Processing of oil by steam addition

Patent metadata

Field	Value
Publication number	US-10180052-B1
Application number	US-201715819680-A
Country	US
Kind code	B1
Filing date	Nov 21, 2017
Priority date	Nov 21, 2017
Publication date	Jan 15, 2019
Grant date	Jan 15, 2019

Abstract

The invention relates to injecting steam into crude oil for several benefits, primarily of which is to remove salt by transferring the salt into the condensed water from the steam. Steam transfers salt via a different transfer mechanism and therefore doesn't require the high shear mixing of conventional water injection systems. As such, steam injection through a variety of procedures, is more efficient at gathering salt into water that itself is easier to remove from the crude oil.

First claim

The invention claimed is:

1. A process for removing salt from crude oil wherein the salt is 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 steam into the crude oil in the form of steam bubbles that are larger relative to any salt particles or relative to the any droplets of brine water so as to contact the steam bubbles with the crude oil along with any nearby suspended salt particles and brine droplets, such that a single steam bubble is adapted to contact numerous salt particles and brine droplets;
b) 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 small brine droplets resulting in enlarged brine droplets having a size more amenable for separation from the crude oil; and
c) separating liquid water from the crude oil where the liquid water includes the salt dissolved therein, wherein the process is more particularly characterized in that it does not include imposing high shear mixing of steam bubbles within the crude oil, and wherein the step of injecting the steam occurs in a steam-crude mixing zone where crude oil flows through a venturi tube and into the steam-crude mixing zone and steam is injected just downstream from peak flow rates of crude oil and drawn in to the venturi tube to aggressively stir the steam bubbles into the crude oil but not shear the steam bubbles.

2. The process according to claim 1 wherein the steam is injected in a manner to deliver water droplets having an average diameter of at least 10 microns and up to about 150 microns after the steam bubbles have collapsed and condensed.

3. The process according to claim 1 further including the step of adding demulsifier into the crude oil prior to the step of separating the liquid water from the crude oil.

4. The process 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.

5. The process according to claim 4 further including the step of adding demulsifier into the crude oil prior to the step of separating the liquid water from the crude oil.

6. The process according to claim 1 wherein the steam is added to the crude oil at between 1 and 8 percent by weight steam to crude oil.

7. The process according to claim 1 wherein the steam is added to the crude oil at between 2 and 6 percent by weight steam to crude oil.

8. The process according to claim 1 wherein the steam is added to the crude oil at between 4 and 6 percent by weight steam to crude oil.

Assignees

• Phillips 66 Co

Inventors

• Lawson Keith H
• Willman Derek H

Classifications

• C10G33/04

  with chemical means · CPC title

• E21B43/2406 Primary

  Steam assisted gravity drainage [SAGD] · CPC title

• B01D17/045 Primary

  with coalescers · CPC title

• B01D17/0205

  by gas bubbles or moving solids · CPC title

• B01D17/0208

  by sedimentation · CPC title