Recovery of hydrocarbon diluent from tailings

Patent metadata

Field	Value
Publication number	US-10508241-B2
Application number	US-201715614381-A
Country	US
Kind code	B2
Filing date	Jun 5, 2017
Priority date	Jun 5, 2017
Publication date	Dec 17, 2019
Grant date	Dec 17, 2019

Abstract

A method for recovering hydrocarbon diluent from tailings comprising bitumen, particulate solids, hydrocarbon diluent and water, is provided comprising introducing the tailings into a high pressure stripping vessel operating at a pressure greater than 100 kPa; and introducing a stripping gas into the high pressure stripping vessel to strip the hydrocarbon diluent and water from the tailings and form a stripped tailings pool at the bottom of the vessel.

First claim

What is claimed:

1. A method for recovering hydrocarbon diluent from tailings comprising bitumen, particulate solids, hydrocarbon diluent and water, the method comprising:
providing a high pressure stripping vessel operating at a pressure greater than 100 kPa, the high pressure stripping vessel having internal, vertically and laterally spaced shed decks in its upper portion and a deck-free bottom portion where a tailings pool forms;
introducing a portion of the tailings into the high pressure stripping vessel above the shed decks or in between the shed decks or both, and a portion of the tailings into the tailings pool formed in the high pressure stripping vessel; and
introducing a stripping gas into the high pressure stripping vessel below the shed decks but above the tailings pool or in between the shed decks or both, and into the tailings pool formed in the high pressure stripping vessel to strip the hydrocarbon diluent and water from the tailings.

2. The method as claimed in claim 1 , wherein the stripping gas is steam.

3. The method as claimed in claim 1 further comprising removing a portion of the tailings from the tailings pool and recycling the portion of tailings back to the high pressure stripping vessel.

4. The method as claimed in claim 1 , wherein the pressure in the high pressure stripping vessel is between 100-200 kPa.

5. A method for recovering hydrocarbon diluent from tailings comprising bitumen, particulate solids, hydrocarbon diluent and water, the method comprising:
introducing the tailings into a high pressure stripping vessel operating at a pressure greater than 100 kPa such that a stripped tailings pool is formed at the bottom of the high pressure stripping vessel and hydrocarbon diluent and water is removed from the top of the high pressure stripping vessel;
introducing steam into the high pressure stripping vessel either above the stripped tailings pool or into the stripped tailings pool or both; and
removing a portion of high temperature stripped tailings from the stripped tailings pool and introducing the portion of high temperature stripped tailings into a low pressure flash vessel operating at a pressure below 100 kPa to remove additional hydrocarbon diluent from the portion of high temperature stripped tailings.

6. The method as claimed in claim 5 , wherein the high pressure stripping vessel comprises a stack of internal, vertically and laterally spaced shed decks and the tailings are introduced into the vessel such that the tailings are distributed over at least some of the shed decks.

7. The method as claimed in claim 6 , wherein the steam is introduced below the shed decks but above the stripped tailings pool.

8. The method of claim 6 , wherein the steam is introduced both below the shed decks but above the stripped tailings pool and into the tailings pool.

9. The method of claim 6 , wherein the tailings are injected in between the stack of shed decks and directly above the stack of shed decks.

10. The method as claimed in claim 5 , wherein the steam is introduced into the stripped tailings pool.

11. The method of claim 5 , wherein the tailings are introduced into the high pressure stripping vessel by injecting the tailings into the stripped tailings pool.

12. The method of claim 5 , wherein a portion of high temperature stripped tailings from the stripped tailings pool is recycled back to the high pressure stripping vessel.

13. A method for recovering hydrocarbon diluent from tailings comprising bitumen, particulate solids, hydrocarbon diluent and water, the method comprising:
separating the tailings into a fine tailings slurry and a coarse tailings slurry;
introducing the fine tailings slurry into a first high pressure stripping vessel operating at a pressure greater than 100 kPa;
introducing a stripping gas into the first high pressure stripping vessel to strip the hydrocarbon diluent and water from the fine tailings slurry and form a stripped fine tailings pool at the bottom of the vessel;
introducing the coarse tailings slurry into a second high pressure stripping vessel operating at a pressure greater than 100 kPa; and
introducing a stripping gas into the second high pressure stripping vessel to strip the hydrocarbon diluent and water from the coarse tailings slurry and form a stripped coarse tailings pool at the bottom of the vessel.

14. The method as claimed in claim 13 , further comprising:
removing a portion of high temperature stripped fine tailings from the stripped fine tailings pool and a portion of high temperature stripped coarse tailings from the stripped coarse tailings pool; and
introducing the portion of high temperature stripped fine tailings and the portion of high temperature stripped coarse tailings into a low pressure flash vessel operating at a pressure below 100 kPa to remove additional hydrocarbon diluent from the portions.

15. The method as claimed in claim 13 , wherein the first high pressure stripping vessel comprises trays or packings and the second high pressure stripping vessel comprises shed decks.

Assignees

• Syncrude Canada Ltd
• Syncrude Canada Ltd

Inventors

• Bhattacharya Sujit
• Bara Barry
• Mcknight Craig A
• Bulbuc Daniel John
• Cymerman George

Classifications

• C10G1/045

  Separation of insoluble materials · CPC title

• C10G1/04 Primary

  by extraction · CPC title