Membrane catalytic heater
A portable catalytic combustion heater, wherein fuel vapor ( 11 ) and air ( 10 ) are supplied to a catalyst ( 6 ) which promotes the flameless combustion of fuel and releases that. The fuel is supplied as a liquid, passes through a selectively permeable membrane ( 8 ) such that fuel vapor exits the membrane and is fed to the catalyst ( 6 ). Additional features include porous supports and means of enhancing and diminishing the catalytic rate of combustion and controlling the heat output.
1. A heat-generating device comprising
a. a fuel source;
b. a fuel delivery connected to the fuel source;
c. a catalyst dispersed over a porous substrate; wherein the catalyst is in diffusive contact with an oxidizing gas;
d. a first molecular selectively permeable membrane for selective molecular delivery of fuel by diffusion from the fuel source to the catalyst, wherein the first molecular selectively permeable membrane only allows gasses and fuel vapors to diffuse through the membrane to the catalyst;
e. one or more heat exchangers configured for transferring heat from the catalytic reaction site to the fuel or the oxidizing gas or both;
f. a second selectively permeable membrane, wherein the second selectively permeable membrane is fuel and oxidizer permeable and regulates delivery of oxidizing gas to the catalyst, wherein the oxidizing gas moves to the catalyst through the second selectively permeable membrane by diffusion; and
g. wherein the device further comprising an upper temperature limit setting on a thermal output caused by boiling the fuel.
2. The device of claim 1 , wherein by containing the fuel behind the first molecular selectively permeable membrane and using only diffusion to deliver the fuel, the rate of delivery of fuel vapor to the catalyst is dependent upon the concentration of liquid in contact with the fuel membrane rather than the fuel vapor pressure.
3. The device of claim 1 , wherein the selective permeability of the first selectively permeable membrane to fuels over water produced by combustion at the catalyst keeps the liquid fuel reservoir from being contaminated with the water and maintains the fuel concentration and a steady rate of fuel delivery.
4. The device of claim 1 , further comprising an additional fuel and oxidizer permeable protective coating that protects the combustion catalyst from contamination and retains fuel at the catalyst.
5. The device of claim 1 , wherein the vaporized fuel can be condensed in the one or more heat exchanger and deliver the thermal output of the heater efficiently.
6. The device of claim 1 , wherein fuel vaporization and departure from the first selectively permeable membrane to catalyst reaction area act as a thermostat and thereby creates an upper temperature limit mechanism.
7. The device of claim 1 , wherein a maximum pressure of the fuel reservoir is selected to set the boiling point of the fuel and therefore set the maximum temperature of the heater.
8. The device of claim 1 , wherein fuel boiling in combination with back diffusion of carbon dioxide and nitrogen through the first selectively permeable membrane can also be used to keep the fuel homogeneous and self-purging.
9. The device of claim 1 , wherein the catalytic heater is insensitive to orientation.
10. The device of claim 1 , wherein a steady delivery of liquid fuel or gas fuel is needed to maintain contact with the selectively permeable membrane.
11. The device of claim 1 , wherein bubbles and gas pockets in the fuel will not significantly affect the diffusion of fuel through the selectively permeable membrane as long as the surface of the membrane is wetted by fuel.
12. The device of claim 1 , wherein wet coating or wicking material could be used to spread liquid fuel uniformly over the surface of the selectively permeable membranes.
13. The device of claim 1 , wherein increasing the hydraulic pressure will not significantly increase the concentration of a liquid fuel against the first selectively permeable membrane.
14. The device of claim 1 , wherein the diffusion rate of fuel will not be changed if the system is inverted causing a low or high hydraulic pressure on the first selectively permeable membrane.
15. The device of claim 1 , wherein the first selectively permeable membrane is a silicone rubber membrane.
16. The device of claim 1 , wherein the second selectively permeable membrane comprises silicone rubber or a solid polymer electrolyte.
17. The device of claim 1 , wherein catalyst layer is over-coated with a thin protective coating, such as a solid polymer electrolyte or silicone rubber.
18. The device of claim 1 , wherein second selectively permeable membrane has a high solubility and affinity for the fuel and water so it increases the concentration of the fuel on the catalyst.
19. The device of claim 1 , wherein the second selectively permeable membrane also has limited permeability to fuel and oxygen, which limits the rates of catalytic combustion on the catalyst surface and keeps the catalyst from going into high temperature or flame combustion.
20. The device of claim 1 , wherein the second selectively permeable membrane has a permeability that changes with temperature to act as a fuel and oxidizer moderator.
21. The device of claim 1 , wherein the selective permeability of the first selectively permeable membrane prevents water from diluting the fuel and reducing the fuel delivery rate.
22. The device of claim 1 , wherein the selective diffusion through membranes is dominated by the concentration gradient across them and its permeability at particular temperatures.
23. The device of claim 1 , wherein the fuel delivery is independent of the vapor pressure of the fuel when the first selectively permeable membrane is immersed in fuel.
24. The device of claim 1 , further comprising an oxygen membrane comprising a porous material or mechanical filter mechanism for diffusion of oxygen from a source of oxygen to the surface of the catalyst to react with the fuel on the catalyst.
25. The device of claim 1 , wherein the oxygen membrane can also be a material or mechanical mechanism that increases or decreases its rate of oxygen diffusion depending on temperature, thus limiting the catalytic combustion.
26. The device of claim 1 , wherein carbon dioxide and other gasses diffuse into the first permeable membrane and vent and circulate through the fuel with the fuel boiling.
27. The device of claim 1 , wherein gravity is used to separate fuel, gases, and vapor and circulate fuel.
28. The device of claim 1 , further comprising stoma for thermally regulating the air or oxidant to the reaction area.
29. The device of claim 1 , wherein the fuel is a liquid fuel, and wherein the fuel is removed from a catalytic reaction area by boiling.
30. The device of claim 1 , further comprising valves, flow restrictions, or pressure reliefs for regulating a boiling temperature of the fuel.
31. The device of claim 1 , further comprising regulation of fuel delivery rate with self-pressurization of the fuel.
32. The device of claim 1 , wherein the first selectively permeable membrane is selectively permeable to gases and fuel boiling in the device and wherein the membrane uses the selective permeability to aspirate, circulate, or prevent motion of the fuel.
33. The device of claim 1 , wherein the selectively permeable membranes change diffusion rates with temperature changes for regulating temperature of the device.