Desalter emulsion separation by direct contact vaporization

Patent metadata

Field	Value
Publication number	US-10119080-B2
Application number	US-201414467110-A
Country	US
Kind code	B2
Filing date	Aug 25, 2014
Priority date	Sep 25, 2013
Publication date	Nov 6, 2018
Grant date	Nov 6, 2018

Abstract

A petroleum desalting process in which the oil/water emulsion layer which forms in the desalter vessel between the settled water layer and the settled oil layer is separated into the oil and water components by contact with a heated high boiling hydrocarbon to break the emulsion and vaporize water from the emulsion in a flash drum. The vessel has an emulsion outlet for removing an emulsion stream from the emulsion layer and a conduit connecting the emulsion withdrawal port to an inlet of an optional settling drum to effect and initial separation into an oil-enriched phase and a water phase with the oil-enriched phase led to the flash drum.

First claim

The invention claimed is:

1. A petroleum desalter which comprises:
a desalter vessel having a top, a bottom, a lower portion, an upper portion, and a feed inlet, wherein the feed inlet is configured for admitting a mixture of crude oil with desalting water into the vessel in order to perform a desalting operation to form (i) a settled water layer containing salts dissolved from the crude oil located in the lower portion of the vessel, (ii) a settled supernatant desalted oil layer located in the upper portion of the vessel and (iii) an emulsion layer located between the settled water layer and the settled supernatant desalted oil layer, wherein the emulsion layer contains crude oil and water,
a water outlet conduit at the bottom of the vessel for removing water from the settled water layer in the lower portion of the vessel,
an oil outlet conduit at the top of the vessel for removing desalted oil from the settled supernatant desalted oil layer in the upper portion of the vessel,
at least one emulsion outlet formed in the vessel for removing an emulsion stream from the emulsion layer,
a flash drum having at least one inlet,
a conduit connecting the at least one emulsion outlet to the at least one inlet of the flash drum,
a mixing point located along the conduit for admitting the emulsion stream removed from the emulsion layer to a stream of a hydrocarbon heating medium to transfer heat from the heating medium to the emulsion stream, to break the emulsion and vaporize water from the broken emulsion in the flash drum, wherein the mixing point is the location in the conduit where the emulsion stream mixes with the hydrocarbon heating medium.

2. A desalter according to claim 1 further comprising a plurality of vertically spaced emulsion withdrawal points for removing the emulsion stream from the emulsion layer, wherein the plurality of vertically spaced emulsion withdrawal points are connected to the at least one emulsion outlet.

3. A desalter according to claim 1 in which the emulsion outlet of the desalter vessel is connected to a settling drum having an upper outlet and a lower outlet, to settle the emulsion stream and remove water from the emulsion stream, to form an oil-enriched stream to be withdrawn from the settling drum through the upper outlet and passed to the flash drum.

4. A desalter according to claim 1 further comprising a heat exchanger in the conduit connecting the at least one emulsion outlet to the at least one inlet of the flash drum.

5. A desalter according to claim 1 , wherein the mixing point for admitting the withdrawn emulsion stream removed from the emulsion layer to a stream of a hydrocarbon heating medium comprises a quill injector for the emulsion stream.

6. A desalter according to claim 1 in which the conduit connecting the at least one emulsion outlet to the at least one inlet of the flash drum is branched to provide two branch conduits for the emulsion stream, respectively connected to two flash drum inlets.

7. A desalter according to claim 6 in which each branch conduit has a tangential feed horn in the flash drum.

8. A petroleum desalter which comprises:
a desalter vessel having a top, a bottom, a lower portion, an upper portion, and a feed inlet, wherein the feed inlet is configured for admitting a mixture of crude oil with desalting water into the vessel in order to perform a desalting operation to form (i) a settled water layer containing salts dissolved from the crude oil located in the lower portion of the vessel, (ii) a settled supernatant desalted oil layer located in the upper portion of the vessel and (iii) an emulsion layer located between the settled water layer and the settled supernatant desalted oil layer, wherein the emulsion layer contains crude oil and water,
a water outlet conduit at the bottom of the vessel for removing water from the settled water layer in the lower portion of the vessel,
an oil outlet conduit at the top of the vessel for removing desalted oil from the settled supernatant desalted oil layer in the upper portion of the vessel,
at least one emulsion outlet formed in the vessel for removing an emulsion stream from the emulsion layer,
a flash drum having at least one inlet,
a conduit connecting the at least one emulsion outlet to a settling drum having an upper outlet and a lower outlet, to settle the emulsion stream and remove water from the emulsion stream, to form an oil-enriched emulsion stream to be withdrawn from the settling drum through the upper outlet and passed to a flash drum,
a second conduit connecting the upper outlet of the settling drum to the at least one inlet of the flash drum,
an inlet in the second conduit for admitting a hydrocarbon heating medium from a source to the stream of oil-enriched emulsion to transfer heat from the heating medium to the stream of oil-enriched emulsion, to break the emulsion and vaporize water from the broken emulsion in the flash drum.

9. A desalter according to claim 8 which includes a heat exchanger in the conduit connecting the at least one emulsion outlet to the settling drum.

10. A desalter according to claim 8 in which the inlet along the second conduit for admitting the hydrocarbon heating medium to the stream of oil-enriched emulsion comprises a quill injector for the emulsion.

11. A desalter according to claim 8 in which the second conduit is branched to provide two branch conduits for the stream of oil-enriched emulsion, respectively connected to two flash drum inlets.

12. A desalter according to claim 11 in which each branch conduit has a tangential feed horn in the flash drum.

13. A desalter according to claim 8 in which the inlet along the second conduit comprises a quill injector for the emulsion feeding vertically into a vertically oriented portion of the conduit.

14. A desalter according to claim 8 further comprising a plurality of vertically spaced emulsion withdrawal points for removing the emulsion stream from the emulsion layer, wherein the plurality of vertically spaced emulsion withdrawal points are connected to the at least one emulsion outlet.

Assignees

• Albert Brian D
• Trier Theodore Trent
• Simonetty Jose X
• Barroeta Magaly C
• Alva Victor
• Hergenrother Michael Louis
• Jacobs Owen P
• Exxonmobil Res & Eng Co

Inventors

• Albert Brian D
• Trier Theodore Trent
• Simonetty Jose X
• Barroeta Magaly C
• Alva Victor
• Hergenrother Michael Louis
• Jacobs Owen P

Classifications

• C10G33/00

  Dewatering or demulsification of hydrocarbon oils (by distillation C10G7/04) · CPC title

• C10G31/06

  by heating, cooling, or pressure treatment · CPC title

• C10G31/08 Primary

  by treating with water · CPC title