System and method to process effluent brine and interface rag from an oil dehydration/desalting system

Patent metadata

Field	Value
Publication number	US-10913013-B2
Application number	US-201614997877-A
Country	US
Kind code	B2
Filing date	Jan 18, 2016
Priority date	Sep 29, 2011
Publication date	Feb 9, 2021
Grant date	Feb 9, 2021

Abstract

A system and method for processing interface emulsion, water, and solids contained within a separator vessel that comprises the steps of continually extracting those components from the vessel and then passing them through a gas flotation cell. The cell, which is preferably a vertical induced gas flotation cell, separates the oil and water contained in the interface emulsion and discharges recovered oil from an upper portion of the cell and treated water from a bottom portion of the cell. The recovered oil and treated water may be further processed and recycled to the vessel or sent elsewhere. The treated water may also be recycled to the cell or sent to a process sewer. Fuel gas residing in an upper portion of the cell may be cooled and passed through a splitter. All the steps of occur in a closed system with no air emissions.

First claim

What is claimed is:

1. A method for processing interface emulsion, water, and solids contained within a separator vessel comprising the steps of:
extracting the interface emulsion, water, and solids from at least one discrete extraction point for each, the extraction points being located within the separator vessel; and
treating the extracted interface emulsion, water, and solids in an induced gas flotation cell arranged downstream of the separator vessel.

2. The method according to claim 1 wherein the extracting step occurs at a first removal rate for the interface emulsion and at a second removal rate for at least one of the water and the solids.

3. The method according to claim 2 wherein at least one of the first and second removal rates is a continuous removal rate.

4. The method according to claim 2 further comprising the step of setting the first removal rate and the second removal rate to maintain a thickness of the interface emulsion at a pre-determined value.

5. The method according to claim 1 further comprising the extracting step including the sequencing removal of the interface emulsion, water, and solids.

6. The method according to claim 1 further comprising the step of combining at least two of the extracted interface emulsion, water, and solids into a single stream.

7. The method according to claim 6 further comprising the step of injecting a reverse emulsion breaker into the single stream.

8. The method according to claim 1 further comprising the step of recycling a portion of at least one of an oil stream and a water stream being discharged from the induced gas flotation cell back to the separator vessel.

9. A system for processing interface emulsion, water, and solids contained within a separator vessel, the system comprising:
an interface emulsion extraction point, a solids extraction point, and a water extraction point located at discrete locations within the separator vessel; and
an induced gas flotation cell arranged downstream of the separator vessel to receive interface emulsion, water, and solids removed from the separator vessel through a respective extraction point.

10. A system according to claim 9 further comprising the interface emulsion extraction point being at a first removal rate and at least one of the water and solids extraction points being at a second removal rate.

11. A system according to claim 10 wherein at least one of the first and second removal rates is a continuous removal rate.

12. A system according to claim 10 wherein the first removal rate and the second removal rate are set to maintain a thickness of the interface emulsion at a pre-determined value.

13. A system according to claim 9 further comprising one or more valves to sequence removal of the interface emulsion, water, and solids from the separator vessel according to a respective removal rate.

14. A system according to claim 9 wherein at least two of the interface emulsion, the water and the solids removed from the separator vessel are combined into a single stream.

15. A system according to claim 9 further comprising a recycling loop wherein a portion of at least one of the oil and the water discharged from the induced gas flotation cell is recycled to the separator vessel.

Assignees

• Cameron Int Corp
• Schlumberger Technology Corp

Inventors

• Sams Gary W
• Hypes Ronald D

Classifications

• C02F1/24 Primary

  by flotation (C02F1/465 takes precedence) · CPC title

• C02F1/008

  Control or steering systems not provided for elsewhere in subclass C02F · CPC title

• C02F2301/046

  Recirculation with an external loop · CPC title

• C02F2209/42

  Liquid level · CPC title

• B03D1/1475

  Flotation tanks having means for discharging the pulp, e.g. as a bleed stream · CPC title