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

Patent metadata

Field	Value
Publication number	US-9238183-B2
Application number	US-201414556987-A
Country	US
Kind code	B2
Filing date	Dec 1, 2014
Priority date	Sep 29, 2011
Publication date	Jan 19, 2016
Grant date	Jan 19, 2016

Abstract

A system 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 the system comprise a closed system with no air emissions.

First claim

What is claimed is:

1. A system for processing interface emulsion, water, and solids contained within a separator vessel, the system comprising:
a separator vessel having a set of discrete extraction points located within the separator vessel, at least one discrete extraction point each for the interface emulsion, for the water, and for the solids, the discrete extraction point for the interface emulsion having a first removal rate and the discrete extraction point and said induced gas flotation cell discharges treated oil and water therefrom for at least one of the water and solids having a second removal rate;
an induced gas flotation cell arranged downstream of the separator vessel to receive the interface emulsion, water, and solids removed from the separator vessel through their respective extraction point.

2. A system according to claim 1 wherein at least one of the first and second removal rates is a continuous removal rate.

3. A system according to claim 1 wherein the first removal rate is independent of the second removal rate.

4. A system according to claim 1 wherein the second removal rate is a different removal rate for the water than for the solids.

5. A system according to claim 1 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.

6. A system according to claim 1 wherein the first removal rate and the second removal rate are set to maintain a level of the interface emulsion at a pre-determined value.

7. A system according to claim 1 further comprising one or more valves to sequence removal of one or more of the interface emulsion, water, and solids from the separator vessel according to a respective first or second removal rate.

8. A system according to claim 1 wherein the water and solids removed from the separator vessel are combined into a single stream.

9. A system according to claim 1 wherein the interface emulsion removed from the separator vessel is combined with the water and solids in a single stream.

10. A system according to claim 9 wherein the single stream is at a temperature in the range of 225° F. to 275° F.

11. A system according to claim 1 wherein water discharged from the induced gas flotation cell contains no greater than 100 ppm total hydrocarbon.

12. A system according to claim 1 wherein the water discharged from the induced gas flotation cell is cooled to a temperature of no greater than 130° F.

13. A system according to claim 1 further comprising a recycling loop wherein at least a portion of the water discharged from the induced gas flotation cell is recycled to the separator vessel.

14. A system according to claim 13 wherein the at least a portion of the water discharged from the induced gas flotation cell is filtered prior to being recycled to the separator vessel.

15. A system according to claim 1 further comprising a recycling loop wherein a portion of the oil discharged from the induced gas flotation cell is recycled to the separator vessel.

16. A system according to claim 1 further comprising a splitter located downstream of the induced gas flotation cell.

17. A system according to claim 16 wherein gas exiting the induced gas flotation cell is at a first temperature and the gas entering the splitter is at a lower second temperature.

18. A system according to claim 17 wherein the first temperature is greater than 130° F. and the lower second temperature is no greater than 75° F.

19. A system according to claim 1 wherein the induced gas flotation cell is a vertical induced gas flotation cell.

20. A system according to claim 1 wherein the system comprises a closed system with no air emissions.

Assignees

• Cameron Int Corp

Inventors

• Sams Gary W
• Hypes Ronald D

Classifications

• B03D1/1475

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

• B03D1/1418

  using centrifugal forces · CPC title

• C02F1/001

  Processes for the treatment of water whereby the filtration technique is of importance (C02F1/44 takes precedence; construction of filters in general B01D24/00 - B01D41/00) · CPC title

• C02F1/24 Primary

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

• B01D21/0084

  Enhancing liquid-particle separation using the flotation principle (flotation in general B03D1/00) · CPC title