WO2001074967A1 - Methods for reducing lost circulation in wellbores - Google Patents
Methods for reducing lost circulation in wellbores Download PDFInfo
- Publication number
- WO2001074967A1 WO2001074967A1 PCT/US2001/008278 US0108278W WO0174967A1 WO 2001074967 A1 WO2001074967 A1 WO 2001074967A1 US 0108278 W US0108278 W US 0108278W WO 0174967 A1 WO0174967 A1 WO 0174967A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- water
- fluids
- lost circulation
- polymer
- fluid
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 53
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 97
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- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
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- 229920003171 Poly (ethylene oxide) Polymers 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 244000124765 Salsola kali Species 0.000 description 1
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- TZCXTZWJZNENPQ-UHFFFAOYSA-L barium sulfate Chemical compound [Ba+2].[O-]S([O-])(=O)=O TZCXTZWJZNENPQ-UHFFFAOYSA-L 0.000 description 1
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- ZOMBKNNSYQHRCA-UHFFFAOYSA-J calcium sulfate hemihydrate Chemical compound O.[Ca+2].[Ca+2].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O ZOMBKNNSYQHRCA-UHFFFAOYSA-J 0.000 description 1
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- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 description 1
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- MDKGKXOCJGEUJW-UHFFFAOYSA-N suprofen Chemical compound C1=CC(C(C(O)=O)C)=CC=C1C(=O)C1=CC=CS1 MDKGKXOCJGEUJW-UHFFFAOYSA-N 0.000 description 1
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/50—Compositions for plastering borehole walls, i.e. compositions for temporary consolidation of borehole walls
- C09K8/504—Compositions based on water or polar solvents
- C09K8/506—Compositions based on water or polar solvents containing organic compounds
- C09K8/508—Compositions based on water or polar solvents containing organic compounds macromolecular compounds
- C09K8/512—Compositions based on water or polar solvents containing organic compounds macromolecular compounds containing cross-linking agents
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/02—Well-drilling compositions
- C09K8/03—Specific additives for general use in well-drilling compositions
- C09K8/035—Organic additives
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B21/00—Methods or apparatus for flushing boreholes, e.g. by use of exhaust air from motor
- E21B21/003—Means for stopping loss of drilling fluid
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K2208/00—Aspects relating to compositions of drilling or well treatment fluids
- C09K2208/04—Hulls, shells or bark containing well drilling or treatment fluids
Definitions
- This invention concerns the use of specially crosslinked polyacrylamide, water absorbing polymers for reducing lost circulation when aqueous drilling fluids are used and a method for reducing such lost circulation. These polymers are able to reach the areas of fissures and thief zones before absorbing water and expanding to plug those fissures and thief zones.
- Drilling fluids or drilling muds as they are sometimes called, are slurries of solids used in the drilling of wells in the earth for the purpose of recovering hydrocarbons and other fluid materials.
- Drilling fluids have a number of functions, the most important of which are lubricating the drilling tool and drill pipe which carries thgotool, removing formation cuttings from the well, counterbalancing formation pressures to prevent the inflow of gas, oil or water from permeable rocks which may be encountered at various levels as drilling continues, and holding the cuttings in suspension in the event of a shutdown in the drilling and the pumping of the drilling fluid.
- Drilling fluid can leave the borehole through large or small fissures or fractures in the formation or through pores in the rock matrix surrounding the borehole.
- Most wells are drilled with the intent of forming a filter cake of varying thickness on the sides of the borehole.
- the primary purpose of the filter cake is to reduce the large losses of drilling fluid to the surrounding formation.
- formation conditions frequently are encountered which may result in unacceptable losses of drilling fluid to the surrounding formation despite the type of drilling fluid employed and filter cake established.
- gunk-squeeze Another process that is employed to close off large lost circulation areas is referred to in the art as gunk-squeeze.
- a quantity of a powdered bentonite is mixed into diesel oil and pumped down the well bore. Water injection follows and if the water and bentonite will harden to form a gunky, semi- solid mass which can reduce lost circulation.
- This process must be carefully controlled; first the bentonite must be kept dry until it reaches the desired location in the well and then problems frequently occur in trying to mix the bentonite and water in the well. This method is disclosed in U.S. Patent No. 3,082,823.
- U.S. Patent No. 2,890,169 discloses a lost circulation fluid made by forming a slurry of bentonite and cement in oil. The slurry is mixed with a surfactant and water to form a composition comprising a water-in-oil emulsion having the bentonite and cement dispersed in the continuous oil phase. As this composition is pumped down the well bore, the oil expands and flocculates the bentonite which, under the right conditions, forms a cake on the wellbore surface in the lost circulation area. Ultimately, the settling of the cake of the walls will cause the emulsion to break thus causing the previously emulsified water to react with the cement to form a solid coating on the cake. But such a complex process can easily go wrong.
- U.S. Patent No. 3,448,800 discloses another method wherein a water soluble polymer is slurried in a non-aqueous medium and injected into a well. Another slurry of a mineral material such a barite, cement or plaster of paris is subsequently injected into the well to mix with the first slurry to form a cementlike plug in the wellbore.
- U.S. Patent No. 4,261 ,422 describes the use of an expandable clay such as bentonite or montmorillonite which is dispersed in a liquid hydrocarbon into the well. After injection the clay will expand on contact with water in the formation. Thus it is hoped that the expanding clay will close off water producing intervals, but not harm oil producing intervals.
- an expandable clay such as bentonite or montmorillonite
- U.S. Patent No. 3,078,920 uses a solution of a polymerized methacrylate dissolved in a non-aqueous solvent such as acetic acid, acetic anhydride, propionic acid and liquid aliphatic ketones such as acetone or methyl-ethyl ketone.
- a non-aqueous solvent such as acetic acid, acetic anhydride, propionic acid and liquid aliphatic ketones such as acetone or methyl-ethyl ketone.
- the methacrylate will expanchon contact with formation water in the water producing formations in the well.
- 4,503,170; 4,457,594; 4,445,576; 4,442,241; and 4,391,925 teach the use of a water expandable clay dispersed in the oily phase of a water-in-oil emulsion containing a surfactant to stabilize the emulsion and a polymer dispersed in the aqueous phase. When the emulsion is sheared, it breaks and a bentonite paste is formed which hardens into a cement-like plug.
- the patent discloses the use of such polymers as polyacrylamide, polyethylene oxide and copolymers of acrylamide and acrylic or methylacrylic acid.
- U.S. Patent No. 4,124,748 discloses a cross-linked copolymer of a vinyl ester and an ethylenically unsaturated carboxylic acid or derivative thereof that can absorb about 200 to 800% of its weight in water and expand substantially in volume when doing so.
- U.S. Patent No. 3,997,484 is typical of a group of related patents by Fanta, Doane and co-workers at the USDA Northern Regional Laboratory which describe various water swellable polymers made by grafting acryl ⁇ nitrile onto starch and then hydrolyzing the resultant copolymers. These polymers are capable of absorbing large amounts of water very rapidly with the concomitant swelling have been used in a specific form as lost circulation materials as described below.
- U.S. Patent No. 5,065,822 teaches the use of a polyvalent metal such as iron which is formed as the ingredients are passing down the borehole to contact a previously placed starch hybrid polymer, thus crosslinking the polymer to make the polymer formation impermeable.
- U.S. Patent No. 4,036,301 describes an encapsulated material useful in cementing a well, wherein a cement accelerator is encapsulated in a waxy material and placed within a highly retarded cement slurry. The cement slurry is pumped into the well with the encapsulated accelerator. After proper placement of the cement, circulation is decrease so that the temperature of the cement fluid approaches the bottom hole temperature of the well and melts the encapsulated material, freeing the accelerator which sets the cement.
- a similar technique is disclosed in U.S. Patent No. 4,362,566 which suggests encapsulating one component of a two or more component adhesive of cement mixture not start until the encapsulated component is freed from its reaction-preventive casing.
- U.S. Patent No. 4,664,8116 teaches introducing a water absorbent polymer encapsulated by a selected waxy substance which prevents the polymer from expanding by absorbing water until it reaches the lost circulation zone. This encapsulation material then dissolves or melts at the desired temperature within the borehole, thereby releasing the water absorbent polymer to absorb water and expand to seal the lost circulation zone.
- the selected polymers are in granular form which can be readily introduced into the wellbore along with the aqueous drilling fluid and the granules will pass through the wellbore substantially in a non-swollen state.
- the granules can accumulate, absorb water and swell to form a "soft gel", watertight plug thereby sealing the porous formation.
- the materials ban be used in conjunction with other lost circulation materials such as compacted cottonseed hulls or fibrous materials to reinforce the plug or improve the economics of the sealing operation.
- the products are only slowly biodegraded in contrast with starch or cellulose based materials but can be readily removed when desired by the addition of appropriate acids.
- the selected polymers are in granular form which can be readily introduced into the wellbore along with the aqueous drilling fluid and the granules will pass through the wellbore substantially in a non-swollen state. Once in the area of lost circulation the granules can accumulate, absorb water and swell to form a "soft gel", watertight plug thereby sealing the porous formation.
- the materials can be used in conjunction with other lost circulation materials such as compacted cottonseed hulls or fibrous materials to reinforce the plug or improve the economics of the sealing operation.
- the products are only slowly biodegraded in contrast with starch or cellulose based materials. They can be readily removed, however when desired, by the addition of appropriate acid or metallic salt solutions.
- lost circulation additives are specific, suitably crosslinked polyacrylamides which can be added directly to the drilling fluid and thereby be transported to the lost circulation area where they will then absorb large quantities of water and swell drastically in the borehole. This swelling substantially closes the fissures and pores through which drilling fluid would be lost.
- polymers can be used in conjunction with other swellable or non-swellable lost circulation materials which may also be added to the borehole.
- the "soft gel" formed by the polyacrylamides can then act alone or in conjunction with the other additives to close any rather large fissures or pores.
- Crosslinked polyacrylamides became available in the mid-1970's and the polymers made by graft polymerization of acrylonitrile with starch followed by hydrolysis became available about the same time. Many variations in the properties of each could be made by varying the conditions of synthesis. Both classes of polymers found use in various applications where absorption of water is important. A large market developed and still exists for their use in disposable diapers and other similar incontinence products. Another major market which evolved was for their use as soil amendments to retain moisture for grasses, trees, crops and the like which increases the survival rate as well as appearance, crop yield, root structure, etc. Since both classes of copolymers are hydrolyzed from their copolymer precursors, they can be obtained as salts of various anions such as but not limited to sodium, potassium or magnesium and each have unique physical properties.
- the physical appearance of the two classes of copolymers as initially prepared is significantly different by nature of the chemical compounds used to synthesize them.
- the starch graft copolymers are usually fine powders as they leave the manufacturing process but some can be manufactured In flake or film form.
- the crosslinked polyacrylamide copolymers as manufactured generally appear as semi-crystalline or amorphous clumps of rather large size. These materials then can be ground by various means to the particle size most suited to the application intended. For example the materials described in U.S. Patent No. 4,559,074 mentioned above can be obtained in various particle sizes and particle size distributions. For example one can obtain the crosslinked polyacrylamide described in this patent from Broadleaf Industries Inc. of Costa Mesa, CA in several particle size ranges.
- Broadleaf P4® can be obtained in the range of 0.50 - 2.50 millimeters as their standard size, 0.075 - 0.500 millimeters as their fine size and ⁇ 0.075 millimeters as the ultra-fine size (often called Root Dip).
- Polymers for use in disposable diapers are required to be able to absorb urine which is primarily water and as rapidly as possible to immobilize the urine as quickly as possible.
- the ability of such materials to biodegrade in a reasonably short time is also an advantage.
- the starch graft copolymers are ideal for this application because of their small particle size which hastens the water absorption and the very nature of the starch base itself; starch based materials in general are easily biodegraded. Variations in the rate of absorption of water by commercially available polyacrylamides can be seen in the Examples which follow. The difference in biodegradability is shown by M. S. Johnson, Arab. Gulf J. Scient. Res. 3 (2) 745-750 (1985).
- starch graft copolymers do get to the borehole properly and do swell there, they can biodegrade rather rapidly and once again open the fissures and pores allowing circulation material to be lost again. Although it is sometimes desirable to remove the caked lost circulation material, the rate and time when this occurs via biodegradation depends on the microbiolgical environment of the borehole which cannot be controlled. Unfortunately the very properties of the starch based copolymers and some crosslinked polyacrylamides which make them ideal for use in disposable diapers make them difficult to use as lost circulation materials. A review of Superabsorbent Polymers, Science and Technology, Bucholz and Peppas, American Chemical Society, 1994 pps.
- the finely divided particles of either type of polymer will absorb water so rapidly from the drilling fluid used to carry them into the borehole, they swell on the way to the borehole. This increases the viscosity of the drilling fluid considerably, or they form agglomerated clumps which also interferes with the movement of the drilling fluid and traps solids from that fluid which, in turn, modifies its characteristics.
- the swelling occurred before settling in the borehole and coating the fissures and voids therein the swollen copolymer particle can be carried back out of the borehole to the surface and accumulate there.
- Crosslinked Polyacrylamide copolymers in general are less biodegradable than the starch based materials as mentioned above; those designed for use in disposable diapers and the like are the most biodegradable.
- Crosslinked Polyacrylamides also vary in the amount of water they will absorb which in turn reflects the amount of swelling they will undergo, and in the amount of water they can retain overtime. This is shown by Wang & Gregg in J. Amer. Soc. Hort Sci. 115(6):943-948 (1990) and demonstrated below. Lotto lot variation has been found also in the various other crosslinked Polyacrylamide copolymers although some might still be suitable for use as lost circulation materials if properly tested before use. The products described in U.S. Patent No.
- the selected, suitable crosslinked Polyacrylamide copolymer or other suitable water absorbing polymer which will not interfere with the drilling fluid operation or inadvertently biodegrade is added to the drilling fluid via a hopper or pouring the material by hand from the bag or container or by any other means suitable to adding granular particulate matter.
- the material is then carried to the borehole where it absorbs water, swells and the swollen material forms a "soft gel" on the fissures.
- the amount of copolymer to be added to the drilling fluid can readily be adapted to the characteristics of the particular borehole.
- suitable materials may be mixed with the polymer in an amount equal to or up to 150 times the weight of said polymer and the mixture similarly put into the drilling fluid and allowed to proceed to the borehole. Similarly the materials can be added sequentially to the drilling fluid and allowed to proceed to the borehole. This is illustrated in the Examples.
- Such suitable materials may or may not be swellable and may include but are not limited to walnut hulls, cottonseed hulls, thermoset rubber, coal, graphite, other mixed nut shells, perlite, kenaf and the like.
- hydrochloric acid or other suitable acid is added to the drilling fluid in the proper amount necessary to develop the necessary acid strength to dissolve or otherwise cause the destruction of the polymer cake in the borehole.
- Fifteen percent (15%) hydrochloric acid is convenient to use but the concentration need not be limited to this.
- solutions of various metallic salts such as sodium chloride, potassium chloride, calcium chloride and the like may be added to the borehole which after contacting the cake will shrink the cake so that it will fragment and be pumped from the borehole.
- This example illustrates a method of determining whether a polymer absorbs water at an appropriate rate, absorbs a useful quantity of water and retains the absorbed water.
- Such polymers comprise a solid, water insoluble polyacrylamide polymer or copolymer, which typically swells from 25- 300 times its weight of tap water at room temperature when placed therein.
- Such polymer may further comprise an alkali metal salt, such as a sodium salt, of a partially hydrolyzed crosslinked polyacrylamide. Then 400 ml of tap water was added and the samples are allowed to stand at room temperature.
- the now swollen granules were isolated by pouring the contents of the beakers into a strainer placed upon another beaker of a size sufficient to hold all of the unbound water from the first beaker.
- the gelled polymers were allowed to drain with mild, intermittent shaking for 5 minutes.
- the gelled material was then transferred to a previously tared container of size sufficient to hold the entire gelled mass.
- the containers were then placed on a suitable balance, weighed and the tare weight subtracted from the gross weight. After subtracting the weight of the original dry sample, the net weight was recorded.
- Example 1 The water Sources used were Tap Water and Purchased Distilled Water which is similar to rainwater in dissolved solids content.
- the samples of crosslinked Polyacrylamides A and B are from the same sources as above.
- Three samples of crosslinked Polyacrylamide gel were prepared by adding 1.1 gr. of Broadleaf P4® to 300ml of tap water in each of 3 beakers. The beakers were placed on an orbital shaker and shaken moderately until the material had absorbed and swelled until each sample had absorbed ⁇ 185 gr. water/ 1.0 gr. Polyacrylamide which is typical for this product. To one beaker was then added 10 ml. of 0.5N hydrochloric acid, to another was added 10 ml of 0.1 N hydrochloric acid and to the third was added 10ml of 5% acetic acid. After 30 minutes the shrinking and/or dissolving of the gel in each sample was noticeable. After 150 minutes, the remaining gel was removed using a strainer and the remaining gel was ⁇ 25% of the weight of the original amount of gel which had been formed.
- Magma Fiber is a Lost Circulation Material available from Lost Circulation Specialists Inc., Spring, TX. It is a fiber made when molten rock is extrusion spun.
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Abstract
This invention discloses methods for reducing lost circulation in wellbores. The invention utilizes certain selected water swellable polymers that swell at a rate slow enough to reach the lost circulation zone of a well before those polymers have swollen to an extent that disrupts the drilling process. These selected polymers may be used alone or in conjunction with other lost circulation materials which do not swell or also swell slowly enough to reach the lost circulation zone without interfering with the drilling operation. Mixtures of such materials are also disclosed.
Description
Methods for Reducing Lost Circulation in Wellbores
Background-Field of Invention
This invention concerns the use of specially crosslinked polyacrylamide, water absorbing polymers for reducing lost circulation when aqueous drilling fluids are used and a method for reducing such lost circulation. These polymers are able to reach the areas of fissures and thief zones before absorbing water and expanding to plug those fissures and thief zones.
Background
Drilling fluids or drilling muds as they are sometimes called, are slurries of solids used in the drilling of wells in the earth for the purpose of recovering hydrocarbons and other fluid materials. Drilling fluids have a number of functions, the most important of which are lubricating the drilling tool and drill pipe which carries thgotool, removing formation cuttings from the well, counterbalancing formation pressures to prevent the inflow of gas, oil or water from permeable rocks which may be encountered at various levels as drilling continues, and holding the cuttings in suspension in the event of a shutdown in the drilling and the pumping of the drilling fluid.
For a drilling fluid to perform these functions and allow drilling to continue, the drilling fluid must stay in the borehole. Frequently, undesirable formation conditions are encountered in which substantial amounts or, in some cases, practically all of the drilling fluid may be lost into the formation. Drilling fluid can leave the borehole through large or small fissures or fractures in the formation or through pores in the rock matrix surrounding the borehole.
Most wells are drilled with the intent of forming a filter cake of varying thickness on the sides of the borehole. The primary purpose of the filter cake is to reduce the large losses of drilling fluid to the surrounding formation. Unfortunately, formation conditions frequently are encountered which may result in unacceptable losses of drilling fluid to the surrounding formation despite the type of drilling fluid employed and filter cake established.
A variety of different substances are often pumped down well bores in attempts to reduce the large losses of drilling fluid to fractures and the like in the surrounding formation. Different forms of cellulose are preferred materials by some persons. Other substances which are pumped into well bores to control lost circulation are: almond hulls, black walnut hulls, bagasse, dried tumbleweed, kenaf, paper, coarse and fine rice. These and a number of other prior art materials are described in U.S. Patent 4,498,995.
Another process that is employed to close off large lost circulation areas is referred to in the art as gunk-squeeze. In that process, a quantity of a powdered bentonite is mixed into diesel oil and pumped down the well bore. Water injection follows and if the water and bentonite will harden to form a gunky, semi- solid mass which can reduce lost circulation. This process must be carefully controlled; first the bentonite must be kept dry until it reaches the desired location in the well and then problems frequently occur in trying to mix the bentonite and water in the well. This method is disclosed in U.S. Patent No. 3,082,823.
Many of the methods devised or proposed to limit lost circulation involve the use of water expandable materials. The black walnut hulls and other nut hulls have been found to undergo some swelling when used in this operation, (see Glowka et al, Journal of Petroleum Technology, March 1990, pages 328 & ff.) Cremeans in U.S. Patent No.4,217,965 teaches the use of compressed, swellable, pelletized cottonseed hulls in combination with cottonseed meal, bentonite, residual lint and a surface active agent. The advantage of this
compressed material is that it does not expand quickly when added to the drilling fluid but only after it is well down the well bore.
Another swellable material sometimes used is a water expandable clay such as bentonite which may be mixed with another ingredient to form a viscous paste or cement. U.S. Patent No. 2,890,169 discloses a lost circulation fluid made by forming a slurry of bentonite and cement in oil. The slurry is mixed with a surfactant and water to form a composition comprising a water-in-oil emulsion having the bentonite and cement dispersed in the continuous oil phase. As this composition is pumped down the well bore, the oil expands and flocculates the bentonite which, under the right conditions, forms a cake on the wellbore surface in the lost circulation area. Hopefully, the settling of the cake of the walls will cause the emulsion to break thus causing the previously emulsified water to react with the cement to form a solid coating on the cake. But such a complex process can easily go wrong.
U.S. Patent No. 3,448,800 discloses another method wherein a water soluble polymer is slurried in a non-aqueous medium and injected into a well. Another slurry of a mineral material such a barite, cement or plaster of paris is subsequently injected into the well to mix with the first slurry to form a cementlike plug in the wellbore.
U.S. Patent No. 4,261 ,422 describes the use of an expandable clay such as bentonite or montmorillonite which is dispersed in a liquid hydrocarbon into the well. After injection the clay will expand on contact with water in the formation. Thus it is hoped that the expanding clay will close off water producing intervals, but not harm oil producing intervals.
A similar method is disclosed in U.S. Patent No. 3,078,920 which uses a solution of a polymerized methacrylate dissolved in a non-aqueous solvent such as acetic acid, acetic anhydride, propionic acid and liquid aliphatic ketones such
as acetone or methyl-ethyl ketone. The methacrylate will expanchon contact with formation water in the water producing formations in the well.
It has also been proposed to mix bentonite with water in the presence of a water soluble polymer which will flocculate and congeal the clay to form a much stronger and stiffer cement-like plug than will form when bentonite is mixed with water alone. U.S. Patent No. 3,909,421 discloses such a fluid made by blending a dry powdered polyacrylamide with bentonite followed by mixing the powder blend with water. U.S. Patent No. 4,128,528 claims a powdered bentonite/polyacrylamide thickening composition prepared by mixing a water-in- oil emulsion with bentonite to form a powdered composition which rapidly becomes a viscous, stiff material when mixed with water. U.S. Patents No. 4,503,170; 4,457,594; 4,445,576; 4,442,241; and 4,391,925 teach the use of a water expandable clay dispersed in the oily phase of a water-in-oil emulsion containing a surfactant to stabilize the emulsion and a polymer dispersed in the aqueous phase. When the emulsion is sheared, it breaks and a bentonite paste is formed which hardens into a cement-like plug. The patent discloses the use of such polymers as polyacrylamide, polyethylene oxide and copolymers of acrylamide and acrylic or methylacrylic acid.
U.S. Patent No. 4,124,748 discloses a cross-linked copolymer of a vinyl ester and an ethylenically unsaturated carboxylic acid or derivative thereof that can absorb about 200 to 800% of its weight in water and expand substantially in volume when doing so. U.S. Patent No. 3,997,484 is typical of a group of related patents by Fanta, Doane and co-workers at the USDA Northern Regional Laboratory which describe various water swellable polymers made by grafting acrylόnitrile onto starch and then hydrolyzing the resultant copolymers. These polymers are capable of absorbing large amounts of water very rapidly with the concomitant swelling have been used in a specific form as lost circulation materials as described below. The rights to use these patents have been granted to several companies and some are commercially available. Advances on this
technology have been regularly made to the present time. For example, U.S. Patent No. 5,065,822 teaches the use of a polyvalent metal such as iron which is formed as the ingredients are passing down the borehole to contact a previously placed starch hybrid polymer, thus crosslinking the polymer to make the polymer formation impermeable.
Another highly water absorbent copolymer which expands upon water absorption is described in U.S. Patent No. 4,320,040. The described compound is derived by polymerizing acrylic acid and/or methacrylic acid in the presence of polyvinyl alcohol followed by neutralization and a heat treatment.
Highly absorbent spongy polymers which may absorb large quantities of water and hydrocarbons causing an increase in volume are disclosed in U.S. Patent No. 3,878,175. These are copolymers of an acyl acrylate and a heterocyclic N-vinyl monomer containing a carbonyl functionality and a crosslinking agent in the presence of a hydrophobic liquid diluent. U.S. Patent No. 4,182,677 discloses that natural and synthetic rubbers will also swell in size upon absorbing water.
Many of the approaches mentioned here and later have used crosslinked polyacrylamides as the water absorbing polymer. One of the first disclosures of such materials in U.S. Patent 3,247,171 which teaches the preparation and then hydrolysis of a crosslinked polacrylamide polymer. Variations in method of polymerization as well as the type and depth of hydrolysis were shown to vary the properties of the products such as rate of absorption or water and propensity to retain the water absorbed. Many variations of that theme have been subsequently reported with U.S. Patent No.4,559,074 being quite notable. This mildly ionic crosslinked polyacrylamide has a high water absorbtivity, retains the water well and can be manufactured reproducibly.
Much research has been dedicated to the use of encapsulants and methods to produce encapsulated products of carious types. Although this is typical of the pharmaceutical and cosmetic field, the use of encapsulated materials to provide useful, swellable lost circulation materials have not been overlooked. This technique is sometimes useful in preventing the swelling of water absorbing polymers and other materials prior to their reaching the thief zone or otherwise interfering with the drilling operation itself.
An invention using encapsulation of materials for use in boreholes is described in U.S. Patent No.4,078,612. The patent describes an explodable material encapsulated in natural gums slurried in a liquid vehicle. The material is pumped into the formation around the wellbore and exploded to decrease permeability.
The use of bentonite encapsulated within a water insoluble polymeric coating within a water-insoluble polymeric coating has been disclosed for lost circulation control. U.S. Patent No. 2,836,555 describes bentonite encapsulated within a polymeric coating having a tiny hole drilled therethrough. When the encapsulated bentonite is pumped down the wellbore, water will seep through the hole in the encapsulant causing the bentonite to swell and ultimately rupture the coating.
Another U.S. Patent No. 4,036,301 describes an encapsulated material useful in cementing a well, wherein a cement accelerator is encapsulated in a waxy material and placed within a highly retarded cement slurry. The cement slurry is pumped into the well with the encapsulated accelerator. After proper placement of the cement, circulation is decrease so that the temperature of the cement fluid approaches the bottom hole temperature of the well and melts the encapsulated material, freeing the accelerator which sets the cement.
A similar technique is disclosed in U.S. Patent No. 4,362,566 which suggests encapsulating one component of a two or more component adhesive of cement mixture not start until the encapsulated component is freed from its reaction-preventive casing.
Similarly, U.S. Patent No. 4,664,8116 teaches introducing a water absorbent polymer encapsulated by a selected waxy substance which prevents the polymer from expanding by absorbing water until it reaches the lost circulation zone. This encapsulation material then dissolves or melts at the desired temperature within the borehole, thereby releasing the water absorbent polymer to absorb water and expand to seal the lost circulation zone.
Each of the above discussed methods has sufficient disadvantages making it necessary to continue the search for an effective, efficient and readily controlled method of reducing or eliminating lost circulation without undue interruption of the drilling process. The methods mentioned generally go to great lengths to prevent the swollen lost circulation material from being finally generated in the drilling zone thereby impeding the flow of the drilling mud or making it so viscous that the drilling becomes inefficient. When some of the materials mentioned above do reach the lost circulation zone they must be somehow activated to absorb water and swell still in the proper region which against difficult to control. In addition some of the materials are difficult or remove when desired and other because of their nature are removed too soon.
In accordance with the method of this present invention, the selected polymers are in granular form which can be readily introduced into the wellbore along with the aqueous drilling fluid and the granules will pass through the wellbore substantially in a non-swollen state. Once in the area of lost circulation the granules can accumulate, absorb water and swell to form a "soft gel", watertight plug thereby sealing the porous formation. In addition the materials ban be used in conjunction with other lost circulation materials such as
compacted cottonseed hulls or fibrous materials to reinforce the plug or improve the economics of the sealing operation. Finally, the products are only slowly biodegraded in contrast with starch or cellulose based materials but can be readily removed when desired by the addition of appropriate acids.
Objects and Advantages
In accordance with the method of this present invention, the selected polymers are in granular form which can be readily introduced into the wellbore along with the aqueous drilling fluid and the granules will pass through the wellbore substantially in a non-swollen state. Once in the area of lost circulation the granules can accumulate, absorb water and swell to form a "soft gel", watertight plug thereby sealing the porous formation. In addition the materials can be used in conjunction with other lost circulation materials such as compacted cottonseed hulls or fibrous materials to reinforce the plug or improve the economics of the sealing operation. Finally, the products are only slowly biodegraded in contrast with starch or cellulose based materials. They can be readily removed, however when desired, by the addition of appropriate acid or metallic salt solutions.
Several objects and advantages of this invention are to present simple products and methods for their use as lost circulation materials which may be used in conjunction with on-shore, off-shore, water drilling, coring and geothermal wells for oil and gas. The lost circulation additives discovered are specific, suitably crosslinked polyacrylamides which can be added directly to the drilling fluid and thereby be transported to the lost circulation area where they will then absorb large quantities of water and swell drastically in the borehole. This swelling substantially closes the fissures and pores through which drilling fluid would be lost. In addition the polymers can be used in conjunction with other swellable or non-swellable lost circulation materials which may also be added to
the borehole. The "soft gel" formed by the polyacrylamides can then act alone or in conjunction with the other additives to close any rather large fissures or pores.
Unlike the materials described in Background Section, there is no need to encapsulate, compound, slurry or otherwise pre-treat these lost circulation materials before use. Also there is no need to interrupt or otherwise change the drilling procedure, wait an undue period or depend on the adjustment of the temperature in the borehole for the lost circulation materials to take effect,
Still further objects and advantages will become apparent from a consideration of the ensuing description.
General Description of the Invention
Crosslinked polyacrylamides became available in the mid-1970's and the polymers made by graft polymerization of acrylonitrile with starch followed by hydrolysis became available about the same time. Many variations in the properties of each could be made by varying the conditions of synthesis. Both classes of polymers found use in various applications where absorption of water is important. A large market developed and still exists for their use in disposable diapers and other similar incontinence products. Another major market which evolved was for their use as soil amendments to retain moisture for grasses, trees, crops and the like which increases the survival rate as well as appearance, crop yield, root structure, etc. Since both classes of copolymers are hydrolyzed from their copolymer precursors, they can be obtained as salts of various anions such as but not limited to sodium, potassium or magnesium and each have unique physical properties.
The physical appearance of the two classes of copolymers as initially prepared is significantly different by nature of the chemical compounds used to synthesize them. The starch graft copolymers are usually fine powders as they
leave the manufacturing process but some can be manufactured In flake or film form. The crosslinked polyacrylamide copolymers as manufactured generally appear as semi-crystalline or amorphous clumps of rather large size. These materials then can be ground by various means to the particle size most suited to the application intended. For example the materials described in U.S. Patent No. 4,559,074 mentioned above can be obtained in various particle sizes and particle size distributions. For example one can obtain the crosslinked polyacrylamide described in this patent from Broadleaf Industries Inc. of Costa Mesa, CA in several particle size ranges. The products named Broadleaf P4® can be obtained in the range of 0.50 - 2.50 millimeters as their standard size, 0.075 - 0.500 millimeters as their fine size and <0.075 millimeters as the ultra-fine size (often called Root Dip).
Polymers for use in disposable diapers are required to be able to absorb urine which is primarily water and as rapidly as possible to immobilize the urine as quickly as possible. In addition the ability of such materials to biodegrade in a reasonably short time is also an advantage. The starch graft copolymers are ideal for this application because of their small particle size which hastens the water absorption and the very nature of the starch base itself; starch based materials in general are easily biodegraded. Variations in the rate of absorption of water by commercially available polyacrylamides can be seen in the Examples which follow. The difference in biodegradability is shown by M. S. Johnson, Arab. Gulf J. Scient. Res. 3 (2) 745-750 (1985). Therefore if the starch graft copolymers do get to the borehole properly and do swell there, they can biodegrade rather rapidly and once again open the fissures and pores allowing circulation material to be lost again. Although it is sometimes desirable to remove the caked lost circulation material, the rate and time when this occurs via biodegradation depends on the microbiolgical environment of the borehole which cannot be controlled.
Unfortunately the very properties of the starch based copolymers and some crosslinked polyacrylamides which make them ideal for use in disposable diapers make them difficult to use as lost circulation materials. A review of Superabsorbent Polymers, Science and Technology, Bucholz and Peppas, American Chemical Society, 1994 pps. 88 - 111, clearly shows that the use of such polymers in disposable diapers has driven the technology and the similar development of such materials for other uses such as in agriculture and the drilling industry has been minor. Fortunately Clarke in U.S. Patent No. 4,559,074 deals with this trend by inventing a crosslinked polyacrylamide specifically designed to have the properties more suitable for the agricultural industry. The careful examination of these materials led to the trial of these products for use as lost circulation materials as described in this invention. When working with the three grades of Broadleaf P4 mentioned above, it was noticed that the finely ground known as Ultra-fine material absorbed water rapidly to form a very viscous slurry which would make it difficult to pump that material to the borehole and for it to congregate there to form a cake. The material designated as Fine forms clumps when first contacting water and requires undue agitation to break apart the clumps so that all of the material will become swollen.
Therefore since the finely divided particles of either type of polymer will absorb water so rapidly from the drilling fluid used to carry them into the borehole, they swell on the way to the borehole. This increases the viscosity of the drilling fluid considerably, or they form agglomerated clumps which also interferes with the movement of the drilling fluid and traps solids from that fluid which, in turn, modifies its characteristics. In addition since the swelling occurred before settling in the borehole and coating the fissures and voids therein, the swollen copolymer particle can be carried back out of the borehole to the surface and accumulate there. It is for this reason that earlier so much effort was placed on finding encapsulants for the starch based copolymers or otherwise keep them from swelling and the same is true for some other water absorbing polymers,
Typical examples of this were described above in U.S. Patents ,Nos. 4,664,516 and 4,836,940.
It was therefore determined that the standard Broadleaf P4® or that type of product in larger particle size were most useful for this present invention. Of course other materials having similar properties might be used.
Crosslinked Polyacrylamide copolymers in general are less biodegradable than the starch based materials as mentioned above; those designed for use in disposable diapers and the like are the most biodegradable. Crosslinked Polyacrylamides also vary in the amount of water they will absorb which in turn reflects the amount of swelling they will undergo, and in the amount of water they can retain overtime. This is shown by Wang & Gregg in J. Amer. Soc. Hort Sci. 115(6):943-948 (1990) and demonstrated below. Lotto lot variation has been found also in the various other crosslinked Polyacrylamide copolymers although some might still be suitable for use as lost circulation materials if properly tested before use. The products described in U.S. Patent No. 4,559,074 (mentioned above) and sold as Broadleaf P4® were especially designed to avoid the problems of other crosslinked polyacrylamides and do have a high rate of water absorption, also a high level of water retention and possess resistance to rapid biodegradation. This resistance to biodegradation was illustrated by Johnson, Arab. Gulf J. scient. Res. 3(2) 745 - 750 (1985). However a swollen cake of those materials can be removed when desired by adding a quantity of dilute hydrochloric acid, acetic acid and the like to the well bore whereupon the cake will completely dissolve or disintegrate as shown in the Examples below.
In the practice of the invention, the selected, suitable crosslinked Polyacrylamide copolymer or other suitable water absorbing polymer which will not interfere with the drilling fluid operation or inadvertently biodegrade, is added to the drilling fluid via a hopper or pouring the material by hand from the bag or
container or by any other means suitable to adding granular particulate matter. The material is then carried to the borehole where it absorbs water, swells and the swollen material forms a "soft gel" on the fissures. The amount of copolymer to be added to the drilling fluid can readily be adapted to the characteristics of the particular borehole.
Other suitable materials may be mixed with the polymer in an amount equal to or up to 150 times the weight of said polymer and the mixture similarly put into the drilling fluid and allowed to proceed to the borehole. Similarly the materials can be added sequentially to the drilling fluid and allowed to proceed to the borehole. This is illustrated in the Examples.
Such suitable materials may or may not be swellable and may include but are not limited to walnut hulls, cottonseed hulls, thermoset rubber, coal, graphite, other mixed nut shells, perlite, kenaf and the like.
To remove a formed cake of these lost circulation materials in the borehole, a quantity of dilute hydrochloric acid or other suitable acid is added to the drilling fluid in the proper amount necessary to develop the necessary acid strength to dissolve or otherwise cause the destruction of the polymer cake in the borehole. Fifteen percent (15%) hydrochloric acid is convenient to use but the concentration need not be limited to this. Alternatively, solutions of various metallic salts such as sodium chloride, potassium chloride, calcium chloride and the like may be added to the borehole which after contacting the cake will shrink the cake so that it will fragment and be pumped from the borehole.
The following examples are intended only to illustrate the various aspects of the invention which is defined by the claims.
EXAMPLE 1
Determination of the Rate of Water Absorption of Swellable Polymers
The general properties of a polymer suitable for use in this invention are discussed above. This example illustrates a method of determining whether a polymer absorbs water at an appropriate rate, absorbs a useful quantity of water and retains the absorbed water.
Approximately 0.200gr. samples of the candidate polymers were weighed out and placed in 600 ml beakers. Such polymers comprise a solid, water insoluble polyacrylamide polymer or copolymer, which typically swells from 25- 300 times its weight of tap water at room temperature when placed therein. Such polymer may further comprise an alkali metal salt, such as a sodium salt, of a partially hydrolyzed crosslinked polyacrylamide. Then 400 ml of tap water was added and the samples are allowed to stand at room temperature. Periodically over a selected time period of at least 20 hours, the now swollen granules were isolated by pouring the contents of the beakers into a strainer placed upon another beaker of a size sufficient to hold all of the unbound water from the first beaker. The gelled polymers were allowed to drain with mild, intermittent shaking for 5 minutes. The gelled material was then transferred to a previously tared container of size sufficient to hold the entire gelled mass. The containers were then placed on a suitable balance, weighed and the tare weight subtracted from the gross weight. After subtracting the weight of the original dry sample, the net weight was recorded. The gelled samples were returned to their original beakers, the water that had been separated by the strainer was returned and the samples were then allowed to stand for another period of time whereupon this procedure was repeated. This procedure was repeated periodically for 18 hours. The quantity of water absorbed was then calculated as gr. water/ gr. sample and the trend of water absorption and/or water desorption can be noticed.
Water Absorption as Grams Water Absorbed by 1 Gram of Polymer
Sample Description Polyacrylamide A Polyacrylamide B
Sample Weight 0.139 gr. 0.188 gr. gr. water/ gr. sample 162.3 gr. 127.3 gr.
After I hour immersion
After 2 hours 164.3 gr. 165.0 gr.
After 20 hours 126.3 gr. 189.7 gr.
These results indicate that Polyacrylamide A absorbs water more rapidly than Polyacrylamide B which in this case is the standard grade of Broadleaf P4®. The results also show that after 20 hours the water swollen Polyacrylamide A gave up a considerable amount of its originally absorbed water while Polyacrylamide B did not.
EXAMPLE 2
Determination of the Extent of Swelling in Different water Sources
These determinations were made as in Example 1. The water Sources used were Tap Water and Purchased Distilled Water which is similar to rainwater in dissolved solids content. The samples of crosslinked Polyacrylamides A and B are from the same sources as above.
Water Type Tap Distilled
TIME A B A B
2 hrs. 164* 165 345 346 20 hrs. 126 189 358 467 gr. water absorbed per gr. polymer
EXAMPLE 3
Determining Temperature Effect on Swelling of Water
Swellable Polymers
One gram (1.0 gr.) of crosslinked Polyacrylamide C was added to 300 ml of tap water at room temperature with stirring by a magnetic stirring device. The mixture was heated on a hot plate. After 35 minutes some gel was noticed and the temperature had reached 80°C; stirring was not impeded. After a total of 125 minutes the temperature had reached 90°C and there was the expected amount of swelling as visually observed. The stirring was not impeded' until the temperature exceeded 80°C ; stirring was increased and was continued for another 2 hours. With continued stirring the mixture was allowed to return to room temperature and the product resembled polymer that had been swollen at room temperature.
EXAMPLE 4
The procedure of EXAMPLE 3was repeated using 1.0 gr. of crosslinked Polyacrylamide B (standard Broadleaf P4®) with very similar results.
EXAMPLE 5
Removal of Crosslinked Polyacrylamide Gel or Cake
Three samples of crosslinked Polyacrylamide gel were prepared by adding 1.1 gr. of Broadleaf P4® to 300ml of tap water in each of 3 beakers. The beakers were placed on an orbital shaker and shaken moderately until the material had absorbed and swelled until each sample had absorbed ~185 gr. water/ 1.0 gr. Polyacrylamide which is typical for this product. To one beaker was then added 10 ml. of 0.5N hydrochloric acid, to another was added 10 ml of 0.1 N
hydrochloric acid and to the third was added 10ml of 5% acetic acid. After 30 minutes the shrinking and/or dissolving of the gel in each sample was noticeable. After 150 minutes, the remaining gel was removed using a strainer and the remaining gel was <25% of the weight of the original amount of gel which had been formed.
EXAMPLE 6
Use of Crosslinked Polyacrylamide B in Conjunction with Treated and Compressed Cottonseed Hulls at Room
Temperature
Fourteen and seven tenths grams (14.7) of treated and compressed cottonseed hulls (Product PCH from Suprol Management Co.) and 1.0 gr. crosslinked Polyacrylamide B were simultaneously added to 300 ml of tap water at room temperature with stirring. After 25 minutes the cottonseed hulls were observed to be swelling; after another 30 minutes the entire mixture had swollen considerably and the rate of stirring had to be increased. The mixture was heated to 90°C with no additional apparent change; the swollen particles of the 2 additives were quite compatible and had become intermixed.
EXAMPLE 7
Use of Crosslinked Polyacrylamide B in Conjunction with Treated and Compressed Cottonseed Hulls at Elevated Temperature
Experiment 6 was repeated except that the PCH and Polyacrylamide were added simultaneously with stirring to water already at 90°C. After 5 minutes the stirring was slowing and 15 minutes the power on the stirring system had to be increased to maintain movement. After 35 minutes the stirring stopped and the
heating was also stopped. In this Experiment/the swollen particles of each additive were distinct from each other.
EXAMPLE 8
Destruction of Mixed Gels or Cakes
The free water in the flask used in Experiment 6 was removed using a strainer. To the residual material was added 200 ml of 15% hydrochloric acid and stirring was started. After 2.5 hours heating was started; after another 1.5 hours, the temperature was 90°C and the whole appearance of the mixture had changed from that of a jelly-like mass to a slurry of small, powder-like particles. When the slurry was put through a strainer, there were no gel-like particles retained on the strainer.
EXAMPLES 9 & 10
Experiments 7 and 8 were repeated but Polyacrylamide B was replaced with Polyacrylamide C. The results were almost identical.
EXAMPLE 11
Use of Crosslinked Polyacrylamides in Conjunction with Magma Fiber
Magma Fiber is a Lost Circulation Material available from Lost Circulation Specialists Inc., Spring, TX. It is a fiber made when molten rock is extrusion spun.
To 300 ml of tap water with stirring, was added 3.5 gr. of Magma Fiber. After stirring briefly to disperse the fiber, 1.0 gr. of Broadleaf P4® crosslinked Polyacrylamide was added. The stirred mixture was heated and after about 25
minutes the slurry thickened and the rate of stirring was increased to maintain mixing. Shortly thereafter large, swollen globules of Broadleaf P4® having Magma Fibers adhering to and/or trapped therein appeared; the temperature was then 90°C. The stirring was stopped and the mixture was allowed to cool to return to room temperature.
About 100 ml of free water was removed and 200 ml of 15% hydrochloric acid was added and stirring was resumed. After 15 minutes most of the gelled mixture had either dissolved or disintegrated. The mixture was then reheated and in about one hour there was only a hazy, yellow solution; no particles remained.
It should be understood that the invention is not necessarily limited to the specific details described above. Changes to certain features and aspects which do not affect the overall basic concepts thereof may be made by those skilled in the art without departing from the spirit and scope of the invention as described in the appended claims.
Claims
Claims: What is claimed is:
1. A method for reducing the loss of circulation fluids into flow passages of a subterranean formation during well drilling, completion, or workover operations, said circulation fluids being selected from the group consisting of drilling fluids, completion fluids and workover fluids, said method comprising:
(a) introducing into a circulation fluid selected from a group consisting of drilling fluids, completion fluids and workover fluids an effective amount of a solid, water insoluble but gel-forming polyacrylamide polymer which has a particle size range of about 0.50 millimeters to about 2.5 millimeters and which swells from 25 to 300 times its weight of tap water at room temperature when placed therein, and
(b) allowing the gel-forming polymer to enter the lost circulation zone and allowing the gel-forming polymer to remain in said zone to absorb the aforesaid weight of water and swell to the appropriate volume thereby reducing the loss of said circulation fluid upon resuming well drilling, completion or workover operation.
2. A method for reducing the loss of circulation fluids into flow passages of a subterranean formation during well drilling, completion, or workover operations, said circulation fluids being selected from the group consisting of drilling fluids, completion fluids and workover fluids, said method comprising:
(a) introducing into a circulation fluid selected from a group consisting of drilling fluids, completion fluids and workover fluids an effective amount of a solid, water insoluble but gel-forming polyacrylamide polymer which has a particle size range of about 0.50 millimeters to about 2.5 millimeters and which swells from 25 to 300 times its weight of tap water at room temperature when placed therein, and
(b) introducing a second, solid, hydrophilic lost circulation material in an amount equal to the weight the said water swellable polymer or up to 150 times the weight of the said water swellable polymer, and
(c) allowing both the said gel-forming polymer and the other loέt circulation material to enter the lost circulation zone and allowing the said aforementioned materials to remain in said zone to absorb water and swell to the expected volume thereby reducing the loss of said circulation fluid upon resuming well drilling, completion or workover operation.
3. The method of claim 1, wherein the said water swellable polymer is a partially hydrolyzed, crosslinked polyacrylamide.
4. The method of claim 1, wherein the selected water swellable polymer is an alkali metal salt of said partially hydrolyzed, crosslinked polyacrylamide.
5. The method of claim 3 wherein the said salt is the sodium salt of said partially hydrolyzed, crosslinked polyacrylamide. β.The method of claim 5 wherein the particle size distribution of said salt of said water swellable polymer is in the range of about 0.50 millimeters to about 2.50 millimeters.
7. The method of claim 2 wherein the second lost circulation material is compressed and compounded cottonseed hulls.
8. The method of claim 2 wherein the second lost circulation material is fiber derived from molten rock.
9. The method of claim 2 wherein the second material is ground walnut hulls.
10. The method of claim 2 wherein the second material is kenaf fibers.
11. The method of claim 2 wherein a second material is ground oyster shells.
12. The method of claim 2 wherein the said water swellable polymer is previously admixed with the aforesaid other solid lost circulation material before it is added to the said drilling mud, completion fluid or workover fluid.
13. The method of claim 2 wherein the said water swellable polymer and other aforesaid solid lost circulation materials are added simultaneously to said drilling fluid, completion fluid, or workover fluid.
14. The method of claim 2 wherein the said water swellable polymer and other aforesaid solid, water swellable polymer are added sequentially in either order to said drilling fluid, completion fluid or workover fluid.
15. A method for removing said water swollen polymer from the lost circulation
zone of Claim 1 by adding an aqueous solution of an acid or metallic salt thus causing said swollen polymer to dissolve or disintegrate.
16. The method of claim 15 where the removing agent is an aqueous solution of hydrochloric acid.
17. The method of claim 15 where the removing agent is an aqueous solution of acetic acid.
18. The method of claim 15 where the removing agent is and aqueous solution of sodium chloride.
19. A method for removing the swollen mixture formed in the said lost circulation zone of Claim 2 by adding an aqueous solution of an acid or metallic salt thus causing said swollen mixture to dissolve or disintegrate.
20. The method of claim 19 where the removing agent is an aqueous solution of hydrochloric acid.
21. The method of claim 19 where the removing agent is an aqueous solution of acetic acid.
22. The method of claim 19 where the removing agent is and aqueous solution of sodium chloride.
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AU2001245750A AU2001245750A1 (en) | 2000-04-04 | 2001-03-15 | Methods for reducing lost circulation in wellbores |
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US54241600A | 2000-04-04 | 2000-04-04 | |
US09/542,416 | 2000-04-04 |
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Cited By (11)
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WO2003062594A1 (en) * | 2002-01-16 | 2003-07-31 | Halliburton Energy Services, Inc. | Lost circulation compositions |
WO2004076812A1 (en) * | 2003-02-27 | 2004-09-10 | Halliburton Energy Services, Inc. | Methods for passing a swelling agent into a reservoir to block undesirable flow paths during oil production |
WO2004101952A1 (en) * | 2003-05-14 | 2004-11-25 | Services Petroliers Schlumberger | Self adaptive cement systems |
WO2005078235A1 (en) * | 2004-02-12 | 2005-08-25 | Shell Internationale Research Maatschappij B.V. | Suppressing fluid communication to or from a wellbore |
US7690429B2 (en) | 2004-10-21 | 2010-04-06 | Halliburton Energy Services, Inc. | Methods of using a swelling agent in a wellbore |
US7866394B2 (en) | 2003-02-27 | 2011-01-11 | Halliburton Energy Services Inc. | Compositions and methods of cementing in subterranean formations using a swelling agent to inhibit the influx of water into a cement slurry |
US7870903B2 (en) | 2005-07-13 | 2011-01-18 | Halliburton Energy Services Inc. | Inverse emulsion polymers as lost circulation material |
US7891424B2 (en) | 2005-03-25 | 2011-02-22 | Halliburton Energy Services Inc. | Methods of delivering material downhole |
US8043997B2 (en) | 2008-02-29 | 2011-10-25 | Halliburton Energy Services Inc. | Lost circulation material formulation and method of use |
US8469095B2 (en) | 2003-05-14 | 2013-06-25 | Schlumberger Technology Corporation | Self adaptive cement systems |
WO2015026713A1 (en) * | 2013-08-19 | 2015-02-26 | Schlumberger Canada Limited | Methods for servicing subterranean wells |
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US7066285B2 (en) | 2002-01-16 | 2006-06-27 | Halliburton Energy Services, Inc. | Method and composition for preventing or treating lost circulation |
US7534744B2 (en) | 2002-01-16 | 2009-05-19 | Halliburton Energy Services, Inc. | Method and composition for preventing or treating lost circulation |
WO2003062594A1 (en) * | 2002-01-16 | 2003-07-31 | Halliburton Energy Services, Inc. | Lost circulation compositions |
WO2004076812A1 (en) * | 2003-02-27 | 2004-09-10 | Halliburton Energy Services, Inc. | Methods for passing a swelling agent into a reservoir to block undesirable flow paths during oil production |
US7866394B2 (en) | 2003-02-27 | 2011-01-11 | Halliburton Energy Services Inc. | Compositions and methods of cementing in subterranean formations using a swelling agent to inhibit the influx of water into a cement slurry |
US8469095B2 (en) | 2003-05-14 | 2013-06-25 | Schlumberger Technology Corporation | Self adaptive cement systems |
WO2004101952A1 (en) * | 2003-05-14 | 2004-11-25 | Services Petroliers Schlumberger | Self adaptive cement systems |
US8551244B2 (en) | 2003-05-14 | 2013-10-08 | Schlumberger Technology Corporation | Self adaptive cement systems |
WO2005078235A1 (en) * | 2004-02-12 | 2005-08-25 | Shell Internationale Research Maatschappij B.V. | Suppressing fluid communication to or from a wellbore |
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US7690429B2 (en) | 2004-10-21 | 2010-04-06 | Halliburton Energy Services, Inc. | Methods of using a swelling agent in a wellbore |
US7891424B2 (en) | 2005-03-25 | 2011-02-22 | Halliburton Energy Services Inc. | Methods of delivering material downhole |
US7870903B2 (en) | 2005-07-13 | 2011-01-18 | Halliburton Energy Services Inc. | Inverse emulsion polymers as lost circulation material |
US8703657B2 (en) | 2005-07-13 | 2014-04-22 | Halliburton Energy Services, Inc. | Inverse emulsion polymers as lost circulation material |
US8043997B2 (en) | 2008-02-29 | 2011-10-25 | Halliburton Energy Services Inc. | Lost circulation material formulation and method of use |
WO2015026713A1 (en) * | 2013-08-19 | 2015-02-26 | Schlumberger Canada Limited | Methods for servicing subterranean wells |
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