# US 10,479,925 B2 · Use of hexamethylenetetramine intensifier for high temperature emulsified acid system

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- Number: US 10,479,925 B2
- Document ID: US10479925B2
- Status: Granted
- Kind: B2
- Application number: 15/502,761
- Filed: 2014-09-15
- Published: 2017-08-17
- Granted: 2019-11-19
- Earliest claimed: 2014-09-15
- Assignees: Halliburton Energy Services, Inc.
- Applicants: Halliburton Energy Services, Inc.
- Inventors: Nisha Kaustubh Pandya; Juanita Cassidy
- Web page: https://patentgrep.com/patent/US10479925B2

## CPC

- C09K 8/54: Compositions for in situ inhibition of corrosion in boreholes or wells
- C09K 8/602: {containing surfactants}
- C09K 8/74: combined with additives added for specific purposes
- E21B 41/02: in situ inhibition of corrosion in boreholes or wells
- E21B 43/25: Methods for stimulating production {(by vibrating earth formations E21B43/003)}
- C09K 2208/32: Anticorrosion additives
- C09K: MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- E21B: EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS

## Abstract

The invention provides a method, composition, and system for inhibiting corrosion where the composition forms an acid-in-oil emulsion comprising hexamethylenetetramine, a corrosion inhibitor; and at least one emulsifier.

## Claims

### Claim 1

A method of treating a subterranean formation comprising: contacting the subterranean formation with a corrosion inhibition composition consisting essentially of:
(A) hexamethylenetetramine,
(B) a corrosion inhibitor,
(C) a combination of emulsifiers, the combination comprising a long chain polyamine and an alkoxylate amine,
(D) an acid in an aqueous acid solution, and
(E) optionally, a corrosion inhibiting intensifier,
wherein the corrosion inhibition composition does not comprise an acetylenic alcohol, and
wherein the corrosion inhibition composition is a stable acid-in-oil emulsion at temperatures above about 300° F.

### Claim 2 (depends on 1)

The method according to claim 1, wherein the corrosion inhibition composition has the corrosion inhibiting intensifier.

### Claim 3 (depends on 2)

The method according to claim 2, wherein the corrosion inhibiting intensifier is potassium iodide, cuprous chloride, or a combination thereof.

### Claim 4 (depends on 1)

The method according to claim 1, wherein the corrosion inhibitor has cinnamaldehyde.

### Claim 5 (depends on 4)

The method according to claim 4, wherein the corrosion inhibitor has a quaternized quinoline, a quaternized isoquinoline, or a combination thereof.

### Claim 6 (depends on 1)

The method according to claim 1 wherein the acid is present in an amount of about 5% to about 35% by weight of the aqueous acid solution in the corrosion inhibition composition.

### Claim 7 (depends on 6)

The method according to claim 6, wherein the acid is present in an amount of about 20% to about 30% by weight of the aqueous acid solution in the corrosion inhibition composition.

### Claim 8 (depends on 1)

The method according to claim 1, wherein the contacting occurs at a temperature of about 300° F. to about 370° F.

### Claim 9 (depends on 8)

The method according to claim 8, wherein the contacting occurs at a temperature of about 325° F. to about 350° F.

### Claim 10 (depends on 1)

The method according to claim 1, wherein the hexamethylenetetramine is present in an amount of about 0.5% to about 5% based upon the total weight of the corrosion inhibition composition.

### Claim 11 (depends on 10)

The method according to claim 10, wherein the hexamethylenetetramine is present in an amount of about 1% to about 4% based upon the total weight of the corrosion inhibition composition.

### Claim 12 (depends on 11)

The method according to claim 11, wherein the hexamethylenetetramine is present in an amount of about 2.5% based upon the total weight of the corrosion inhibition composition.

### Claim 13 (depends on 1)

The method according to claim 1, wherein the corrosion inhibitor is present in an amount of about 0.1% to about 5% based upon the total weight of the corrosion inhibition composition.

### Claim 14 (depends on 1)

The method according to claim 1, wherein the emulsifier is present in an amount of about 0.1% to about 5% based upon the total weight of the corrosion inhibition composition.

### Claim 15 (depends on 1)

The method according to claim 1, wherein the long chain polyamine is PIBA (polyisobutyl amine) and the alkoxylate amine is Ethomeen T/12 (tallow amine ethoxylate).

### Claim 16 (depends on 1)

A system configured to perform the method of claim 1, wherein the system comprises:
the corrosion inhibition composition; and
a drill string disposed in a wellbore, the drill string comprising a drill bit at a subterranean end of the drill string.

### Claim 17 (depends on 16)

The system according to claim 16, wherein the system further comprises:
an annulus between the drill string and the wellbore; and
a pump configured to circulate the corrosion inhibition composition through the drill string.

### Claim 18 (depends on 17)

The system according to claim 17, wherein the system further comprises a fluid processing unit configured to process the composition exiting the annulus to generate a cleaned composition for recirculation through the wellbore.

### Claim 19 (depends on 1)

A system configured to perform the method of claim 1, wherein the system comprises:
the corrosion inhibition composition;
a tubular disposed in a wellbore; and
a pump configured to pump the corrosion inhibition composition into the subterranean formation.

### Claim 20

A corrosion inhibition composition consisting essentially of:
(A) hexamethylenetetramine,
(B) a corrosion inhibitor,
(C) a combination of emulsifiers, the combination comprising a long chain polyamine and an alkoxylate amine,
(D) an aqueous acid, and
(E) optionally, a corrosion inhibiting intensifier,
wherein the corrosion inhibition composition does not comprise an acetylenic alcohol, and
wherein the corrosion inhibition composition is a stable acid-in-oil emulsion at temperatures above about 300° F.

### Claim 21 (depends on 20)

The composition according to claim 20, wherein the corrosion inhibition composition has the corrosion inhibiting intensifier.

### Claim 22 (depends on 21)

The composition according to claim 21, wherein the corrosion inhibiting intensifier is potassium iodide, cuprous chloride, or a combination thereof.

### Claim 23 (depends on 20)

The composition according to claim 20, wherein the corrosion inhibitor has cinnamaldehyde.

### Claim 24 (depends on 23)

The composition according to claim 23, wherein the corrosion inhibitor has a quaternized quinoline, a quaternized isoquinoline, or a combination thereof.

### Claim 25 (depends on 20)

The corrosion inhibition composition according to claim 20, wherein the long chain polyamine is PIBA (polyisobutyl amine) and the alkoxylate amine is Ethomeen T/12 (tallow amine ethoxylate).
