IP Library › Granted Patent US 9,234,126
Granted Patent B2
US 9,234,126 · App. 13/887,462 · Granted Jan 12, 2016

Dual retarded acid system for well stimulation

Inventor: Chaitanya M Karale (Pune, IN)
Assignee: Halliburton Energy Services, Inc.
C09K8/725C09K8/72C09K8/82
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Quick Facts
Patent No.
US 9,234,126
App. No.
13/887,462
Granted
Jan 12, 2016
Kind
B2
Abstract

A composition in the form of an emulsion having: (i) a continuous oil phase comprising: (a) an oil; (b) an emulsifier; and (ii) an internal aqueous phase comprising: (a) water; (b) acid such that the aqueous phase has an initial pH of less than about 2; (c) a viscosity-increasing agent; and (d) a crosslinker, wherein the crosslinker is selected or controlled to crosslink the viscosity-increasing agent at a pH range somewhere in a range of about 1.5 to about 6.5 and that is at least higher than the initial pH of the aqueous phase. A method of acidizing a treatment zone of a subterranean formation in a well includes the steps of: (A) forming a treatment fluid comprising such a composition; and (B) introducing the treatment fluid into a well.

Claims (21)

1. A method of acidizing a treatment zone of a subterranean formation in a well, the method comprising the steps of:

(A) forming a treatment fluid in the form of an emulsion, the treatment fluid comprising:

(i) a continuous oil phase comprising:

(a) an oil; and

(b) an emulsifier; and

(ii) an internal aqueous phase comprising:

(a) water;

(b) acid such that the aqueous phase has an initial pH of less than about 2;

(c) a viscosity-increasing agent; and

(d) a crosslinker, wherein the crosslinker is selected or controlled to crosslink the viscosity-increasing agent at a pH range somewhere in a range of about 1.5 to about 6.5 and that is at least higher than the initial pH of the aqueous phase; and

(B) introducing the treatment fluid into a well, wherein a design temperature in the subterranean formation is at least about 121° C. (about 250° F.).

2. The method according to claim 1 , wherein the oil of the external oil phase comprises an oil selected from the group consisting of petroleum, diesel, kerosene, or synthetic oil.

3. The method according to claim 1 , wherein the emulsifier is a cationic amine.

4. The method according to claim 1 , wherein the acid comprises a strong acid.

5. The method according to claim 4 , wherein the strong acid comprises hydrochloric acid in a concentration of at least 5% by weight of water of the internal aqueous phase.

6. The method according to claim 4 , wherein the strong acid comprises hydrochloric acid in a concentration in the range of about 24% to about 28% by weight of water of the internal aqueous phase.

7. The method according to claim 1 , wherein the viscosity-increasing agent comprises a polyacrylamide based-polymer.

8. The method according to claim 1 , wherein the crosslinker comprises ferric chloride.

9. The method according to claim 1 , additionally comprising a corrosion inhibitor.

10. The method according to claim 9 , additionally comprising a corrosion inhibitor intensifier.

11. The method according to claim 1 , wherein the subterranean formation is a carbonate formation.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 6, 2013
From: KARALE, CHAITANYA M
To: HALLIBURTON ENERGY SERVICES, INC.
Reel/Frame 030353/0065 →
Continuity (1)
Related Publication 20140329725A1 · Nov 6, 2014