Sealant material for subterranean wells

09688578 ยท 2017-06-27

Assignee

Inventors

Cpc classification

International classification

Abstract

A method is for sealing hydrocarbon wells, wherein a composition is used. The composition comprises a prepolymer; a free radical initiator; a hydraulic material; a monomer and water. The composition further comprises an inhibitor.

Claims

1. A method for sealing hydrocarbon wells, the method comprising: Step Ainjecting a composition for sealing hydrocarbon wells into a hydrocarbon well, wherein the composition comprises a prepolymer, a free radical initiator, a hydraulic material, a monomer and water and inhibitor, wherein a setting time and a hardening time of the composition are set by choosing the amounts of initiator and inhibitor for precisely tailoring of the composition to the relevant well conditions and placement times involved, and Step Bletting the composition of step A cure in the hydrocarbon well at a temperature of 0 C. to 150 C., wherein in step A the prepolymer comprises a curable material, wherein the curable material is selected from a group consisting of unsaturated polyesters and epoxy vinyl esters, and wherein in step A the monomer comprises an unsaturated compound, wherein the unsaturated compound is selected from a group consisting of vinyl-, allyl- and acrylate compounds, wherein the composition is prepared by blending the prepolymer and a cement slurry comprising the hydraulic material prior to injection, and wherein the composition comprises a weight ratio of the prepolymer to the cement slurry between 1:99 to 20:80.

2. The method according to claim 1, wherein in step A the inhibitor comprises p-benzoquinone.

3. The method according to claim 1, wherein in step A the composition further comprises an accelerator.

4. The method according to claim 3, wherein in step A the accelerator comprises a compound, wherein the compound is selected from a group consisting of inorganic salts, transition metal compounds, inorganic hydroxides, amides, amines and aromatic compounds.

5. The method according to claim 4, wherein in step A the accelerator comprises N,N-dimethyl-p-toluidine.

6. The method according to claim 1, wherein in step A the unsaturated compound is selected from a group consisting of styrene and vinyl toluene.

7. The method according to claim 1, wherein in step A the unsaturated compound comprises diallylphthalate.

8. The method according to claim 1, wherein in step A the unsaturated compound is selected from a group consisting of 2-hydroxy ethyl methacrylate, 2-hydroxy propyl methacrylate and butanediol dimethacrylate.

9. The method according to claim 1, wherein in step A the hydraulic material comprises a hydratable material selected from a group consisting of Portland cement, Portland blastfurnace cement, Portland flyash cement, Portland pozzolan cement, Portland silica fume cement, masonry cement, pozzolan-lime cements, supersulfated cements, calcium aluminate cements, phosphate cements and geopolymer cements, and gypsum.

10. The method according to claim 9, wherein in step A the hydratable material comprises Portland cement.

11. The method according to claim 1, wherein in step A the water is present in an amount of 20 to 60 weight percent of the hydraulic material.

12. The method according to claim 1, wherein in step A the prepolymer is present in an amount of 10 to 90 weight percent of the total mass of the composition.

13. The method according to claim 1, wherein in step A the free radical initiator comprises a dissociable compound, wherein the dissociable compound is selected from a group consisting of peroxides and azo compounds.

14. The method according to claim 13, wherein in step A the dissociable compound is selected from a group consisting of tert-Butyl cumyl peroxide and dibenzoyl peroxide.

15. The method according to claim 1, wherein in step A the composition further comprises a setting inhibitor, wherein the setting inhibitor is selected from a group consisting of sucrose, tartaric acid, gluconic acid -lactone, lignosulfonates and organic phosphonic acids.

16. The method according to claim 15, wherein in step A the setting inhibitor comprises calcium lignosulfonate.

17. The method according to claim 1, wherein in step A the composition further comprises a setting accelerator, wherein the setting accelerator is selected from a group consisting of chloride salts, carbonates, silicates, aluminates, nitrates, nitrites, sulfates, thiosulfates and hydroxides.

18. The method according to claim 1, wherein in step A the composition further comprises a dispersing agent.

19. The method according to claim 1, wherein in step A the composition further comprises a viscosifying agent.

20. The method according to claim 1, wherein in step A the composition further comprises a stabilizing agent.

21. The method according to claim 1, wherein in step A the composition further comprises a density modifying agent.

22. The method according to claim 21, wherein in step A the density modifying agent is selected from a group consisting of glass beads, trimanganese tetroxide, calcium carbonate and barite.

23. The method according to claim 1, wherein the composition is prepared by blending a prepolymer mixture, the prepolymer mixture comprising the prepolymer and the free radical initiator, and the cement slurry, the cement slurry comprising the hydraulic material and water.

24. A method for sealing hydrocarbon wells, the method comprising: Step Ainjecting a composition for sealing hydrocarbon wells into a hydrocarbon well, wherein the composition comprises a prepolymer, a free radical initiator, a hydraulic material, a monomer and water and inhibitor, wherein a setting time and a hardening time of the composition are set by choosing the amounts of initiator and inhibitor for precisely tailoring of the composition to the relevant well conditions and placement times involved, and Step Bletting the composition of step A cure in the hydrocarbon well at a temperature of 0 C. to 150 C., wherein in step A the prepolymer comprises epoxy vinyl esters, wherein in step A the monomer comprises an unsaturated compound, wherein the unsaturated compound is selected from a group consisting of vinyl-, allyl- and acrylate compounds, and wherein the composition is prepared by blending the prepolymer and hydraulic material prior to injection.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) In the following it is described examples of preferred embodiments illustrated in the accompanying drawings, wherein:

(2) FIG. 1 shows a time vs. temperature trace of experiments 1-3;

(3) FIG. 2 shows a time vs. temperature trace of experiments 4-5;

(4) FIG. 3 shows a time vs. temperature trace of experiments 6-9; and

(5) FIG. 4 shows a composition vs. compressive strength bar-graph.

DETAILED DESCRIPTION OF THE DRAWINGS

(6) It should be noted that the below-mentioned embodiments illustrate rather than limit the invention, and that those skilled in the art will be able to design many alternative embodiments without departing from the scope of the appended claims. In the claims, any reference signs placed between parentheses shall not be construed as limiting the claim. Use of the verb comprise and its conjugations does not exclude the presence of elements or steps other than those stated in a claim. The article a or an preceding an element does not exclude the presence of a plurality of such elements. In the device claim enumerating several means, several of these means may be embodied by one and the same item. The mere fact that certain measures are recited in mutually different dependent claims does not indicate that a combination of these measures cannot be used to advantage.

(7) In the following a series of experiments are described to illustrate preferred embodiments of the invention.

(8) A first series of experiments (experiment 1 to 5, see FIG. 1-2 and table 1) were carried out to examine the effect of varying amounts of radical initiator, inhibitor and a cement setting time inhibitor on the setting time and hardening time of the compositions. The radical initiator used was t-butyl cumyl peroxide, and the radical- and cement inhibitors were -benzoquinone and calcium lignosulfonate, respectively. The compositions were made by blending a prepolymer mixture (part A) and cement slurry (part B).

(9) The prepolymer mixture (part A) was prepared by mixing prepolymer, radical initiator and optionally an inhibitor. The cement slurry (part B) was prepared by blending cement, water and optionally a setting time inhibitor. When part A and part B had been blended separately to achieve sufficient homogeneity, quantities of part A and part B were weighed in and part A and B were blended. The quantities of the components that were used are shown in table 1. All quantities are given in weight percent. The setting time and hardening time for each of the mixtures was recorded. The setting time was defined as the time from start of the reaction until appearance of the exothermic peak. The hardening time was defined as the time from start of the reaction until the exothermic peak returned to the baseline. In case of an unclear exothermic peak, the setting time was defined as the time from start of the reaction until the composition resisted flow by pouring.

(10) TABLE-US-00001 TABLE 1 Components EX. 1 EX. 2 EX. 3 EX. 4 EX. 5 Prepolymer mixture (part A): Prepolymer 100 100 100 100 100 Initiator: Tert-Butyl cumyl peroxide 2 1 0.3 0.3 0.3 Inhibitor: p-penzoquinone 0.1 0.2 Cement slurry (Part B): Cement type G 100 100 100 100 100 Water 30 30 30 30 30 Inhibitor: calcium lignosulfonate 0.1 0.1 Part A/Part B 4/1 4/1 4/1 4/1 4/1 Application Temperature ( C.) 115 115 115 115 115 Setting time (min) 20 30 65 80 110 Hardening time (min) 50 70 110 120 240

(11) It could be observed from experiment 1 through 3 that the reduction of the amount of initiator increased both the setting time and the hardening time, providing a means for controlling these parameters. Additional inclusion of an inhibitor and a cement hardening inhibitor in experiments 4-5 further increased the setting time and hardening time.

(12) A second series of experiments (experiment 6-9, see FIG. 3 and table 2) were carried out to examine the effect of increasing amounts of accelerator on the setting time and hardening time. The amount of radical initiator was held fixed at 3 weight percent and the cement slurry (Part B) did not contain any inhibitor. The experimental procedure concerning blending of the components was identical to the procedure described for experiments 1-5. The quantities of the components are shown in table 2. All quantities are given in weight percent.

(13) TABLE-US-00002 TABLE 2 Components EX. 6 EX. 7 EX. 8 EX. 9 Prepolymer mixture (part A): Prepolymer 100 100 100 100 Initiator: Dibenzoyl Peroxide 3 3 3 3 Accelerator: N,N-deimethyl-p-toluidine 0.2 0.3 0.4 Cement slurry (Part B) Cement type G 100 100 100 100 Water 30 30 30 30 Part A/Part B (weight parts) 1/1 1/1 1/1 1/1 Application Temperature ( C.) 25 25 25 25 Setting time (min) 1 day 35 20 10 Hardening time (min) 1 day 180 140 100

(14) It could be observed from experiment 6-9 that increasing the amount of accelerator reduced both the setting time and the hardening time, providing an additional means for controlling these parameters.

(15) A third series of experiments were carried out to determine the compressive strength of several blend ratios of prepolymer mixture and cement slurry (see FIG. 4). The various blends of prepolymer mixture and the cement slurry was blended and hardened in a container to form cylindrical test specimens of approximately 1.4 inches in diameter and 1.4 inches in length. All samples were stored for 4 weeks after preparation before measuring the compressive strength. The test specimens were subjected to pressure using a Carver press (model 3851-CE), and the forces at which the samples failed were recorded. The leftmost column in FIG. 4 shows the force at which pure, hardened cement failed (4000 lbs.). The rightmost column in FIG. 4 shows the force at which pure, hardened polymer failed (7000 lbs.). It was sought to find a ratio at which the blend of prepolymer mixture and cement slurry would show a higher compressive strength than either pure hardened cement or pure hardened prepolymer alone. Such a blend would exhibit a synergistic property in relation to the maximum attainable compressive strength. The ratio between the prepolymer mixture and cement that showed a synergistic effect was found to be a blend with a 20/80 polymer/cement ratio, which attained a compressive strength of 8400 lbs. Specimens made from ratios of 50/50 weight percent polymer/cement were found to show a lower compressive strength than either hardened prepolymer or hardened cement alone, and consequently this ratio proved to exhibit an antagonistic effect on the compressive strength.

(16) A significant advantage is gained from the ability to increase the compressive strength of pure cement by addition of the said prepolymer mixture. At even low levels of addition of the prepolymer mixture (20/80 prepolymer/cement ratio), the compressive strength of the cement was surprisingly found to be more than doubled compared to cement alone.

(17) Furthermore, another significant advantage related to the invention is the ability to control the setting time and the hardening time of the composition by varying the amounts of initiator, accelerator and cement inhibitor. This allows for a precise tailoring of the composition to the relevant well conditions and placement times involved.