspension capabilities and associated methods |
US8113278B2 (en) * | 2008-02-11 | 2012-02-14 | Hydroacoustics Inc. | System and method for enhanced oil recovery using an in-situ seismic energy generator |
US7690427B2 (en) * | 2008-03-07 | 2010-04-06 | Halliburton Energy Services, Inc. | Sand plugs and placing sand plugs in highly deviated wells |
US8096358B2 (en) * | 2008-03-27 | 2012-01-17 | Halliburton Energy Services, Inc. | Method of perforating for effective sand plug placement in horizontal wells |
US20090253594A1 (en) | 2008-04-04 | 2009-10-08 | Halliburton Energy Services, Inc. | Methods for placement of sealant in subterranean intervals |
US9212535B2 (en) * | 2008-04-15 | 2015-12-15 | Schlumberger Technology Corporation | Diversion by combining dissolvable and degradable particles and fibers |
US8936085B2 (en) | 2008-04-15 | 2015-01-20 | Schlumberger Technology Corporation | Sealing by ball sealers |
US7819193B2 (en) * | 2008-06-10 | 2010-10-26 | Baker Hughes Incorporated | Parallel fracturing system for wellbores |
US7900696B1 (en) | 2008-08-15 | 2011-03-08 | Itt Manufacturing Enterprises, Inc. | Downhole tool with exposable and openable flow-back vents |
US8267177B1 (en) | 2008-08-15 | 2012-09-18 | Exelis Inc. | Means for creating field configurable bridge, fracture or soluble insert plugs |
US8960292B2 (en) * | 2008-08-22 | 2015-02-24 | Halliburton Energy Services, Inc. | High rate stimulation method for deep, large bore completions |
US8439116B2 (en) | 2009-07-24 | 2013-05-14 | Halliburton Energy Services, Inc. | Method for inducing fracture complexity in hydraulically fractured horizontal well completions |
US8794322B2 (en) | 2008-10-10 | 2014-08-05 | Halliburton Energy Services, Inc. | Additives to suppress silica scale build-up |
US8881811B2 (en) | 2008-10-10 | 2014-11-11 | Halliburton Energy Services, Inc. | Additives to suppress silica scale build-up and methods of use thereof |
US8561696B2 (en) | 2008-11-18 | 2013-10-22 | Schlumberger Technology Corporation | Method of placing ball sealers for fluid diversion |
US7775285B2 (en) * | 2008-11-19 | 2010-08-17 | Halliburton Energy Services, Inc. | Apparatus and method for servicing a wellbore |
US20100132946A1 (en) | 2008-12-01 | 2010-06-03 | Matthew Robert George Bell | Method for the Enhancement of Injection Activities and Stimulation of Oil and Gas Production |
US9080431B2 (en) * | 2008-12-01 | 2015-07-14 | Geodynamics, Inc. | Method for perforating a wellbore in low underbalance systems |
US8074715B2 (en) * | 2009-01-15 | 2011-12-13 | Halliburton Energy Services, Inc. | Methods of setting particulate plugs in horizontal well bores using low-rate slurries |
US8631872B2 (en) * | 2009-09-24 | 2014-01-21 | Halliburton Energy Services, Inc. | Complex fracturing using a straddle packer in a horizontal wellbore |
US9796918B2 (en) | 2013-01-30 | 2017-10-24 | Halliburton Energy Services, Inc. | Wellbore servicing fluids and methods of making and using same |
US8887803B2 (en) | 2012-04-09 | 2014-11-18 | Halliburton Energy Services, Inc. | Multi-interval wellbore treatment method |
US9016376B2 (en) | 2012-08-06 | 2015-04-28 | Halliburton Energy Services, Inc. | Method and wellbore servicing apparatus for production completion of an oil and gas well |
US7762329B1 (en) | 2009-01-27 | 2010-07-27 | Halliburton Energy Services, Inc. | Methods for servicing well bores with hardenable resin compositions |
US7882894B2 (en) | 2009-02-20 | 2011-02-08 | Halliburton Energy Services, Inc. | Methods for completing and stimulating a well bore |
US7998910B2 (en) | 2009-02-24 | 2011-08-16 | Halliburton Energy Services, Inc. | Treatment fluids comprising relative permeability modifiers and methods of use |
US8109335B2 (en) * | 2009-07-13 | 2012-02-07 | Halliburton Energy Services, Inc. | Degradable diverting agents and associated methods |
US8450391B2 (en) * | 2009-07-29 | 2013-05-28 | Halliburton Energy Services, Inc. | Weighted elastomers, cement compositions comprising weighted elastomers, and methods of use |
US8623936B2 (en) | 2009-07-29 | 2014-01-07 | Halliburton Energy Services, Inc. | Weighted elastomers, cement compositions comprising weighted elastomers, and methods of use |
US9023770B2 (en) * | 2009-07-30 | 2015-05-05 | Halliburton Energy Services, Inc. | Increasing fracture complexity in ultra-low permeable subterranean formation using degradable particulate |
US8657003B2 (en) * | 2010-12-01 | 2014-02-25 | Halliburton Energy Services, Inc. | Methods of providing fluid loss control or diversion |
US8853137B2 (en) | 2009-07-30 | 2014-10-07 | Halliburton Energy Services, Inc. | Increasing fracture complexity in ultra-low permeable subterranean formation using degradable particulate |
US8697612B2 (en) | 2009-07-30 | 2014-04-15 | Halliburton Energy Services, Inc. | Increasing fracture complexity in ultra-low permeable subterranean formation using degradable particulate |
US8420576B2 (en) | 2009-08-10 | 2013-04-16 | Halliburton Energy Services, Inc. | Hydrophobically and cationically modified relative permeability modifiers and associated methods |
US8695710B2 (en) | 2011-02-10 | 2014-04-15 | Halliburton Energy Services, Inc. | Method for individually servicing a plurality of zones of a subterranean formation |
US8668012B2 (en) | 2011-02-10 | 2014-03-11 | Halliburton Energy Services, Inc. | System and method for servicing a wellbore |
US8668016B2 (en) | 2009-08-11 | 2014-03-11 | Halliburton Energy Services, Inc. | System and method for servicing a wellbore |
US8276675B2 (en) | 2009-08-11 | 2012-10-02 | Halliburton Energy Services Inc. | System and method for servicing a wellbore |
US8272443B2 (en) * | 2009-11-12 | 2012-09-25 | Halliburton Energy Services Inc. | Downhole progressive pressurization actuated tool and method of using the same |
US8739881B2 (en) | 2009-12-30 | 2014-06-03 | W. Lynn Frazier | Hydrostatic flapper stimulation valve and method |
US8347960B2 (en) * | 2010-01-25 | 2013-01-08 | Water Tectonics, Inc. | Method for using electrocoagulation in hydraulic fracturing |
US8210257B2 (en) | 2010-03-01 | 2012-07-03 | Halliburton Energy Services Inc. | Fracturing a stress-altered subterranean formation |
US8297358B2 (en) | 2010-07-16 | 2012-10-30 | Baker Hughes Incorporated | Auto-production frac tool |
US8579023B1 (en) | 2010-10-29 | 2013-11-12 | Exelis Inc. | Composite downhole tool with ratchet locking mechanism |
US8470746B2 (en) | 2010-11-30 | 2013-06-25 | Halliburton Energy Services, Inc. | Methods relating to the stabilization of hydrophobically modified hydrophilic polymer treatment fluids under alkaline conditions |
US8727002B2 (en) | 2010-12-14 | 2014-05-20 | Halliburton Energy Services, Inc. | Acidic treatment fluids containing non-polymeric silica scale control additives and methods related thereto |
NZ612773A (en) * | 2010-12-14 | 2014-09-26 | Altarock Energy Inc | High temperature temporary diverter and lost circulation material |
US8770276B1 (en) | 2011-04-28 | 2014-07-08 | Exelis, Inc. | Downhole tool with cones and slips |
US9034803B2 (en) | 2011-04-29 | 2015-05-19 | Schlumberger Technology Corporation | Fluids comprising chitosan crosslinked by titanate |
US8905133B2 (en) * | 2011-05-11 | 2014-12-09 | Schlumberger Technology Corporation | Methods of zonal isolation and treatment diversion |
US10808497B2 (en) * | 2011-05-11 | 2020-10-20 | Schlumberger Technology Corporation | Methods of zonal isolation and treatment diversion |
US8869898B2 (en) | 2011-05-17 | 2014-10-28 | Baker Hughes Incorporated | System and method for pinpoint fracturing initiation using acids in open hole wellbores |
US8893811B2 (en) | 2011-06-08 | 2014-11-25 | Halliburton Energy Services, Inc. | Responsively activated wellbore stimulation assemblies and methods of using the same |
US9920600B2 (en) | 2011-06-10 | 2018-03-20 | Schlumberger Technology Corporation | Multi-stage downhole hydraulic stimulation assembly |
US8899334B2 (en) | 2011-08-23 | 2014-12-02 | Halliburton Energy Services, Inc. | System and method for servicing a wellbore |
US8662178B2 (en) | 2011-09-29 | 2014-03-04 | Halliburton Energy Services, Inc. | Responsively activated wellbore stimulation assemblies and methods of using the same |
AU2012318528A1 (en) | 2011-10-07 | 2014-05-22 | Boral Ip Holdings (Australia) Pty Limited | Inorganic polymer/organic polymer composites and methods of making same |
US8864901B2 (en) | 2011-11-30 | 2014-10-21 | Boral Ip Holdings (Australia) Pty Limited | Calcium sulfoaluminate cement-containing inorganic polymer compositions and methods of making same |
US8991509B2 (en) | 2012-04-30 | 2015-03-31 | Halliburton Energy Services, Inc. | Delayed activation activatable stimulation assembly |
US8997859B1 (en) | 2012-05-11 | 2015-04-07 | Exelis, Inc. | Downhole tool with fluted anvil |
US10023783B2 (en) | 2012-06-23 | 2018-07-17 | Pumprock, Llc | Compositions and processes for downhole cementing operations |
US8387695B1 (en) * | 2012-06-23 | 2013-03-05 | Newbasis West Llc | Compositions and processes for downhole cementing operations |
US9784070B2 (en) | 2012-06-29 | 2017-10-10 | Halliburton Energy Services, Inc. | System and method for servicing a wellbore |
US9840896B2 (en) * | 2012-09-21 | 2017-12-12 | Thru Tubing Solutions, Inc. | Acid soluble abrasive material and method of use |
US8967264B2 (en) * | 2012-09-25 | 2015-03-03 | Halliburton Energy Services, Inc. | Methods of enhancing fracturing stimulation in subterranean formations using in situ foam generation and pressure pulsing |
US10138707B2 (en) | 2012-11-13 | 2018-11-27 | Exxonmobil Upstream Research Company | Method for remediating a screen-out during well completion |
WO2014099207A1 (en) * | 2012-12-21 | 2014-06-26 | Exxonmobil Upstream Research Company | Fluid plugs as downhole sealing devices and systems and methods including the same |
WO2014099208A1 (en) | 2012-12-21 | 2014-06-26 | Exxonmobil Upstream Research Company | Systems and methods for stimulating a multi-zone subterranean formation |
CA2894504C (en) | 2012-12-21 | 2016-10-11 | Exxonmobil Upstream Research Company | Flow control assemblies for downhole operations and systems and methods including the same |
WO2014099306A2 (en) | 2012-12-21 | 2014-06-26 | Exxonmobil Upstream Research Company | Flow control assemblies for downhole operations and systems and methods including the same |
US9038717B2 (en) * | 2013-03-07 | 2015-05-26 | Halliburton Energy Services, Inc. | Methods of transporting proppant particulates in a subterranean formation |
WO2015112186A1 (en) * | 2014-01-21 | 2015-07-30 | Baker Hughes Incorporated | Method of improving cleanout of a wellbore |
US9790762B2 (en) | 2014-02-28 | 2017-10-17 | Exxonmobil Upstream Research Company | Corrodible wellbore plugs and systems and methods including the same |
WO2015156800A1 (en) * | 2014-04-09 | 2015-10-15 | Halliburton Energy Services, Inc. | Water-soluble linear polyphosphazenes in water-based fluids for use in wells or pipelines |
US20160347986A1 (en) * | 2014-05-13 | 2016-12-01 | Halliburton Energy Services, Inc. | Degradable Fluid Sealing Compositions Incorporating Non-Degradable Microparticulates And Methods For Use Thereof |
CN104121005B (en) * | 2014-07-15 | 2016-10-05 | äøåå¤§å¦ | High energy air stream drives proppant imports the equipment on underground fracture stratum |
US10738577B2 (en) | 2014-07-22 | 2020-08-11 | Schlumberger Technology Corporation | Methods and cables for use in fracturing zones in a well |
US10001613B2 (en) | 2014-07-22 | 2018-06-19 | Schlumberger Technology Corporation | Methods and cables for use in fracturing zones in a well |
US9856720B2 (en) | 2014-08-21 | 2018-01-02 | Exxonmobil Upstream Research Company | Bidirectional flow control device for facilitating stimulation treatments in a subterranean formation |
AU2014406526B2 (en) * | 2014-09-15 | 2018-02-08 | Halliburton Energy Services, Inc. | Resin and hardener consolidation composition |
US9951596B2 (en) | 2014-10-16 | 2018-04-24 | Exxonmobil Uptream Research Company | Sliding sleeve for stimulating a horizontal wellbore, and method for completing a wellbore |
WO2016076747A1 (en) * | 2014-11-14 | 2016-05-19 | Schlumberger Canada Limited | Chemical assisted selective diversion during multistage well treatments |
US9810051B2 (en) | 2014-11-20 | 2017-11-07 | Thru Tubing Solutions, Inc. | Well completion |
US20160168969A1 (en) * | 2014-12-15 | 2016-06-16 | Oil Well Consulting, LLC | Method for Increasing Productivity of Wells |
US9845658B1 (en) | 2015-04-17 | 2017-12-19 | Albany International Corp. | Lightweight, easily drillable or millable slip for composite frac, bridge and drop ball plugs |
US10233719B2 (en) | 2015-04-28 | 2019-03-19 | Thru Tubing Solutions, Inc. | Flow control in subterranean wells |
US9567826B2 (en) | 2015-04-28 | 2017-02-14 | Thru Tubing Solutions, Inc. | Flow control in subterranean wells |
US10774612B2 (en) | 2015-04-28 | 2020-09-15 | Thru Tubing Solutions, Inc. | Flow control in subterranean wells |
US9567824B2 (en) | 2015-04-28 | 2017-02-14 | Thru Tubing Solutions, Inc. | Fibrous barriers and deployment in subterranean wells |
US9523267B2 (en) | 2015-04-28 | 2016-12-20 | Thru Tubing Solutions, Inc. | Flow control in subterranean wells |
US11851611B2 (en) | 2015-04-28 | 2023-12-26 | Thru Tubing Solutions, Inc. | Flow control in subterranean wells |
US10655427B2 (en) | 2015-04-28 | 2020-05-19 | Thru Tubing Solutions, Inc. | Flow control in subterranean wells |
US10641069B2 (en) | 2015-04-28 | 2020-05-05 | Thru Tubing Solutions, Inc. | Flow control in subterranean wells |
US9816341B2 (en) | 2015-04-28 | 2017-11-14 | Thru Tubing Solutions, Inc. | Plugging devices and deployment in subterranean wells |
US10851615B2 (en) | 2015-04-28 | 2020-12-01 | Thru Tubing Solutions, Inc. | Flow control in subterranean wells |
US9708883B2 (en) | 2015-04-28 | 2017-07-18 | Thru Tubing Solutions, Inc. | Flow control in subterranean wells |
US9745820B2 (en) | 2015-04-28 | 2017-08-29 | Thru Tubing Solutions, Inc. | Plugging device deployment in subterranean wells |
US9567825B2 (en) | 2015-04-28 | 2017-02-14 | Thru Tubing Solutions, Inc. | Flow control in subterranean wells |
US10513653B2 (en) | 2015-04-28 | 2019-12-24 | Thru Tubing Solutions, Inc. | Flow control in subterranean wells |
US20180142137A1 (en) * | 2015-05-27 | 2018-05-24 | Lubrizol Oilfield Solutions, Inc. | Aggregating compositions, modified particulate solid compositions, and methods for making and using same |
US10753174B2 (en) | 2015-07-21 | 2020-08-25 | Thru Tubing Solutions, Inc. | Plugging device deployment |
WO2017079210A1 (en) * | 2015-11-02 | 2017-05-11 | Board Of Regents, The University Of Texas System | Acid soluble diverting agents for refracturing applications |
CA3001837C (en) | 2015-11-12 | 2021-05-04 | Halliburton Energy Services, Inc. | Method for fracturing a formation |
US20170159419A1 (en) | 2015-12-02 | 2017-06-08 | Randy C. Tolman | Selective Stimulation Ports, Wellbore Tubulars That Include Selective Stimulation Ports, And Methods Of Operating The Same |
US10196886B2 (en) | 2015-12-02 | 2019-02-05 | Exxonmobil Upstream Research Company | Select-fire, downhole shockwave generation devices, hydrocarbon wells that include the shockwave generation devices, and methods of utilizing the same |
US10309195B2 (en) | 2015-12-04 | 2019-06-04 | Exxonmobil Upstream Research Company | Selective stimulation ports including sealing device retainers and methods of utilizing the same |
US9920589B2 (en) | 2016-04-06 | 2018-03-20 | Thru Tubing Solutions, Inc. | Methods of completing a well and apparatus therefor |
US10927639B2 (en) | 2016-12-13 | 2021-02-23 | Thru Tubing Solutions, Inc. | Methods of completing a well and apparatus therefor |
CA3046920C (en) | 2017-03-02 | 2023-07-04 | Halliburton Energy Services, Inc. | Control of far field fracture diversion by low rate treatment stage |
WO2018200698A1 (en) | 2017-04-25 | 2018-11-01 | Thru Tubing Solutions, Inc. | Plugging undesired openings in fluid conduits |
US11022248B2 (en) | 2017-04-25 | 2021-06-01 | Thru Tubing Solutions, Inc. | Plugging undesired openings in fluid vessels |
CN107255020B (en) * | 2017-06-14 | 2019-08-30 | äøå½ē³ę²¹éå¢ęø¤ęµ·é»ę¢å·„ēØęéå ¬åø | A kind of workover fluid dehydration liquid and its dewatering for solidifying water |
US10875209B2 (en) | 2017-06-19 | 2020-12-29 | Nuwave Industries Inc. | Waterjet cutting tool |
RU2655310C1 (en) * | 2017-08-04 | 2018-05-25 | ŠŃŠ±Š»ŠøŃŠ½Š¾Šµ Š°ŠŗŃŠøŠ¾Š½ŠµŃŠ½Š¾Šµ Š¾Š±ŃŠµŃŃŠ²Š¾ "Š¢Š°ŃŠ½ŠµŃŃŃ" ŠøŠ¼ŠµŠ½Šø Š.Š. ŠØŠ°ŃŠøŠ½Š° | Method for determining efficiency of hydraulic well formation fracturing |
US10385261B2 (en) | 2017-08-22 | 2019-08-20 | Covestro Llc | Coated particles, methods for their manufacture and for their use as proppants |
US11254860B2 (en) | 2017-10-31 | 2022-02-22 | Halliburton Energy Services, Inc. | Diversion using solid particulates |
WO2019131939A1 (en) * | 2017-12-28 | 2019-07-04 | äøč±ć±ćć«ć«ę Ŗå¼ä¼ē¤¾ | Diverting agent and method for occluding cracks on well using same |
US10364659B1 (en) | 2018-09-27 | 2019-07-30 | Exxonmobil Upstream Research Company | Methods and devices for restimulating a well completion |
RU2727986C1 (en) * | 2020-02-04 | 2020-07-28 | ŠŠ»ŠµŠŗŃŠ°Š½Š“Ń ŠŠ°Š»ŠµŃŃŠµŠ²ŠøŃ ŠŠ¾ŃŠ¾ŃŠøŠ»Š¾Š² | Oil displacement composition |
CN112647916B (en) * | 2020-12-22 | 2023-03-24 | äøęµ·ē³ę²¹(äøå½)ęéå ¬åø | Well selecting and layer selecting method and system for offshore low-permeability oilfield fracturing technology |
Family Cites Families (173)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3123138A (en) | 1964-03-03 | robichaux | ||
US2238671A (en) | 1940-02-09 | 1941-04-15 | Du Pont | Method of treating wells |
US2703316A (en) | 1951-06-05 | 1955-03-01 | Du Pont | Polymers of high melting lactide |
US3765804A (en) | 1951-08-13 | 1973-10-16 | Brandon O | Apparatus for producing variable high frequency vibrations in a liquid medium |
US2869642A (en) | 1954-09-14 | 1959-01-20 | Texas Co | Method of treating subsurface formations |
US3047067A (en) | 1958-09-08 | 1962-07-31 | Jersey Prod Res Co | Sand consolidation method |
US3297086A (en) | 1962-03-30 | 1967-01-10 | Exxon Production Research Co | Sand consolidation method |
US3272650A (en) | 1963-02-21 | 1966-09-13 | Union Carbide Corp | Process for cleaning conduits |
US3199590A (en) | 1963-02-25 | 1965-08-10 | Halliburton Co | Method of consolidating incompetent sands and composition therefor |
US3316965A (en) | 1963-08-05 | 1967-05-02 | Union Oil Co | Material and process for treating subterranean formations |
US3176768A (en) | 1964-07-27 | 1965-04-06 | California Research Corp | Sand consolidation |
US3492147A (en) | 1964-10-22 | 1970-01-27 | Halliburton Co | Method of coating particulate solids with an infusible resin |
US3375872A (en) | 1965-12-02 | 1968-04-02 | Halliburton Co | Method of plugging or sealing formations with acidic silicic acid solution |
US3308885A (en) | 1965-12-28 | 1967-03-14 | Union Oil Co | Treatment of subsurface hydrocarbon fluid-bearing formations to reduce water production therefrom |
US3404735A (en) | 1966-11-01 | 1968-10-08 | Halliburton Co | Sand control method |
US3336980A (en) * | 1967-02-09 | 1967-08-22 | Exxon Production Research Co | Sand control in wells |
US3415320A (en) | 1967-02-09 | 1968-12-10 | Halliburton Co | Method of treating clay-containing earth formations |
US3659651A (en) | 1970-08-17 | 1972-05-02 | Exxon Production Research Co | Hydraulic fracturing using reinforced resin pellets |
US4305463A (en) | 1979-10-31 | 1981-12-15 | Oil Trieval Corporation | Oil recovery method and apparatus |
US3681287A (en) | 1971-03-03 | 1972-08-01 | Quaker Oats Co | Siliceous materials bound with resin containing organosilane coupling agent |
US3842911A (en) | 1971-04-26 | 1974-10-22 | Halliburton Co | Method of fracture acidizing a well formation |
US3768564A (en) | 1971-04-26 | 1973-10-30 | Halliburton Co | Method of fracture acidizing a well formation |
US3708013A (en) * | 1971-05-03 | 1973-01-02 | Mobil Oil Corp | Method and apparatus for obtaining an improved gravel pack |
US3709298A (en) * | 1971-05-20 | 1973-01-09 | Shell Oil Co | Sand pack-aided formation sand consolidation |
US3784585A (en) | 1971-10-21 | 1974-01-08 | American Cyanamid Co | Water-degradable resins containing recurring,contiguous,polymerized glycolide units and process for preparing same |
US3754598A (en) | 1971-11-08 | 1973-08-28 | Phillips Petroleum Co | Method for producing a hydrocarbon-containing formation |
US3819525A (en) | 1972-08-21 | 1974-06-25 | Avon Prod Inc | Cosmetic cleansing preparation |
US3857444A (en) | 1972-10-06 | 1974-12-31 | Dow Chemical Co | Method for forming a consolidated gravel pack in a subterranean formation |
US3854533A (en) | 1972-12-07 | 1974-12-17 | Dow Chemical Co | Method for forming a consolidated gravel pack in a subterranean formation |
US3828854A (en) | 1973-04-16 | 1974-08-13 | Shell Oil Co | Dissolving siliceous materials with self-acidifying liquid |
US3912692A (en) | 1973-05-03 | 1975-10-14 | American Cyanamid Co | Process for polymerizing a substantially pure glycolide composition |
US4042032A (en) | 1973-06-07 | 1977-08-16 | Halliburton Company | Methods of consolidating incompetent subterranean formations using aqueous treating solutions |
US3888311A (en) | 1973-10-01 | 1975-06-10 | Exxon Production Research Co | Hydraulic fracturing method |
US4015995A (en) | 1973-11-23 | 1977-04-05 | Chevron Research Company | Method for delaying the setting of an acid-settable liquid in a terrestrial zone |
US3863709A (en) | 1973-12-20 | 1975-02-04 | Mobil Oil Corp | Method of recovering geothermal energy |
US3948672A (en) | 1973-12-28 | 1976-04-06 | Texaco Inc. | Permeable cement composition and method |
US3955993A (en) | 1973-12-28 | 1976-05-11 | Texaco Inc. | Method and composition for stabilizing incompetent oil-containing formations |
US3868998A (en) | 1974-05-15 | 1975-03-04 | Shell Oil Co | Self-acidifying treating fluid positioning process |
US3960736A (en) | 1974-06-03 | 1976-06-01 | The Dow Chemical Company | Self-breaking viscous aqueous solutions and the use thereof in fracturing subterranean formations |
US4172066A (en) | 1974-06-21 | 1979-10-23 | The Dow Chemical Company | Cross-linked, water-swellable polymer microgels |
US4031958A (en) | 1975-06-13 | 1977-06-28 | Union Oil Company Of California | Plugging of water-producing zones in a subterranean formation |
US3983941A (en) * | 1975-11-10 | 1976-10-05 | Mobil Oil Corporation | Well completion technique for sand control |
US4070865A (en) | 1976-03-10 | 1978-01-31 | Halliburton Company | Method of consolidating porous formations using vinyl polymer sealer with divinylbenzene crosslinker |
US4008763A (en) | 1976-05-20 | 1977-02-22 | Atlantic Richfield Company | Well treatment method |
US4029148A (en) | 1976-09-13 | 1977-06-14 | Atlantic Richfield Company | Well fracturing method |
US4074760A (en) | 1976-11-01 | 1978-02-21 | The Dow Chemical Company | Method for forming a consolidated gravel pack |
US4085801A (en) | 1976-11-05 | 1978-04-25 | Continental Oil Company | Control of incompetent formations with thickened acid-settable resin compositions |
US4169798A (en) | 1976-11-26 | 1979-10-02 | Celanese Corporation | Well-treating compositions |
US4127173A (en) | 1977-07-28 | 1978-11-28 | Exxon Production Research Company | Method of gravel packing a well |
GB1569063A (en) | 1978-05-22 | 1980-06-11 | Shell Int Research | Formation parts around a borehole method for forming channels of high fluid conductivity in |
US4291766A (en) | 1979-04-09 | 1981-09-29 | Shell Oil Company | Process for consolidating water-wet sands with an epoxy resin-forming solution |
US4273187A (en) | 1979-07-30 | 1981-06-16 | Texaco Inc. | Petroleum recovery chemical retention prediction technique |
US4443380A (en) | 1979-08-31 | 1984-04-17 | Asahi-Dow Limited | Organic europlum salt phosphor |
FR2473180A1 (en) | 1980-01-08 | 1981-07-10 | Petroles Cie Francaise | METHOD OF TRACING THE DRILLING MUD BY DETERMINING THE CONCENTRATION OF A SOLUBLE ION |
US4353806A (en) | 1980-04-03 | 1982-10-12 | Exxon Research And Engineering Company | Polymer-microemulsion complexes for the enhanced recovery of oil |
US4336842A (en) | 1981-01-05 | 1982-06-29 | Graham John W | Method of treating wells using resin-coated particles |
US4415805A (en) | 1981-06-18 | 1983-11-15 | Dresser Industries, Inc. | Method and apparatus for evaluating multiple stage fracturing or earth formations surrounding a borehole |
US4716964A (en) | 1981-08-10 | 1988-01-05 | Exxon Production Research Company | Use of degradable ball sealers to seal casing perforations in well treatment fluid diversion |
US4387769A (en) | 1981-08-10 | 1983-06-14 | Exxon Production Research Co. | Method for reducing the permeability of subterranean formations |
US4460052A (en) | 1981-08-10 | 1984-07-17 | Judith Gockel | Prevention of lost circulation of drilling muds |
US4498995A (en) | 1981-08-10 | 1985-02-12 | Judith Gockel | Lost circulation drilling fluid |
US4526695A (en) | 1981-08-10 | 1985-07-02 | Exxon Production Research Co. | Composition for reducing the permeability of subterranean formations |
US4564459A (en) | 1981-12-03 | 1986-01-14 | Baker Oil Tools, Inc. | Proppant charge and method |
US4443347A (en) | 1981-12-03 | 1984-04-17 | Baker Oil Tools, Inc. | Proppant charge and method |
US4664819A (en) | 1981-12-03 | 1987-05-12 | Baker Oil Tools, Inc. | Proppant charge and method |
US4494605A (en) | 1981-12-11 | 1985-01-22 | Texaco Inc. | Sand control employing halogenated, oil soluble hydrocarbons |
US4439489A (en) | 1982-02-16 | 1984-03-27 | Acme Resin Corporation | Particles covered with a cured infusible thermoset film and process for their production |
US4470915A (en) | 1982-09-27 | 1984-09-11 | Halliburton Company | Method and compositions for fracturing subterranean formations |
US4553596A (en) | 1982-10-27 | 1985-11-19 | Santrol Products, Inc. | Well completion technique |
US4501328A (en) | 1983-03-14 | 1985-02-26 | Mobil Oil Corporation | Method of consolidation of oil bearing sands |
US4527627A (en) | 1983-07-28 | 1985-07-09 | Santrol Products, Inc. | Method of acidizing propped fractures |
US4493875A (en) | 1983-12-09 | 1985-01-15 | Minnesota Mining And Manufacturing Company | Proppant for well fractures and method of making same |
US4681165A (en) | 1984-03-01 | 1987-07-21 | Dowell Schlumberger Incorporated | Aqueous chemical wash compositions |
US4541489A (en) | 1984-03-19 | 1985-09-17 | Phillips Petroleum Company | Method of removing flow-restricting materials from wells |
US4546012A (en) | 1984-04-26 | 1985-10-08 | Carbomedics, Inc. | Level control for a fluidized bed |
GB8412423D0 (en) | 1984-05-16 | 1984-06-20 | Allied Colloids Ltd | Polymeric compositions |
KR920006865B1 (en) | 1984-05-18 | 1992-08-21 | ģģ±ķ¤ ģ ėė²ģķ° ķ ķ¬ėė¬ģ§ ģ“ģģ°ģģģ“ģø ģøģ½ģ¤ķ¼ė ģ“ķ°ė | Method and apparatus for coating particles or liquid droplets |
US4715967A (en) | 1985-12-27 | 1987-12-29 | E. I. Du Pont De Nemours And Company | Composition and method for temporarily reducing permeability of subterranean formations |
US4665988A (en) | 1986-04-04 | 1987-05-19 | Halliburton Company | Method of preparation of variable permeability fill material for use in subterranean formations |
EP0421980B1 (en) | 1986-04-18 | 1993-08-25 | Hosokawa Micron Corporation | Particulate material treating apparatus |
US4694905A (en) | 1986-05-23 | 1987-09-22 | Acme Resin Corporation | Precured coated particulate material |
US4785884A (en) | 1986-05-23 | 1988-11-22 | Acme Resin Corporation | Consolidation of partially cured resin coated particulate material |
US4669543A (en) | 1986-05-23 | 1987-06-02 | Halliburton Company | Methods and compositions for consolidating solids in subterranean zones |
US4693808A (en) | 1986-06-16 | 1987-09-15 | Shell Oil Company | Downflow fluidized catalytic cranking reactor process and apparatus with quick catalyst separation means in the bottom thereof |
US4649998A (en) | 1986-07-02 | 1987-03-17 | Texaco Inc. | Sand consolidation method employing latex |
US4683954A (en) | 1986-09-05 | 1987-08-04 | Halliburton Company | Composition and method of stimulating subterranean formations |
US4733729A (en) | 1986-09-08 | 1988-03-29 | Dowell Schlumberger Incorporated | Matched particle/liquid density well packing technique |
MX168601B (en) | 1986-10-01 | 1993-06-01 | Air Prod & Chem | PROCEDURE FOR THE PREPARATION OF A HIGH MOLECULAR WEIGHT VINYLAMINE HOMOPOLYMER |
US4787453A (en) | 1986-10-30 | 1988-11-29 | Union Oil Company Of California | Permeability stabilization in subterranean formations containing particulate matter |
US4772646A (en) | 1986-11-17 | 1988-09-20 | Halliburton Company | Concentrated hydrophilic polymer suspensions |
FR2618846A2 (en) | 1986-11-25 | 1989-02-03 | Schlumberger Cie Dowell | PROCESS FOR SEALING UNDERGROUND FORMATIONS, PARTICULARLY IN THE OIL DRILLING SECTOR AND CORRESPONDING COMPOSITIONS AND APPLICATIONS |
US4856590A (en) * | 1986-11-28 | 1989-08-15 | Mike Caillier | Process for washing through filter media in a production zone with a pre-packed screen and coil tubing |
US4739832A (en) | 1986-12-24 | 1988-04-26 | Mobil Oil Corporation | Method for improving high impulse fracturing |
US4850430A (en) | 1987-02-04 | 1989-07-25 | Dowell Schlumberger Incorporated | Matched particle/liquid density well packing technique |
US4796701A (en) | 1987-07-30 | 1989-01-10 | Dowell Schlumberger Incorporated | Pyrolytic carbon coating of media improves gravel packing and fracturing capabilities |
US4829100A (en) | 1987-10-23 | 1989-05-09 | Halliburton Company | Continuously forming and transporting consolidatable resin coated particulate materials in aqueous gels |
US4817721A (en) | 1987-12-14 | 1989-04-04 | Conoco Inc. | Reducing the permeability of a rock formation |
US4800960A (en) | 1987-12-18 | 1989-01-31 | Texaco Inc. | Consolidatable gravel pack method |
US4809783A (en) | 1988-01-14 | 1989-03-07 | Halliburton Services | Method of dissolving organic filter cake |
US4848467A (en) | 1988-02-16 | 1989-07-18 | Conoco Inc. | Formation fracturing process |
US4886354A (en) | 1988-05-06 | 1989-12-12 | Conoco Inc. | Method and apparatus for measuring crystal formation |
US4842072A (en) | 1988-07-25 | 1989-06-27 | Texaco Inc. | Sand consolidation methods |
US4986353A (en) * | 1988-09-14 | 1991-01-22 | Conoco Inc. | Placement process for oil field chemicals |
US4848470A (en) | 1988-11-21 | 1989-07-18 | Acme Resin Corporation | Process for removing flow-restricting materials from wells |
US4895207A (en) * | 1988-12-19 | 1990-01-23 | Texaco, Inc. | Method and fluid for placing resin coated gravel or sand in a producing oil well |
US4986355A (en) * | 1989-05-18 | 1991-01-22 | Conoco Inc. | Process for the preparation of fluid loss additive and gel breaker |
US5182051A (en) * | 1990-01-17 | 1993-01-26 | Protechnics International, Inc. | Raioactive tracing with particles |
US6184311B1 (en) * | 1990-03-26 | 2001-02-06 | Courtaulds Coatings (Holdings) Limited | Powder coating composition of semi-crystalline polyester and curing agent |
US5082056A (en) * | 1990-10-16 | 1992-01-21 | Marathon Oil Company | In situ reversible crosslinked polymer gel used in hydrocarbon recovery applications |
US5105886A (en) * | 1990-10-24 | 1992-04-21 | Mobil Oil Corporation | Method for the control of solids accompanying hydrocarbon production from subterranean formations |
US5095987A (en) * | 1991-01-31 | 1992-03-17 | Halliburton Company | Method of forming and using high density particulate slurries for well completion |
US5278203A (en) * | 1991-03-21 | 1994-01-11 | Halliburton Company | Method of preparing and improved liquid gelling agent concentrate and suspendable gelling agent |
US5178218A (en) * | 1991-06-19 | 1993-01-12 | Oryx Energy Company | Method of sand consolidation with resin |
CA2062395A1 (en) * | 1991-06-21 | 1992-12-22 | Robert H. Friedman | Sand consolidation methods |
US5293939A (en) * | 1992-07-31 | 1994-03-15 | Texaco Chemical Company | Formation treating methods |
US5396957A (en) * | 1992-09-29 | 1995-03-14 | Halliburton Company | Well completions with expandable casing portions |
US5338822A (en) * | 1992-10-02 | 1994-08-16 | Cargill, Incorporated | Melt-stable lactide polymer composition and process for manufacture thereof |
US5295542A (en) * | 1992-10-05 | 1994-03-22 | Halliburton Company | Well gravel packing methods |
CA2119316C (en) * | 1993-04-05 | 2006-01-03 | Roger J. Card | Control of particulate flowback in subterranean wells |
US5377759A (en) * | 1993-05-20 | 1995-01-03 | Texaco Inc. | Formation treating methods |
US5422183A (en) * | 1993-06-01 | 1995-06-06 | Santrol, Inc. | Composite and reinforced coatings on proppants and particles |
US5359026A (en) * | 1993-07-30 | 1994-10-25 | Cargill, Incorporated | Poly(lactide) copolymer and process for manufacture thereof |
US5388648A (en) * | 1993-10-08 | 1995-02-14 | Baker Hughes Incorporated | Method and apparatus for sealing the juncture between a vertical well and one or more horizontal wells using deformable sealing means |
US5386874A (en) * | 1993-11-08 | 1995-02-07 | Halliburton Company | Perphosphate viscosity breakers in well fracture fluids |
US5381864A (en) * | 1993-11-12 | 1995-01-17 | Halliburton Company | Well treating methods using particulate blends |
US5559086A (en) * | 1993-12-13 | 1996-09-24 | Halliburton Company | Epoxy resin composition and well treatment method |
US5390741A (en) * | 1993-12-21 | 1995-02-21 | Halliburton Company | Remedial treatment methods for coal bed methane wells |
US5393810A (en) * | 1993-12-30 | 1995-02-28 | Halliburton Company | Method and composition for breaking crosslinked gels |
US5494178A (en) * | 1994-07-25 | 1996-02-27 | Alu Inc. | Display and decorative fixture apparatus |
US5499678A (en) * | 1994-08-02 | 1996-03-19 | Halliburton Company | Coplanar angular jetting head for well perforating |
US5498280A (en) * | 1994-11-14 | 1996-03-12 | Binney & Smith Inc. | Phosphorescent and fluorescent marking composition |
US5591700A (en) * | 1994-12-22 | 1997-01-07 | Halliburton Company | Fracturing fluid with encapsulated breaker |
US5649323A (en) * | 1995-01-17 | 1997-07-15 | Kalb; Paul D. | Composition and process for the encapsulation and stabilization of radioactive hazardous and mixed wastes |
US5604186A (en) * | 1995-02-15 | 1997-02-18 | Halliburton Company | Encapsulated enzyme breaker and method for use in treating subterranean formations |
US5501274A (en) * | 1995-03-29 | 1996-03-26 | Halliburton Company | Control of particulate flowback in subterranean wells |
US5775425A (en) * | 1995-03-29 | 1998-07-07 | Halliburton Energy Services, Inc. | Control of fine particulate flowback in subterranean wells |
US5497830A (en) * | 1995-04-06 | 1996-03-12 | Bj Services Company | Coated breaker for crosslinked acid |
US5604184A (en) * | 1995-04-10 | 1997-02-18 | Texaco, Inc. | Chemically inert resin coated proppant system for control of proppant flowback in hydraulically fractured wells |
DE19627469A1 (en) * | 1995-07-12 | 1997-01-16 | Sanyo Chemical Ind Ltd | Epoxy resin crosslinking agent and one-component epoxy resin composition |
US5595245A (en) * | 1995-08-04 | 1997-01-21 | Scott, Iii; George L. | Systems of injecting phenolic resin activator during subsurface fracture stimulation for enhanced oil recovery |
US6028113A (en) * | 1995-09-27 | 2000-02-22 | Sunburst Chemicals, Inc. | Solid sanitizers and cleaner disinfectants |
US5669448A (en) * | 1995-12-08 | 1997-09-23 | Halliburton Energy Services, Inc. | Overbalance perforating and stimulation method for wells |
US5704426A (en) * | 1996-03-20 | 1998-01-06 | Schlumberger Technology Corporation | Zonal isolation method and apparatus |
US5864003A (en) * | 1996-07-23 | 1999-01-26 | Georgia-Pacific Resins, Inc. | Thermosetting phenolic resin composition |
US5712314A (en) * | 1996-08-09 | 1998-01-27 | Texaco Inc. | Formulation for creating a pliable resin plug |
GB9619418D0 (en) * | 1996-09-18 | 1996-10-30 | Urlwin Smith Phillip L | Oil and gas field chemicals |
US5865936A (en) * | 1997-03-28 | 1999-02-02 | National Starch And Chemical Investment Holding Corporation | Rapid curing structural acrylic adhesive |
GB9708484D0 (en) * | 1997-04-25 | 1997-06-18 | Merck Sharp & Dohme | Therapeutic agents |
US6028534A (en) * | 1997-06-02 | 2000-02-22 | Schlumberger Technology Corporation | Formation data sensing with deployed remote sensors during well drilling |
US6169058B1 (en) * | 1997-06-05 | 2001-01-02 | Bj Services Company | Compositions and methods for hydraulic fracturing |
US5873413A (en) * | 1997-08-18 | 1999-02-23 | Halliburton Energy Services, Inc. | Methods of modifying subterranean strata properties |
US6177484B1 (en) * | 1997-11-03 | 2001-01-23 | Texaco Inc. | Combination catalyst/coupling agent for furan resin |
US6012524A (en) * | 1998-04-14 | 2000-01-11 | Halliburton Energy Services, Inc. | Remedial well bore sealing methods and compositions |
US6024170A (en) * | 1998-06-03 | 2000-02-15 | Halliburton Energy Services, Inc. | Methods of treating subterranean formation using borate cross-linking compositions |
US6016870A (en) * | 1998-06-11 | 2000-01-25 | Halliburton Energy Services, Inc. | Compositions and methods for consolidating unconsolidated subterranean zones |
US6006838A (en) * | 1998-10-12 | 1999-12-28 | Bj Services Company | Apparatus and method for stimulating multiple production zones in a wellbore |
US6446727B1 (en) * | 1998-11-12 | 2002-09-10 | Sclumberger Technology Corporation | Process for hydraulically fracturing oil and gas wells |
US6176315B1 (en) * | 1998-12-04 | 2001-01-23 | Halliburton Energy Services, Inc. | Preventing flow through subterranean zones |
US6196317B1 (en) * | 1998-12-15 | 2001-03-06 | Halliburton Energy Services, Inc. | Method and compositions for reducing the permeabilities of subterranean zones |
US6189615B1 (en) * | 1998-12-15 | 2001-02-20 | Marathon Oil Company | Application of a stabilized polymer gel to an alkaline treatment region for improved hydrocarbon recovery |
US6192985B1 (en) * | 1998-12-19 | 2001-02-27 | Schlumberger Technology Corporation | Fluids and techniques for maximizing fracture fluid clean-up |
US6244344B1 (en) * | 1999-02-09 | 2001-06-12 | Halliburton Energy Services, Inc. | Methods and compositions for cementing pipe strings in well bores |
US6187839B1 (en) * | 1999-03-03 | 2001-02-13 | Halliburton Energy Services, Inc. | Methods of sealing compositions and methods |
US6187834B1 (en) * | 1999-09-08 | 2001-02-13 | Dow Corning Corporation | Radiation curable silicone compositions |
US6253851B1 (en) * | 1999-09-20 | 2001-07-03 | Marathon Oil Company | Method of completing a well |
US6394184B2 (en) * | 2000-02-15 | 2002-05-28 | Exxonmobil Upstream Research Company | Method and apparatus for stimulation of multiple formation intervals |
US6357527B1 (en) * | 2000-05-05 | 2002-03-19 | Halliburton Energy Services, Inc. | Encapsulated breakers and method for use in treating subterranean formations |
US6202751B1 (en) * | 2000-07-28 | 2001-03-20 | Halliburton Energy Sevices, Inc. | Methods and compositions for forming permeable cement sand screens in well bores |
US6601648B2 (en) * | 2001-10-22 | 2003-08-05 | Charles D. Ebinger | Well completion method |
US6626241B2 (en) * | 2001-12-06 | 2003-09-30 | Halliburton Energy Services, Inc. | Method of frac packing through existing gravel packed screens |
US6962203B2 (en) * | 2003-03-24 | 2005-11-08 | Owen Oil Tools Lp | One trip completion process |
US7066258B2 (en) * | 2003-07-08 | 2006-06-27 | Halliburton Energy Services, Inc. | Reduced-density proppants and methods of using reduced-density proppants to enhance their transport in well bores and fractures |
US7036589B2 (en) * | 2003-08-14 | 2006-05-02 | Halliburton Energy Services, Inc. | Methods for fracturing stimulation |
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AU2005311147B2 (en) | 2010-06-17 |
CA2589798A1 (en) | 2006-06-08 |
WO2006059056A1 (en) | 2006-06-08 |
MX2007006620A (en) | 2008-01-11 |
AU2005311147A1 (en) | 2006-06-08 |
US20060118301A1 (en) | 2006-06-08 |
US7273099B2 (en) | 2007-09-25 |
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