Patent Application
20120014850
This application claims priority to and the benefit of Korean Patent Application No. 10-2010-0069037, filed on Jul. 16, 2010, in the Korean Intellectual Property Office, the entire content of which is incorporated herein by reference.
1. Field
Aspects of embodiments according to the present invention relate to a combustor that provides heat to a reformer.
2. Description of the Related Art
The reforming reaction in a fuel cell is a reaction that produces hydrogen that is used as fuel in the fuel cell from hydrocarbon-based fossil fuel, and an apparatus that performs such a reaction is referred to as a fuel processor. In addition to a reformer that performs a reforming reaction, the fuel processor may further include a reactor for decreasing the concentration of carbon monoxide if necessary and a desulfurizer for removing sulfur contained in the fuel.
In the case of an external reforming method, a fuel reformer includes a heat source and a reforming reactor. The heat source supplies heat necessary for a reforming reaction in the reforming reactor, and the reforming reactor reforms fuel to generate gas containing abundant hydrogen. In this instance, the reforming reactor reforms the supplied fuel using a steam reforming (SR or STR) method, a partial oxidation (POX) method or an autothermal reforming (ATR) method obtained by combining the two methods. Among these methods, the SR method is a method of obtaining hydrogen through a reaction of hydrocarbon fuel and steam. Since high-concentration hydrogen is obtained using the SR method, the power of a fuel cell can be increased. However, since the SR method is an endothermic reaction, external heat is necessarily supplied from the reforming reactor.
A combustor is a device that generates heat and high-temperature gas by oxidizing fuel. The heat and high temperature gas generated from the combustor may be used as a heat source for preheating of fuel or water. The combustor may be implemented using a method of directly burning fuel injected into a combustion chamber through spark ignition, a method of burning fuel through an oxidation catalyst, or the like. The device that oxidizes fuel through an oxidation catalyst is referred to as a catalyst combustor.
Since such a combustor is operated under a high-temperature atmosphere, there have been proposed various methods for durability of providing various types of components in the interior of the combustor.
An aspect of one embodiment is directed toward a combustor for a reformer, which can increase the durability of a thermocouple for measuring the internal temperature of the combustor.
An aspect of one embodiment is directed toward a combustor for a reformer, which can perform separate fuel distribution and prevent flashback.
An aspect of one embodiment is directed toward a connection structure between a combustor and an evaporator, which can simplify the number of components and enhance the power of a reformer.
According to an embodiment of the present invention, there is provided a combustor for a reformer. The combustor includes an inner wall, a thermocouple, a fuel supply tube, a fuel distribution portion and a first oxidation catalytic layer.
The inner wall has a shape of a hollow cylinder with a first oxidation portion in a space therein. The thermocouple extends to the first oxidation portion by passing through a top portion of the first oxidation portion so as to measure a temperature of the first oxidation portion. The fuel supply tube has a shape of a hollow cylinder surrounding the thermocouple, and has fuel discharge holes formed at a lower portion thereof. The fuel distribution portion is located below the fuel supply tube, and has distribution nozzles through which fuel is distributed. The first oxidation catalytic layer is located beneath the fuel distribution portion. The inner wall may have a shape of a hollow circular or polygonal cylinder. The fuel supply tube may have a shape of a hollow circular or polygonal cylinder.
The combustor may further include an outer wall surrounding the inner wall with a second oxidation portion in a space therebetween, a lower portion of the second oxidation portion being in fluid communication with the first oxidation portion, and a second oxidation catalyst layer in the second oxidation portion. A second oxidation catalytic layer may be located in the second oxidation portion.
The fuel discharge holes may be formed in a horizontal direction on a lower outer circumferential surface of the fuel supply tube.
The fuel distribution portion may include a nozzle plate having distribution nozzles formed therein and a thermal capacity portion with a cylindrical shape extending downward from a periphery of the nozzle plate. The thermal capacity portion may be in a shape of a circular or polygonal cylinder.
An area of the distribution nozzles may increase in proportion to a distance from a center axis of the nozzle plate.
According to an embodiment of the present invention, there is provided a reformer. The reformer includes an inner wall, an outer wall, a first oxidation catalytic layer, a second oxidation catalytic layer, a thermocouple, a fuel supply tube, a fuel distribution portion, an evaporator and a reforming portion.
The inner wall has a shape of a hollow cylinder with a first oxidation portion in a space therein. The outer wall surrounds the inner wall with a second oxidation portion in a space therebetween, and a lower portion of the second oxidation portion is in fluid communication with the first oxidation portion. The fuel distribution portion is in the first oxidation portion. The first oxidation catalyst layer is located beneath the fuel distribution portion. The second oxidation catalyst layer is located in the second oxidation portion. The thermocouple extends to the first oxidation portion by passing through a top portion of the first oxidation portion so as to measure a temperature of the first oxidation portion. The fuel supply tube has a shape of a hollow cylinder surrounding the thermocouple, and has fuel discharge holes formed at a lower portion thereof. The fuel distribution portion is located below the fuel supply tube, and has distribution nozzles through which fuel is distributed. The evaporator receives reforming fuel and water supplied thereto and evaporates the supplied water using heat energy of exhaust gas exhausted from the second oxidation catalyst layer. The evaporator discharges the reforming fuel and the evaporated water. The reforming portion receives heat energy transferred from the first and second oxidation portions to reform the reforming fuel and the evaporated water from the evaporator. The inner wall may have a shape of a hollow circular or polygonal cylinder. The fuel supply tube may have a shape of a hollow circular or polygonal cylinder.
The evaporator may include a plurality of plates formed in a multi-layered structure with a plurality of layers and flow path tubes for passing the water and exhaust gas between the layers so that the layers corresponding to the water and exhaust gas are alternately arranged. The inner wall may be welded to a second bottom plate at a bottom of the evaporator, and the outer wall may be welded to a first bottom plate at the bottom of the evaporator.
The fuel discharge holes may be formed in a horizontal direction on a lower outer circumferential surface of the fuel supply tube.
The fuel distribution portion may include a nozzle plate having distribution nozzles formed therein and a thermal capacity portion with a cylindrical shape extending downward from a periphery of the nozzle plate.
An area of the distribution nozzles may increase in proportion to a distance from a center axis of the nozzle plate.
As described above, according to embodiments of the present invention, a fuel supply tube is formed to surround a thermocouple, so that the durability of the thermocouple can be enhanced.
Also, a fuel distribution portion has a cap shape, so that its thermal capacity is increased, thereby reducing flashback. Thus, in a case where a separate flashback reduction device is not employed, the durability of the fuel distribution portion and the thermocouple can be enhanced.
Also, welding points are minimized in the connection structure between a combustor and an evaporator, so that heat exchange efficiency can be increased, and manufacturing time and cost can be saved.
The accompanying drawings, together with the specification, illustrate exemplary embodiments of the present invention, and, together with the description, serve to explain the principles of the present invention.
In the following detailed description, only certain exemplary embodiments of the present invention have been shown and described, simply by way of illustration. As those skilled in the art would realize, the described embodiments may be modified in various different ways, all without departing from the spirit or scope of the present invention. Accordingly, the drawings and description are to be regarded as illustrative in nature and not restrictive. In addition, when an element is referred to as being “on” another element, it can be directly on the another element or be indirectly on the another element with one or more intervening elements interposed therebetween. Also, when an element is referred to as being “connected to” another element, it can be directly connected to the another element or be indirectly connected to the another element with one or more intervening elements interposed therebetween. Hereinafter, like reference numerals refer to like elements. When terms that indicate directions, such as top, bottom, left and right, are used without special notation, the terms indicate directions represented in the drawings.
As shown in
An aspect of embodiments according to the present invention is directed toward a combustor that supplies heat to the fuel reformer 10 in the fuel cell system.
A combustor 200 will be described with reference to
The first oxidation portion 225 is in the interior of a combustor inner wall 210 formed in the shape of a hollow cylinder (e.g., circular or polygonal cylinder). The second oxidation portion 235 is a space that surrounds an outside of the combustor inner wall 210. That is, a combustor outer wall 230 is formed in the shape of a hollow cylinder (e.g., circular or polygonal cylinder), and surrounds the combustor inner wall 210. That is, the second oxidation portion 235 is a space between the combustor inner and outer walls 210 and 230. The first and second oxidation portions 225 and 235 are connected so that fluid can flow therebetween at a lower portion of the combustor 200.
As shown in
A fuel supply tube 250 is formed in the shape of a hollow circular or polygonal cylinder, and surrounds the exterior of the thermocouple 260. Fuel discharge holes 251 are formed at a lower portion of the fuel supply tube 250. Here, the fuel discharge holes 251 may be formed in a horizontal direction on a lower outer surface (e.g., a circumferential surface) of the fuel supply tube 250 so that fuel flowing in the fuel supply tube 250 is supplied to the first oxidation portion 225 in the horizontal direction. That is, the fuel supply tube 250 functions to supply oxide fuel supplied therethrough to the interior of the combustor 200 and to protect the thermocouple 260 in a high-temperature environment.
Here, the oxide fuel refers to a main fuel such as liquefied petroleum gas (LPG) for generating heat through an oxidation reaction. The oxide fuel may include alcohol series such as methanol, hydrocarbon series such as methane and butane, fossil fuel such as naphtha, liquefied natural gas (LNG), biomass, landfill gas (LFG), or a combination thereof. The AOG refers to non-combustible gas having hydrogen as a main component, exhausted from an anode of a fuel cell after electricity is produced in a fuel cell stack.
A fuel distribution portion 211 will be described with reference to
As shown in
Here, since the fuel distribution portion 211 has a high thermal capacity, it serves as an anti-backfire portion. However, a separate anti-backfire portion may be provided to the fuel distribution portion 211. That is, an anti-backfire portion may be located between the fuel distribution portion 211 and the first oxidation catalyst layer 220. High-temperature hot spots are formed at an upper portion of the first oxidation catalyst layer 220, at which oxidation reaction is most actively performed. Here, the anti-backfire portion prevents the fuel from flowing backward in the direction of the fuel distribution portion 211. The anti-backfire portion may be made of a porous member or metal monolith having a cell density between about 400 and 600 cells per square inch (CPSI), which is similar to a support body of the first oxidation catalyst layer 220.
The first oxidation catalyst layer 220 is located in the interior of the first oxidation portion 225. The first oxidation catalyst layer 220 is provided with a mesh- or monolith-shaped support body having a space through which a fluid passes, and an active material is coated on the surface of the support body. The first oxidation catalyst layer 220 functions to increase a combustion rate by inducing stable combustion without flashback of the oxide fuel or AOG, and to control positions at which hot spots are formed. The active material may include Pd, Pt, Co3O4, PdO, Cr2O3, Mn2O3, CuO, Fe2O3, V2O3, NiO, MoO3, TiO2 or a mixture thereof. The support body of the first oxidation catalyst layer 220 may have a cell density between about 400 and 600 CPSI for the purpose of proper fluid pressure and effective oxidation reaction of the fuel.
A second oxidation catalyst layer 231 is located in the interior of the second oxidation portion 235. The second oxidation catalyst layer 231 may be formed by forming a mesh- or monolith-shaped support body having a cell density between about 100 and 200 CPSI, and an oxidation catalyst is coated on the surface of the support body. The support body may be made of metal such as chrome-based stainless steel (Fe—Cr) having a high melting point, alloy, complex material or the like, so as to have suitable durability at a high temperature. Like the active material in the first oxidation catalyst layer 220, the oxidation catalyst may include Pd, Pt, Co3O4, PdO, Cr2O3, Mn2O3, CuO, Fe2O3, V2O3, NiO, MoO3, TiO2 or a mixture thereof. Here, the second oxidation catalyst layer 231 may be divided into two portions spaced apart from each other at a suitable interval in the interior of the second oxidation portion 235.
Portions such as a reforming portion, an igniter and a preheater, which are not directly related to the present invention, will be omitted.
A combustor according to a second embodiment will be described with reference to
First, heat is generated by oxidizing the oxide fuel in the first oxidation catalyst layer 220. Subsequently, the oxide fuel not reacted at the lower portion of the first oxidation portion 225 and the AOG flowed into the first oxidation portion 225 through the AOG inlet port 240 are burned in flame. Finally, the non-reacted oxide fuel and the AOG are burned in the second oxidation catalyst layers 231 and 232 while moving through the second oxidation portion 235. The exhaust gas due to the combustion is exhausted to the exterior of the combustor 200.
In this case, hot spots are increasingly formed due to the AOG flowed into the first oxidation portion 225, and it is highly likely that flashback will occur in the first oxidation portion 225, as compared with the first embodiment. However, the flashback has no influence on the fuel discharge holes due to the high thermal capacity of the fuel distribution portion 211 described above.
This embodiment including an evaporator 300 will be described with reference to
The evaporator 300 is a component that evaporates water using heat energy of the exhaust gas exhausted from the combustor 200 and transfers the evaporated water together with the reforming fuel to a reformer. In
While the present invention has been described in connection with certain exemplary embodiments, it is to be understood that the invention is not limited to the disclosed embodiments, but, on the contrary, is intended to cover various modifications and equivalent arrangements included within the spirit and scope of the appended claims, and equivalents thereof.
| Number | Date | Country | Kind |
|---|---|---|---|
| 10-2010-0069037 | Jul 2010 | KR | national |
