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A fuel stabilization system includes a first deoxygenator and a second deoxygenator both for removing dissolved oxygen from a hydrocarbon fuel. The first and second deoxygenators are arranged in parallel or series to sequentially remove a portion of dissolved oxygen from the hydrocarbon fuel. The

A fuel stabilization system includes a first deoxygenator and a second deoxygenator both for removing dissolved oxygen from a hydrocarbon fuel. The first and second deoxygenators are arranged in parallel or series to sequentially remove a portion of dissolved oxygen from the hydrocarbon fuel. The arrangement of several deoxygenators for a single fuel stream improves removal of dissolved oxygen and provides for scalability of the fuel system to meet application specific demands. The arrangement also provides for the preservation of partial system functionality in the event of the failure of one of the deoxygenator modules.

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What is claimed is: 1. A fuel stabilization system comprising: a first fuel deoxygenator for removing a first portion of oxygen from a fuel at a first temperature lower than a temperature that produces undesirable by-products responsive to an amount of dissolved oxygen within the fuel prior to ente

What is claimed is: 1. A fuel stabilization system comprising: a first fuel deoxygenator for removing a first portion of oxygen from a fuel at a first temperature lower than a temperature that produces undesirable by-products responsive to an amount of dissolved oxygen within the fuel prior to entering the first fuel deoxygenator; and a second fuel deoxygenator for removing a second portion of oxygen from the fuel at a second temperature greater than the first temperature, wherein said first fuel deoxygenator and said second deoxygenator remove oxygen from a common fuel stream. 2. The system as recited in claim 1, wherein said second fuel deoxygenator comprises a plurality of fuel deoxygenators. 3. The system as recited in claim 1, wherein said first fuel deoxygenator and said second deoxygenator are arranged in series. 4. The system as recited in claim 1, wherein said first deoxygenator and said second deoxygenator are arranged in parallel. 5. The system as recited in claim 1, wherein said first portion of oxygen removed from the fuel by the first deoxygenator is greater than said second portion of oxygen removed by said second fuel deoxygenator. 6. The system as recited in claim 1, wherein said first deoxygenator has a greater capacity for removing dissolved oxygen from the fuel than said second fuel deoxygenator. 7. The system as recited in claim 1, including a heat transfer device for transferring heat into the fuel, wherein said heat transfer device is disposed downstream of at least one of said first deoxygenator and said second deoxygenator. 8. The system as recited in claim 1, including a first heat transfer device for transferring heat to the fuel before entering said first fuel deoxygenator. 9. The system as recited in claim 8, including a second heat transfer device for transferring heat to the fuel after exiting said first deoxygenator. 10. The system as recited in claim 9, including a third heat transfer device for transferring heat to the fuel after exiting said second heat transfer device. 11. A method of stabilizing a fuel for a fuel delivery system comprising the steps of: a) flowing a fuel at a first temperature through a first deoxygenator and removing a first portion of dissolved oxygen; b) flowing the hydrocarbon fuel through a second deoxygenator and removing a second portion of dissolved oxygen; and c) increasing a temperature of the fuel to a second temperature greater than said first temperature after the fuel exits the first deoxygenator and prior to entering the second deoxygenator. 12. The method as recited in claim 11, wherein the first temperature is below a temperature that produces undesirable by-products responsive to an amount of dissolved oxygen with the fuel prior to entering the first deoxygenator. 13. A method of stabilizing a fuel for a fuel delivery system comprising the steps of: a) flowing a fuel at a first temperature through a first deoxygenator and removing a first portion of dissolved oxygen, wherein the first temperature is below a temperature that produces undesirable by-products responsive to an amount of dissolved oxygen with the fuel prior to entering the first deoxygenator; b) flowing the hydrocarbon fuel through a second deoxygenator and removing a second portion of dissolved oxygen; and c) increasing a temperature of the fuel to a second temperature greater than said first temperature after the fuel exits the first deoxygenator and prior to entering the second deoxygenator. 14. The method as recited in claim 13, wherein said second temperature is greater than a temperature that causes formation of insoluble materials in fuel including said first portion of dissolved oxygen, such that said second temperature is only obtainable without producing insoluble materials after removing the first portion of dissolved oxygen from the fuel. 15. The method as recited in claim 11, wherein said first deoxygenator and said second deoxygenator are arranged in series. 16. The method as recited in claim 11, wherein said first deoxygenator and said second deoxygenator are arranged in parallel. 17. The method as recited in claim 11, wherein said first portion of dissolved oxygen removed by said first deoxygenator is less than said second portion removed by said second deoxygenator. 18. The method as recited in claim 11, including the step of flowing the fuel through a heat transfer device to transfer heat into the fuel. 19. The system as recited in claim 1, including a heat exchanger receiving fuel exiting the first fuel deoxygenator and communicating fuel to the second fuel deoxygenator, for increasing fuel temperature form the first temperature to the second temperature. 20. The system as recited in claim 1, wherein the second temperature is greater than a temperature that causes formation of insoluble materials in fuel including the first portion of dissolved oxygen, such that the second temperature is only obtainable without producing insoluble material after removing the first portion of dissolved oxygen from the fuel.