Startup of a catalytic inerting system with recycle

Patent metadata

Field	Value
Publication number	US-10967985-B2
Application number	US-201815921169-A
Country	US
Kind code	B2
Filing date	Mar 14, 2018
Priority date	Mar 14, 2018
Publication date	Apr 6, 2021
Grant date	Apr 6, 2021

Abstract

A method for startup of a catalytic oxidation unit includes flowing air from an air source into the catalytic oxidation unit, recycling air from an outlet of the catalytic oxidation unit to an inlet of the catalytic oxidation unit through a recycle duct, and flowing a fuel from a fuel source into the catalytic oxidation to cause a catalytic reaction.

First claim

The invention claimed is:

1. A method for startup of a catalytic oxidation unit for an aircraft gas inerting system, the method comprising:
continuously flowing air from an air source into the catalytic oxidation unit;
recycling at least a portion of the air from an outlet of the catalytic oxidation unit to an inlet of the catalytic oxidation unit through a recycle duct;
flowing a fuel from a fuel tank into the catalytic oxidation unit, wherein flowing the fuel initiates a catalytic reaction and produces an exhaust gas comprising a chemical product of catalytic oxidation, and wherein the exhaust gas exits the catalytic oxidation unit through the outlet; and
directing a portion of the exhaust gas to an ullage space of the fuel tank;
wherein the air is recycled to establish an air flow through the catalytic oxidation unit and wherein flowing fuel into the catalytic oxidation unit occurs after the air flow has been established.

2. The method of claim 1 , wherein a ratio of the air to the fuel entering the catalytic oxidation unit is at relative stoichiometric ratio of oxygen to fuel between 1 and 7.

3. The method of claim 1 , wherein a ratio of the air to the fuel entering the catalytic oxidation unit is at relative stoichiometric ratio of oxygen to fuel between 7 and 21.

4. The method of claim 3 and further comprising reducing the flow of the fuel such that a ratio of the air to the fuel entering the catalytic oxidation unit is at a relative stoichiometric ratio of oxygen to fuel between 1 and 7.

5. The method of claim 1 , wherein the air and fuel flow into a catalytic oxidation unit as a gaseous mixture at a relative stoichiometric ratio of oxygen to fuel between 7 and 21 and wherein the air is recycled as a portion of the exhaust gas produced by the catalytic reaction.

6. The method of claim 5 and further comprising:
reducing the ratio of the air to the fuel entering the catalytic oxidation unit to a relative stoichiometric ratio of oxygen to fuel between 1 and 7.

7. The method of claim 1 and further comprising:
injecting the fuel into the recycle duct, wherein the fuel is a liquid hydrocarbon fuel and wherein injecting the fuel comprises atomizing the fuel for mixture with the air.

8. The method of claim 1 and further comprising:
mixing the fuel with the air upstream of the catalytic oxidation unit.

9. The method of claim 1 , wherein the exhaust gas has a temperature less than 230 degrees Celsius at the outlet to cool the catalytic oxidation unit.

10. The method of claim 1 , wherein the at least portion of air is recycled by diverting a portion of the exhaust gas through the recycle duct to the inlet of the catalytic oxidation unit.

11. The method of claim 10 , wherein at least 95% of the exhaust gas is diverted through the recycle duct to the inlet of the catalytic oxidation unit.

12. A method for startup of a catalytic oxidation unit for an aircraft gas inerting system, the method comprising:
flowing a gaseous mixture of air and a fuel into a catalytic oxidation unit, wherein a ratio of the air to the fuel entering the catalytic oxidation unit is at a relative stoichiometric ratio of oxygen to fuel between 7 and 21;
initiating a catalytic reaction of the air and the fuel;
producing an exhaust gas comprising a chemical product of catalytic oxidation; and
recycling at least a portion of the exhaust gas from an outlet of the catalytic oxidation unit to an inlet of the catalytic oxidation unit through a recycle duct;
reducing the ratio of the air to the fuel entering the catalytic oxidation unit to a relative stoichiometric ratio of oxygen to fuel between 1 and 7; and
delivering at least a portion of the exhaust gas to an ullage of a fuel tank.

13. The method of claim 12 , wherein the exhaust gas has a temperature below 230 degrees Celsius at the outlet to cool catalytic oxidation unit.

14. The method of claim 12 , wherein a recycle ratio relative to a flow rate of the exhaust gas is equal to or greater than 20.

15. The method of claim 12 , wherein the fuel is an atomized liquid fuel.

16. An inert gas generating system comprising:
an adjustable supply of air;
a fuel tank providing an adjustable supply of liquid fuel;
a nozzle configured atomize the liquid fuel;
a catalytic oxidation unit arranged to receive the air and the liquid fuel, wherein the catalytic oxidation unit comprises:
an inlet for receiving the air and the liquid fuel; and
an outlet for delivering the air and the exhaust gas, wherein exhaust gas is a product of a reaction between the air and the liquid fuel;

a recycle duct fluidly connecting the inlet and the outlet of the catalytic oxidation unit;
an exhaust duct fluidly connecting the outlet of the catalytic oxidation unit to an ullage of the fuel tank; and
a controller configured to adjust at least one of the supply of fuel and the supply of air to the catalytic oxidation unit by way of one or more valves.

17. The system of claim 16 , wherein the controller is configured to recycle only air during a portion of a startup operation of the catalytic oxidation unit.

Assignees

• Hamilton Sundstrand Corp

Inventors

• Emerson Sean C
• Dardas Zissis A
• Hebert Robert R
• Murray Allen
• Surawski Eric
• Mcgee Randolph Carlton

Classifications

• B64D37/32 Primary

  Safety measures not otherwise provided for, e.g. preventing explosive conditions · CPC title

• B01D53/265

  by refrigeration (condensation) · CPC title