Method of direct steam generation using an oxyfuel combustor

• US 8,522,871 B2
• Filed: 03/04/2010
• Issued: 09/03/2013
• Est. Priority Date: 03/04/2009
• Status: Active Grant

• Current Assignee: World Energy Systems
• Original Assignee: World Energy Systems
• Inventors: Anderson, Roger E., Pronske, Keith L., Propp, Murray
• Primary Examiner(s): DiTrani, Angela M
• Assistant Examiner(s): LOIKITH, CATHERINE A
• Application Number:
  US12/660,780
• Publication Number:
  US 20100224363A1
• Time in Patent Office: 1,279 Days
• Field of Search: 166/272.1, 166/302, 166/303
• US Class Current: 166/272.1
• CPC Class Codes: E21B 43/164 Injecting CO2 or carbonated water in combination with organic material C09K8/594
• CPC Class Codes: E21B 43/24 using heat, e.g. steam injection
• CPC Class Codes: E21B 43/2406 Steam assisted gravity drainage [SAGD]
• CPC Class Codes: E21B 43/2408 SAGD in combination with other methods
• CPC Class Codes: E21B 43/34 Arrangements for separating materials produced by the well
• CPC Class Codes: F22B 1/003 using combustion of hydrogen with oxygen power plants using steam created by combustion of hydrogen with oxygen F01K25/005
• CPC Class Codes: F22B 1/1853 coming in direct contact with water in bulk or in sprays

Abstract

A gas generator is provided with a combustion chamber into which oxygen and a hydrogen containing fuel are directed for combustion therein. The gas generator also includes water inlets and an outlet for a steam and CO₂ mixture generated within the gas generator. The steam and CO₂ mixture can be used for various different processes, with some such processes resulting in recirculation of water from the processor back to the water inlets of the gas generator. In one process a hydrocarbon containing subterranean space is accessed by a well and the steam and CO₂ mixture is directed into the well to enhance removability of hydrocarbons within the subterranean space. Fluids are then removed from the subterranean space include hydrocarbons and water, with a portion of the hydrocarbons then removed in a separator/recovery step. The resulting hydrocarbon removal system can operate with no polluting emissions and with no water requirements.

Claims

1. A method for direct steam and CO₂ mixed gas generation and utilization, including the steps of:

providing a gas generator having a combustion chamber, an oxygen inlet leading into the combustion chamber, a fuel inlet leading into the combustion chamber, a plurality of water inlets leading into the gas generator and a steam and CO₂ mixture outlet from the combustion chamber;

configuring the gas generator to include multiple adjacent chambers with separate water inlets passing into the gas generator between the adjacent chambers, such that temperatures in the adjacent chambers are progressively lower as distance from the combustion chamber increases;

coupling the steam and CO₂ mixture outlet of the gas generator to an inlet of a steam and CO₂ utilizing processor;

configuring the processor to be in the form of a steam assisted gravity drain site including a hydrocarbon containing subterranean space and a well extending into the subterranean space, the well coupled to the steam and CO₂ mixture outlet of the gas generator;

recirculating at least a portion of water and hydrocarbons exiting from a drain of the steam assisted gravity drain site to the water inlets of the gas generator; and

combusting at least a portion of the hydrocarbons contained within the water within the gas generator.

2. The method of claim 1 wherein said recirculating step includes interposing a softener upstream of the at least one water inlet of the gas generator to soften the water before entry into the gas generator.

3. The method of claim 1 including the further step of recirculating water to the gas generator water inlets from a discharge of the processor, such that the method is at least partially a closed loop process.

4. The method of claim 1 including the further step of configuring the processor to include a separate water discharge and carbon dioxide discharge, the water discharge coupled to said gas generator water inlets for recirculating of water to the gas generator water inlet.

5. The system of claim 1 including the further step of locating a separator between the steam and CO₂ mixture outlet of the gas generator and the processor, the separator adapted to separate non-steam and CO₂ constituents from the steam and CO₂ mixture.

6. The method of claim 1 including the further step of recirculating at least a portion of water exiting from a drain of the steam assisted gravity drain site to the water inlets of the gas generator.