The present disclosure relates to a concentrated solar power (CSP) receiver, as well as to a CSP tower assembly incorporating such a receiver.
In one type of CSP system, a concentrating array of heliostats reflects sunlight towards one or more solar power receiver modules mounted on a central solar tower. Typically, the heliostats are in the form of solar tracking mirrors reflecting and focussing sunlight or solar thermal energy towards a central receiver module mounted on a solar tower.
The receiver module may include an array of pipes or conduits which carry a circulating heat transfer fluid, such as sodium or molten salt. This conveys heat to a heat storage facility such as a salt reservoir, which in turn may be used to heat water to drive one or more steam turbines. The peak heat flux to which the receivers are subjected is typically the range of up to 1500 KW/m2, which results in metal temperatures in excess of 600° or 700° C. The extreme thermal stress and thermal variation to which the receiver is subjected makes demands on the types of material used and impacts the life of the receiver, and it is not uncommon for receivers to fail prematurely under such thermal stress.
Under these extreme operating conditions, it is desirable that so called “hot spots” be avoided, and that there is a relatively even heat distribution across the receiver by the conduits efficiently receiving and conducting away the heat.
Reference to any prior art in the specification is not, and should not be taken as, an acknowledgment or any form of suggestion that this prior art forms part of the common general knowledge in any jurisdiction or that this prior art could reasonably be expected to be understood, regarded as relevant and/or combined with other pieces of prior art by a person skilled in the art.
According to a first aspect of the disclosure there is provided a concentrated solar thermal receiver for receiving concentrated solar thermal energy from a concentrating array of solar reflectors, the receiver comprising a single layered array of tubes configured to carry a heat transfer fluid and defining in combination an exposed concentrated solar thermal energy receiving surface, the array of tubes having a fluid inlet communicating with at least one inlet conduit, and a fluid outlet communicating with at least one outlet conduit, wherein the array of tubes are arranged in a serpentine configuration, and the array has predominantly transverse passes or components.
According to a second aspect of the disclosure there is provided a concentrated solar thermal receiver according to any one of the preceding claims in which the array includes a mounting arrangement for mounting the tubular array to a support or enclosure which is in turn mounted to a solar tower, the mounting arrangement being configured to allow transverse and upward/downward movement of the tubes in the array due to thermal contraction and expansion, the mounting arrangement including separation means for preventing adjacent tubes from touching but maintaining them in an almost touching position.
According to a third aspect of the disclosure there is provided a concentrated solar thermal receiver for receiving concentrated solar thermal energy from a concentrating array of solar reflectors, the receiver comprising a single layered array of tubes configured to carry a heat transfer fluid and defining a concentrated solar thermal energy receiving surface, the array of tubes having a fluid inlet communicating with at least one inlet conduit, and a fluid outlet communicating with at least one outlet conduit, wherein the array of tubes are arranged in a serpentine configuration, defining in combination an exposed concentrated solar thermal energy receiving surface, the receiver including a thermally insulating cover movable between an open position in which the solar thermal energy receiving surface is exposed to receive solar flux and a closed position in which the solar thermal energy receiving surface is covered to block or reduce the incidence of solar flux on the tubes or to reduce heat loss from the array of tubes under conditions where the incidence of solar flux is substantially reduced or non-existent.
The fluid inlet may comprise an operatively lower inlet header and the fluid outlet comprises an operatively upper outlet header, the array of tubes in combination defining the concentrated thermal energy receiving surface and extending between an inlet header and an outlet header.
The array of tubes may define a fluid flow path which is predominantly transverse and upward, or monotonic.
The transverse component may be substantially horizontal, and the upright or longitudinal component may be vertical in at least one plane. The array may include a mounting arrangement for mounting the tubular array to a support or enclosure which is in turn mounted to a solar tower, the mounting arrangement being configured to allow transverse and upward/downward movement of the tubes in the array due to thermal contraction and expansion, the mounting arrangement including separation means for preventing adjacent tubes from touching but maintaining them in an almost touching position.
The mounting arrangement may comprise at least two elongate support beams which are longitudinally or vertically aligned relative to the array of tubes and which carry movable linkages mounting the transverse tube components to the supports to permit transverse and upward/downward movement thereof.
The support beams may be in the form of conduits to which the linkages are rotatably and slidably mounted, the linkages in turn being rotatably mounted to tabs on the transversely extending tube components, the linkages being separated by slidable spacers.
The lengths of each of the tubes in the array may be substantially similar, and the flow resistance of each tube may be substantially similar so as to provide a similar dwell time of heat conductive fluid.
The receiver may include a thermally insulating cover movable between an open position in which the solar thermal energy receiving surface is exposed to receive solar flux and a closed position in which the solar thermal energy receiving surface is covered to block or reduce the incidence of solar flux on the tubes.
The array of tubes may comprise a plurality of multi-pass tubes which extend alongside one another in a parallel and serpentine array from an inlet manifold of the inlet header to an outlet manifold of the outlet header.
The number of parallel tubes and the number of passes per tube are typically in inverse relationship with one another so that the overall number of transverse tube passes, whether from the same or different tubes, remains substantially the same.
The array of tubes may be substantially co-planar so as to provide a co-planar energy receiving surface. While the tubes in the co-planar array are arranged such that adjacent tubes are almost touching, while allowing for play between tubes, certain tubes may be bent out of plane when an in-plane bend radius would be too small to allow bending without excessive deformation or thinning of the tube.
The overall configuration of the array may be a billboard configuration which is square or rectangular.
The array of tubes may define a curved or multi-faceted surface.
The array of tubes may define a cylindrical or hemi-cylindrical surface, in which case the solar tower is respectively fully or partly surrounded by heliostats.
The array of tubes may define an inverted frusto-cone, or part thereof, at an optimum angle from the vertical for receiving an optimum solar flux concentration.
At least one of the inlet or outlet headers may have a floating mount which allows it to move in concert with the thermal expansion and contraction of the array of tubes.
The lower inlet header may be provided with a floating mount and the upper outlet header may be provided with a fixed mount for mounting it to a frame or enclosure, with the support beams being movably anchored to the support frame or enclosure.
The cover may include one side suited to resisting high incident radiation and a mounting arrangement for maintaining the one side facing the source or high incident radiation in the both the open and closed positions and in moving therebetween.
Conveniently, when the cover is in the open position it is located immediately below the receiver to provide protection from high incident radiation to that part of the receiver supporting structure immediately below the receiver and behind the cover.
The mounting means may include a four bar linkage-type mount for movably mounting the cover to the supporting structure or tower.
The insulating door may be configured to reduce convective and radiative heat loss from the array of tubes, in a system where the heat transfer fluid is not drained from the tubes when there is no solar flux on the tubes.
The heat conductive fluid may be sodium and the tubes may be constructed from a stainless steel alloy such as 230 or 625 or a nickel based alloy such as Inconel.
The disclosure extends to a concentrated solar thermal tower assembly including a solar thermal tower, and a concentrated solar thermal receiver of the type described mounted to an upper portion of the tower.
The tower may be pivotable between an upright position and a prone position for enabling maintenance thereof.
The disclosure includes a concentrated solar power solar tower including at least one solar thermal receiver of the type defined above.
The disclosure may also include a concentrated solar thermal installation including at least one concentrated solar thermal tower assembly of the type defined, an array of heliostats arranged around the receiver and adjustable to focus solar radiation on the receiver, and a control means for controlling operation of the receiver to prevent overheating thereof, the control means being operable to open and close the cover.
Further aspects of the present disclosure and further embodiments of the aspects described in the preceding paragraphs will become apparent from the following description, given by way of example and with reference to the accompanying drawings.
Further aspects of the present disclosure and further embodiments of the aspects described in the preceding paragraphs will become apparent from the following description, given by way of example only with reference to the accompanying drawings.
Referring first to
Referring now to
As is clearly depicted in
Most of the bends in the tubes are coplanar with the face of the receiver, as is shown at 28. However, where the required return bend radius is smaller than can be achieved, at location 30, for example, certain of the tubes (26.9 and 26.10) are bent out of plane as shown at 32, 34 and 36. The outer plane tubes are in turn bent back into uniplanar configuration with the remaining tubes of the receiver at locations 40 for example. The tubes are designed to ensure substantially equal resistance across each tube, so that the flow rate through each tube is similar. The dwell time of fluid through each tube is also similar due to most of the tubes being of substantially the same length. The tubes 26.9 and 26.10 are slightly longer due to the additional out of plane bends, but this is compensated for by virtue of the partly shielded out of plane portions not absorbing as much heat.
It can clearly be seen how at the inlet and outlet manifolds 18A and 22A alternate tubes extend from opposite sides of the inlet and outlet headers to allow sufficient space for the inlet and outlet manifold connections to be made, with the even numbered tubes having re-entrant portions allowing them to merge back into the uniplanar receiver.
The tubes are mounted together on a parallel pair of tubular support beams 42 and 44, details of which are shown more clearly in
The tube supports 42 and 44 are mounted to the enclosure 12 using an array of tie bars including inwardly extending tie bars 68 extending to the base of the enclosure 12 and upwardly extending tie bars 69 extending to the upper horizontal frame of the enclosure. The tie bars are fitted with universal couplings 70 to allow for some freedom of movement during expansion and contraction of the array of tubes.
Referring now to
In the particular embodiment the tubes have an external diameter of 26.7 mm and an internal diameter of 23.4 mm, with a resultant wall thickness of 1.65 mm. The overall height of the tube array is 1.73 m and the width of the array from each header, is approximately 2.2 m, with the width between outer vertical components being approximately 1.8 m. It will be appreciated that all of these dimensions may vary widely, depending on the desired target size, the type of heat transfer fluid being carried, materials used, and other variables. Typical dimension ranges are as follows, but are not limited to these ranges:
Suitable materials were selected for the receiver so as to allow for high and variable temperature operating conditions and subject to creep and fatigue. It was found that stainless steel alloys 230 and 625 were potentially viable alloys based on an evaluation of life used under 1000 hours of creep conditions, with mid-wall temperatures in the region of 650 C, but that other stainless steel alloys could also be used, such as 316H, 347H as well as nickel based alloys, such as Inconel.
It will be appreciated that the number of passes as well as the number of tubes may be varied, and that the supports may be arranged so that the receiver face may be flat, curved or multi-faceted, depending on the application. For example, a single tube may be used with say 60 passes, 2 tubes with 30 passes, 3 tubes with 20, 4 with 15, 5 with 12, 6 with 10, 10 with 6, or 20 with 3. In each case optimum duration of heating to a desired temperature of say 600 C needs to be balanced with optimum through flow.
It will be appreciated that the array of tubes extend from the operatively lower inlet header 18 to the operatively upper outlet header 22 so as to define a fluid flow path which is horizontal or upward (i.e. monotonic), and at no location downward, so as to facilitate the natural outflow or venting of gases through the outlet header and avoid or at least reduce the formation or accumulation of gas pockets, as well as to ensure relatively uniform flow resistance and constant fluid flow. At low flow rates with vertical up/down flow configuration, buoyancy effects can lead to local stagnation of flow in one or more tubes.
Referring now to
An array of tubes 19 extend between an inlet manifold of the inlet header and an outlet manifold of the outlet header in a serpentine configuration. The array of tubes is similarly angled forward at about twenty degrees from the vertical. The array of tubes 19 is similar to the array of 24 of the first embodiment.
An insulating door assembly 20A comprises a frame 22A having a forward frame portion 24A carrying a door 26A and a rearward frame portion 28A carrying a counterweight 30A. The frame is mounted pivotally on a shaft 32A via a pair of upright supports 34A. The shaft 32A is in turn carried on a pair of trunnions 36A which are mounted to the top portion of the closure 12 of the receiver. Extending rearwards from the upright supports 34A are pairs of tubular extension arms 38A, 40A making up the rear frame 28A. The counterweight 30A is bolted between the rearmost ends of the extension arms 38A.
Extending forwardly from the upright supports 34A are an inner pair of extension arms 40A which are mounted to an upper end of the door and an outer pair of extension arms 42A which are mounted on connecting apertured lugs 44A located midway along the outer face of the door 26A. A cross bar 47A extends between the uprights 34A. The outer face of the door 26A as well as the extension arms 40A, 42A are fitted with refractory boards 48A formed from a high-strength reinforced silica matrix composite, or other suitable temperature-resistant rigid materials to provide shielding from concentrated solar radiation. The front portion of the framework 12A is similarly fitted with refractory boards or plates 48AA.
The composition of the insulating door assembly can more clearly be ascertained from
The door assembly 20A pivots between an open position indicated in
As shown in
The actuator 64A can comprise any prime mover, including a compressed-air actuator, an electric or internal combustion motor or the like. The actuator is in turn configured to receive control signals from a remote controller. It will be appreciated that the door may be opened or closed in response to a number of such signals, including direct operator control or automatic opening and closing in response to one or more sensors, such as infrared sensors or cameras or flow sensors, detecting conditions requiring, for example, closure of the door. These could include overheating or cooling of the receiver, which would be measured by the temperature of sodium exiting the receiver, a blockage or restriction in the flow of sodium or other heat transfer fluid travelling through the tubular array, a power failure or extreme weather conditions.
Referring now to
As is clear form
An advantage of these arrangements over a door which pivots from the upper frame of the receiver is that in the open position the door protects that portion of the tower closest to the receiver from excess solar thermal radiation from the heliostat array, avoiding the need for additional refractory plating. In addition the additional load on the receiver mountings is avoided by the separate mounting arrangement of the door. In one embodiment, however, the upper and lower parts of the door surround may be formed with catches (not shown) with which the uppermost portion of the door 72 may engage via complemental catches (not shown) to increase the stability of the door in the open and closed positions. A further advantage is that it is the same side of the door which is exposed to the solar thermal radiation at all times, with the result that this exposed side of the door may be specifically configured to resist high thermal radiation.
In the case of the receiver, different configurations of tubes may be used, including the predominantly transverse serpentine configuration as exemplified above, or other configurations in which the flow of fluid through the tubes is predominantly transverse and upward (i.e. monotonic) from a lower inlet to an upper outlet.
It was found that in general the life of the receiver could be extended by distributing the heat flux evenly and arranging the receiver tubes in a serpentine pattern, as opposed to a single pass multi-tube array in which the tubes were predominantly vertical or upright.
A wide variety of heat transfer fluids may also be utilised, including molten salts, liquid metals, such as sodium, and water/steam. In the particular embodiments sodium was the preferred heat transfer fluid due to its high thermal conductivity, allowing it to heat up relatively quickly, and its relatively high heat capacity at high temperatures. The broad temperature range at which it remains a liquid (98 C to 883 C), provides a sufficient ceiling above operating temperatures in the range of 500 C to 600 C in the event of overheating, as well as a lower temperature of solidification, in comparison with salt, which has traditionally been used.
It will be understood that the invention disclosed and defined in this specification extends to all alternative combinations of two or more of the individual features mentioned or evident from the text or drawings. All of these different combinations constitute various alternative aspects of the invention.
Number | Date | Country | Kind |
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2017904632 | Nov 2017 | AU | national |
2018902236 | Jun 2018 | AU | national |
Filing Document | Filing Date | Country | Kind |
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PCT/AU2018/051220 | 11/15/2018 | WO | 00 |