IP Library Granted Patent US 8,899,326
Granted Patent B2
US 8,899,326 · App. 13/185,797 · Granted Dec 2, 2014

Oil recovery process

View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 8,899,326
App. No.
13/185,797
Granted
Dec 2, 2014
Kind
B2
Abstract

An oil recovery process entails recovering an oil-water mixture from an oil bearing formation and separating the oil-water mixture to produce an oil product and produced water. The produced water includes suspended and dissolved solids and is subjected to treatment which removes suspended and dissolved solids therefrom. The treated water is then directed to a forced circulation steam generator that includes a furnace having a burner, water cooled walls and an evaporator unit. The treated water is pumped through the water cooled walls and the evaporator unit. The water passing through the water cooled walls and evaporator unit are heated to produce approximately 10% to approximately 30% quality steam in both the water cooled walls and the evaporator unit. The steam is collected and separated from a water-steam mixture to produce high quality steam, on the order of 95% or greater quality steam. This steam constitutes injection steam which is injected into an injection well to facilitate the recovery of the oil-water mixture.

Claims (69)

1. A method of recovering oil and producing steam for injection into an injection well to assist in the recovery of oil, the method comprising:

recovering an oil-water mixture from an oil bearing formation;

separating oil from the oil-water mixture to produce an oil product and produced water where the produced water includes suspended solids and dissolved solids;

directing the produced water having the suspended and dissolved solids to a treatment system;

treating the produced water by removing suspended solids and dissolved solids from the produced water and producing treated water;

directing the treated water to a forced circulation steam generator comprising a furnace having a burner, at least one water cooled wall and an evaporator unit;

pumping a first portion of the treated water through at least one water cooled wall and pumping a second portion of the treated water through the evaporator unit in the furnace;

heating the water passing through the water cooled wall to form a first water-steam mixture comprising approximately 10% to approximately 30% quality steam;

heating the water passing through the evaporator unit to produce a second water-steam mixture comprising approximately 10% to approximately 30% quality steam;

directing the first and second water-steam mixtures to a steam separator and separating steam from the first and second water-steam mixtures to form injection steam comprising 95% or more quality steam; and

directing the injection steam into the injection well to facilitate the recovery of the oil-water mixture from the oil bearing formation.

2. The method of claim 1 wherein the forced circulation steam generator produces a blow-down stream that is 2% or less of the treated water directed to the forced circulation steam generator.

3. The method of claim 1 wherein the injection steam produced by the steam separator comprises 99% or more quality steam.

4. The method of claim 3 wherein the forced circulation steam generator produces a blow down stream that is 2% or less of the treated water directed to the forced circulation steam generator.

5. The method of claim 1 wherein the steam separator includes a steam drum and where the method further includes:

directing the first and second water-steam mixtures from the furnace into the steam drum and separating steam from the first and second water-steam mixtures;

directing the treated water into the steam drum;

pumping the treated water from the steam drum through the water cooled wall and evaporator unit; and

wherein the quantity of the treated water pumped from the steam drum through the water cooled wall and evaporator unit is more than five times the quantity of steam produced in the water cooled wall and evaporator unit.

6. The method of claim 1 including maintaining the flow of water to the furnace such that the flow of water to the water cooled wall and evaporator unit substantially exceeds the quantity of steam produced by the water cooled wall and evaporator unit.

7. The method of claim 1 including controlling the flow of the treated water to the furnace such that the steam quality of the water-steam mixture produced in each of the water cooled wall and evaporator unit is maintained at approximately 10% to approximately 30%.

8. The method of claim 1 wherein the steam separator includes a steam drum and the method further includes:

directing the treated water into the steam drum;

directing water from the steam drum to and through the water cooled wall and evaporator unit; and

controlling the flow of water through the water cooled wall and evaporator unit as a function of a firing rate of the burner.

9. The method of claim 8 including controlling the flow of water through the water cooled wall and evaporator unit such that the quality of steam produced by each of the water cooled wall and the evaporator unit is approximately 10% to approximately 30% quality steam.

10. The method of claim 1 wherein the steam separator includes a steam drum and the method further includes:

directing the treated water to the steam drum wherein the treated water mixes with water separated from the first and second water-steam mixtures to yield water held within the steam drum;

directing water from the steam drum to at least two pumps that are operatively connected between the steam drum and the water cooled wall and evaporator unit;

pumping a first portion of the water through a first line to and through the water cooled wall and pumping a second portion of the water through a second line to and through the evaporator unit; and

generally limiting the quality of steam produced in each of the water cooled wall and evaporator unit to approximately 30% or less quality steam.

11. A method of recovering oil and producing steam for injection into an injection well to assist in the recovery of oil from an oil bearing formation, the method comprising:

recovering an oil-water mixture from an oil bearing formation;

separating oil from the oil-water mixture to produce an oil product and produced water where the produced water includes suspended solids and dissolved solids;

directing the produced water having the suspended and dissolved solids to a treatment system;

treating the produced water by removing suspended solids and dissolved solids from the produced water and producing treated water;

directing the treated water to a forced circulation steam generator;

pumping the treated water through the forced circulation steam generator;

heating the water passing through the forced circulation steam generator to produce at least one water-steam mixture;

limiting the steam produced in the forced circulation steam generator to 30% or less quality steam;

generally maintaining the flow of treated water to the forced circulation steam generator such that the flow of water to the forced circulation steam generator is at least five times greater than the steam produced by the forced circulation steam generator;

collecting the steam produced by the forced circulation steam generator and directing the collected steam into the injection well;

wherein the forced circulation steam generator includes water cooled walls and an evaporator unit;

pumping a first portion of the treated water through the water cooled walls and pumping a second portion of the treated water through the evaporator unit;

heating the water passing through the water cooled walls to form a first water-steam mixture comprising approximately 10% to approximately 30% quality steam; and

heating the water passing through the evaporator unit to produce a second water-steam mixture comprising approximately 10% to 30% quality steam.

12. The method of claim 11 wherein the collected steam comprises 95% or more quality steam and wherein the forced circulation steam generator produces a blow down stream that is 2% or less of the treated water directed to the forced circulation steam generator.

13. The method of claim 11 wherein the forced circulation steam generator includes a steam separator and the method including:

directing the treated water to the steam separator;

pumping water from the steam separator to and through water cooled walls forming a part of a furnace of the steam generator; and

pumping water from the steam separator to and through an evaporator unit disposed in the furnace of the forced circulation steam generator;

heating the water in the water cooled walls and the evaporator unit such that the steam quality produced in the water cooled walls and the evaporator unit is limited to 30% or less quality steam.

14. A method of recovering oil and producing steam for injection into an injection well to assist in the recovery of oil from an oil bearing formation, the method comprising:

recovering an oil-water mixture from an oil bearing formation;

separating oil from the oil-water mixture to produce an oil product and produced water where the produced water includes suspended solids and dissolved solids;

directing the produced water having the suspended and dissolved solids to a treatment system;

treating the produced water by removing suspended solids and dissolved solids from the produced water and producing treated water;

directing the treated water to a forced circulation steam generator;

pumping the treated water through the forced circulation steam generator;

heating the water passing through the forced circulation steam generator to produce at least one water-steam mixture;

limiting the steam produced in the forced circulation steam generator to 30% or less quality steam;

generally maintaining the flow of treated water to the forced circulation steam generator such that the flow of water to the forced circulation steam generator is at least five times greater than the steam produced by the forced circulation steam generator;

collecting the steam produced by the forced circulation steam generator and directing the collected steam into the injection well; and

wherein the forced circulation steam generator includes a steam separator and the method includes:

i. directing the treated water to the steam separator;

ii. pumping water from the steam separator to and through water cooled walls forming a part of a furnace of the steam generator;

iii. pumping water from the steam separator to and through an evaporator unit disposed in the furnace of the forced circulation steam generator; and

iv. heating the water in the water cooled walls and the evaporator unit such that the steam quality produced in the water cooled walls and the evaporator unit is limited to 30% or less quality steam.

15. The method of claim 14 wherein the collected steam comprises 95% or more quality steam and wherein the forced circulation steam generator produces a blowdown stream that is 2% or less of the treated water directed to the forced circulation steam generator.

Assignments (15)
RELEASE OF SECURITY INTEREST Recorded May 15, 2024
From: BARINGS FINANCE LLC, AS COLLATERAL AGENT
To: THE CLEAVER-BROOKS COMPANY, INC.
Reel/Frame 067424/0729 →
RELEASE OF SECURITY INTEREST Recorded Oct 27, 2022
From: CLEAVER-BROOKS OF CANADA LIMITED
To: ROYAL BANK OF CANADA
Reel/Frame 061556/0326 →
RELEASE OF SECURITY INTEREST Recorded Oct 27, 2022
From: THE CLEAVER-BROOKS COMPANY, INC; THE CLEAVER-BROOKS COMPANY, INC.
To: U.S. BANK TRUST COMPANY, NATIONAL ASSOCIATION, SUCCESSOR IN INTEREST TO U.S. BANK NATIONAL ASSOCIATION
Reel/Frame 061556/0369 →
SECURITY INTEREST Recorded Jul 18, 2022
From: THE CLEAVER- BROOKS COMPANY, INC.
To: BARINGS FINANCE LLC, AS COLLATERAL AGENT
Reel/Frame 060532/0952 →
PATENT SECURITY AGREEMENT Recorded Dec 16, 2021
From: THE CLEAVER BROOKS COMPANY, INC.
To: ROYAL BANK OF CANADA
Reel/Frame 058533/0405 →
CHANGE OF NAME Recorded Aug 30, 2021
From: CLEAVER-BROOKS, INC.
To: CLEAVER-BROOKS, LLC
Reel/Frame 057392/0177 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 30, 2021
From: CLEAVER-BROOKS, LLC
To: THE CLEAVER-BROOKS COMPANY, INC.
Reel/Frame 057329/0669 →
SECURITY INTEREST Recorded Aug 30, 2021
From: THE CLEAVER-BROOKS COMPANY, INC.
To: ROYAL BANK OF CANADA
Reel/Frame 057331/0131 →
SECURITY INTEREST Recorded Aug 30, 2021
From: THE CLEAVER-BROOKS COMPANY, INC.
To: U.S. BANK NATIONAL ASSOCIATION
Reel/Frame 057331/0182 →
RELEASE OF SECURITY INTEREST Recorded Dec 15, 2017
From: WILMINGTON TRUST NATIONAL ASSOCIATION
To: CLEAVER-BROOKS, INC.
Reel/Frame 044405/0919 →
RELEASE OF SECURITY INTEREST Recorded Dec 14, 2017
From: U.S. BANK NATIONAL ASSOCIATION, AS COLLATERAL AGENT
To: CLEAVER-BROOKS, INC.
Reel/Frame 044393/0297 →
SECURITY INTEREST Recorded Dec 14, 2017
From: CLEAVER-BROOKS, INC.
To: U.S. BANK NATIONAL ASSOCIATION, AS COLLATERAL AGENT
Reel/Frame 044401/0702 →
SECURITY INTEREST Recorded Jul 17, 2014
From: CLEAVER-BROOKS, INC.
To: WILMINGTON TRUST NATIONAL ASSOCIATION
Reel/Frame 033350/0617 →
SECURITY AGREEMENT Recorded Dec 26, 2012
From: CLEAVER-BROOKS, INC.
To: U.S. BANK NATIONAL ASSOCIATION, AS COLLATERAL AGENT; ROYAL BANK OF CANADA
Reel/Frame 029540/0164 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 20, 2011
From: VASUDEVAN, MEENATCHINATHAN
To: CLEAVER-BROOKS, INC.
Reel/Frame 026935/0753 →