This application claims priority to U.S. Provisional Patent Application Ser. No. 61/560,527, filed on Nov. 16, 2011. The disclosure of this application is hereby fully incorporated herein by reference in its entirety.
The present disclosure relates broadly to the field of solar power generation used to produce electricity. More particularly, this disclosure relates to a dual-exposure or two-sided heat absorption panel, and a solar receiver including one or more of such panels. These solar receiver designs can be used with Concentrated Solar Tower technology, also known as Concentrating Solar Power (CSP) technology to harness the sun's energy to produce “green” electricity.
A solar receiver is a primary component of a solar energy generation system whereby sunlight is used as a heat source for the eventual production of superheated high quality steam that is used to turn a turbine generator, and ultimately produce electricity using the Rankine cycle or provide steam for other thermal processes.
Generally, the solar receiver is positioned on top of an elevated support tower which rises above a ground level or grade. The solar receiver is strategically positioned within an array of reflective surfaces, namely a field of heliostats (or mirrors), that collect rays of sunlight and then reflect and concentrate those rays back to the heat absorbing surfaces of the solar receiver. This solar energy is then absorbed by the working heat transfer fluid (HTF) flowing through the solar receiver. The reflective surfaces may be oriented in different positions throughout the day to track the sun and maximize reflected sunlight to the heat absorbing surfaces of the receiver.
The solar receiver is an assembly of tubes with water, steam, molten salts, or other heat transfer fluid (HTF) flowing inside the tubes. The HTF inside the tubes of the receiver absorbs the concentrated solar energy, causing the HTF to increase in temperature and/or change phases, so that the HTF captures the solar energy. The heated HTF is then either directly routed to a turbine generator to generate electrical power or is indirectly routed to a storage tank for later use.
Solar receiver designs typically include an arrangement of panels with vertically oriented tubes, i.e. tube panels, along with a support structure for maintaining the tube panels in place and other associated equipment (pumps, pipes, storage vessels, heat shields, etc.). In conventional designs, the solar receiver has a square, rectangular, or circular cross-section (in a plan view from above). The tube panels are arranged on the exterior of the cross-section, so that the solar energy from the heliostats is directed at (and absorbed by) only one face of a tube panel. This is illustrated in, for example, U.S. patent application Ser. No. 12/605,241, which is entitled “Shop-Assembled Solar Receiver Heat Exchanger” and is assigned to Babcock & Wilcox Power Generation Group, Inc., and which is hereby fully incorporated by reference herein.
In this regard,
The interior non-absorbing face of a tube panel usually has a buckstay system that supports the tube panels against high wind, seismic forces, and thermally induced forces. The buckstay system typically includes “I” beams or other structural steel shapes that are clipped onto the tube panel in such a way that the tube panel can expand independent of the support structure itself and independent of the other tubes and panels. Clips are usually welded to the tubes so that the tube panel can move relative to the stationary support structure when heat is applied to the tubes, yet the support structure can still provide rigidity to the tube panel. On a solar receiver, the tubes in the tube panel are not welded together along their axes (i.e. membrane construction) as in a fossil fuel fired boiler, but are of loose construction. This allows the tubes to expand independently of each other when heat is applied. As a result, each tube must have a clip to attach to the buckstay at a support elevation.
One problem that results due to only one face of a tube being exposed to solar energy is that a temperature differential arises between the exposed hot face and the non-exposed cold face. This results in differential expansion between the hot and cold faces of the tube, which causes the tube to bow. The severity of bowing depends on the magnitude of the temperature differential and the rigidity of the tube panel. Because the clip connecting the tube to the buckstay keeps the tube in place at the support elevation, bowing occurs between support elevations. This creates high compressive stress on the heated side of the tube at each support elevation.
Due to daily heating and cooling of the tubes during startup, shutdown, and cloud passages, such stresses are cyclic, which can eventually lead to fatigue failure. For receivers that use molten salt as the HTF, impurities in the molten salt can also cause corrosion, which can be exacerbated where stress is located.
The present disclosure relates, in various embodiments, to heat absorbing tube panels and solar receivers incorporating such panels that are exposed to solar energy on two opposite faces. Compared to panels that absorb energy on a single face, heat absorption on two faces can reduce the temperature differential between the hot face and the cold face and therefore provide more uniform tube temperature around the circumference of the tube. This results in significantly reduced thermal stresses in the tube and lower potential for tube failures. With lower tube stresses, the risk of failure due to stress corrosion is also reduced. Also, for a given panel size the available heat absorbing area is doubled compared to a single side heated panel. The combination of reduced stresses and doubled absorbing area results in a panel that can accept more than twice as much solar energy, significantly increasing the efficiency of the panel. The solar receivers comprise an arrangement of heat transfer surfaces, a heat transfer fluid system structurally and functionally interconnected thereto, a vertical support structure, and a stiffener structure. Various structural features and other additions are also described herein.
Disclosed in embodiments herein is a dual-exposure heat absorption panel, comprising a tube panel and a structural support frame. The tube panel comprises a plurality of vertical tubes for conveying a heat transfer fluid. The tubes are interconnected by at least one upper header and at least one lower header. The tube panel has a first exposed face, an opposite second exposed face, an upper edge, a lower edge, a first side edge, and a second side edge. The structural support frame runs along the upper edge, the first side edge, and the second side edge of the tube panel. At least one tube in the tube panel is connected to the at least one upper header or the at least one lower header by a repair coupling surrounding the at least one tube and a prior header tube stub.
The repair coupling may be located behind heat shields mounted to the structural support frame so that the repair coupling is not exposed to direct sunlight.
The dual-exposure panel may further comprise a first stiffener structure running from the first side edge to the second side edge across the first exposed face and the second exposed face of the tube panel at a first support elevation.
In some embodiments, the stiffener structure is formed from a first support assembly and a second support assembly, each support assembly including: a support tube a horizontal flange extending from the support tube and having a slot therein and a scallop bar engaging one or more vertical tubes of the tube panel and having at least one lug, the scallop bar engaging the horizontal flange by a pin passing through the at least one lug and the slot of the horizontal flange. The support tube of each support assembly may have a different diameter from any tube in the tube panel, and in some embodiments is larger.
The dual-exposure panel may further comprise a second stiffener structure running from the first side edge to the second side edge across the first exposed face and the second exposed face of the tube panel at a second support elevation. In specific embodiments, the first support elevation and the second support elevation are not located at a middle section of the tube panel.
Also disclosed herein in different embodiments is a dual-exposure heat absorption panel, comprising a tube panel and a structural support frame. The tube panel comprises a plurality of vertical tubes for conveying a heat transfer fluid. The tubes are interconnected by at least one upper header and at least one lower header. The tube panel has a first exposed face, an opposite second exposed face, an upper edge, a lower edge, a first side edge, and a second side edge. The structural support frame runs along the upper edge, the first side edge, and the second side edge of the tube panel. The tube panel includes at least one tube joined to a header tube stub on either the at least one upper header or the at least one lower header, an exterior diameter of the header tube stub being greater than a central exterior diameter of the at least one tube. In more specific embodiments, an interior diameter of the at least one tube is the same as an interior diameter of the header tube stub.
Also disclosed herein in different embodiments is a dual-exposure heat absorption panel, comprising a tube panel and a structural support frame. The tube panel comprises a plurality of vertical tubes for conveying a heat transfer fluid. The tubes are interconnected by at least one upper header and at least one lower header. The tube panel has a first exposed face, an opposite second exposed face, an upper edge, a lower edge, a first side edge, and a second side edge. The structural support frame runs along the upper edge, the first side edge, and the second side edge of the tube panel. The structural support frame includes a first heat shield framing the first exposed face of the tube panel, an open space being present between the first heat shield and the tube panel.
Also disclosed herein in different embodiments is a dual-exposure heat absorption panel, comprising a tube panel, a structural support frame, a curtain, and means for guiding the curtain. The tube panel comprises a plurality of vertical tubes for conveying a heat transfer fluid. The tubes are interconnected by at least one upper header and at least one lower header. The tube panel has a first exposed face, an opposite second exposed face, an upper edge, a lower edge, a first side edge, and a second side edge. The structural support frame runs along the upper edge, the first side edge, and the second side edge of the tube panel. The structural support frame includes a first heat shield framing the first exposed face of the tube panel, the first heat shield including an upper face, a first side face, and a second side face. The curtain is located on the upper face of the first heat shield above the tube panel. The means for guiding the curtain is located on the first side face and the second side face of the heat shield.
The curtain may have a length sufficient to cover the entirety of the tube panel. The means for guiding can include rails or cables. Sometimes, a bottom edge of the curtain includes weights.
These and other non-limiting aspects and/or objects of the disclosure are more particularly described below.
The following is a brief description of the drawings, which are presented for the purposes of illustrating the exemplary embodiments disclosed herein and not for the purposes of limiting the same.
A more complete understanding of the processes and apparatuses disclosed herein can be obtained by reference to the accompanying drawings. These figures are merely schematic representations based on convenience and the ease of demonstrating the existing art and/or the present development, and are, therefore, not intended to indicate relative size and dimensions of the assemblies or components thereof.
Although specific terms are used in the following description for the sake of clarity, these terms are intended to refer only to the particular structure of the embodiments selected for illustration in the drawings, and are not intended to define or limit the scope of the disclosure. In the drawings and the following description below, it is to be understood that like numeric designations refer to components of like function.
The modifier “about” used in connection with a quantity is inclusive of the stated value and has the meaning dictated by the context (for example, it includes at least the degree of error associated with the measurement of the particular quantity). When used with a specific value, it should also be considered as disclosing that value. For example, the term “about 2” also discloses the value “2” and the range “from about 2 to about 4” also discloses the range “from 2 to 4.”
It should be noted that many of the terms used herein are relative terms. For example, the terms “interior”, “exterior”, “inward”, and “outward” are relative to a center, and should not be construed as requiring a particular orientation or location of the structure. Similarly, the terms “upper” and “lower” are relative to each other in location, i.e. an upper component is located at a higher elevation than a lower component.
The terms “horizontal” and “vertical” are used to indicate direction relative to an absolute reference, i.e. ground level. However, these terms should not be construed to require structures to be absolutely parallel or absolutely perpendicular to each other. For example, a first vertical structure and a second vertical structure are not necessarily parallel to each other.
To the extent that explanations of certain terminology or principles of the solar receiver, boiler and/or steam generator arts may be necessary to understand the present disclosure, the reader is referred to Steam/its generation and use, 40th Edition, Stultz and Kitto, Eds., Copyright 1992, The Babcock & Wilcox Company, and to Steam/its generation and use, 41st Edition, Kitto and Stultz, Eds., Copyright 2005,The Babcock & Wilcox Company, the texts of which are hereby incorporated by reference as though fully set forth herein.
The present disclosure relates to a dual-exposure or two-sided heat absorption panel and to solar receivers incorporating one or more two-sided heat absorption panels. The panels are designed to accept heat on two opposite sides or faces, rather than on only one side or face. This can reduce tube failures due to fatigue or stress corrosion, and for a given panel size the available heat absorbing area is doubled compared to a single side heated panel. The panels may include one or more stiffener structures or heat shields. Generally, the solar receiver is located at the top of a vertical support structure which rises above a ground level or grade. The vertical support structure may be supported from a base. The heat transfer surfaces advantageously comprise loose tangent tube panels, which allows for unrestrained thermal expansion of the tubes/tube panels in both the horizontal and vertical directions, thereby eliminating additional tube stresses. As is known to those skilled in the art, the sizes of tubes, their material, diameter, wall thickness, number and arrangement for the heat transfer surfaces are based upon temperature and pressure for service, according to applicable design codes. Required heat transfer characteristics, circulation ratios, spot absorption rates, mass flow rates of the working fluid within the tubes, etc. are also important parameters which must be considered. Depending upon the geographic location where the solar receiver is to be installed, applicable seismic loads and design codes are also considered.
It should be noted that in some embodiments, molten salt is used as the heat transfer fluid (HTF) that is run through the absorption panel. In this regard, molten salt solidifies at approximately 430° F. (221° C., 494° K.). When the tube panel(s) of the solar receiver is not exposed to light/heat, either intentionally at shutdown or unexpectedly due to a heliostat field malfunction, the molten salt can quickly cool and form plugs. Plugged tubes can cause delays at start up and could lead to tube failures. Thus, the ability to drain molten salt quickly is typically part of the solar receiver design. The valves and additional piping for such draining may not be depicted herein, but should be considered as being present. The present disclosure also contemplates the use of water, steam, or any other heat transfer fluid, with appropriate modifications made to other components of the solar receiver.
In
A structural support frame 300 runs along the upper edge 212, the first side edge 216, and the second side edge 218 of the tube panel. The structural support frame 300 includes a first vertical column 310, a second vertical column 320, and an upper horizontal beam 330 extending from an upper end 312 of the first vertical column to an upper end 322 of the second vertical column. As seen here, the first vertical column 310 is adjacent the first side edge 216, the second vertical column 320 is adjacent the second side edge 218, and the upper horizontal beam 330 is adjacent the upper edge 212 of the absorption panel. The tube panel 210 is connected to the structural support frame 300 through the upper header 242. Here, the tube panel is top supported. At least one panel support rod 202 extends between the structural support frame 300 and the upper header 242 three such panel support rods are shown here.
The structural support frame 300 rests upon a base platform 204, which may be considered as providing a platform for the absorption panel. The base platform 204 is attached to or located upon a tower 206.
Generally, a tube panel 210 requires at least one tube pass 240, an upper header 242, and a lower header 250. HTF flows from the inlet header to the outlet header (e.g. here the upper header can be the inlet header) and is heated in the tube pass by solar energy from heliostats. Each tube pass 240 includes at least one tube, and generally includes a plurality of such tubes. In
In
Generally, the number of stiffener structures can depend on the maximum unsupported length of the tube panel that will resist wind and seismic loads. In this regard, the tube panel 210 can be considered as being divided into an upper section 230, a middle section 232, and a lower section 234, which generally (but not necessarily) divide the exposed portion of the tube panel into equal sections along its height. The first stiffener structure 401 is shown in the upper section 230, and the second stiffener structure 402 is shown in the lower section 234. Put another way, the stiffener structures are typically not located in the middle section. This keeps the stiffener structures out of the peak heat flux zone and reduces their operating temperatures. It is contemplated that the stiffener structures will include support tubes that will be cooled by some heat transfer fluid, which could be the same as or different from the HTF that is passed through the tube panel. For example, the use of oil or water can eliminate the potential for molten salt freezing in the stiffener structure during startup and shutdown. Here, the stiffener structures are illustrated as being formed in part by a support tube 400 which is connected to the upper header 242 and lower header 250, which uses the same HTF as that passing through the tube panel 210. The stiffener structures 401, 402 are the portions of the support tube 400 that run across the face 222 of the tube panel 210. The circuitry is ultimately designed to minimize temperatures and stresses, allow independent thermal expansion of the stiffener structure, and minimize the potential for freezing of fluid during startup. The outer face of the stiffener structure can be painted or coated to reduce/minimize heat absorption.
In
As noted in
Referring to
The stiffener structure allows for independent thermal expansion of the individual tubes in the tube panel, as well as for independent thermal expansion of the stiffener structure and the support tubes. The pin/slot arrangement between the scallop bar and the support tube permits the support tubes to thermally expand axially independently of the radial expansion of the tubes in the tube panel. (Note the axis of the support tube is perpendicular to the axis of the tubes in the tube panel.)
The support system described above allows the individual tubes 460 to be arranged in a tangent tube fashion with minimal gap between the tubes. This reduces energy loss from light passing through the gaps and therefore increases receiver heat absorption and efficiency. The individual tubes 460 are seen here with their centers 462 along the midline 405 of the tube panel. Other variations on the tube layout are also contemplated.
Referring now to
Referring to
It is also noted that in
The flow path begins at inlet 504 and ends at outlet 506. It should be noted that if there is an even number of tube passes 510, the inlet 504 and the outlet 506 may be located along a common edge 508 or 544 of the tube panel 500. Alternatively, the inlet 504 and outlet 506 can be located on opposite edges 508 and 544 of the tube panel 500 when an odd number of tube passes is used. In other words, the inlet and the outlet can be independently located at the top edge 544 or the bottom edge 508, as required by the design of the receiver. As depicted here, the inlet 504 and the outlet 506 are both located along the top edge 544.
An inlet header is defined as such relative to the direction of flow. Thus, for tube pass 530, header 531 is considered the inlet header and header 532 is considered the outlet header. However, for adjacent tube pass 540, header 542 is considered the inlet header and header 541 is considered the outlet header. The headers of the tube passes can also be designated as upper headers 531, 541, 551, 561 and lower headers 532, 542, 552, 562 wherein the upper headers are located above the lower headers. Put another way, one set of headers 532, 542, 552, 562 is located in lower plane 508, and the other set of headers 531, 541, 551, 561 is located in an upper plane 544.
Referring again to tube pass 530, the tubes 536 form a body 537. The tubes are closely spaced and parallel to each other. The upper header 531 has a width 533, and the lower header 532 has a width 534. In some contemplated embodiments, and as illustrated here, the body 537 can have a width 538 that is greater than the header widths 533, 534. In other words, the body 537 may be wider than the lower header 532 and the upper header 531. The width is measured in the horizontal direction. The lower header and the upper header of each tube panel are the same width. The ratio of the body width 537 to the width of the lower header or upper header 532, 531 can at least 1.01:1, and may range from 1.01 to 1.5. This permits the spacing between edge tubes in adjacent panels to be the same as the close spacing between tubes within a panel. In such embodiments, the upper headers of adjacent tube panels would be laterally separated from each other. The lower headers of adjacent tube panels would also be laterally separated from each other. This may allow the tube panels to expand differentially with respect to each other because they are operating at different temperatures.
The inlet vessel 660 is optional and not required, which is indicated by the use of dotted lines, for example if the heat transfer fluid is steam/water. The outlet pipe 678 and outlet vessel 662 are also optional and not required, which is indicated by dotted line. Without an outlet vessel, the HTF flows from the tube panel outlet 676 directly to the downcomer pipe 688 via outlet pipe 691. A bypass line 690 also connects the riser 670 to the downcomer pipe 688. If desired, this bypass flow path can prevent the HTF from flowing through the tube panel 684.
This completes the energy collection process. The stored thermal energy in the heat transfer fluid can be used to generate steam and electricity. This is done by, for example, pumping the hot HTF from the hot storage tank 650 through the shell side of a heat exchanger 654. Water enters the tube side of heat exchanger 654 and is converted to steam. The steam can be sent to turbine 656, which drives an electrical generator 658. The cooler HTF leaving the heat exchanger then returns to the cold storage tank 652, where it is pumped to the receivers to repeat the energy collection process described above.
For a molten salt receiver, the tube panels must be fully drainable and ventable. The receiver is usually drained when not in use, at sunset, or when available solar energy is too low. Molten salt solidifies at approximately 430° F. (221° C., 494° K.). If not drained, the salt can freeze inside the tubes, plug the receiver, and could rupture the tubes. As seen here, the solar receiver can include a vent valve 692 for each independent flow path which are both vented through the top of the downcomer pipe 688. The vent valve is typically located near the top of the downcomer pipe 688, and the vent piping 694 is also illustrated connecting the flow path to the downcomer pipe. One drain valve 697 is typically provided for each pair of tube passes, and is located beneath the tube passes. The drain piping 698 is also illustrated, and connects to the downcomer 688 so that fluid present in the tube panel drains and flows into the downcomer pipe 688. The vent valves and drain valves are automated.
It should be noted that in
One problem with traditional solar receiver arrangements that have only one exposed face is that there is only limited access to the tubes in the tube panels if a tube should fail. Referring back to
Traditional solar receivers typically use a tube-to-tube butt weld of very thin tubes. Because the new/repair weld is out of the concentrated sunlight, different tube couplings can be used. One such repair tube coupling is seen in
The tube panel can be stiffened using different means, such as the stiffener structure seen in
Another consideration in designing a solar receiver is a scenario in which heat transfer fluid (HTF) ceases to flow through the tube panel, for example by loss of plant power or loss of the pumps used to move the HTF through the solar receiver. In this scenario, the heliostats are all still focused on the tube panel(s) of the solar receiver. The heliostats cannot be instantaneously defocused, and without HTF flow the high heat flux can quickly overheat the tube panel.
In a prior solar receiver known as Solar Two, which was operated from January 1998 to April 1999, inlet and outlet HTF vessels were used as buffers. The inlet vessel was pressurized with compressed air at a pressure high enough to continue flowing HTF contained within the inlet vessel through the tube panels long enough to allow the heliostats to be defocused off of the receiver.
When a trip condition exists, the curtain would be released and fall in front of the tube panel to block the concentrated sunlight coming from the heliostats. This would protect the tube panel from overheating until the heliostats could be defocused off of the receiver, eliminating the need for an inlet vessel. One benefit of this solar receiver design is that the edges of the curtain can be positively guided to pull the curtain down and keep the curtain from blowing in the wind, which could uncover portions of the tube panel. Here, the curtain can extend beyond the width of the tube panel. Thus, the edges of the curtain can be guided, for example via rails (like a garage door) or using guide cables. Here, the guidance means is shown as a path 758 through the heat shield, with cables attached to the curtain. This also protects the mechanism for driving the curtain down over the tube panel. For example, the bottom edge of the curtain may be weighted. Alternatively, cables could be used to pull the curtain down from the sides.
The present disclosure has been described with reference to exemplary embodiments. Obviously, modifications and alterations will occur to others upon reading and understanding the preceding detailed description. It is intended that the present disclosure be construed as including all such modifications and alterations insofar as they come within the scope of the appended claims or the equivalents thereof.
Number | Date | Country | |
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61560527 | Nov 2011 | US |