USE OF OZONE CONVERSION IN AIRCRAFT AIR MANAGEMENT

• US 20100021360A1
• Filed: 09/07/2007
• Published: 01/28/2010
• Est. Priority Date: 09/08/2006
• Status: Abandoned Application

• Current Assignee: Parker Filtration & Separation B.V.
• Original Assignee: Parker Filtration & Separation B.V.
• Inventors: Leenders, Paulus Hendrikus Maria, Van Oers, Jacobus Petrus Cornelis Maria, Ault, Brian Andrew, Roks, Martinus Franciscus Maria, Rathfelder, Robert William
• Application Number:
  US12/440,515
• Publication Number:
  US 20100021360A1
• Time in Patent Office: Days
• US Class Current: 423/219
• CPC Class Codes: B01D 2255/2073 Manganese
• CPC Class Codes: B01D 2255/9205 Porosity
• CPC Class Codes: B01D 53/8675 Ozone
• CPC Class Codes: B01J 23/34 Manganese
• CPC Class Codes: B01J 23/50 Silver
• CPC Class Codes: B01J 23/688 with manganese, technetium or rhenium
• CPC Class Codes: B01J 35/04 Foraminous structures, sieves, grids, honeycombs
• CPC Class Codes: B01J 35/06 Fabrics or filaments
• CPC Class Codes: B01J 35/065 Membranes
• CPC Class Codes: B01J 35/56 Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional monoliths
• CPC Class Codes: B01J 35/58 Fabrics or filaments
• CPC Class Codes: B01J 35/59 Membranes
• CPC Class Codes: B64D 13/00 Arrangements or adaptations of air-treatment apparatus for aircraft crew or passengers, or freight space , or structural parts of the aircraft treatment rooms with artificial climate for medical purposes A61G10/02; respiratory apparatus in general A62B; for vehicles in general B60H
• CPC Class Codes: B64D 2013/0677 comprising on board oxygen generator systems
• CPC Class Codes: B64D 2013/0685 with ozone control
• CPC Class Codes: Y02T 50/40 Weight reduction
• CPC Class Codes: Y02T 50/50 On board measures aiming to increase energy efficiency

Abstract

A low-temperature ozone converter contains an ozone catalyst composition supported on a honeycomb structure in cabin conditioning and/or inerting fuel tanks. The ozone converter preferably contains an ozone cracking catalyst including active manganese oxide, carried on a fiber aggregate, preferably a ceramic fiber aggregate. A gas separation unit (OBIGGS) including such an ozone converter and a hollow fiber membrane, suitable for inerting the fuel tank of an aircraft are also disclosed.

Claims

1-10. -10. (canceled)

11. Use of a low-temperature ozone converter containing an ozone catalyst composition supported on a honeycomb structure in cabin conditioning and/or inerting fuel tanks,

low-temperature meaning an ozone conversion efficiency of more than 95% at a temperature lower than 120°

C.,

wherein said ozone converter contains an ozone cracking catalyst comprising active manganese oxide, wherein said honeycomb structure comprises a fiber aggregate such as to provide more than 0.02 cm³/g of micropores 10-200 nm in diameter, wherein said fiber aggregate is being composed of walls having vacant pores larger than 500 nm in diameter and in an amount of more than 0.1 cm³/g.

12. An Environmental Control System (ECS) for aircraft cabin air management, wherein air having a temperature below 120°

C. is passed through an ozone converter containing an ozone catalyst composition supported on a honeycomb structure,

wherein said ozone converter contains an ozone cracking catalyst comprising active manganese oxide, wherein said honeycomb structure comprises a fiber aggregate such as to provide more than 0.02 cm³/g of micropores 10-200 nm in diameter, wherein said fiber aggregate is being composed of walls having vacant pores larger than 500 nm in diameter and in an amount of more than 0.1 cm³/g.

18. The ECS according to claim 12, wherein said active manganese oxide is amorphous.

13. An Onboard Inert Gas Generating System (OBIGGS) for inerting fuel tanks, wherein air having a temperature below 120°

C. is passed through an ozone converter containing an ozone catalyst composition supported on a honeycomb structure,

wherein said ozone converter contains an ozone cracking catalyst comprising active manganese oxide, wherein said honeycomb structure comprises a fiber aggregate such as to provide more than 0.02 cm³/g of micropores 10-200 nm in diameter, wherein said fiber aggregate is being composed of walls having vacant pores larger than 500 nm in diameter and in an amount of more than 0.1 cm³/g,

and wherein the ozone-treated air is passed through a hollow fiber membrane, for removing at least a part of the oxygen present in the ozone-treated air.

14. The OBIGGS according to claim 13, wherein said ozone converter is immediately succeeded by said hollow fiber membrane.

15. The OBIGGS according to claim 14, wherein said air is cabin air.

16. A gas separation unit for generating inert gas on a vehicle having a fuel tank, wherein said gas separation unit comprises an ozone converter containing an ozone catalyst composition on a honeycomb support, and a hollow fiber membrane suitable for selective removal of oxygen located downstream from said ozone converter, and wherein said gas separation unit has no cooler,

wherein said ozone converter contains an ozone cracking catalyst comprising active manganese oxide, wherein said honeycomb structure comprises a fiber aggregate such as to provide more than 0.02 cm³/g of micropores 10-200 nm in diameter, wherein said fiber aggregate is being composed of walls having vacant pores larger than 500 nm in diameter and in an amount of more than 0.1 cm³/g.

17. The gas separation unit according to claim 16, wherein said hollow fiber membrane is formed from poly(2,6-dimethyl-p-phenylene oxide) having a molecular weight of 10⁵-10⁶, and wherein the top layer of said membrane has a thickness of less than 100 nm.

19. A method for inerting a fuel tank of a vehicle, wherein said method involves providing air at a temperature in the range of 20-120°

C. through a gas separation unit according to claim 16, to obtain a nitrogen-enriched airstream and an oxygen-enriched airstream, whereafter said nitrogen-enriched air is provided to the fuel tank.

20. A low-temperature ozone converter containing an ozone catalyst composition in cabin conditioning and/or inerting fuel tanks, having an ozone conversion efficiency of more than 95% at a temperature lower than 120°

C., wherein said ozone converter contains an ozone cracking catalyst comprising active manganese oxide.