Processing of oil by steam addition

Patent metadata

Field	Value
Publication number	US-10087732-B1
Application number	US-201715819596-A
Country	US
Kind code	B1
Filing date	Nov 21, 2017
Priority date	Nov 21, 2017
Publication date	Oct 2, 2018
Grant date	Oct 2, 2018

Abstract

Salt is removed from crude oil by exposing the salt bearing crude to successive stages of water injection and steam injection where the water injection includes high shear and the stream injection does not include high shear applied to the steam bubbles. The steam is seen to transfer salt from the crude via a different transfer mechanism and therefore doesn't require the high shear mixing of conventional water injection systems.

First claim

The invention claimed is:

1. A process for removing salt from crude oil wherein the salt may be in the form of particles of crystalline salt suspended in the crude oil or as small droplets of brine water suspended in the crude oil, or both, wherein the process comprises the steps of:
a) injecting a first stream of liquid water into the crude oil forming water drops in the crude oil;
b) imposing aggressive high shear mixing on the injected water and the crude oil to break up the injected water into smaller droplets of water and, at the same time, enhance contact of the smaller droplets of water with remaining salt particles and remaining brine droplets to enhance dissolving of salt particles and also coalesce droplets of water whether brine droplets or droplets of injected water;
c) injecting a first stream of steam into the crude oil in the form of steam bubbles that are larger relative to any salt particles or relative to any droplets of brine water so as to create steam bubbles that will have broad contact due to the larger size with the crude oil along with any nearby suspended salt particles and brine droplets, such that a single steam bubble may contact a plurality of salt particles and brine droplets;
d) condensing the steam bubbles into droplets of liquid water while at the same time dissolving available salt particles forming new brine water droplets and also delivering liquid or vaporous water from the steam bubbles into any available brine droplets resulting in coalesced brine droplets having a size more amenable for separation from the crude oil;
e) separating liquid water from the crude oil where the liquid water includes the dissolved salt therein that were formerly suspended in the crude oil to thereby remove the salt and water from the crude oil and also thereby form a first pass desalted crude oil,
f) injecting a second stream of liquid water into the first pass desalted crude oil forming water drops in the crude oil;
g) imposing aggressive high shear mixing on the injected water and first pass desalted crude oil to break up the injected water into smaller droplets of water and, at the same time, enhance contact of the smaller droplets of water with remaining salt particles and remaining brine droplets to enhance dissolving of salt particles and also coalesce droplets of water whether brine droplets or droplets of injected water;
h) after the aggressive high shear mixing, injecting a second stream of steam into the first pass desalted crude oil in the form of steam bubbles that are larger relative to any salt particles or relative to the any small droplets of brine water so as to create steam bubbles that will have broad contact due to the larger size with the first pass desalted crude oil along with any nearby remaining suspended salt particles and remaining water droplets including any remaining brine droplets, such that a single steam bubble may contact a plurality of salt particles and brine droplets;
i) condensing the steam bubbles into droplets of liquid water while at the same time dissolving any remaining and available salt particles forming new brine water droplets and also delivering liquid or vaporous water from the steam bubbles into any remaining and available small brine droplets resulting in new brine droplets and/or enlarged brine droplets having a size more amenable for separation from the crude oil; and
j) separating liquid water from the first pass desalted crude oil with any dissolved salt therein to thereby remove salt and water from the first pass desalted crude, wherein the process is more particularly characterized in that it does not include imposing high shear mixing of uncondensed steam bubbles within the crude oil.

2. The process for removing salt from crude oil according to claim 1 wherein the steps for separating the liquid water from the crude oil includes subjecting the crude oil to low shear coalescer mixing followed by gravity separation of the water droplets from the crude oil.

3. The process for removing salt from crude oil according to claim 2 further including the step of adding demulsifier into the crude oil prior to the first step of separating the liquid water from the crude oil.

4. The process for removing salt from crude oil according to claim 3 wherein the steps of injecting steam further include injecting the steam into a vertically oriented chamber where the crude oil and steam flow vertically as the steam bubbles condense.

5. The process for removing salt from crude oil according to claim 4 wherein the vertical flow in the chamber is downward.

6. The process for removing salt from crude oil according to claim 4 wherein the vertical flow in the chamber is upward.

7. The process for removing salt from crude oil according to claim 2 wherein the steps of injecting steam further include injecting the steam into a vertically oriented chamber where the crude oil and steam flow vertically as the steam bubbles condense.

8. The process for removing salt from crude oil according to claim 7 wherein the vertical flow in the chamber is downward.

9. The process for removing salt from crude oil according to claim 7 wherein the vertical flow in the chamber is upward.

10. The process for removing salt from crude oil according to claim 1 wherein the steps of injecting steam further include injecting the steam into a vertically oriented chamber where the crude oil and steam flow vertically as the steam bubbles condense.

11. The process for removing salt from crude oil according to claim 10 wherein the vertical flow in the chamber is downward.

12. The process for removing salt from crude oil according to claim 10 wherein the vertical flow in the chamber is upward.

13. The process for removing salt from crude oil according to claim 1 further including the step of adding demulsifier into the crude oil prior to the first step of separating the liquid water from the crude oil.

Assignees

• Phillips 66 Co

Inventors

• Lawson Keith H
• Willman Derek H

Classifications

• E21B43/2406 Primary

  Steam assisted gravity drainage [SAGD] · CPC title

• C10G33/04 Primary

  with chemical means · CPC title

• B01D17/045

  with coalescers · CPC title

• C10G31/08

  by treating with water · CPC title

• B01D17/042

  by changing the temperature · CPC title