IP Library Granted Patent US 10,683,397
Granted Patent B2
US 10,683,397 · App. 15/275,701 · Granted Jun 16, 2020

Remediation of agglomerated flow improvers

Inventors: William F. Harris, Jr. (Palm Harbor, FL); Ray L. Johnston (Ponca City, OK)
Assignee: LIQUIDPOWER SPECIALTY PRODUCTS INC.
C08J3/12C08F2/005C08J2300/00
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Quick Facts
Patent No.
US 10,683,397
App. No.
15/275,701
Granted
Jun 16, 2020
Kind
B2
Abstract

The present embodiment can teach a method of feeding to a materials processor a mixture containing an agglomerated drag reducer. The mixture is then homogenized to produce a remediated drag reducer. The maximum particle size diameter of the agglomerated drag reducing polymer is at least 5% larger than the maximum particle diameter of the remediated drag reducer.

Claims (31)

1. A method comprising:

forming a drag reducing polymer;

storing the drag reducing polymer, wherein an agglomerated drag reducing polymer is formed during storage;

feeding a mixture comprising the agglomerated drag reducing polymer to an inline materials processor;

homogenizing the mixture using the inline materials processor to produce a remediated drag reducing polymer, wherein homogenizing the mixture is performed inline of an injection pump; and

supplying the remediated drag reducing polymer into a pipeline using the injection pump,

wherein a maximum particle size diameter of the agglomerated drag reducing polymer is at least 5% larger than a maximum particle size diameter of the remediated drag reducing polymer.

2. The method of claim 1 , wherein the agglomerated drag reducing polymer is incapable of flowing through a 10 mm pore filter without leaving any substantial solids residue.

3. The method of claim 1 , wherein the agglomerated drag reducing polymer is incapable of flowing through a 3 mm pore filter without leaving any solids residue.

4. The method of claim 1 , wherein the agglomerated drag reducing polymer is incapable of being injected through an injection pump using ¼ to 1 inch diameter check valves without clogging the injection pump.

5. The method of claim 1 , wherein a minimum shear rate of the inline materials processor is 2,000 sec −1 .

6. A method, comprising:

forming a drag reducing polymer;

storing the drag reducing polymer for at least one year or at a temperature above 90 degrees Fahrenheit, wherein an agglomerated drag reducing polymer is formed during storage;

feeding a mixture comprising the agglomerated drag reducing polymer and at least one liquid to an inline materials processor;

homogenizing the mixture using the inline materials processor to produce a remediated drag reducing polymer, wherein the homogenizing the mixture is performed inline of an injection pump, wherein a maximum particle size diameter of the agglomerated drag reducing polymer is at least 5% larger than a maximum particle size diameter of the remediated drag reducing polymer; and

supplying the remediated drag reducing polymer into a pipeline using the injection pump.

7. The method of claim 6 , wherein the agglomerated drag reducing polymer is incapable of flowing through a 10 mm pore filter without leaving any substantial solids residue.

8. The method of claim 6 , wherein the agglomerated drag reducing polymer is incapable of flowing through a 3 mm pore filter without leaving any substantial solids residue.

9. The method of claim 6 , wherein the agglomerated drag reducing polymer is incapable of being injected through an injection pump using ¼ to 1 inch diameter check valves without clogging the injection pump.

10. The method of claim 6 , wherein the at least one liquid is selected from a liquid component used to manufacture the agglomerated drag reducing polymer.

11. The method of claim 6 , wherein the at least one liquid is a stabilizer.

12. The method of claim 6 , wherein a minimum shear rate of the inline materials processor is 2,000 sec −1 .

13. A method comprising:

forming a drag reducing polymer;

storing the drag reducing polymer;

feeding the drag reducing polymer to an inline materials processor; homogenizing the drag reducing polymer using the inline materials processor to produce a remediated drag reducing polymer, wherein the homogenizing the drag reducing polymer is performed inline of an injection pump; and

supplying the remediated drag reducing polymer into a pipeline using the injection pump.

14. The method of claim 12 , wherein the drag reducing polymer comprises agglomerated drag reducing polymer.

15. The method of claim 12 , further comprising feeding at least one liquid with the drag reducing polymer to the inline materials processor.

16. The method of claim 15 , wherein the at least one liquid comprises a nonionic surfactant, an ionic surfactant, a partitioning agent, water, alcohol having one to eight carbon atoms, glycols, or mixtures thereof.

Assignments (5)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 22, 2018
From: HARRIS, WILLIAM FRANKLIN, JR.; JOHNSTON, RAY LYLE
To: CONOCOPHILLIPS COMPANY
Reel/Frame 045870/0144 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 22, 2018
From: CONOCOPHILLIPS COMPANY
To: PHILLIPS 66 COMPANY
Reel/Frame 045870/0638 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 22, 2018
From: PHILLIPS 66 COMPANY
To: PHILLIPS SPECIALTY PRODUCTS INC.
Reel/Frame 046207/0161 →
CHANGE OF NAME Recorded May 22, 2018
From: PHILLIPS SPECIALTY PRODUCTS INC.
To: LUBRIZOL SPECIALTY PRODUCTS, INC.
Reel/Frame 046209/0518 →
CHANGE OF NAME Recorded Jan 26, 2017
From: LUBRIZOL SPECIALTY PRODUCTS, INC.
To: LIQUIDPOWER SPECIALTY PRODUCTS INC.
Reel/Frame 041513/0087 →
Continuity (3)
Continuation 13194409 · Jul 29, 2011
Provisional Application 61371976 · Aug 9, 2010
Related Publication 20170009027A1 · Jan 12, 2017