초록 ▼

A method for recovering oil (24) from a natural oil reservoir (18) includes the steps of separating air to produce an oxygen rich stream (40) and a nitrogen rich stream (34), providing a natural gas stream (12) and feeding at least part of the oxygen rich stream (40) and the natural gas stream (12)

A method for recovering oil (24) from a natural oil reservoir (18) includes the steps of separating air to produce an oxygen rich stream (40) and a nitrogen rich stream (34), providing a natural gas stream (12) and feeding at least part of the oxygen rich stream (40) and the natural gas stream (12) into a gas to liquid or GTL conversion installation (42) to produce hydrocarbon products (44) and heat. The heat produced in the gas to liquid conversion installation is used to produce energy ( 20) to pressurize (16) the nitrogen in the nitrogen rich stream (34) to produce a pressurized nitrogen rich stream ( 22). The pressurized nitrogen rich stream (22) is passed into a natural oil reservoir (18) to enhance the recovery of oil ( 24) from the reservoir.

대표청구항 ▼

The invention claimed is: 1. A method for recovering oil from a natural oil reservoir, the method including the steps of separating air to produce an oxygen rich stream and a nitrogen rich stream; providing a natural gas stream and feeding at least part of the oxygen rich stream and the natural gas

The invention claimed is: 1. A method for recovering oil from a natural oil reservoir, the method including the steps of separating air to produce an oxygen rich stream and a nitrogen rich stream; providing a natural gas stream and feeding at least part of the oxygen rich stream and the natural gas stream into a gas to liquid or GTL conversion installation to produce hydrocarbon products and heat; using heat produced in the gas to liquid conversion installation to produce energy to pressurize the nitrogen in the nitrogen rich stream to produce a pressurized nitrogen rich stream; and passing the pressurized nitrogen rich stream into a natural oil reservoir to enhance the recovery of oil from the reservoir. 2. A method as claimed in claim 1, in which the energy is in a form selected from electrical energy and high pressure steam. 3. A method as claimed in claim 1, in which the air is separated to produce an oxygen rich stream containing about 0-25% nitrogen and a nitrogen rich stream containing about 0-5% oxygen. 4. A method as claimed in claim 3, in which the nitrogen rich stream contains less than about 10 ppm of oxygen. 5. A method for recovering oil from a natural oil reservoir as claimed in claim 1, in which the natural gas is obtained from the natural oil reservoir from which oil recovery is being enhanced. 6. A method for recovering oil from a natural oil reservoir as claimed in claim 5, in which nitrogen is separated from the natural gas before feeding the natural gas into the gas to liquid conversion installation. 7. A method of modifying an enhanced oil recovery process of the type in which a natural gas is fed into a natural oil reservoir to enhance oil recovery the method including diverting at least part of the natural gas to a gas to a liquid (GTL) conversion installation which is linked to an air separation plant which produces an oxygen rich stream and a nitrogen rich stream; feeding the oxygen rich steam into the gas to liquid conversion installation; and passing at least part of the nitrogen rich stream into the oil reservoir to replace the natural gas which has been diverted. 8. A method as claimed in claim 7 which includes using at least some of the heat produced in the gas to liquid installation to generate energy to raise the pressure of the nitrogen rich stream. 9. A method of modifying an enhanced oil recovery installation of the type in which a natural gas is fed into a natural oil reservoir, and which includes at least one natural gas feed line for feeding the natural gas into the reservoir, the method including providing a gas to liquid (GTL) conversion installation and an air separation plant capable of producing an oxygen rich stream and a nitrogen rich stream, the air separation plant having an oxygen outlet and a nitrogen outlet, and linking the oxygen outlet to the gas to liquid conversion installation so that oxygen can be fed into the gas to liquid conversion installation; linking the natural gas feed line to the gas to liquid conversion installation with a gas flow line so that at least part of the natural gas can be diverted to the gas to liquid conversion installation; providing a nitrogen pressurization installation and linking it to the nitrogen outlet of the air separation plant so that nitrogen can flow to the pressurization installation to be pressurized; and providing a flow line to extend from the nitrogen pressurization installation to the natural oil reservoir so that pressurized nitrogen can flow to the oil reservoir. 10. A method as claimed in claim 9 which includes providing an energy converter and linking it to the nitrogen pressurization installation and the gas to liquid conversion installation so that heat generated in the gas to liquid conversion installation can be converted to energy for the pressurization installation. 11. A method of modifying an enhanced oil recovery installation of the type in which a natural gas is fed into a natural oil reservoir, and which includes at least one natural gas feed line and a natural gas pressurization installation for feeding the natural gas into the reservoir, the method including providing a gas to liquid (GTL) conversion installation and an air separation plant capable of producing an oxygen rich stream and a nitrogen rich stream, the air separation plant having an oxygen outlet and a nitrogen outlet, and linking the oxygen outlet to the gas to liquid conversion installation so that oxygen can be fed into the gas to liquid conversion installation; linking the natural gas feed line to the gas to liquid conversion installation with a gas flow line so that at least part of the natural gas can be diverted to the gas to liquid conversion installation; linking the natural gas pressurization installation to the nitrogen outlet of the air separation plant so that nitrogen can flow to the pressurization installation to be pressurized; and providing a flow line to extend from the nitrogen pressurization installation to the natural oil reservoir so that pressurized nitrogen can flow to the oil reservoir. 12. A method as claimed in claim 11, in which the pressurizing installation comprises at least one natural gas compressor and in which the method includes modifying the compressor for nitrogen service. 13. A method as claimed in claim 11 which includes providing an energy converter and linking it to the nitrogen pressurization installation and the gas to liquid conversion installation so that heat generated in the gas to liquid conversion installation can be converted to energy for the pressurization installation. 14. An installation as claimed in claim 13, in which the waste heat converter is a waste heat boiler which generates high pressure steam. 15. In a method of recovering oil from a natural oil reservoir in which pressurized nitrogen is pumped into the natural oil reservoir to enhance recovery of oil from the reservoir, the nitrogen being produced in an air separation plant which produces a waste oxygen stream having a purity of 70-100% and a high purity nitrogen stream, there is provided the improvement of providing a natural gas stream and feeding the natural gas stream together with the waste oxygen stream into a gas to liquid conversion installation to produce hydrocarbon products and heat; and using at least some of the heat produced in the gas to liquid installation to generate energy to pressurize the nitrogen stream. 16. A method as claimed in claim 15, in which the waste oxygen stream has a purity of 90-100%. 17. An installation for the production of gas to liquid (GTL) products and enhanced oil recovery from a natural oil reservoir, the installation including a pressurizing installation for raising the pressure of nitrogen for the enhanced recovery of oil; an air separation plant capable of producing nitrogen having an oxygen content of less than 10 ppm; a gas to liquid conversion plant; flow lines arranged to feed natural gas to the gas to liquid conversion plant and nitrogen from the air separation plant to the pressurizing installation; and a waste heat converter arranged to convert waste heat produced in the gas to liquid conversion plant into energy and which is operably linked to the pressurizing installation to provide energy for driving the pressurizing installation. 18. A modified installation for the production of gas to liquid (GTL) products and enhanced oil recovery from a natural oil reservoir, the installation including pressurizing installation; an air separation plant capable of producing nitrogen having an oxygen content of less than 10 ppm; a gas to liquid conversion plant; flow lines and control valves arranged to divert at least some natural gas from a natural gas enhanced oil recovery service to the gas to liquid conversion plant and nitrogen from the air separation plant to the pressurizing installation; and a waste heat converter arranged to convert waste heat produced in the gas to liquid conversion plant into energy and which is operably linked to the pressurizing installation to provide energy for driving the pressurizing installation. 19. In a process in which pressurized natural gas is used for the enhanced recovery of oil, there is provided a method of replacing at least some of the natural gas with nitrogen such that the volume of the nitrogen is 1.5 to 2.5 times greater than that of the natural gas which it replaces, the method including diverting at least part of the natural gas to a gas to liquid (GTL) conversion installation which is linked to an air separation plant which produces an oxygen rich stream and a nitrogen rich stream; feeding the oxygen rich stream into the gas to liquid conversion installation; and passing at least part of the nitrogen rich stream into the oil reservoir to replace the natural gas which has been diverted. 20. A method as claimed in claim 19, which includes using at least some of the heat produced in the gas to liquid installation to generate energy to raise the pressure of the nitrogen rich stream. 21. In a process in which pressurized natural gas is passed into a natural oil reservoir for the enhanced recovery of oil, there is provided a method of reducing the volume of natural gas required for the enhanced oil recovery by between about 20% and 60%, the method including diverting at least part of the natural gas to liquid (GTL) conversion installation which is linked to an air separation plant which produces an oxygen rich stream and a nitrogen rich stream; and passing at least part of the nitrogen rich stream into the oil reservoir to replace the natural gas which has been diverted. 22. A method as claimed in claim 21, which includes using at least some of the heat produced in the gas to liquid installation to generate energy to raise the pressure of the nitrogen rich stream.