IP Library Granted Patent US 11,454,623
Granted Patent B2
US 11,454,623 · App. 16/594,833 · Granted Sep 27, 2022

Method for quantitatively assessing stability additive performance at field dosages

Inventors: Carl E. Weaver (Conroe, TX); Roger D. Metzler (Sugar Land, TX); Koushik Gumaste (Houston, TX)
Assignee: Baker Hughes Holdings LLC
G01N33/2823E21B49/02G01N21/51G01N21/83G01N33/2835
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Quick Facts
Patent No.
US 11,454,623
App. No.
16/594,833
Granted
Sep 27, 2022
Kind
B2
Abstract

The impact of a stabilizing additive for treating oil-based fluids having destabilized solids, such as asphaltenes and polynuclear aromatics, may be quantitatively assessed, by determining the settling rate of flocculated destabilized solids in samples of untreated oil-based fluids and oil-based fluids treated with the stabilizing additive through the use of a turbidity meter or nephelometer while the field and quantifying the difference between the two settling rates to determine if a change in the amount of stabilizing additive applied to the oil-based fluid is necessary.

Claims (22)

1. A method for determining the impact of a stabilizing additive on the settling rate of destabilized solids in an oil-based fluid comprising:

preparing a sample of an oil-based fluid containing flocculated destabilized solids and a field dosage amount of a stabilizing additive and preparing a sample of an oil-based fluid containing flocculated destabilized solids with no stabilizing additive; and

measuring the change in turbidity over time of each sample to determine a settling rate of the flocculated destabilized solids in each sample; and

quantifying the difference between settling rate of the flocculated destabilized solids in the sample of the oil-based fluid having a field dosage amount of stabilizing additive and the settling rate of the flocculated destabilized solids in the sample of the oil-based fluid having no stabilizing additive to assess performance of the stabilizing additive.

2. The method of claim 1 , wherein the step of preparing samples of an oil-based fluid containing flocculated destabilized solids and a field dosage amount of a stabilizing additive and an oil-based fluid containing flocculated destabilized solids with no stabilizing additive comprises:

titrating an oil-based fluid containing destabilized solids and a field dosage amount of a stabilizing additive and an oil-based fluid containing destabilized solids with no stabilizing additive by dosing the oil-based fluids with a paraffinic solvent until there is flocculation of the destabilized solids; and

extracting a sample from each oil-based fluid after the titration and once the destabilized solids in each oil-based fluid have flocculated; and

mixing each extracted sample with a cycloparaffin.

3. The method of claim 2 , wherein the step of mixing each extracted sample with a cycloparaffin results in the dispersion of the destabilized solid flocs present in each extracted sample.

4. The method of claim 2 , wherein the paraffinic solvent is selected from the group consisting of cetane, heptane, xylene, toluene, hexane, pentane, methylnaphthalene, a paraffinic solvent having a solubility range of about 6.8 to 7.2 (cal/cm 3 ) 1/2 , and combinations thereof.

5. The method of claim 2 , wherein the cycloparaffin is cyclohexane.

6. The method of claim 1 , wherein the oil-based fluid is selected from the group consisting of crude oil, fuel oil, atmospheric residua, vacuum, residua, distillation residua, quench oil, visbreaker tar, H-Oil process stream, LC Fining process stream, fluidized catalytic cracker slurry, and combinations thereof.

7. The method of claim 1 , wherein the destabilized solids are selected from a group consisting of asphaltenes, polynuclear aromatics, coke, coke precursors, and combinations thereof.

8. The method of claim 1 , wherein the field dosage amount ranges from about 1 ppm to about 500 ppm based on the oil-based fluid.

9. The method of claim 1 , wherein the step of measuring the change in turbidity over time of each sample to determine a settling rate of the flocculated destabilized solids in each sample is carried out by a turbidity meter.

10. The method of claim 9 , wherein the turbidity meter is portable.

11. The method of claim 9 , wherein the turbidity meter is in the field.

12. The method of claim 1 , further comprising implementing a change to the amount of stabilizing additive applied to the oil-based fluid based upon quantifying the difference between settling rate of the flocculated destabilized solids in the sample of the oil-based fluid having a field dosage amount of stabilizing additive and the settling rate of the flocculated destabilized solids in the sample of the oil-based fluid having no stabilizing additive.

13. The method of claim 1 , wherein the step of measuring the change in turbidity over time of each sample to determine a settling rate of the flocculated destabilized solids in each sample is carried out by a nephelometer.

14. The method of claim 13 , wherein the nephelometer is portable.

15. The method of claim 1 , wherein the field dosage amount ranges from about 10 ppm to about 50 ppm based on the oil-based fluid.

16. The method of claim 1 , further comprising implementing a change to a production, transportation, or refining process based upon quantifying the difference between settling rate of the flocculated destabilized solids in the sample of the oil-based fluid having a field dosage amount of stabilizing additive and the settling rate of the flocculated destabilized solids in the sample of the oil-based fluid having no stabilizing additive, the change being selected from a group consisting of: adding an additional feed stream to the oil-based fluid to stabilize the oil-based fluid, adding an additive to the oil-based fluid, adding a different demulsifier to the oil-based fluid than any demulsifier already present in the oil-based fluid, changing a temperature of the oil-based fluid, changing a water feed rate of a unit within the refinery process, and combinations thereof.

Assignments (3)
CERTIFICATE OF AMENDMENT OF NAME CHANGE Recorded Aug 22, 2022
From: BAKER HUGHES, A GE COMPANY, LLC
To: BAKER HUGHES HOLDINGS LLC
Reel/Frame 061297/0920 →
CHANGE OF NAME Recorded Feb 16, 2022
From: BAKER HUGHES, A GE COMPANY, LLC
To: BAKER HUGHES HOLDINGS LLC
Reel/Frame 059141/0762 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 12, 2020
From: WEAVER, CARL E.; METZLER, ROGER D.; GUMASTE, KOUSHIK
To: BAKER HUGHES, A GE COMPANY, LLC
Reel/Frame 052931/0729 →