US 10,294,429 B1Granted

Processing of oil by steam addition

AssigneePhillips 66 Company

InventorsKeith H. Lawson, Derek H. Willman

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Abstract

The invention relates to injecting steam into crude oil in two separate desalting steps to remove salt by transferring the salt into the condensed water from the steam and gravity separating the water from the crude oil. Steam transfers salt from crude oil via a different transfer mechanism and therefore doesn't require the high shear mixing of conventional water injection systems. In the invention, salt is also removed via an intermediate step of adding water with harshly mixing the added water with the crude oil.

Claims20

Dependent claims

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 droplets of brine water suspended in the crude oil, or both, wherein the process comprises the steps of:

a) 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 the any droplets of brine water so as to create steam bubbles that will have contact 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;
b) injecting liquid water into the crude oil;
c) condensing the steam bubbles into droplets of liquid water while at the same time dissolving available salt particles forming new brine droplets and also delivering liquid or vaporous water from the steam bubbles into any available brine droplets resulting in enlarged brine droplets having a size more amenable for separation from the crude oil;
d) imposing high shear mixing on the crude oil and water in a high shear mixer to enhance contact between salt particles, brine droplets and water droplets to enhance dissolving of salt particles and coalescence of brine droplets with water;
e) separating liquid water from the crude oil including water with salt dissolved therein to form a first pass desalted crude oil;
f) 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 remaining salt particles or relative to the any remaining droplets of brine water so as to create steam bubbles that will have contact with the first pass desalted crude oil along with any nearby suspended salt particles and brine droplets, such that a single steam bubble may contact a number of remaining salt particles and remaining brine droplets;
g) condensing the steam bubbles from the second stream into droplets of liquid water while at the same time dissolving any remaining available salt particles forming new brine droplets and also delivering liquid or vaporous water from the steam bubbles into any remaining available brine droplets resulting in enlarged brine droplets having a size more amenable for separation from the first pass desalted crude oil;
h) separating and removing liquid water from the first pass desalted crude oil including water with salt dissolved therein to form a twice desalted crude oil;
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 or within the first pass desalted crude oil.

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Dependencies are inferred from the claim text.

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Abstract

a) 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 the any droplets of brine water so as to create steam bubbles that will have contact 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;
b) injecting liquid water into the crude oil;
c) condensing the steam bubbles into droplets of liquid water while at the same time dissolving available salt particles forming new brine droplets and also delivering liquid or vaporous water from the steam bubbles into any available brine droplets resulting in enlarged brine droplets having a size more amenable for separation from the crude oil;
d) imposing high shear mixing on the crude oil and water in a high shear mixer to enhance contact between salt particles, brine droplets and water droplets to enhance dissolving of salt particles and coalescence of brine droplets with water;
e) separating liquid water from the crude oil including water with salt dissolved therein to form a first pass desalted crude oil;
f) 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 remaining salt particles or relative to the any remaining droplets of brine water so as to create steam bubbles that will have contact with the first pass desalted crude oil along with any nearby suspended salt particles and brine droplets, such that a single steam bubble may contact a number of remaining salt particles and remaining brine droplets;
g) condensing the steam bubbles from the second stream into droplets of liquid water while at the same time dissolving any remaining available salt particles forming new brine droplets and also delivering liquid or vaporous water from the steam bubbles into any remaining available brine droplets resulting in enlarged brine droplets having a size more amenable for separation from the first pass desalted crude oil;
h) separating and removing liquid water from the first pass desalted crude oil including water with salt dissolved therein to form a twice desalted crude oil;
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 or within the first pass desalted crude oil.

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