Systems and methods for generating superheated steam with variable flue gas for enhanced oil recovery

• US 10,641,481 B2
• Filed: 05/03/2017
• Issued: 05/05/2020
• Est. Priority Date: 05/03/2016
• Status: Active Grant

• Current Assignee: Energy Analyst LLC
• Original Assignee: Energy Analyst LLC
• Inventors: Donaldson, A. Burl, Hughes, Brian
• Primary Examiner(s): Gay, Jennifer H
• Application Number:
  US15/586,125
• Publication Number:
  US 20170321883A1
• Time in Patent Office: 1,098 Days
• CPC Class Codes: E21B 43/24 using heat, e.g. steam injection
• CPC Class Codes: F22D 1/02 with water tubes arranged in the boiler furnace, fire tubes, or flue ways heat-exchange tubes in general F28F
• CPC Class Codes: F22D 11/00 Feed-water supply not provided for in other main groups
• CPC Class Codes: F22G 1/12 by mixing steam with furnace gases or other combustion products
• CPC Class Codes: F22G 1/16 by using a separate heat source independent from heat supply of the steam boiler, e.g. by electricity, by auxiliary combustion of fuel oil
• CPC Class Codes: F22G 5/20 by combined controlling procedures
• CPC Class Codes: F22G 7/12 in flues

Abstract

Systems and methods are disclosed for producing a superheated steam having a specified ratio of water vapor to combustion gases for injection into a well to enhance heavy oil production. Embodiments comprise indirect-contact steam generators and direct-contact steam generators.

Claims

1. A system for generating superheated steam for injection into an oil well comprising:

a direct-contact superheater performing combustion and operating on feedwater in either a liquid state or a gas state or some combination of both states and generating a superheated steam having a specified ratio of non-condensable combustion gases to steam for injection into the oil well, the superheated steam causing pyrolysis of the oil;

a boiler heating the feedwater before the feedwater is passed to a separator;

said separator separating liquid from the feedwater before at least a fraction of vapor phase of the feedwater is passed to the direct-contact superheater; and

returning the liquids separated by said separator to the boiler.

2. The system of claim 1 further comprising a water purifier for receiving the feedwater before the feedwater is operated on by said direct-contact superheater and purifying the feedwater such that the amount of solids within the feedwater does not exceed a predetermined amount for delivery to said direct-contact superheater.

3. The system of claim 1 wherein said direct-contact superheater operates using compressed air, gaseous oxygen, and/or liquid oxidizers.

4. The system of claim 1 wherein said direct-contact superheater comprises a combustion chamber lined with a refractory material.

5. The system of claim 1 wherein said direct-contact superheater comprises a combustion chamber fabricated of a metal alloy with a low coefficient of thermal expansion.

6. The system of claim 1 wherein said direct-contact superheater is located within the oil well and below a thermal packer.

7. The system of claim 1 wherein said boiler comprises an indirect-contact steam generator connected to said direct-contact superheater through said separator, said indirect-contact steam generator operating on the feedwater before the feedwater is operated on by said separator and said direct-contact superheater, said indirect-contact steam generator generating a specified quantity and/or quality of feedwater vapor for delivery to said direct-contact superheater through said separator.

8. The system of claim 7 further comprising a water purifier for receiving the feedwater before the feedwater is operated on by said indirect-contact steam generator and purifying the feedwater such that the amount of solids within the feedwater does not exceed a predetermined amount for delivery to said indirect-contact steam generator.

9. The system of claim 7 wherein said direct-contact steam generator comprises a combustion chamber comprising at least one fin on an external surface of said combustion chamber and a metal sleeve surrounding said at least one fin and said combustion chamber.

10. The system of claim 7 wherein said direct-contact superheater comprises a combustion chamber comprising openings to receive at least a fraction of feedwater vapor generated by said indirect-contact steam generator.

11. The system of claim 7 wherein, said direct-contact superheater receives the feedwater for cooling before the feedwater is operated on by said indirect-contact steam generator.

12. The system of claim 7 further comprising a programmable logic control system for directing the operation of said direct-contact superheater and said indirect-contact steam generator.

13. A method for generating superheated steam for injection into a well comprising:

receiving feedwater;

producing heated feedwater by heating the feedwater with a boiler, wherein the heated feedwater is either in a liquid state or a gas state or some combination of both states;

passing at least some of the heated feedwater to a separator that separates liquid-phase feedwater from vapor feedwater;

passing at least some of the vapor feedwater from the separator to a direct-contact superheater;

feeding the liquid-phase feedwater from the separator to the boiler;

generating superheated steam having a specified ratio of non-condensable combustion gases to steam using the direct-contact superheater to perform combustion and operate on the heated feedwater;

injecting the superheated steam into the well; and

using gas created by pyrolysis of oil in the well as fuel for the boiler.

14. The method of claim 13 further comprising purifying the feedwater or the heated feedwater such that the amount of solids within the feedwater or the heated feedwater does not exceed a predetermined amount.

15. The method of claim 13 wherein producing heated feedwater by heating the feedwater with a boiler comprises generating feedwater vapor using an indirect-contact steam generator connected to the direct-contact superheater through the separator, wherein the indirect-contact steam generator operates on the received feedwater before at least some of the vapor from the heated feedwater is operated on by the direct-contact superheater, and wherein the indirect-contact steam generator generates a specified quantity and/or quality of feedwater vapor for delivery to the direct-contact superheater.

16. The method of claim 15 further comprising cooling the direct-contact superheater using at least a fraction of the feedwater vapor generated by the indirect-contact steam generator, wherein the direct-contact superheater comprises a combustion chamber comprising at least one fin on an external surface of the combustion chamber and a metal sleeve surrounding the at least one fin and the combustion chamber.

17. The method of claim 15 further comprising cooling the direct-contact superheater using at least a fraction of the feedwater vapor generated by the indirect-contact steam generator, wherein the direct-contact superheater comprises a combustion chamber comprising small openings to receive at least a fraction of the feedwater vapor generated by the indirect-contact steam generator.

18. The method of claim 15 further comprising cooling the direct-contact superheater using the feedwater before the feedwater is operated on by the indirect-contact steam generator.

19. A method for generating superheated steam for injection into an oil well comprising:

receiving feedwater;

generating feedwater vapor from the feedwater using an indirect-contact steam generator, wherein the indirect-contact steam generator comprises fuel and oxidizer inputs for combustion;

generating superheated steam using the feedwater vapor using a direct-contact superheater, wherein the direct-contact superheater comprises fuel and oxidizer inputs for combustion;

separating liquid feedwater from the feedwater vapor after the feedwater vapor is generated by the indirect contact steam generator and before passing at least some of the water vapor to the direct contact superheater;

controlling the fuel and oxidizer inputs on the indirect-contact steam generator and the direct-contact superheater to specify a ratio of non-condensable combustion gases to steam; and

generating gas by pyrolysis of oil in the oil well with heat introduced by the superheated steam.