CA1233408A - Process for plugging a subterranean formation - Google Patents
Process for plugging a subterranean formationInfo
- Publication number
- CA1233408A CA1233408A CA000492014A CA492014A CA1233408A CA 1233408 A CA1233408 A CA 1233408A CA 000492014 A CA000492014 A CA 000492014A CA 492014 A CA492014 A CA 492014A CA 1233408 A CA1233408 A CA 1233408A
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- Prior art keywords
- aqueous
- water soluble
- phosphate salt
- silicate
- spacer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Abstract
ABSTRACT OF THE DISCLOSURE
Aqueous silicate solutions when admixed, inter-mingled or otherwise contacted with hydraulic cement slurries cause a very rapid gelation and accelerated setting of the hydraulic cement composition.
It has now been discovered that this rapid gelation/accelerated setting phenomenon can be controlled and substantially delayed by incorporating a water soluble inorganic phosophate salt into an aqueous spacer fluid positioned between said silicate solution and said cement slurry as such materials are being sequentially injected into a subterranean formation.
Aqueous silicate solutions when admixed, inter-mingled or otherwise contacted with hydraulic cement slurries cause a very rapid gelation and accelerated setting of the hydraulic cement composition.
It has now been discovered that this rapid gelation/accelerated setting phenomenon can be controlled and substantially delayed by incorporating a water soluble inorganic phosophate salt into an aqueous spacer fluid positioned between said silicate solution and said cement slurry as such materials are being sequentially injected into a subterranean formation.
Description
33~
PROCFSS FOR PLUGGING
A SUBTERRANEAN FORMAT :t ON
. . .
The present invention pertains to an improved method for plugging or sealing selectea zones in a sub-terranean formation. More particularly, -this lnvention relates to an improved method Eor plugging such sub-terrane~n zonks via -the sequential injection thex~in of an aqueous solution of a water soluble silicate material, an aqueous spacer material, and an aqueous hydraulic cement slurry.
In the drilling, comple-tion and servicing of oil and gas wells, it is known that selected zones of a subterranean formation can be sealed or plugged off by injecting therein an aqueous sodium silicate solution. In connection with such a treatment, gel-lation of said sodium silicate solution can be brought about by causing said solution to contac-t a suitable brine in the desired subterranean location or by the addition to said solution, prior to injection thereof into the fQrmation, of a reagent which induces a con-trolled, gradual gellation of said sodium silicate solution.
PROCFSS FOR PLUGGING
A SUBTERRANEAN FORMAT :t ON
. . .
The present invention pertains to an improved method for plugging or sealing selectea zones in a sub-terranean formation. More particularly, -this lnvention relates to an improved method Eor plugging such sub-terrane~n zonks via -the sequential injection thex~in of an aqueous solution of a water soluble silicate material, an aqueous spacer material, and an aqueous hydraulic cement slurry.
In the drilling, comple-tion and servicing of oil and gas wells, it is known that selected zones of a subterranean formation can be sealed or plugged off by injecting therein an aqueous sodium silicate solution. In connection with such a treatment, gel-lation of said sodium silicate solution can be brought about by causing said solution to contac-t a suitable brine in the desired subterranean location or by the addition to said solution, prior to injection thereof into the fQrmation, of a reagent which induces a con-trolled, gradual gellation of said sodium silicate solution.
2 9 , 440 -F - 1 --2- ~33~0~
It is also known that the aforementioned sodium silicate gel formation can be followed 'oy the injection of a hydraulic cement slurry. However, since hydraulic cement slurries rapidly gel and set up (i.e. harden) upon contact with such sodium silicate material, it is common practice to employ a water spacer to separate -the cement slurry and the silicate solution from each othe-r during the injection thereof into the subterranean formation of interest. ` `
While the use of a water spacer during injection to separate the cement slurry from the silicate solution can be reasonably effec-tive in preven-ting premature admixture thereof, it is nonetheless s-till possible Eor the materials to pre~naturely come into contact with each other and to set up it an undesired location during injection such as, for example, in the wel:Lbore itself or at an unintended position within the subterranean formation.
Accordingly, it would be highly desirable to provide a means of controlling (e.g., delaying) the gellation rate exhibited by a mixture of such materials and to thereby ensure or obtain continued mobility or pumpability of such a mixture for a limited period of time after the individual silicate solution and cement slurry ingredients -thereof come into direct contact with each other.
It has now been discovered tha-t if an aqueous silicate solution and a hydraulic cement slurry are mixed together in the presence of an.effective amount of a water soluble, polybasic inorganic phosphate salt, the gellation and setting up of the resulting mixture is 3Q substantially delayed (e.g., for a period of up to several hours) as compared to the almost instantaneous gellation (e.g., in just a few seconds) which otherwise occurs in the absence of said phosphate salt.
29,440-F -2-
It is also known that the aforementioned sodium silicate gel formation can be followed 'oy the injection of a hydraulic cement slurry. However, since hydraulic cement slurries rapidly gel and set up (i.e. harden) upon contact with such sodium silicate material, it is common practice to employ a water spacer to separate -the cement slurry and the silicate solution from each othe-r during the injection thereof into the subterranean formation of interest. ` `
While the use of a water spacer during injection to separate the cement slurry from the silicate solution can be reasonably effec-tive in preven-ting premature admixture thereof, it is nonetheless s-till possible Eor the materials to pre~naturely come into contact with each other and to set up it an undesired location during injection such as, for example, in the wel:Lbore itself or at an unintended position within the subterranean formation.
Accordingly, it would be highly desirable to provide a means of controlling (e.g., delaying) the gellation rate exhibited by a mixture of such materials and to thereby ensure or obtain continued mobility or pumpability of such a mixture for a limited period of time after the individual silicate solution and cement slurry ingredients -thereof come into direct contact with each other.
It has now been discovered tha-t if an aqueous silicate solution and a hydraulic cement slurry are mixed together in the presence of an.effective amount of a water soluble, polybasic inorganic phosphate salt, the gellation and setting up of the resulting mixture is 3Q substantially delayed (e.g., for a period of up to several hours) as compared to the almost instantaneous gellation (e.g., in just a few seconds) which otherwise occurs in the absence of said phosphate salt.
29,440-F -2-
3 71456-28 The discovery is embodied in one aspect of the present invention in the form of an improved process :Eor plugging a zone in a subterranean formation by secluentially injecting an aqueous solu-tion of water soluble silicate material followed by an aqueous spa-cer material and an aqueous hydraulic cement slurry, characterized by incorporating into said silicate solution, said aqueous spacer material or said hydraulic cement slurry, a water soluble, inorganic polybasic phosphate salt to reduce the rate of gel formation which occurs when said silicate material, spaeer and hydraulic cement are interminc,Jled.
In ano-ther aspect, the present invention ls a methocl o:E
retard:ing the gel~-t:ion ox an a~ueou~ mi.xture o.E a waif sol.ubl.~ sl-licate material and a hydraulic cement material whieh eomprises in-eorporating into said mixture a water soluble, polybasic inorganic phosphate salt in an amount sufficient to substantially reduce the gelation rate of said mixture.
The aforementioned method and improved process are par-ticularly useful in those instances where it is desired to plug or seal o:EE a selected zone of a subterranean formation such as, for example, where it is desired to plug ofE a lost circulation zone during a well drilling or cementing operation; to reduce or elimi-nate undesired formation brine flow in a producing well; to block oEf regions of high formation permeability in an injection well as-sociated with an enhanced oil recovery operation; and the like.
Silicate materials useful in the prac-tice of the present invention include those water soluble silicate materials whose aclueous solutions are already known in ~4~ ~Z3~
the art to produce relatively rigid gels upon contact or admixture with concentrated sodium-based brines or with calcium-containing brines or upon having their pH adjusted into a rapid gelation region via the addition oE an acid or an acid producing material. Such silicate materials include the various alkali metal salts of silicic acid such as, for example, the lithium, sodium and potassium salts thereof.
.
A particularly preferred water soluble silicate material for use in the practice of the present invention is an aqueous sodium silicate solution having a 3~3 weight percent total dissolved solids con-tent and llaving silicon dioxide ~SiO2) to sodium oxide (Na20) we.ight r~tio~ ox about 3.2:1. However, sodium silicate solutions having different S.iO2:Na20 rakios (e.g., ranging from 0.5:1 to
In ano-ther aspect, the present invention ls a methocl o:E
retard:ing the gel~-t:ion ox an a~ueou~ mi.xture o.E a waif sol.ubl.~ sl-licate material and a hydraulic cement material whieh eomprises in-eorporating into said mixture a water soluble, polybasic inorganic phosphate salt in an amount sufficient to substantially reduce the gelation rate of said mixture.
The aforementioned method and improved process are par-ticularly useful in those instances where it is desired to plug or seal o:EE a selected zone of a subterranean formation such as, for example, where it is desired to plug ofE a lost circulation zone during a well drilling or cementing operation; to reduce or elimi-nate undesired formation brine flow in a producing well; to block oEf regions of high formation permeability in an injection well as-sociated with an enhanced oil recovery operation; and the like.
Silicate materials useful in the prac-tice of the present invention include those water soluble silicate materials whose aclueous solutions are already known in ~4~ ~Z3~
the art to produce relatively rigid gels upon contact or admixture with concentrated sodium-based brines or with calcium-containing brines or upon having their pH adjusted into a rapid gelation region via the addition oE an acid or an acid producing material. Such silicate materials include the various alkali metal salts of silicic acid such as, for example, the lithium, sodium and potassium salts thereof.
.
A particularly preferred water soluble silicate material for use in the practice of the present invention is an aqueous sodium silicate solution having a 3~3 weight percent total dissolved solids con-tent and llaving silicon dioxide ~SiO2) to sodium oxide (Na20) we.ight r~tio~ ox about 3.2:1. However, sodium silicate solutions having different S.iO2:Na20 rakios (e.g., ranging from 0.5:1 to
4:1) may be employed instead if such should prove to be desirable from some practical standpoint such as cost, availability, etc. Similarly, the silicate material can be initially acquired in the form of different solids content aqueous solutions or in solid form. However, the latter option is typically less desirable since special equipment is required to convert the solid material into an aqueous solution prior to its injection into -the subterranean formation of interest.
In using the aforementioned aqueous silicate solution in the practice of the present invention, it is typically diluted prior to injection into the formation to a silicon dioxide content of from 5 to 25 weight percent. Preferably, the SiO2 content of the solution during injection is from 10 to 20 percent by weigh-t.
29,440-F -4-3L~33'~
In the present invention, it is typically desired to cause the soiuble silicate solution to gel after it has reached the desired location in the sub-terranean formation and to then utilize the resulting silicate gel to cause the subsequently injected aqueous hydraulic cement slurry to be directed, confined and/or emplaced in a particular, desired location within said formation. Any conventional, known technique can be employed for inducing the:initial gelation of the silicate solution. For example, if the zone of interest already contains a fairly concentrated sodium-based brine or a calcium-containing brine, the desired gela-ton will occur spontaneously upon the silicate soluton coming into contact with said brine. O-the~wise, the lnjecti~n ox the silicate solutiQn can be preceded by the injection of a quantity o a suitdble, na-turall~ occurring or sy~the-tic brine. In this latter instance, of course, a fresh water spacer will typically be pumped between said brine injec-tion and said silicate solution in order to prevent the inter-mingling, and accompanying gelation, thereof until after said materials exit the wellbore and enter the formation region of interest.
As yet another alternative, the initial gelation of the injected silicate solution can be induced by the incorporation therein (i.e., at -the earth's surface prior to pumping or injection) of a suitable reagent to bring about gelation in a sufficiently gradual fashion -to permit emplacement of said material prior to the gelation or setting thereof. For example, a strongly acidic ma-terial such as hydrochloric acid can be employed to adjust the pH of the aqueous silicate solution (which is 29,440-F -5-~3~
normally in a pH range of 11.5 or above into a range of, for example, 0.5 to 1.5 in which the gel time is suffici-ently long to allow emplacement thereof in the desired subterranean location. (See for example, U.S. Patent No.
3,375,872~. Alternatively, a reagent which gradually releases a gel inducing material (e.g., multivalent metallic or alkaline earth metal ions or a weak acid material) can be incorporated into the agueous silicate solution to bring about gradual gelation thereof following its emplacFment into the desired underground location.
(See fur example, U.S. Patent No. 2,208,766; Canadian Patent No. 1,070,936; U.S. Patent No. 3,435,899 and U.S.
Patent No. 3,294,563).
Hydraulic cement materials suitable Eor us in the present invention include those conventionally employed in oil and/or gas well cementing practices. Portland cements are preferred for this purpose and, of -those, API
Class A and API Class C Portland cements are more preferred for use in the present invention.
The preparation and pumping of the hydraulic cement slurry in the present invention is generally pursuant to conven-tional oil and gas well cement slurry preparation and handling practices. For example, conven-tional cementing additives such as dispersants, fluid loss additives, etc. can be employed, if desired. Similarly, the water contents of the cement slurries can suitably ye in the normally employed range, but may vary somewhat in quantitative terms depending upon various factors such as the specific type of cement employed, etc. For example, when an API Class A Portland cement is employed, it is preferred to employ it in the form of a slurry having a water content of about 46% by weight of cement. On-the 29,440-F -6-~33~0~
other hand, when an API Class H Portland cement is employed, it is preferred to use a slurry containing about 38 weight percent water by weight of cement.
When an aqueous spacer is employed to separate the cement slurry from the silicate solution during the sequential injection thereof, i-t is preferred to employ a fresh water spacer. Otherwise, high concentrations of sodium ions and/or the presence of significant calci~lm ion concentrations in said spacer could induce gelation of the silicate solution at the silicate solution/spacer interface during injection through the wellbore. Na-turally, however, it is possible to use a brine as the spacer it desired, so long as the na-ture o it (e.g~, the salt concentration and/or calcium content) is ah -that prem~-~u~e silicate gelat.ion is avoided during injection.
Regardless of whether the agueous spacer is based on fresh water or dilute brine materials, it can further contain various conventional spacer components such as polymeric thickener materials, and the like, as desired.
As has been previously noted, a key ~ea-ture of the present invention involves the discovery that certain polybasic, inorganic phosphate salts are capable ox substantially delaying or retarding the otherwise very rapid (e.g., in just a few seconds) gelation or setting up which occurs when a cement slurry and an aqueous silicate solution are admixed or intermingled. Suitable inorganic phosphate salts for this purpose include the various known water soluble, polybasic inorganic phosphate salts such as, for example the water soluble dibasic or tribasic alkali metal or ammonium phosphate salts.
29,440-F -7-~233a~ 8 Preferably the alkali metal phosphate salts, or alkali metal/ammonium phosphate salt mixtures, are employed to eliminate, or minimize, the generation or release of ammonia during use. Especially preferred phosphate salts
In using the aforementioned aqueous silicate solution in the practice of the present invention, it is typically diluted prior to injection into the formation to a silicon dioxide content of from 5 to 25 weight percent. Preferably, the SiO2 content of the solution during injection is from 10 to 20 percent by weigh-t.
29,440-F -4-3L~33'~
In the present invention, it is typically desired to cause the soiuble silicate solution to gel after it has reached the desired location in the sub-terranean formation and to then utilize the resulting silicate gel to cause the subsequently injected aqueous hydraulic cement slurry to be directed, confined and/or emplaced in a particular, desired location within said formation. Any conventional, known technique can be employed for inducing the:initial gelation of the silicate solution. For example, if the zone of interest already contains a fairly concentrated sodium-based brine or a calcium-containing brine, the desired gela-ton will occur spontaneously upon the silicate soluton coming into contact with said brine. O-the~wise, the lnjecti~n ox the silicate solutiQn can be preceded by the injection of a quantity o a suitdble, na-turall~ occurring or sy~the-tic brine. In this latter instance, of course, a fresh water spacer will typically be pumped between said brine injec-tion and said silicate solution in order to prevent the inter-mingling, and accompanying gelation, thereof until after said materials exit the wellbore and enter the formation region of interest.
As yet another alternative, the initial gelation of the injected silicate solution can be induced by the incorporation therein (i.e., at -the earth's surface prior to pumping or injection) of a suitable reagent to bring about gelation in a sufficiently gradual fashion -to permit emplacement of said material prior to the gelation or setting thereof. For example, a strongly acidic ma-terial such as hydrochloric acid can be employed to adjust the pH of the aqueous silicate solution (which is 29,440-F -5-~3~
normally in a pH range of 11.5 or above into a range of, for example, 0.5 to 1.5 in which the gel time is suffici-ently long to allow emplacement thereof in the desired subterranean location. (See for example, U.S. Patent No.
3,375,872~. Alternatively, a reagent which gradually releases a gel inducing material (e.g., multivalent metallic or alkaline earth metal ions or a weak acid material) can be incorporated into the agueous silicate solution to bring about gradual gelation thereof following its emplacFment into the desired underground location.
(See fur example, U.S. Patent No. 2,208,766; Canadian Patent No. 1,070,936; U.S. Patent No. 3,435,899 and U.S.
Patent No. 3,294,563).
Hydraulic cement materials suitable Eor us in the present invention include those conventionally employed in oil and/or gas well cementing practices. Portland cements are preferred for this purpose and, of -those, API
Class A and API Class C Portland cements are more preferred for use in the present invention.
The preparation and pumping of the hydraulic cement slurry in the present invention is generally pursuant to conven-tional oil and gas well cement slurry preparation and handling practices. For example, conven-tional cementing additives such as dispersants, fluid loss additives, etc. can be employed, if desired. Similarly, the water contents of the cement slurries can suitably ye in the normally employed range, but may vary somewhat in quantitative terms depending upon various factors such as the specific type of cement employed, etc. For example, when an API Class A Portland cement is employed, it is preferred to employ it in the form of a slurry having a water content of about 46% by weight of cement. On-the 29,440-F -6-~33~0~
other hand, when an API Class H Portland cement is employed, it is preferred to use a slurry containing about 38 weight percent water by weight of cement.
When an aqueous spacer is employed to separate the cement slurry from the silicate solution during the sequential injection thereof, i-t is preferred to employ a fresh water spacer. Otherwise, high concentrations of sodium ions and/or the presence of significant calci~lm ion concentrations in said spacer could induce gelation of the silicate solution at the silicate solution/spacer interface during injection through the wellbore. Na-turally, however, it is possible to use a brine as the spacer it desired, so long as the na-ture o it (e.g~, the salt concentration and/or calcium content) is ah -that prem~-~u~e silicate gelat.ion is avoided during injection.
Regardless of whether the agueous spacer is based on fresh water or dilute brine materials, it can further contain various conventional spacer components such as polymeric thickener materials, and the like, as desired.
As has been previously noted, a key ~ea-ture of the present invention involves the discovery that certain polybasic, inorganic phosphate salts are capable ox substantially delaying or retarding the otherwise very rapid (e.g., in just a few seconds) gelation or setting up which occurs when a cement slurry and an aqueous silicate solution are admixed or intermingled. Suitable inorganic phosphate salts for this purpose include the various known water soluble, polybasic inorganic phosphate salts such as, for example the water soluble dibasic or tribasic alkali metal or ammonium phosphate salts.
29,440-F -7-~233a~ 8 Preferably the alkali metal phosphate salts, or alkali metal/ammonium phosphate salt mixtures, are employed to eliminate, or minimize, the generation or release of ammonia during use. Especially preferred phosphate salts
5 . for use herein are disodium phosphate and trisodium phosphate.
The aforementioned water soluble polybasic inorganic phosphate salt-can be incorporated into the soluble silicate/cement slurry system in any convenient fashion so long as it is caused to be present at the time that said cement slurry and silicate solution ini-tially come into contact or intermingle wi-th each other. For example, -the phosphate sal-t can be admixed into -the cement slurry itself, -thy s.ilic~te solution i-tsel~ or it both. Alternatively, an aqueous spacer fluid havirlg -the phosphate salt dissolved therein can be employed to separate the cement slurry from the silicate solution during the sequential injection thereof. Most preferably an aqueous spacer fluid is employed in the present inven-tion and at least a portion of the requisite inorganicphosphate salt is dissolved therein.
The minimum amoun-t of the water soluble, polybasic inorganic phosphate salt -to be employed herein corresponds to an amount sufficient to reduce the gel forma-tion rate upon the admixing or intermingling together of the hydraulic cement slurry and the silicate solution. The normal gelation time upon admixing such components in the absence of the aforementioned phosphate salt typically corresponds to just a few seconds. Preferably, the afore-mentioned phosphate salt is employed in the present invention in an amount sufficient to provide a delayed gelation time of at least about onehalf hour, and preferably at least 29,440-F -8-gL;23~
about one full hour, following the initi.al intermingling of the cement slurry and silicate solution components hereof.
In quantitative terms, the aforementioned phosphate salt will typically be employed in an amount ranging, on an anhydrous salt basis, of from 0.5 to 5 (preferably from 0.75 to 2) weight percent based upon the combined weight of the cement slu-rry, the aqueous spacer (if any) and the silicate solution. In those cases where an aqueous spacer fluid is employed and wherein the phosphate salt is introduced into the system by clissolu-tion into the spacer fluid, the phosphate sal-t will typically constitute from 2 to 20 (preferably from 2 to 10 and most pr~:erably from 2 . 5 to 5 ) weight percen-t of slid aqueous 15 spacer fluid.
The present invention is further illustrated by reference to the following working examples Example 1 ._ A 40 Baume aqueous sodium silicate solution having a 3.22:1 Si0 to Na20 weight ratio is diluted by admixing 42.6 parts of weight thereof with 57.4 parts by weight of water.
One (1) part by weight of the resulting diluted sodium silicate solution is simultaneously admixed with two (2) parts by weight of an API Class A Portland cemenk slurry containing 46 percent water based on the weight of the cement and with one (1) part by weight of a series of different aqueous spacer compositions having dlfferent amounts of trisodium phosphate or disodium phosphate dissolved therein.
29,440-F -9--10- 23~8 The phosphate salt content of the various spacer compositions along with the gel -time for the corresponding blends prepared therewith are summarized in Table I below.
TABLE I
Phosphate Salt _ Run Number Type Contentl~Gel Time (Weight %) l* None None 2 Sec.
2 Na3P0~,.12H20 5% 5 Sec.
3 Na3P04-1 2 8% 5 min.
4 Na3Po4 l2H2 10% 2 hrs.
N~2HP04 5% 15 min.
* Not an example of the present invention.
1. Weight percent based on the -total weigh-t of the aqueous spacer material.
Large quantities of brine are being produced in an oi]. well. Normal perforation and cement squeeze operations in the water zone allow cement to enter the weaker water zone without sealing channels between the water and oil zone.
29,440-F -10-3~8 A 500 gallon ~1.89 m3) batch of calcium chloride brine solution is prepared containing 9 weight percent CaCl2 on a total weight basis. Two lO00 gallon ~3.785 m ) batches of an aqueous sodium silicate solution are also prepared. Each lO00 gallon (3.785 m3) batch is prepared by adding ~40 gallons (2.42 m3) of water to a tank and adding 350 gallons (1.32 m3) of 40Be liquid sodium silicate solution(water glass containing about 38 - percent solids, 3;22 ratio SiO2 to Na20 by weight) with agitation.
The well is perforated in -the water zone and a squeeze packer is set between the per:~or~tions in the water æone and the producing perEora-tions. the 500 gallon (1.89 m3) batch ox CaCl2 solu-tion is p-lmped down lS the tubing into the water zone followed by 200 gallons (0.757 m ) of fresh water which is in turn followed by 2000 gallons (7.57 m3) of the sodium silicate mix and another 200 gallons (0.757 m3) of water containing lO
percent tri sodium phosphate dodecyl hydrate and then by an aqueous slurry containing lO0 sacks (4268 kg) of Portland cement containing 4 percent calcium chloride to accelerate set.
The initial sodium silicate solu-tion orms a gel upon admixture with the CaCl2 brine in the ini-tial flow areas of the formation and thereby diver-ts the remaining fluid to other areas. The Portland cement sets fairly rapidly on contacting the sodium silicate solution thus reinforcing the weak section and forcing the remaining cement into the channels leading to the producing section. The setting of the Portland cement is, however, substantially delayed relative to what i-t would have been in the absence of the trisodium phosphate component in the abovenoted aqueous spacer composition.
29,440-F -11-"
~2~34~
While the present invention has been described herein by reference to certain specific embodimen-ts and illustrative examples thereof, such is not to be under-stood or interpreted as in any way limiting the scope of the instantly claimed invention.
29,440-F -12-
The aforementioned water soluble polybasic inorganic phosphate salt-can be incorporated into the soluble silicate/cement slurry system in any convenient fashion so long as it is caused to be present at the time that said cement slurry and silicate solution ini-tially come into contact or intermingle wi-th each other. For example, -the phosphate sal-t can be admixed into -the cement slurry itself, -thy s.ilic~te solution i-tsel~ or it both. Alternatively, an aqueous spacer fluid havirlg -the phosphate salt dissolved therein can be employed to separate the cement slurry from the silicate solution during the sequential injection thereof. Most preferably an aqueous spacer fluid is employed in the present inven-tion and at least a portion of the requisite inorganicphosphate salt is dissolved therein.
The minimum amoun-t of the water soluble, polybasic inorganic phosphate salt -to be employed herein corresponds to an amount sufficient to reduce the gel forma-tion rate upon the admixing or intermingling together of the hydraulic cement slurry and the silicate solution. The normal gelation time upon admixing such components in the absence of the aforementioned phosphate salt typically corresponds to just a few seconds. Preferably, the afore-mentioned phosphate salt is employed in the present invention in an amount sufficient to provide a delayed gelation time of at least about onehalf hour, and preferably at least 29,440-F -8-gL;23~
about one full hour, following the initi.al intermingling of the cement slurry and silicate solution components hereof.
In quantitative terms, the aforementioned phosphate salt will typically be employed in an amount ranging, on an anhydrous salt basis, of from 0.5 to 5 (preferably from 0.75 to 2) weight percent based upon the combined weight of the cement slu-rry, the aqueous spacer (if any) and the silicate solution. In those cases where an aqueous spacer fluid is employed and wherein the phosphate salt is introduced into the system by clissolu-tion into the spacer fluid, the phosphate sal-t will typically constitute from 2 to 20 (preferably from 2 to 10 and most pr~:erably from 2 . 5 to 5 ) weight percen-t of slid aqueous 15 spacer fluid.
The present invention is further illustrated by reference to the following working examples Example 1 ._ A 40 Baume aqueous sodium silicate solution having a 3.22:1 Si0 to Na20 weight ratio is diluted by admixing 42.6 parts of weight thereof with 57.4 parts by weight of water.
One (1) part by weight of the resulting diluted sodium silicate solution is simultaneously admixed with two (2) parts by weight of an API Class A Portland cemenk slurry containing 46 percent water based on the weight of the cement and with one (1) part by weight of a series of different aqueous spacer compositions having dlfferent amounts of trisodium phosphate or disodium phosphate dissolved therein.
29,440-F -9--10- 23~8 The phosphate salt content of the various spacer compositions along with the gel -time for the corresponding blends prepared therewith are summarized in Table I below.
TABLE I
Phosphate Salt _ Run Number Type Contentl~Gel Time (Weight %) l* None None 2 Sec.
2 Na3P0~,.12H20 5% 5 Sec.
3 Na3P04-1 2 8% 5 min.
4 Na3Po4 l2H2 10% 2 hrs.
N~2HP04 5% 15 min.
* Not an example of the present invention.
1. Weight percent based on the -total weigh-t of the aqueous spacer material.
Large quantities of brine are being produced in an oi]. well. Normal perforation and cement squeeze operations in the water zone allow cement to enter the weaker water zone without sealing channels between the water and oil zone.
29,440-F -10-3~8 A 500 gallon ~1.89 m3) batch of calcium chloride brine solution is prepared containing 9 weight percent CaCl2 on a total weight basis. Two lO00 gallon ~3.785 m ) batches of an aqueous sodium silicate solution are also prepared. Each lO00 gallon (3.785 m3) batch is prepared by adding ~40 gallons (2.42 m3) of water to a tank and adding 350 gallons (1.32 m3) of 40Be liquid sodium silicate solution(water glass containing about 38 - percent solids, 3;22 ratio SiO2 to Na20 by weight) with agitation.
The well is perforated in -the water zone and a squeeze packer is set between the per:~or~tions in the water æone and the producing perEora-tions. the 500 gallon (1.89 m3) batch ox CaCl2 solu-tion is p-lmped down lS the tubing into the water zone followed by 200 gallons (0.757 m ) of fresh water which is in turn followed by 2000 gallons (7.57 m3) of the sodium silicate mix and another 200 gallons (0.757 m3) of water containing lO
percent tri sodium phosphate dodecyl hydrate and then by an aqueous slurry containing lO0 sacks (4268 kg) of Portland cement containing 4 percent calcium chloride to accelerate set.
The initial sodium silicate solu-tion orms a gel upon admixture with the CaCl2 brine in the ini-tial flow areas of the formation and thereby diver-ts the remaining fluid to other areas. The Portland cement sets fairly rapidly on contacting the sodium silicate solution thus reinforcing the weak section and forcing the remaining cement into the channels leading to the producing section. The setting of the Portland cement is, however, substantially delayed relative to what i-t would have been in the absence of the trisodium phosphate component in the abovenoted aqueous spacer composition.
29,440-F -11-"
~2~34~
While the present invention has been described herein by reference to certain specific embodimen-ts and illustrative examples thereof, such is not to be under-stood or interpreted as in any way limiting the scope of the instantly claimed invention.
29,440-F -12-
Claims (11)
- THE EMBODIMENTS OF THE INVENTION IN WHICH AN EXCLUSIVE
PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:
l. A process for plugging a zone in a subter-ranean formation by sequentially injecting an aqueous solution of a water soluble silicate material followed by an aqueous spacer material and an aqueous hydraulic cement slurry, characterized by incorporating into said silicate solution, said aqueous spacer material or said hydraulic cement slurry, a water soluble, inorganic polybasic phosphate salt to reduce the rate of gel forma-tion which occurs when said silicate material, spacer and hydraulic cement are intermingled. - 2. The process of Claim 1 wherein the water soluble phosphate salt is a dibasic or tribasic alkali metal or ammonium phosphate salt, or a mixture thereof.
- 3. The process of Claim 1 wherein the water soluble phosphate salt is trisodium phosphate or disodium phosphate.
- 4. The process of Claim 1 wherein the water soluble phosphate salt is incorporated into the aqueous spacer material in an amount, on an anhydrous basis, of from 2 to 20 weight percent of the aqueous spacer material.
- 5. The process of Claim 4 wherein the water soluble phosphate salt constitutes, on an anhydrous basis, from 2 to 10 weight percent of said aqueous spacer material.
- 6. The process of Claim 4 wherein the water soluble phosphate salt constitutes, on an anhydrous basis, from 2.5 to 5 weight percent of said aqueous spacer material.
- 7. The process of any one of Claims 1 to 3 wherein the water soluble phosphate salt is employed in an amount sufficient to provide a delayed gelation time of at least about 0.5 hours following the intermingling of said water soluble silicate, cement and spacer materials.
- 8. The process of Claim 1 wherein the water soluble phosphate salt is employed in an amount, on an anhydrous salt basis, of from 0.5 to 5 weight per-cent based upon the combined weight of the cement slurry, the silicate solution and, optionally, the aqueous spacer.
- 9. The process of Claim 1 wherein the water soluble silicate comprises silicon dioxide and sodium oxide in a ratio of from 0.5 to 4 parts by weight of silicon dioxide per part by weight of sodium oxide.
- 10. The process of Claim 1 which further comprises preceding the sequential injection of the aqueous silicate solution, spacer and cement slurry by the sequential injection of an aqueous calcium chloride solution followed by an aqueous spacer fluid.
- 11. A method of retarding the gelation of an aqueous mixture of a water soluble silicate material and a hydraulic cement material which comprises incorporating into said mixture a water soluble, polybasic inorganic phosphate salt in an amount sufficient to substantially reduce the gelation rate of said mixture.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA000492014A CA1233408A (en) | 1985-10-01 | 1985-10-01 | Process for plugging a subterranean formation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA000492014A CA1233408A (en) | 1985-10-01 | 1985-10-01 | Process for plugging a subterranean formation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1233408A true CA1233408A (en) | 1988-03-01 |
Family
ID=4131518
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA000492014A Expired CA1233408A (en) | 1985-10-01 | 1985-10-01 | Process for plugging a subterranean formation |
Country Status (1)
| Country | Link |
|---|---|
| CA (1) | CA1233408A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5709267A (en) * | 1995-10-23 | 1998-01-20 | Amoco Corporation | Aqueous particulate dispersion for reducing the water influx rate into a wellbore |
-
1985
- 1985-10-01 CA CA000492014A patent/CA1233408A/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5709267A (en) * | 1995-10-23 | 1998-01-20 | Amoco Corporation | Aqueous particulate dispersion for reducing the water influx rate into a wellbore |
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