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 perform 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.
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.
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:
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.
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
Referring now to
As shown in
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
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
As illustrated in
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
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
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
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 Okla. Another example of a suitable crosslinked aqueous gel is a borate fluid system utilized in the “Seaques®” fracturing service, commercially available from Halliburton Energy Services, Duncan, Okla. 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 Seal™” fluid loss control additive, commercially available from Halliburton Energy Services, Duncan, Okla. An example of a suitable degradable polymeric material is “BioBalls™” perforation ball sealers, commercially available from Santrol Corporation, Fresno, Tex.
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(ε-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 term “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. Pat. Nos. 5,853,048 and 5,833,000, the relevant disclosures of which are herein incorporated by reference.
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 1 percent by weight of the tackifying compound. Suitable multifunctional materials are described in U.S. Pat. No. 5,839,510, the relevant disclosure of which is herein incorporated by reference. Other suitable tackifying agents are described in U.S. Pat. No. 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 first 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)), acrylamido-methyl-propane sulfonate polymers, acrylamido-methyl-propane sulfonate derivative polymers, a thereof. Methods of determining suitable aqueous tackifier agents and additional disclosure on aqueous tackifier agents can be found in U.S. patent application Ser. No. 10/864,061 and filed Jun. 9, 2004 and U.S. patent application Ser. No. 10/864,618 and filed Jun. 9, 2004, the relevant disclosures of which are hereby incorporated by reference.
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, from 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. Pat. No. 6,439,309, the relevant disclosure of which is herein incorporated by reference.
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 300° F. It is within the ability of one skilled in the art, with the benefit 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 Okla. 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, Okla. 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.
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