Nitrogen bubbler system in fuel tank and method
US-9096326-B2 · Aug 4, 2015 · US
US10874980B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10874980-B2 |
| Application number | US-201715673022-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 9, 2017 |
| Priority date | Aug 9, 2017 |
| Publication date | Dec 29, 2020 |
| Grant date | Dec 29, 2020 |
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A gas inerting system employs a carbon dioxide separation unit to remove carbon dioxide and water from an oxygen depleted gas stream generated from a catalytic oxidation unit and subsequently provides a nitrogen rich inerting gas to a fuel tank and/or to a cargo hold. A method of producing an inert gas passes an oxygen depleted gas stream from a catalytic oxidation unit through a carbon dioxide separation unit and provides a nitrogen rich inerting gas for fuel tank inerting and/or cargo hold fire suppression.
Opening claim text (preview).
The invention claimed is: 1. A gas inerting system for supplying an inerting gas stream to an inerting location of an aircraft, the gas inerting system comprising: a fuel tank; a fuel separation unit configured to receive fuel vapor and liquid fuel from the fuel tank and form a concentrated fuel vapor; a catalytic oxidation unit downstream of the fuel separation unit, configured to receive the concentrated fuel vapor from the fuel separation unit, combust the received concentrated fuel vapor to reduce an amount of oxygen, and form an oxygen depleted gas stream; a carbon dioxide separation unit comprising a membrane, the carbon dioxide separation unit located downstream of the catalytic oxidation unit and configured to receive the oxygen depleted gas stream from the catalytic oxidation unit, wherein the carbon dioxide separation unit increases an amount of nitrogen and reduces an amount of carbon dioxide and water in the oxygen depleted gas stream and forms the inerting gas stream; and a gas flow path for the inerting gas stream from the carbon dioxide separation unit to the inerting location. 2. The system of claim 1 , wherein the membrane has a configuration selected from the group consisting of planar geometry, spiral wound, hollow fiber, and combinations thereof. 3. The system of claim 1 , wherein the membrane is formed of at least one material selected from the group consisting of polyether-polyamide block copolymer (PEBAX), polyphenylene oxide (PPO), polyimide, polydimethylphenylene oxide, polysulfone, polyethersulfone, poly(4-vinylpyridine)/polyetherimide, polyacrylonitrile with poly(ethylene glycol), poly(amide-6-b-ethylene oxide), poly-vinilydene fluoride (PVDF), and mixtures thereof. 4. The system of claim 1 , wherein the carbon dioxide separation unit further comprises a partial pressure differential source in flow communication with the membrane. 5. The system of claim 4 , wherein the partial pressure differential source is a vacuum pump. 6. The system of claim 4 , wherein the partial pressure differential source is an ejector. 7. The system of claim 4 , wherein the partial pressure differential source is a sweep gas. 8. The system of claim 1 , wherein the inerting location is the fuel tank. 9. The system of claim 1 , wherein the inerting location is a cargo hold. 10. A method for supplying an inerting gas stream to an inerting location of an aircraft, the method comprising: receiving a fuel vapor and liquid fuel from a fuel tank into a fuel separation unit and forming a concentrated fuel vapor; delivering the concentrated fuel vapor from the fuel separation unit to a catalytic oxidation unit and forming an oxygen depleted gas stream; receiving the oxygen depleted gas stream into a carbon dioxide separation unit comprising a membrane from the catalytic oxidation unit; decreasing an amount of carbon dioxide and water in the oxygen depleted gas stream by the membrane and forming the inerting gas stream, wherein the inerting gas stream is a nitrogen enriched inerting gas stream; and providing the inerting gas stream to the inerting location. 11. The method of claim 10 , wherein decreasing the amount of carbon dioxide and water in the oxygen depleted gas stream further comprises creating a partial pressure gradient across the membrane. 12. The method of claim 11 , wherein the membrane is formed of at least one material selected from the group consisting of polyether-polyamide block copolymer (PEBAX), polyphenylene oxide (PPO), polyimide, polydimethylphenylene oxide, poly sulfone, polyethersulfone, poly(4-vinylpyridine)/polyetherimide, polyacrylonitrile with poly(ethylene glycol), poly(amide-6-b-ethylene oxide), poly-vinilydene fluoride (PVDF), and mixtures thereof. 13. The method of claim 10 , wherein the inerting location is a fuel tank. 14. The method of claim 10 , wherein the inerting location is a cargo hold.
Removing carbon monoxide or hydrocarbons · CPC title
Oxygen · CPC title
Combined chemical and physical processing · CPC title
for containers filled with inflammable liquids · CPC title
using gases or vapours that do not support combustion, e.g. steam, carbon dioxide · CPC title
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