Reactive component reduction system and methods for the use thereof

• US 7,896,292 B2
• Filed: 01/16/2008
• Issued: 03/01/2011
• Est. Priority Date: 01/16/2008
• Status: Active Grant

• Current Assignee: Phyre Technologies, Inc. (Parker-Hannifin Corporation)
• Original Assignee: Phyre Technologies, Inc. (Parker-Hannifin Corporation)
• Inventors: Koenig, Donald, Jung, Wesley, Robertson, Stuart, Limaye, Santosh Y.
• Primary Examiner(s): Sines; Brian J
• Application Number:
  US12/015,452
• Publication Number:
  US 20090227034A1
• Time in Patent Office: 1,140 Days
• Field of Search: 422/204, 422/129, 422/101, 244/135, 423/210, 423/219, 204/157.3
• US Class Current: 244/135.00R
• CPC Class Codes: B01D 2255/10 Noble metals or compounds thereof
• CPC Class Codes: B01D 2255/1026 Ruthenium
• CPC Class Codes: B01D 2255/206 Rare earth metals
• CPC Class Codes: B01D 2255/2073 Manganese
• CPC Class Codes: B01D 2257/104 Oxygen
• CPC Class Codes: B01D 2257/702 Hydrocarbons
• CPC Class Codes: B01D 53/30 Controlling by gas-analysis apparatus regulating non electrical variables in general G05D
• CPC Class Codes: B01D 53/864 Removing carbon monoxide or hydrocarbons
• CPC Class Codes: B01D 53/8696 Controlling the catalytic process
• CPC Class Codes: B64D 37/32 Safety measures not otherwise provided for, e.g. preventing explosive conditions extinguishing or preventing fires in aircraft A62C
• CPC Class Codes: Y10T 436/115831 Condition or time responsive

Abstract

In accordance with the present invention, there are provided simplified systems and methods for catalytically deactivating, removing, or reducing the levels of reactive component(s) from the vapor phase of fuel storage tanks. The simple apparatus described herein can be utilized to replace complex systems on the market. Simply stated, in one embodiment of the invention, the vapor phase from the fuel tank is passed over a catalytic bed operated at appropriate temperatures to allow the reaction between free oxygen and the fuel vapor by oxidation of the fuel vapor, thus deactivating reactive component(s) in the gas phase.

Claims

1. A system for reducing the concentration of one or more reactive component(s) in the vapor space of a container having combustible material therein, thereby reducing the concentration of reactive component(s) in said vapor space below the concentration at which auto-ignition may occur, said system comprising:

said container,

a fluid treating zone comprising;

at least one inlet,

at least one outlet, and

a reaction zone, wherein said reaction zone provides conditions suitable to deactivate said one or more reactive component(s) when contacted therewith,

at least one sensor for

(a) analysis of the concentration of reactive component(s) in the vapor phase,

(b) analysis of the concentration of combustible material in the vapor phase, and/or

(c) analysis of the flow rate of the vapor phase, and

a flow control element,

wherein;

the vapor space of said container is in fluid communication with said sensor;

the sensor is in fluid communication with said flow control element;

the flow control element is capable of controlling the flow rate of the vapor phase through said system, and/or directing all or a portion of the fluid to the inlet of said fluid treating zone or all or a portion of the fluid back into the container; and

the outlet of said fluid treating zone is in fluid communication with the container.

2. The system of claim 1 wherein said fluid treating zone comprises a catalyst which is reactive with said one or more reactive component(s) when contacted therewith under suitable conditions.

3. The system of claim 2 wherein said catalyst is contained within a vessel.

4. The system of claim 3 wherein the vessel has an inlet end and an outlet end, and the catalyst content varies from the inlet end to the outlet end.

5. The system of claim 4 wherein the catalyst content varies non-linearly from the inlet end to the outlet end.

6. The system of claim 5 wherein the catalyst content increases from the inlet end to the outlet end.

7. The system of claim 5 wherein the catalyst content decreases from the inlet end to the outlet end.

8. The system of claim 2 wherein said catalyst is an optionally supported catalyst.

9. The system of claim 8 wherein said catalyst is selected from the group consisting of noble metals, precious metals, transition metal oxides, rare earth oxides, and mixtures of any two or more thereof.

10. The system of claim 2 wherein said suitable conditions for contacting said catalyst with said one or more reactive component(s) comprise a temperature in the range of about 25°

C. up to about 1200°

C.

11. The system of claim 2 wherein the reaction zone is associated with a temperature modulator.

12. The system of claim 11 wherein said temperature modulator is a heat exchanger.

13. The system of claim 12 wherein the heat exchanger is integrated with the catalyst containing vessel.

14. The system of claim 12 wherein said heat exchanger comprises a heat exchange medium.

15. The system of claim 14 wherein the heat exchange medium is selected from external air or a liquid.

16. The system of claim 12 wherein said heat exchanger is a heat pump.

17. The system of claim 11 wherein said temperature modulator is an evaporative cooler.

18. The system of claim 1 wherein said reaction zone comprises a source of microwave energy sufficient to deactivate said one or more reactive component(s) when contacted therewith.

19. The system of claim 1 wherein said reaction zone comprises a source of plasma energy sufficient to deactivate said one or more reactive component(s) when contacted therewith.

20. The system of claim 1 wherein at least one sensor is an oxygen sensor.

21. The system of claim 1 wherein at least one sensor is a chemical sensor.

22. The system of claim 1, wherein said flow control element controls, based on the level of reactive component(s) in said vapor phase, the flow rate of the vapor phase through said fluid treating zone.

23. The system of claim 1, wherein said flow control element controls, based on the level of reactive component(s) in said vapor phase, whether all or a portion of the vapor phase is directed through said fluid treating zone or all or a portion of the vapor phase is returned to said container without passing through the fluid treating zone.

24. The system of claim 1 wherein said fluid treating zone is external to said container.

25. The system of claim 24, further comprising one or more heat exchangers upstream and/or downstream of said fluid treating zone.

26. The system of claim 1 wherein said fluid treating zone is within said container.

27. The system of claim 1 further comprising one or more elements suitable for equilibrating pressure within the system upon exposure to sub- or super-atmospheric conditions.

28. The system of claim 27, wherein said one or more elements suitable for equilibrating pressure within the system comprises a source of make-up fluid to equilibrate pressure within the system upon exposure to sub-atmospheric conditions.

29. The system of claim 27, wherein said one or more elements suitable for equilibrating pressure within the system comprises a vent to equilibrate pressure within the system upon exposure to super-atmospheric conditions.

30. The system of claim 27, wherein said container comprises one or more flexible members, thereby providing one or more elements suitable for equilibrating pressure within the system.

31. The system of claim 1 wherein said reactive component(s) is oxygen.

32. The system of claim 1 wherein said vapor phase further comprises fuel vapor.

33. The system of claim 1 further comprising an independent source of fuel to facilitate deactivation of the reactive components within the reaction zone.

34. The system of claim 1 further comprising an independent source of makeup air in fluid communication with said container and/or said sensor.

35. The system of claim 1 further comprising an inlet for the introduction of fuel into said container.

36. The system of claim 1 wherein said container is provided with an outlet for removal of fuel therefrom and/or vapor phase from the vapor space thereof, and an inlet for introduction of vapor thereto.

37. The system of claim 36 further comprising a flame arrestor.

38. The system of claim 37 wherein said flame arrestor is positioned in the inlet and/or outlet of the container.

39. The system of claim 1 further comprising one or more sensors after the fluid treating zone.

40. The system of claim 39 wherein at least one sensor is an oxygen sensor.

41. The system of claim 40 wherein said oxygen sensor is in fluid communication with the outlet of the fluid treating zone.

42. The system of claim 41 further comprising a flow control element which directs all or a portion of the vapor phase back to the container, or back through said fluid treating zone in response to the oxygen content thereof.

43. The system of claim 39 wherein at least one sensor is a chemical sensor.

44. The system of claim 1 further comprising an element for the removal of water from the vapor phase wherein said element is positioned downstream from the fluid treating zone.