Transient N2O decomposition process and reactor
AssigneeReaction Systems, LLC
InventorsBradley Dean Hitch, Jeffrey Robert Engel, David Thomas Wickham
Life of this patent
Estimating the term…
Loading patent…
AssigneeReaction Systems, LLC
InventorsBradley Dean Hitch, Jeffrey Robert Engel, David Thomas Wickham
Estimating the term…
A N2O decomposition reactor and a method of its use to produce an effluent suitable for use in an ignition device or in the main fuel injection system in high speed aircraft. N2O decomposition is an exothermic reaction and produces a high temperature product containing high concentrations of O2. Combination of fuel with this effluent ignites quickly and is an effective ignition source for the aircraft combustor. Reactor performance is adjusted to meet the conditions required for a selected application by changing the relative concentrations of CO2 and N2O, modifying the reactor length, and varying the quantity of catalyst in the reactor. For use in a pilot ignition device, the desired effluent temperature is between 500° C. and 1200° C. in order to ignite and combust the fuel within the design residence time, between 0.5 and 10 ms. For application as a barbotage gas generator in a fuel injection system, the temperature of the effluent can range from 300° C. up to 800° C. and it is desirable that the effluent temperature remains within this range for periods of up to two minutes.
A catalytic N2O decomposition process to generate an effluent containing oxygen which comprises:
A catalytic N2O decomposition reactor for generating a heated effluent comprising oxygen, which comprises an inner and an outer annulus in flow communication and a reactor exit fitting in the inner annulus, wherein a N2O feed mixture introduced into the outer annulus passes into the inner annulus and the heated effluent leaves the reactor through the exit fitting in the inner annulus, wherein the inner annulus comprises a N2O decomposition catalyst, and wherein the N2O feed mixture is preheated to a selected temperature in the outer annulus prior to contacting the N2O decomposition catalyst in the inner annulus, wherein:
Dependencies are inferred from the claim text.