IP Library Granted Patent US 9,096,805
Granted Patent B2
US 9,096,805 · App. 12/209,845 · Granted Aug 4, 2015

Anhydride demulsifier formulations for resolving emulsions of water and oil

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Quick Facts
Patent No.
US 9,096,805
App. No.
12/209,845
Granted
Aug 4, 2015
Kind
B2
Abstract

The present invention includes the use of anhydride compositions, including alkyl and aryl anhydrides, for use as a demulsifier in resolving water external emulsions of water and oil and complex emulsions of water and oil. In particular, the anhydride composition can be used alone or in a blend with other demulsifiers. Suitable anhydrides suitable for the present invention include acetic and propionic, with acetic anhydride being preferred. The anhydride composition can be added directly to crude oil emulsions or other compositions to be resolved. As such, the demulsifier composition includes an anhydride, such as acetic anhydride, alone or in combination with other demulsifiers. The anhydride can be used in an amount ranging between trace and 100% by weight of the demulsifier composition.

Claims (36)

1. A method of demulsifying a complex emulsion of water and oil, wherein the oil is a crude oil, the method comprising:

a) forming a demulsifier composition including one or more anhydrides in an amount between about 25% and about 50% by weight of the demulsifier composition, wherein the demulsifier composition further comprises

(i) a demulsifier selected from the group consisting of: alkylphenol resins;

alkoxylates and derivatives; polyglycol ethers and derivatives; amine alkoxylates and derivatives; polyamine alkoxylates and derivates; oxyalkylated amines; glycol resin esters; salts of alkylaryl sulfonic acid; dicarbamates; oxyalkylated polyols reacted with diepoxides and polycarboxylic acids; unreacted oxyalkylated polyols; unreacted oxyalkylated phenolic resins; and combinations thereof; and

(ii) optionally non-anhydride solvent in an amount ranging between about 1% and about 10% by total weight of the demulsifier composition;

b) producing a complex emulsion via a steam-assisted gravity drainage process;

c) injecting the demulsifier composition beneath a surface into an oil well; and

d) separating the oil from the water.

2. The method of claim 1 , wherein the demulsifier composition remains fluid at temperatures down to about 40° C. below zero and lower.

3. The method of claim 1 , wherein the demulsifier composition further comprises additional solvents.

4. The method of claim 1 , whereby the anhydride is selected from the group consisting of: alkyl anhydrides and aryl anhydrides.

5. The method of claim 1 , whereby the anhydride is selected from the group consisting of: propionic anhydride and acetic anhydride.

6. The method of claim 1 , wherein the complex emulsion of water and oil is a water external emulsion of water and oil.

7. A method of demulsifying a complex emulsion of water and oil, wherein the oil is a crude oil, the method comprising:

a) forming a demulsifier composition including one or more anhydrides in an amount between about 25% and about 50% by weight of the demulsifier composition, wherein the demulsifier composition further comprises:

(i) a demulsifier selected from the group consisting of: alkylphenol resins; alkoxylates and derivatives; polyglycol ethers and derivatives; amine alkoxylates and derivatives; polyamine alkoxylates and derivates; oxyalkylated amines; glycol resin esters; salts of alkylaryl sulfonic acid; dicarbamates; oxyalkylated polyols reacted with diepoxides and polycarboxylic acids; unreacted oxyalkylated polyols; unreacted oxyalkylated phenolic resins; and combinations thereof; and

(ii) optionally non-anhydride solvent in an amount ranging between about 1% and about 10% by total weight of the demulsifier composition;

b) producing a complex emulsion via a steam-assisted gravity drainage process;

c) injecting the demulsifier composition into the crude oil at a well-head; and

d) separating the oil from the water.

8. The method of claim 7 , wherein the demulsifier composition remains fluid at temperatures down to about 40° C. below zero and lower.

9. The method of claim 7 , wherein the demulsifier composition further comprises additional solvents.

10. The method of claim 7 , whereby the anhydride is selected from the group consisting of: alkyl anhydrides and aryl anhydrides.

11. The method of claim 7 , whereby the anhydride is selected from the group consisting of: propionic anhydride and acetic anhydride.

12. The method of claim 7 , wherein the complex emulsion of water and oil is a water external emulsion of water and oil.

13. A method of demulsifying a complex emulsion of water and oil, wherein the oil is a crude oil, the method comprising:

a) forming a demulsifier composition including one or more anhydrides in an amount between about 25% and about 50% by weight of the demulsifier composition, further comprises:

(i) a demulsifier selected from the group consisting of: alkylphenol resins; alkoxylates and derivatives; polyglycol ethers and derivatives; amine alkoxylates and derivatives; polyamine alkoxylates and derivates; oxyalkylated amines; glycol resin esters; salts of alkylaryl sulfonic acid; dicarbamates; oxyalkylated polyols reacted with diepoxides and polycarboxylic acids; unreacted oxyalkylated polyols; unreacted oxyalkylated phenolic resins; and combinations thereof; and

(ii) optionally non-anhydride solvent in an amount ranging between about 1% and about 10% by total weight of the demulsifier composition;

b) producing a complex emulsion via a steam-assisted gravity drainage process;

c) injecting the demulsifier composition into a crude oil process stream at a point between a well-head and a final oil storage tank; and

d) separating the oil from the water.

14. The method of claim 13 , wherein the demulsifier composition remains fluid at temperatures down to about 40° C. below zero and lower.

15. The method of claim 13 , wherein the demulsifier composition further comprises additional solvents.

16. The method of claim 13 , whereby the anhydride is selected from the group consisting of: alkyl anhydrides and aryl anhydrides.

17. The method of claim 13 , whereby the anhydride is selected from the group consisting of: propionic anhydride and acetic anhydride.

Assignments (12)
RELEASE OF SECURITY INTEREST IN PATENTS Recorded Jul 17, 2025
From: JPMORGAN CHASE BANK, N.A.
To: CHAMPIONX LLC; APERGY ESP SYSTEMS, LLC; APERGY BMCS ACQUISITION CORP; HARBISON-FISCHER, INC.; NORRIS RODS, INC.,; NORRIS RODS, INC.,; NORRISEAL-WELLMARK, INC.; PCS FERGUSON, INC.; QUARTZDYNE, INC.; US SYNTHETIC CORPORATION
Reel/Frame 072004/0019 →
RELEASE OF SECURITY INTEREST Recorded Jun 7, 2022
From: BANK OF AMERICA, N.A.
To: CHAMPIONX USA INC.
Reel/Frame 060304/0267 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 23, 2022
From: ECOLAB USA INC.
To: CHAMPIONX USA INC.
Reel/Frame 059484/0305 →
SECURITY INTEREST Recorded Jun 5, 2020
From: CHAMPIONX USA INC.
To: JPMORGAN CHASE BANK, N.A.
Reel/Frame 053250/0001 →
SECURITY INTEREST Recorded Jun 5, 2020
From: CHAMPIONX USA INC.
To: BANK OF AMERICA, N.A.
Reel/Frame 052848/0368 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 4, 2017
From: NALCO COMPANY
To: ECOLAB USA INC.
Reel/Frame 042147/0420 →
CHANGE OF NAME Recorded Feb 28, 2017
From: NALCO COMPANY
To: NALCO COMPANY LLC
Reel/Frame 041835/0903 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 28, 2017
From: NALCO COMPANY LLC; CALGON CORPORATION; CALGON LLC; ONDEO NALCO ENERGY SERVICES, L.P.
To: ECOLAB USA INC.
Reel/Frame 041836/0437 →
RELEASE OF SECURITY INTEREST Recorded Feb 24, 2017
From: BANK OF AMERICA, N.A.
To: NALCO COMPANY
Reel/Frame 041808/0713 →
RELEASE OF SECURITY INTEREST Recorded May 26, 2015
From: BANK OF AMERICA, N.A.
To: NALCO COMPANY
Reel/Frame 035771/0668 →
SECURITY AGREEMENT Recorded May 18, 2009
From: NALCO COMPANY; CALGON LLC; NALCO ONE SOURCE LLC; NALCO CROSSBOW WATER LLC
To: BANK OF AMERICA, N.A., AS COLLATERAL AGENT
Reel/Frame 022703/0001 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 12, 2008
From: WILLIAMS, DUNCAN E.
To: NALCO COMPANY
Reel/Frame 021525/0066 →