IP Library Granted Patent US 11,186,783
Granted Patent B2
US 11,186,783 · App. 14/987,530 · Granted Nov 30, 2021

Optimization of a method for isolation of paraffinic hydrocarbons

Inventor: Stephen D. Matza (Houston, TX)
Assignee: HPC PetroServ, Inc.
C10G33/04C10G21/27C10G21/30C10G33/08
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Quick Facts
Patent No.
US 11,186,783
App. No.
14/987,530
Granted
Nov 30, 2021
Kind
B2
Abstract

A method and composition for isolating a paraffinic hydrocarbon layer from a sludge comprising paraffinic hydrocarbons, water, and solids. The method includes contacting the sludge with isopropylamine dodecylbenzene sulfonate, a cutter stock, and water. The isopropylamine dodecylbenzene sulfonate comprises a concentration of at least 1500 ppm. The ratio of sludge:cutter:water is at least 4:2:1. The method also includes determining if the sludge has separated into a three phase separation comprising a paraffinic hydrocarbon layer, a water layer, and a layer of settled solids.

Claims (23)

1. A method for determining a paraffinic hydrocarbon isolation composition ratio, the method comprising:

(A) contacting a sludge comprising paraffinic hydrocarbons, water, and solids disposed within a vessel, with isopropylamine dodecylbenzene sulfonate, a cutter stock, and water thereby producing a sludge mixture, wherein step (A) occurs at a high temperature between 35° C. and 80° C., wherein the isopropylamine dodecylbenzene sulfonate is present at a concentration of at least 1500 ppm, wherein a volume ratio of sludge:cutter stock:water is at least 4:2:1, and wherein the cutter stock comprises a light sweet oil with an American Petroleum Institute (API) gravity of 30 or greater, a light cycle oil, a diesel oil, a light sweet crude oil, or combinations thereof;

(B) circulating the sludge mixture to maximize wax crystal formation of the paraffinic hydrocarbons and to break any water-in-oil or oil-in-water emulsions which may form so as to produce as clean a three phase separation as possible;

(C) determining if the sludge mixture has separated into a three phase separation within the vessel, wherein step (C) occurs at a temperature lower than the high temperature of step (A), and wherein the three phase separation comprises a paraffinic hydrocarbon layer, a water layer, and a layer of settled solids by way of viewing the sludge mixture to determine if three distinct phases are present;

(D) thereafter, if the sludge mixture has not separated into the three phase separation, reheating the sludge mixture to the high temperature for a period, increasing or decreasing the concentration of isopropylamine dodecylbenzene sulfonate, increasing or decreasing the volume ratio of sludge:cutter stock:water, or any combinations thereof until the sludge mixture separates into the three phase separation within the vessel; and

(E) testing to measure an amount of settled solids present in the paraffinic hydrocarbon layer within the vessel.

2. The method of claim 1 , wherein if the sludge mixture has not separated into the three phase separation, the concentration of isopropylamine dodecylbenzene sulfonate is increased to at least 3000 ppm.

3. The method of claim 1 , wherein if the sludge mixture has not separated into the three phase separation, the volume ratio of sludge:cutter stock:water is adjusted to at least 4:4:1.

4. The method of claim 3 , further comprising determining if the sludge mixture has separated into the three phase separation comprising a paraffinic hydrocarbon layer, a water layer, and a layer of settled solids after adjustment of the volume ratio of sludge:cutter stock:water to at least 4:4:1.

5. The method of claim 4 , wherein if the sludge mixture has not separated into the three phase separation, the concentration of isopropylamine dodecylbenzene sulfonate is increased to at least 3000 ppm.

6. The method of claim 1 , wherein if the sludge mixture has not separated into the three phase separation, the volume ratio of sludge:cutter stock:water is adjusted to at least 4:4:2.

7. The method of claim 6 , further comprising determining if the sludge mixture has separated into the three phase separation comprising a paraffinic hydrocarbon layer, a water layer, and a layer of settled solids after adjustment of the volume ratio of sludge:cutter stock:water to at least 4:4:2.

8. The method of claim 7 , wherein if the sludge mixture has not separated into the three phase separation, the concentration of isopropylamine dodecylbenzene sulfonate is increased to at least 3000 ppm.

9. The method of claim 1 , wherein the volume ratio of sludge:cutter stock:water is at least 4:4:1, and the concentration of isopropylamine dodecylbenzene sulfonate is at least 3000 ppm.

10. The method of claim 1 , wherein the volume ratio of sludge:cutter stock:water is at least 4:4:2, and the concentration of isopropylamine dodecylbenzene sulfonate is at least 3000 ppm.

11. The method of claim 1 , wherein if the sludge mixture has separated into the three phase separation, removing the paraffinic hydrocarbon layer from contact with the water layer and the layer of settled solids.

12. The method of claim 1 , further comprising performing the Basic Sediment and Water Test of American Society for Testing and Materials (ASTM)D1796 on a recovered hydrocarbon resulting from the three phase separation.

13. The method of claim 12 , wherein the basic sediment and water percentage of the paraffinic hydrocarbon layer is less than 5%, as measured by Basic Sediment and Water Test of American Society for Testing and Materials (ASTM) D1796.

14. The method of claim 1 , further comprising heating the sludge mixture after contacting the sludge with the isopropylamine dodecylbenzene sulfonate, the cutter stock, and the water.

15. The method of claim 1 , wherein a surfactant is added to the isopropylamine dodecylbenzene sulfonate.

16. The method of claim 15 , wherein the surfactant comprises two or more surfactants.

17. The method of claim 16 , wherein one of the surfactants is a zwitterionic surfactant, and the other surfactant is a nonionic surfactant.

18. The method of claim 1 , wherein the paraffinic hydrocarbon comprises a hydrocarbon of 18 to 34.

Assignments (11)
CHANGE OF NAME Recorded May 16, 2025
From: TRISTAR PETROSERV, INC.
To: HPC PETROSERVE, INC.
Reel/Frame 071297/0913 →
SECURITY INTEREST Recorded Oct 12, 2021
From: AQUILEX LLC; GLOBAL VAPOR CONTROL, INC.; HYDROCHEM LLC; HPC PETROSERV, INC.; PSC INDUSTRIAL OUTSOURCING, LP
To: BANK OF AMERICA, N.A.
Reel/Frame 057759/0688 →
ABL RELEASE (REEL 052148 / FRAME 0400) Recorded Oct 11, 2021
From: GOLDMAN SACHS BANK USA
To: GLOBAL VAPOR CONTROL, INC.; HPC PETROSERV, INC.
Reel/Frame 057772/0603 →
FIRST LIEN RELEASE (REEL 052730 / FRAME 0719) Recorded Oct 11, 2021
From: GOLDMAN SACHS BANK USA
To: GLOBAL VAPOR CONTROL, INC.; HPC PETROSERV, INC.
Reel/Frame 057772/0628 →
SECOND LIEN RELEASE (REEL 052730 / FRAME 0729) Recorded Oct 11, 2021
From: GOLDMAN SACHS BANK USA
To: GLOBAL VAPOR CONTROL, INC.; HPC PETROSERV, INC.
Reel/Frame 057772/0643 →
SECURITY AGREEMENT Recorded Oct 8, 2021
From: AQUILEX LLC; GLOBAL VAPOR CONTROL, INC.; HYDROCHEM LLC; HPC PETROSERV, INC.; PCS INDUSTRIAL OUTSOURCING, LP
To: GOLDMAN SACHS LENDING PARTNERS LLC
Reel/Frame 057899/0694 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 26, 2021
From: TRISTAR PETROSERV, INC
To: HPC PETROSERV, INC.
Reel/Frame 055030/0381 →
SECURITY INTEREST Recorded May 22, 2020
From: HPC PETROSERV, INC.; GLOBAL VAPOR CONTROL, INC.
To: GOLDMAN SACHS BANK USA, AS COLLATERAL AGENT
Reel/Frame 052730/0719 →
SECURITY INTEREST Recorded May 22, 2020
From: HPC PETROSERV, INC.; GLOBAL VAPOR CONTROL, INC.
To: GOLDMAN SACHS BANK USA, AS COLLATERAL AGENT
Reel/Frame 052730/0729 →
SECURITY AGREEMENT Recorded Mar 11, 2020
From: HPC PETROSERV, INC.; GLOBAL VAPOR CONTROL, INC.
To: GOLDMAN SACHS BANK USA
Reel/Frame 052148/0400 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 29, 2016
From: MATZA, STEPHEN D.
To: TRISTAR PETROSERV, INC.
Reel/Frame 039043/0881 →