Catalytic decomposition reactors
A catalyst bed includes a structure defining a plurality of channels configured to receive flow of fluid to be chemically catalyzed. The plurality of channels are oriented at least partially non-parallel to an overall flow direction of the flow from inputs of the plurality of channels to outputs of the plurality of channels. A catalyst is exposed at an exterior of the structure.
1. A catalyzing reactor system comprising:
an inlet valve configured to fluidically couple a tank for storing a decomposable fluid to a chamber;
an injector arranged to receive the decomposable fluid from the inlet valve and inject a spray of the decomposable fluid through the chamber;
a heating element disposed in the chamber and arranged to heat the spray of the decomposable fluid;
a catalyst bed comprising a catalyst, the catalyst bed arranged such that heated spray of the decomposable fluid contacts the catalyst and the catalyst promotes decomposition of the heated spray of the decomposable fluid into two or more gaseous decomposition products;
a solid fuel grain mass defining a port;
a nozzle arranged to direct the two or more gaseous decomposition products into the port; and
a flow path that fluidically couples the tank to the port and that bypasses the catalyst bed.
2. The catalyzing reactor system of claim 1 , comprising a distribution plate disposed between the heating element and the catalyst bed, the distribution plate configured to promote dispersion of the heated spray of the decomposable fluid before the heated spray of the decomposable fluid interacts with the catalyst bed.
3. The catalyzing reactor system of claim 1 , comprising a heat-resistant ceramic liner disposed on inner walls of the chamber.
4. The catalyzing reactor system of claim 1 , wherein a heating power of the heating element is such that interaction between the heated spray of the decomposable fluid and the catalyst bed heats the catalyst bed to at least 300° C.
5. The catalyzing reactor system of claim 1 , comprising a control system configured to perform operations comprising:
monitoring a temperature of the catalyst bed during thermal decomposition of the heated spray of the decomposable fluid; and
in response to determining that the temperature of the catalyst bed satisfies a condition, at least one of
adjusting an intensity of the heating element, or
adjusting a flow rate of the decomposable fluid.
6. The catalyzing reactor system of claim 1 , wherein the catalyst bed comprises a plurality of ceramic pellets coated with the catalyst.
7. The catalyzing reactor system of claim 1 , wherein the catalyst bed comprises a structure coated with the catalyst, the structure defining a plurality of channels through the structure.
8. The catalyzing reactor system of claim 1 , wherein the catalyst bed comprises:
a structure having a three-dimensional lattice structure, the three-dimensional lattice structure including gaps both axially along an overall flow direction of the heated spray of the decomposable fluid and radially transverse to the overall flow direction; and
the catalyst coating the structure.
9. The catalyzing reactor system of claim 1 , wherein the catalyst bed comprises:
a structure defining a plurality of channels that twist circumferentially with respect to an overall flow direction of the heated spray of the decomposable fluid; and
the catalyst coating the structure.
10. The catalyzing reactor system of claim 1 , wherein the catalyst bed comprises a structure defining a plurality of channels configured to receive flow of the spray of the decomposable fluid,
wherein the plurality of channels are oriented at least partially non-parallel to an overall flow direction of the flow from inputs of the plurality of channels to outputs of the plurality of channels, and
wherein the catalyst is exposed at an exterior of the structure.
11. The catalyzing reactor system of claim 1 , wherein the catalyst bed comprises an additively-manufactured structure.
12. The catalyzing reactor system of claim 1 , wherein the catalyst comprises a reactive metal.
13. The catalyzing reactor system of claim 1 , wherein the injector and the heating element are configured such that the heated spray of the decomposable fluid is gaseous when the heated spray of the decomposable fluid interacts with the catalyst bed.
14. The catalyzing reactor system of claim 1 , wherein a first gaseous decomposition product of the two or more gaseous decomposition products comprises oxygen gas.
15. The catalyzing reactor system of claim 1 , wherein the solid fuel grain mass comprises a plurality of concentric ring-shaped layers of fuel grain material surrounding the port.
16. The catalyzing reactor system of claim 1 , wherein the nozzle is configured to produce thrust by ejection of at least one of the two or more gaseous decomposition products.
17. The catalyzing reactor system of claim 1 , comprising:
a coupling component configured to provide at least one of pressure or heat to a pressure system component using at least one of the two or more gaseous decomposition products.
18. The catalyzing reactor system of claim 17 , wherein the coupling component comprises a heat exchanger that is arranged to thermally couple the pressure system component to the at least one of the two or more gaseous decomposition products.
19. The catalyzing reactor system of claim 17 , wherein the coupling component comprises a second injector arranged to inject the at least one of the two or more gaseous decomposition products into the pressure system component.
20. The catalyzing reactor system of claim 19 , comprising a gas separator configured to separate a first gaseous decomposition product of the two or more gaseous decomposition products from a second gaseous decomposition product of the two or more gaseous decomposition products and to direct the first gaseous decomposition product to the second injector.
21. The catalyzing reactor system of claim 20 , wherein the first gaseous decomposition product comprises oxygen.
22. The catalyzing reactor system of claim 17 , wherein the pressure system component comprises the tank, a valve, a fluid line, or a pressure regulator.
23. The catalyzing reactor system of claim 17 , wherein the catalyst bed is a secondary catalyst bed, wherein an output of the secondary catalyst bed directs at least one of the two or more gaseous decomposition products into the coupling component, and wherein the catalyzing reactor system comprises a primary catalyst bed having a second output that directs at least one further gaseous decomposition product from the primary catalyst bed into another component distinct from the coupling component.
24. The catalyzing reactor system of claim 23 , wherein the component into which the at least one further gaseous decomposition product from the primary catalyst bed is directed comprises the solid fuel grain mass, and
wherein the at least one further gaseous decomposition product comprises oxygen gas.
25. The catalyzing reactor system of claim 1 , wherein the decomposable fluid comprises nitrous oxide.
26. The catalyzing reactor system of claim 1 , wherein the heating element comprises a metal catalyst arranged to contact the spray of the decomposable fluid.
27. The catalyzing reactor system of claim 1 , comprising a turbine arranged to receive at least one of the two or more gaseous decomposition products.
28. The catalyzing reactor system of claim 1 , wherein the heating element comprises a resistive heater, a cartridge heater, or a glow plug.
29. The catalyzing reactor system of claim 1 , wherein the heating element comprises a catalytic layer.
30. The catalyzing reactor system of claim 1 , wherein the heating element is free of catalytic material.
31. The catalyzing reactor system of claim 1 , wherein the chamber in which the heating element is disposed is separate from a chamber in which the catalyst bed is disposed.
32. A catalyzing reactor system comprising:
an inlet valve configured to fluidically couple a tank for storing a decomposable fluid to a reaction chamber;
a catalyst bed disposed in the reaction chamber and comprising a catalyst, the catalyst bed arranged such that spray of the decomposable fluid from the tank contacts the catalyst and the catalyst promotes decomposition of the spray of the decomposable fluid into two or more gaseous decomposition products;
a tank coupling component configured to provide at least one of pressure or heat to bulk fluid in the tank using at least one of the two or more gaseous decomposition products;
a solid fuel grain mass defining a port;
a nozzle arranged to direct the two or more gaseous decomposition products into the port; and
a flow path that fluidically couples the tank to the port and that bypasses the catalyst bed.
33. The catalyzing reactor system of claim 32 , comprising a distribution plate configured to promote dispersion of the spray of the decomposable fluid before the spray of the decomposable fluid interacts with the catalyst bed.
34. The catalyzing reactor system of claim 32 , wherein the catalyst bed comprises:
a structure having a three-dimensional lattice structure, the three-dimensional lattice structure including gaps both axially along an overall flow direction of the spray of the decomposable fluid and radially transverse to the overall flow direction; and
the catalyst coating the structure.
35. The catalyzing reactor system of claim 32 , wherein the catalyst bed comprises:
a structure defining a plurality of channels that twist circumferentially with respect to an overall flow direction of the spray of the decomposable fluid; and
the catalyst coating the structure.
36. The catalyzing reactor system of claim 32 , wherein the catalyst bed comprises a structure defining a plurality of channels configured to receive flow of the spray of the decomposable fluid,
wherein the plurality of channels are oriented at least partially non-parallel to an overall flow direction of the flow from inputs of the plurality of channels to outputs of the plurality of channels, and
wherein the catalyst is exposed at an exterior of the structure.
37. The catalyzing reactor system of claim 32 , wherein the catalyst bed comprises an additively-manufactured structure.
38. The catalyzing reactor system of claim 32 , wherein the tank coupling component comprises a heat exchanger configured to provide heat to the bulk fluid in the tank.
39. The catalyzing reactor system of claim 32 , wherein the tank coupling component comprises an injector arranged to inject the at least one of the two or more gaseous decomposition products into the tank.
40. The catalyzing reactor system of claim 39 , comprising a gas separator configured to separate a first gaseous decomposition product of the two or more gaseous decomposition products from a second gaseous decomposition product of the two or more gaseous decomposition products and to direct the first gaseous decomposition product to the injector.
41. The catalyzing reactor system of claim 40 , wherein the first gaseous decomposition product comprises oxygen.
42. The catalyzing reactor system of claim 32 , wherein the catalyst bed is a secondary catalyst bed, wherein an output of the secondary catalyst bed directs at least one of the two or more gaseous decomposition products into the tank coupling component, and wherein the catalyzing reactor system comprises a primary catalyst bed having a second output that directs at least one further gaseous decomposition product from the primary catalyst bed into another component distinct from the tank coupling component.
43. The catalyzing reactor system of claim 42 , wherein the at least one further gaseous decomposition product comprises oxygen gas.
44. The catalyzing reactor system of claim 32 , wherein the decomposable fluid comprises nitrous oxide.
45. A catalyzing reactor system comprising:
an inlet valve configured to fluidically couple a tank for storing a decomposable fluid to a chamber;
an injector arranged to receive the decomposable fluid from the inlet valve and inject a spray of the decomposable fluid through the chamber;
a heating element disposed in the chamber and arranged to heat the spray of the decomposable fluid;
a catalyst bed comprising a catalyst, the catalyst bed arranged such that heated spray of the decomposable fluid contacts the catalyst and the catalyst promotes decomposition of the heated spray of the decomposable fluid into two or more gaseous decomposition products;
a coupling component configured to provide at least one of pressure or heat to a pressure system component using at least one of the two or more gaseous decomposition products, wherein the coupling component comprises a second injector arranged to inject the at least one of the two or more gaseous decomposition products into the pressure system component; and
a gas separator configured to separate a first gaseous decomposition product of the two or more gaseous decomposition products from a second gaseous decomposition product of the two or more gaseous decomposition products and to direct the first gaseous decomposition product to the second injector.
46. The catalyzing reactor system of claim 45 , wherein the first gaseous decomposition product comprises oxygen.
47. The catalyzing reactor system of claim 45 , wherein the pressure system component comprises the tank, a valve, a fluid line, or a pressure regulator.
48. The catalyzing reactor system of claim 45 , wherein the catalyst bed is a secondary catalyst bed, wherein an output of the secondary catalyst bed directs at least one of the two or more gaseous decomposition products into the coupling component, and wherein the catalyzing reactor system comprises a primary catalyst bed having a second output that directs at least one further gaseous decomposition product from the primary catalyst bed into another component distinct from the coupling component.
49. The catalyzing reactor system of claim 48 , wherein the component into which the at least one further gaseous decomposition product from the primary catalyst bed is directed comprises a solid fuel grain mass configured to undergo combustion, and
wherein the at least one further gaseous decomposition product comprises oxygen gas.
50. A catalyzing reactor system comprising:
an inlet valve configured to fluidically couple a tank for storing a decomposable fluid to a chamber;
an injector arranged to receive the decomposable fluid from the inlet valve and inject a spray of the decomposable fluid through the chamber;
a heating element disposed in the chamber and arranged to heat the spray of the decomposable fluid;
a secondary catalyst bed comprising a catalyst, the secondary catalyst bed arranged such that heated spray of the decomposable fluid contacts the catalyst and the catalyst promotes decomposition of the heated spray of the decomposable fluid into two or more gaseous decomposition products;
a coupling component configured to provide at least one of pressure or heat to a pressure system component using at least one of the two or more gaseous decomposition products,
wherein an output of the secondary catalyst bed directs the at least one of the two or more gaseous decomposition products into the coupling component; and
a primary catalyst bed having a second output that directs at least one further gaseous decomposition product from the primary catalyst bed into another component distinct from the coupling component.
51. The catalyzing reactor system of claim 50 , wherein the coupling component comprises a heat exchanger that is arranged to thermally couple the pressure system component to the at least one of the two or more gaseous decomposition products.
52. The catalyzing reactor system of claim 50 , wherein the coupling component comprises a second injector arranged to inject the at least one of the two or more gaseous decomposition products into the pressure system component.
53. The catalyzing reactor system of claim 52 , comprising a gas separator configured to separate a first gaseous decomposition product of the two or more gaseous decomposition products from a second gaseous decomposition product of the two or more gaseous decomposition products and to direct the first gaseous decomposition product to the second injector.
54. The catalyzing reactor system of claim 53 , wherein the first gaseous decomposition product comprises oxygen.
55. The catalyzing reactor system of claim 50 , wherein the pressure system component comprises the tank, a valve, a fluid line, or a pressure regulator.
56. The catalyzing reactor system of claim 50 , wherein the component into which the at least one further gaseous decomposition product from the primary catalyst bed is directed comprises a solid fuel grain mass configured to undergo combustion, and
wherein the at least one further gaseous decomposition product comprises oxygen gas.