Desalting plant systems and methods for enhanced tight emulsion crude oil treatment

Patent metadata

Field	Value
Publication number	US-11034893-B2
Application number	US-202016858372-A
Country	US
Kind code	B2
Filing date	Apr 24, 2020
Priority date	Jan 9, 2018
Publication date	Jun 15, 2021
Grant date	Jun 15, 2021

Abstract

Systems and methods for treating a rag layer in a gas oil separation plant. The method includes withdrawing the rag layer from a vessel proximate an oil water interface, conveying the rag layer to a separation device, and recycling separated oil from the separation device back to the gas oil separation plant process.

First claim

What is claimed is:

1. A system for treating a rag layer in a gas oil separation plant process, the system comprising:
an outlet stream to withdraw the rag layer from a first vessel proximate an oil water interface;
a separation device, the separation device in fluid communication with the outlet stream and operable to separate oil and water; and
a recycle line to recycle separated oil from the separation device back to a second vessel of the gas oil separation plant process, where the system comprises insulated electrostatic electrodes and is operable to open a water level control valve in response to a deactivation signal from the insulated electrostatic electrodes to reduce a water level in the first vessel to below an oily water interface skimmer such that the oil water interface is proximate the oily water interface skimmer, and where the system is operable to withdraw the rag layer in part based on a pressure differential between a pressure in the first vessel and a pressure in the second vessel, the pressure in the first vessel being greater than the pressure in the second vessel.

2. The system according to claim 1 , where the first vessel is selected from the group consisting of: a dehydrator and a desalter.

3. The system according to claim 1 , where the separation device comprises at least one component selected from the group consisting of: a three-phase separation device equipped with fully insulated electrostatic electrodes; a spool of pipe equipped with fully insulated electrostatic electrodes; an external steam modulation unit; a direct steam injection mixing unit; a membrane-based separation device; a centrifugal separator; and an evaporative concentration system comprising a heat exchanger.

4. The system according to claim 3 , where the separation device comprises the direct steam injection mixing unit.

5. The system according to claim 3 , where the separation device comprises the direct steam injection mixing unit to apply steam to the rag layer at a temperature of about 300° F. and a pressure of about 50 psig or more.

6. The system according to claim 4 , where the separation device comprises the three-phase separation device equipped with fully insulated electrostatic electrodes following the direct steam injection mixing unit.

7. The system according to claim 4 , where the separation device comprises the spool of pipe equipped with fully insulated electrostatic electrodes following the direct steam injection mixing unit.

8. The system according to claim 4 , where the separation device comprises the membrane-based separation device following the direct steam injection mixing unit, and where the membrane-based separation device includes at least one membrane material selected from the group consisting of: alumina, titania, silica, silicon carbide, and combinations of the same.

9. The system according to claim 4 , where the separation device comprises the centrifugal separator following the direct steam injection mixing unit.

10. The system according to claim 4 , where the separation device comprises the evaporative concentration system following the direct steam injection mixing unit.

11. The system according to claim 1 , where the outlet stream further comprises a restricted orifice.

12. The system according to claim 11 , where the outlet stream effects continuous withdrawal from the first vessel to the restricted orifice during the operation of the gas oil separation plant process.

13. The system according to claim 1 , further comprising a level indicator and controller in communication with the first vessel and in communication with a control valve, the control valve in fluid communication with the first vessel via the outlet stream.

14. The system according to claim 1 , the system operable to automatically discontinue conveying the rag layer to the separation device when the separation device detects 100% water being withdrawn from the first vessel.

15. The system according to claim 1 , further comprising a device to increase the pressure of the rag layer.

16. The system according to claim 15 , where the device to increase the pressure of the rag layer is selected from the group consisting of: a turbocharger; a pump; and combinations of the same.

Assignees

• Saudi Arabian Oil Co

Inventors

• Soliman Mohamed
• Alanazi Khalid
• Salu Samusideen Adewale
• Al-Zahrani Talal

Classifications

• B03C11/00

  Separation by high-voltage electrical fields, not provided for in other groups of this subclass · CPC title

• B03C2201/02

  Electrostatic separation of liquids from liquids · CPC title

• C02F1/40

  Devices for separating or removing fatty or oily substances or similar floating material (cleaning or keeping clear the surface of open water from oil or like materials E02B15/04; devices in sewers for separating liquid or solid substances from sewage E03F5/14, e.g. for use in drains leading to the sewer E03F5/16) · CPC title

• C10G33/08

  Controlling or regulating · CPC title

• B01D17/0217

  by centrifugal force · CPC title