Heat exchanger comprising one or more plate assemblies with a plurality of interconnected channels and related method

Abstract

Plate assemblies configured for use in heat exchangers are provided. The plate assemblies may include one or more plates defining an inlet end, an outlet end, and flow channels configured to receive a flow of fluid from the inlet end and direct the fluid to the outlet end. The flow channels may be defined by protrusions, grooves, and/or orifices defined in flow plates, and spacer plates may separate the plate assemblies from one another. The flow channels may be interconnected such that for each of a plurality of intermediate positions along the flow channels, a plurality of flow paths are defined. Thus, in an instance in which a blockage occurs in one of the flow channels, flow may be prevented through only a portion of the flow channel.

Claims

1. A heat exchanger, comprising: a flow plate and a second flow plate respectively extending between an inlet end and an outlet end, the flow plate and the second flow plate each comprising a plurality of protrusions and a plurality of orifices positioned therebetween, the protrusions of the flow plate extending in a first direction between the inlet end and the outlet end, the protrusions of the second flow plate being the same as the protrusions of the flow plate but extending in a second direction between the inlet end and the outlet end opposite to the first direction, the protrusions of the flow plate contacting the protrusions of the second plate and defining a plurality of flow channels where the orifices of the flow plate overlap with the orifices of the second flow plate, the flow channels being configured to receive a flow of fluid from the inlet end and direct the fluid to the outlet end, wherein the flow channels are interconnected such that for each of a plurality of intermediate positions along the flow channels, a plurality of flow paths are defined.

2. The heat exchanger of claim 1, further comprising a spacer plate.

3. The heat exchanger of claim 2, wherein the flow channels are defined between a plurality of protrusions that are separated by a plurality of grooves.

4. The heat exchanger of claim 3, wherein the protrusions define a parallelogram shape.

5. The heat exchanger of claim 3, wherein the grooves and the protrusions are defined by the flow plate.

6. The heat exchanger of claim 2, further comprising a second spacer plate.

7. The heat exchanger of claim 1, wherein the protrusions each comprise a handle portion and three prongs extending therefrom.

8. The heat exchanger of claim 7, wherein the protrusions are interconnected in the flow plate and in the second flow plate.

9. The heat exchanger of claim 8, wherein the handle portion of one of the protrusions defines one of the prongs of an adjacent one of the protrusions.

10. The heat exchanger of claim 9, wherein the handle portion of one of the protrusions defines a center one of the prongs of the adjacent one of the protrusions.

11. The heat exchanger of claim 7, wherein the handle portion of the protrusions of the flow plate point in an opposite direction relative to the handle portion of the protrusions of the second flow plate.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) In order to assist the understanding of embodiments of the disclosure, reference will now be made to the appended drawings, which are not necessarily drawn to scale. The drawings are exemplary only, and should not be construed as limiting the disclosure.

(2) FIG. 1A illustrates a partially cutaway perspective view through a prior art embodiment of a plate assembly comprising flow plates including orifices that define a plurality of segregated flow paths;

(3) FIG. 1B illustrates a top partially cutaway view through the plate assembly of FIG. 1A;

(4) FIG. 1C illustrates a side sectional view through the plate assembly of FIG. 1A;

(5) FIG. 2A illustrates a partially cutaway perspective view through a prior art embodiment of a plate assembly comprising a flow plate including flow channels therein that define a plurality of segregated flow paths;

(6) FIG. 2B illustrates a top partially cutaway view through the plate assembly of FIG. 2A;

(7) FIG. 3A illustrates a partially cutaway perspective through a plate assembly including a flow plate with grooves and protrusions defined therein that create flow channels with multiple flow paths at intermediate positions along the flow channels, according to one example embodiment of the present disclosure;

(8) FIG. 3B illustrates a top partially cutaway view through the plate assembly of FIG. 3A;

(9) FIG. 4A illustrates a partially cutaway perspective view through a plate assembly including two flow plates with protrusions and orifices defined therein that create flow channels with multiple flow paths at intermediate positions along the flow channels, according to one example embodiment of the present disclosure;

(10) FIG. 4B illustrates a top partially cutaway view through the plate assembly of FIG. 4A;

(11) FIG. 4C illustrates a side sectional view through the plate assembly of FIG. 4A; and

(12) FIG. 5 illustrates a method for resisting blockage in a heat exchanger according to an example embodiment of the present disclosure.

DETAILED DESCRIPTION OF THE DISCLOSURE

(13) The present disclosure now will be described more fully hereinafter with reference to the accompanying drawings. The disclosure may be embodied in many different forms and should not be construed as limited to the embodiments set forth herein; rather, these embodiments are provided so that this disclosure will satisfy applicable legal requirements. Like numbers refer to like elements throughout. As used in this specification and the claims, the singular forms a, an, and the include plural references unless the context clearly dictates otherwise.

(14) The present disclosure relates to heat exchangers. Existing heat exchangers may theoretically provide relatively efficient heat transfer. However, in practice the heat exchangers may suffer from problems that may reduce the heat transfer efficiency thereof. In this regard, existing embodiments of heat exchangers may suffer from clogs that block the flow channels through which the fluid therein is intended to travel.

(15) By way of example, combustion of carbonaceous fuel for various uses, including but not limited to power production, may be carried out according to a system or method incorporating the use of an associated circulating fluid (such as a carbon dioxide (CO.sub.2) circulating fluid). Such systems and methods can comprise a combustor that operates at very high temperatures (e.g., in the range of about 1,600 C. to about 3,300 C., or even greater), and the presence of the circulating fluid can function to moderate the temperature of a fluid stream exiting the combustor so that the fluid stream can be utilized in energy transfer for power production. The combustion product stream can be expanded across at least one turbine to generate power. The expanded gas stream then can be cooled to remove the desired components from the stream, and heat withdrawn from the expanded gas stream can be used to heat the CO.sub.2 circulating fluid that is recycled back to the combustor. Preferably, the CO.sub.2 circulating fluid stream can be pressurized prior to recycling through the combustor. Exemplary power production systems and methods that may be used for the initial combustion process are described in U.S. Patent Application Publication No. 2011/0179799, the disclosure of which is incorporated herein by reference in its entirety. Cooling of a combustion product stream (with or without a preceding expansion) can be carried out using one or more heat exchangers.

(16) Thus, heat exchangers, including those disclosed herein, may be employed, for example, in the heat exchange operations associated with combustion of a carbonaceous fuel as described above. In particular, heat exchangers may be employed to exchange heat from combustion products to heat other fluids. However, combustion products may include components (e.g., particulate components) that could clog a heat exchanger. Likewise, heat exchangers may find use in a variety of other industries generally, or systems or methods specifically, wherein heat exchange capacity or efficiency may be affected if a portion of the heat exchanger becomes clogged, fouled, or otherwise obstructed.

(17) In prior art embodiments of heat exchangers, as already noted above, the flow channels may be segregated from one another and each flow channel may offer only a single flow path that is independent from any further flow paths within the heat exchanger. As a result of this configuration, a clog in a flow channel may partially or completely block the flow channel and cause the entire flow channel to lose at least a portion of its flow capacity and up to 100% of its flow capacity. For example, in the prior art plate assemblies 100, 200 illustrated in FIGS. 1 and 2, a blockage in one of the orifices 102A, 104A or a blockage in one of the channels 202A may cause the flow path 110, 210 associated with the flow channel in which the blockage occurs to be blocked. Since each flow channel offers only one flow path 110, 210, the entire flow channel may essentially cease to assist in heat transfer, regardless of where the blockage occurs along the flow channel. Thus, for example, in a heat exchanger comprising one hundred flow channels, blockage of one flow channel may result in approximately a one percent decrease in heat transfer efficiency.

(18) Thus, there is herein provided embodiments of heat exchangers configured to mitigate the effect of blockages therein. In this regard, FIGS. 3A and 3B illustrate a plate assembly of a heat exchanger according to one embodiment of the present disclosure. As illustrated in FIGS. 3A and 3B, the plate assembly 300 may include a flow plate 302 and a spacer plate 306. The flow plate 302 may include grooves defined therein, which define flow channels 312 and protrusions 314. The flow channels 312 may be defined between an inlet end 309 and an outlet end 311. The grooves may be defined by etching in some embodiments. Since the grooves do not extend all the way through the flow plate 302, the flow plate may function as a second spacer plate with the grooves defining the flow channels 312 between the flow plate and the spacer plate 306.

(19) As illustrated, the protrusions 314 may each define a diamond shape (e.g., parallelogram shape) in some embodiments. The protrusions 314 may be separated from one another and positioned in a pattern, as illustrated, which may create turbulence in the flow through the flow channels 312. The diamond/parallelogram shape of the protrusions 314 may also assist in creating turbulence by intermixing the flow channels 312. However, the flow channels 312 and the protrusions 314 may define other shapes and/or positions in other embodiments.

(20) The flow channels 312 may be interconnected such that for each of a plurality of intermediate positions along the flow channels, a plurality of flow paths may be defined. For example, as illustrated in FIG. 3B, a flow path 316 may begin at the entrance to one of the flow channels 312. The flow path 316 may continue to an intermediate position 318A along the flow channel 312 at which the flow may divide as a result of a protrusion 314 being positioned in the flow channel. Thus, the flow paths 316 may continue to an intermediate position 318B and an intermediate position 318C.

(21) As noted above, it may be possible for blockages to occur in heat exchangers. In this regard, a blockage 320 is illustrated in one of the flow channels 312 between the intermediate position 318C and an intermediate position 318D. However, as a result of providing a plurality of flow paths 316 at each intermediate position, flow may travel around the blockage 320 such that only the portion of the flow channel 312 between intermediate position 318C and an intermediate position 318D does not receive flow. For example, a flow path 316 may extend from intermediate position 318B to intermediate position 318D such that intermediate position 318D receives flow despite the obstruction 320. Accordingly, by providing a plurality of flow paths at a plurality of intermediate positions along the flow channels, the loss in flow from a blockage may be significantly reduced, as compared to prior art embodiments of plate assemblies wherein the flow channels are segregated, and hence a blockage may prevent flow through substantially the entire flow channel. In some embodiments, the heat exchanger of the present disclosure may be characterized as comprising a plurality of flow channels that are each multiply branched.

(22) FIGS. 4A-C illustrate a plate assembly of a heat exchanger according to an alternate embodiment of the disclosure. As illustrated in FIGS. 4A-C, the plate assembly 400 may include first 402 and second 404 flow plates that are sandwiched between spacer plates 406, 408. The spacer plates 406, 408 may separate the plate assembly 400 from adjacent plate assemblies. The flow plates 402, 404 may function to create flow channels 412 through which a fluid may flow from an inlet end 409 to an outlet end 411.

(23) As illustrated, the flow plates 402, 404 may respectively define protrusions 414A, 414B and orifices 415A, 415B. In some embodiments the protrusions 414A, 414B may define interconnected fork-shaped elements each defining a handle portion and three prongs extending therefrom. The handle portion of each protrusion 414A, 414B may define the center prong of an interconnected protrusion. Further, the protrusions 414A, 414B may be positioned such that the protrusions 414A of the first flow plate 402 extend in a first direction, and the protrusions 414B of the second flow plate 404 extend in a second direction, which is opposite to the first direction. As illustrated in FIG. 4C, this configuration may cause the flow channels 412 to define a plurality of flow paths 416 for each of a plurality of intermediate positions 418A-E along the flow channels. In this regard, fluid may flow over or around the protrusions 414A, 414B and/or through the orifices 415A, 415B, which may create turbulence. The orifices 415A, 415B of the flow plates 402, 404 may partially overlap to allow flow therethrough. Further, as discussed above, in an instance in which a blockage occurs in a flow channel 412, the flow may divert around the blockage through one or more alternate flow paths such that only a relatively small area of the flow channel including the blockage losses flow therethrough.

(24) The plate assemblies 300, 400 disclosed herein may be employed in a variety of different embodiments of heat exchangers. The heat exchangers may be formed by brazing or diffusion bonding the plates together to create the plate assemblies in some embodiments. Accordingly, monolithic heat exchangers may be created, which may be attached via manifolds to form even larger heat exchanger devices. However, the plate assemblies may be configured to define various other embodiments of heat exchangers.

(25) A method for resisting blockage in a heat exchanger is also provided. As illustrated in FIG. 5, the method may include directing a fluid through an inlet end to a plurality of plates at operation 500. The inlet can be defined in the heat exchanger, and the plurality of plates can be positioned within the heat exchanger or otherwise define the heat exchanger. Further, the method may include directing the fluid through a plurality of flow channels that are interconnected such that for each of a plurality of intermediate positions along the flow channels, a plurality of flow paths for the fluid are defined at operation 502. The method may additionally include directing the fluid to an outlet end of the plates at operation 504.

(26) In some embodiments directing the fluid through the flow channels at operation 502 may comprise dividing the fluid into the flow paths with a plurality of protrusions. Further, directing the fluid through the flow channels at operation 502 may comprise directing the fluid between a flow plate and a spacer plate. Additionally, directing the fluid through the flow channels at operation 502 may comprise directing the fluid through a plurality of partially overlapping orifices defined in a first flow plate and a second flow plate.

(27) As illustrated at operation 506, in some embodiments the method may further comprise receiving the fluid from a combustor. In this regard, the fluid may comprise a particulate component in some embodiments. Further, the method may include retaining the fluid between a first spacer plate and a second spacer plate at operation 508.

(28) Many modifications and other embodiments of the inventions set forth herein will come to mind to one skilled in the art to which these inventions pertain having the benefit of the teachings presented in the foregoing descriptions. Therefore, it is to be understood that the inventions are not to be limited to the specific embodiments disclosed and that modifications and other embodiments are intended to be included within the scope of the appended claims. Although specific terms are employed herein, they are used in a generic and descriptive sense only and not for purposes of limitation.