# US 5,346,010 A · Precipitation of scale inhibitors in subterranean formations

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- Number: US 5,346,010 A
- Document ID: US5346010A
- Status: Granted
- Kind: A
- Application number: 08/040,784
- Filed: 1993-03-31
- Granted: 1994-09-13
- Earliest claimed: 1993-03-31
- Assignees: Shell Oil Company
- Inventors: Gerald C. Adams; Robert J. Faircloth; Jimmie B. Lawson
- Web page: https://patentgrep.com/patent/US5346010A

## CPC

- C09K 8/528: inorganic depositions, e.g. sulfates or carbonates
- Y10S 507/927: Well cleaning fluid
- Y10S 507/934: with inhibitor
- C09K: MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- Y10S: TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS

## Abstract

Scale inhibitors are precipitated in a formation by injection in an acidic solution comprising a base generating component and a chelating agent. The inhibitor is preferably a calcium salt of an organic phosphonate. The chelating agent prevents iron ions from causing premature hydrolysis of the base generating component.

## Claims

### Claim 1

A process to emplace a scale inhibitor within a brine containing subterranean formation in the vicinity of a producing wellbore comprising:
providing an acidic aqueous solution comprising a dissolved scale inhibitor and a metal cation which combination is slightly soluble in the formation brine, a precursor which is capable of reacting within the formation to become a basic component and a chelating agent in an amount effective to prevent decomposition of the precursor upon contact with steel tubulars;
injecting the acidic aqueous solution into the formation through the wellbore; and
producing formation fluids from the wellbore after the precursor has generated an amount of basic material sufficient to cause an amount of the scale inhibitor and metal cation to precipitate within the formation that is effective to provide scale inhibition.

### Claim 2 (depends on 1)

The process of claim 1 wherein the chelating agent is ethylenediaminetetraacetic acid.

### Claim 3 (depends on 2)

The process of claim 2 wherein the concentration of ethylenediaminetetraacetic acid in the acidic solution is between about 0.002 and about 0.016 moles/liter.

### Claim 4 (depends on 3)

The process of claim 3 wherein the amide is urea.

### Claim 5 (depends on 4)

The process of claim 4 wherein the injection of the overflush fluid is following by a period when fluids are neither injected nor produced for the wellbore.

### Claim 6 (depends on 3)

The process of claim 3 wherein the amide is formamide.

### Claim 7 (depends on 3)

The process of claim 3 wherein the amide is dimethyl formamide.

### Claim 8 (depends on 1)

The process of claim 1 wherein the chelating agent is selected from the group consisting of ethylenediaminetetraacetic acid (EDTA), nitriloacetic Acid, and Citric Acid.

### Claim 9 (depends on 1)

The process of claim 1 wherein the inhibitor comprises nitrilotri(methylene phosphonic acid).

### Claim 10 (depends on 1)

The process of claim 1 wherein the precursor is an amide.

### Claim 11 (depends on 1)

The process of claim 1 wherein the injection of the acidic aqueous solution into the formation is followed by injection of an overflush fluid into the formation.

### Claim 12 (depends on 1)

The process of claim 1 wherein the inhibitor comprises diethylenetriaminepenta(methylene phosphonic acid).

### Claim 13 (depends on 1)

The process of claim 1 wherein the inhibitor comprises a nitrogen containing phosphonate.

### Claim 14 (depends on 1)

The process of claim 1 wherein the precursor comprises urea.

### Claim 15 (depends on 14)

The process of claim 14 wherein the inhibitor comprises a nitrogen containing phosphonate.

### Claim 16 (depends on 14)

The process of claim 14 wherein the chelating agent is selected from the group consisting of ethylenediaminetetraacetic acid (EDTA), nitriloacetic Acid, and Citric Acid.

### Claim 17 (depends on 14)

The process of claim 14 wherein the chelating agent is ethylenediaminetetraacetic acid in a concentration of between about 0.004 and about 0.008 moles per liter.