This invention relates to a solar collector structure that employs a plurality of absorber tubes that are arranged to be illuminated by solar radiation from a reflector field and to transfer absorbed energy to a heat exchange fluid that is, in use of the structure, carried by the tubes. The invention has been developed in the context of a so-called compact linear Fresnel reflector (CLFR) system and is hereinafter described in relation to such a system. However, it will be understood that the invention may have broader application.
Prior art solar collector structures of the type with which the present invention might be compared may be categorized generally as falling within two groups; a first group that employs effectively a single absorber tube that extends along the focal line of a non-inverted trough-type reflector and a second group that employs a single absorber tube that extends along the focal line of an inverted trough-type reflector. Collector systems of the first group suffer the disadvantages that the absorber tube collects incident solar energy from one only reflector element and requires complex mounting and fluid coupling arrangements. Collector systems of the second group largely avoid the disadvantages of the first group but suffer the disadvantage of losses occasioned by the need for multiple reflections, firstly from ground-mounted reflectors and then from the inverted trough reflectors. Moreover, collector systems of the second group (if not both groups) suffer a relatively high emissivity-to-absorptance ratio as a consequence, in part, of the surface area-to-aperture ratio attributable to the relatively large diameter tube required of a single-tube collector system. Furthermore, as a secondary issue, collector systems of both the first and second groups suffer loss of operating efficiency due to movement of unconfined heated air from the interior of the trough-like reflectors. Still further, as a tertiary issue, to the extent that the collector systems of the first and second groups employ a single absorber tube, those collector systems are not capable of providing for a variable absorption aperture.
The present invention provides a collector structure that is arranged to be located at a level above a field of reflectors and to receive solar radiation reflected from reflectors within the field. The collector structure comprises an inverted trough and, located within the trough, a plurality of longitudinally extending absorber tubes that, in use, are arranged to carry a heat exchange fluid. The absorber tubes are supported side-by-side within the trough and each absorber tube has a diameter that is small relative to the aperture of the trough.
The ratio of each absorber tube diameter to the trough aperture dimension may, for example, be in the range of 0.01:1.00 to 0.10:1.00 and typically may be of the order of 0.03:1:00. With this arrangement the plurality of tubes will, in the limit, effectively simulate a flat plate absorber.
The expressions “aperture of the trough” and “trough aperture” are both intended to be understood as defining, effectively, the opening of the trough through which incident radiation may pass to impinge on the absorber tubes.
A plurality of the collector structures as above defined may be connected together co-linearly to form a row of the structures and, in such case, each of the absorber tubes will extend along the full row, either as a single length of tubing or as conjoined lengths of tubing.
The absorber tubes may be constituted by metal tubes and each tube may, if required, be coated over at least a portion of its surface with a solar absorptive coating. In an alternative arrangement, each absorber tube may comprise a glass or metal tubular component that is coated with a solar selective surface coating and a surrounding glass tubular component, with the space between the two tubular components being evacuated.
The inverted trough may (but need not necessarily) be located in spaced relationship below a longitudinally extending roof and, in such case, an insulating material may be located in the space between the trough and the roof.
A window that is substantially transparent to solar radiation may be employed to close (the aperture of) the trough and, in so doing, create a heat confining cavity within the trough. The window may be formed from a rigid material such as glass or it may, for example, be formed from a flexible plastics sheet material that is connected to marginal side wall portions of the trough. In this latter case the cavity may be pressurized to an extent sufficient to inflate the window in a direction away from the absorber tubes.
The heat exchange fluid may in use of the collector structure be controlled to flow in parallel, unidirectional streams through the plurality of absorber tubes. Alternatively, means may be provided for selectively varying the channeling of the heat exchange fluid into and through the plurality of absorber tubes whereby the absorption aperture of the collector structure may, in use, effectively be varied.
The invention will be more fully understood from the following description of an exemplary embodiment of the solar collector structure.
The description is provided, by way of example, with reference to the accompanying drawings.
In the drawings
As shown in
The reflectors 10 may be of the type described in co-pending International patent applications numbered PCT/AU2004/000883 and PCT/AU2004/000884, filed 1 Jul. 2004 by the present Applicant, and the disclosures of these patent applications are incorporated herein by reference.
The reflectors 10 are driven collectively or regionally, as rows or individually, to track movement of the sun (relative to the earth) and they are orientated to reflect incident radiation to respective ones of the collector systems 12, as shown schematically and by way of example in
In the system as illustrated in
Each row 11 of reflectors 10 and, hence, each collector system 12 might typically have an overall length of 300 metres, and the parallel collector systems 12 might typically be spaced apart by 30 to 35 metres. The collector systems 12 are supported at a height of approximately 11 metres by stanchions 14 which are stayed by ground-anchored guy wires 15, although other similar support arrangements might be employed.
As indicated previously, each of the collector systems 12 comprises a plurality of collector structures 13 that are connected together co-linearly to form a row of the structures. Each of the collector structures might typically have a length of the order of 12 metres and an overall width of the order of 1.4 metres.
Each collector structure 13 comprises an inverted trough 16 which might typically be formed from stainless steel sheeting and which, as best seen in
The void between the trough 16 and the roof 21 is filled with a thermal insulating material 23, typically a glass wool material, and desirably with an insulating material that is clad with a reflective metal layer. The function of the insulating material and the reflective metal layer is to inhibit upward conduction and radiation of heat from within the trough.
A longitudinally extending window 24 is provided to interconnect the side walls 18 of the trough. The window is formed from a sheet of material that is substantially transparent to solar radiation and it functions to define a closed (heat retaining) longitudinally extending cavity 25 within the trough.
The window 24 may be formed from glass but it desirably is formed from a transparent heat resistant plastics material having a thickness of the order of 60×10−6 m. As shown in
In the collector structure as illustrated, sixteen longitudinally extending stainless steel absorber tubes 30 are provided for carrying heat exchange fluid (typically water or, following heat absorption, water-steam or steam). However, the actual number of absorber tubes may be varied to suit specific system requirements, provided that each absorber tube has a diameter that is small relative to the dimension of the trough aperture between the side walls 19 of the trough, and the collector system might typically have between ten and thirty absorber tubes 30 supported side-by-side within the trough.
The actual ratio of the absorber tube diameter to the trough aperture dimension may be varied to meet system requirements but, in order to indicate an order of magnitude of the ratio, it might typically be within the range 0.01:1.00 to 0.10:1.00. Each absorber tube 30 might have an outside diameter of 33 mm. and, with an aperture dimension of, for example, 1100 mm, the ratio of the absorber tube diameter to the aperture dimension will be 0.03:1.00.
As indicated previously, with the above described arrangement the plurality of absorber tubes 30 will, in the limit, effectively simulate a flat plate absorber, as compared with a single-tube collector in a concentrating trough. This provides for increased operating efficiency, in terms of a reduced level of heat emission from the upper, non-illuminated circumferential portion of the absorber tubes. Moreover, by positioning the absorber tubes in the inverted trough in the manner described, the underside portion only of each of the absorber tubes is illuminated with incident radiation, this providing for efficient heat absorption in absorber tubes that carry steam above water.
As illustrated in
Each of the absorber tubes 30 is coated, along its length and around a (lower) portion of its circumference that is exposed to incident solar radiation, with a solar absorptive coating. The coating may comprise a solar selective surface coating that remains stable under high temperature conditions in ambient air or it may comprise a black paint that is stable in air under high-temperature conditions.
Under the controlled condition illustrated in
Alternative fluid flow conditions may be established to meet load demands and/or prevailing ambient conditions, and provision may effectively be made for a variable aperture collector structure by closing selected ones of the absorber tubes. Thus, variation of the effective absorption aperture of each collector structure and, hence, of a complete collector system may be achieved by controlling the channeling of the heat exchange fluid in the alternative manners shown in
It is to be understood that the embodiment of the invention as described with reference to the drawings is presented solely as an example of one possible form of the invention. Thus, variations and modifications may be made in the embodiment of the invention as described without departing from the spirit and scope of the invention as defined in the appended claims.
Number | Date | Country | Kind |
---|---|---|---|
2004900786 | Feb 2004 | AU | national |
2004900787 | Feb 2004 | AU | national |
2004900788 | Feb 2004 | AU | national |
This application is a Continuation of U.S. patent application Ser. No. 13/182,653, filed Jul. 14, 2011, and entitled MULTI-TUBE SOLAR COLLECTOR STRUCTURE, which is a Continuation of U.S. patent application Ser. No. 10/597,966, filed Aug. 14, 2006, and entitled MULTI-TUBE SOLAR COLLECTOR STRUCTURE, and now U.S. Pat. No. 7,992,553, which is an application submitted under 35 U.S.C. 371 as a U.S. National Phase application of International patent application Number PCT/AU2005/000208, filed Feb. 17, 2005, which claims priority to Australian Application Serial Number 2004900787, filed Feb. 17, 2004, Australian Application Serial Number 200400788, filed Feb. 17, 2004, and Australian Application Serial Number 200400786, filed Feb. 17, 2004, the contents of which are each hereby incorporated by reference as if recited in full herein for all purposes.
Number | Date | Country | |
---|---|---|---|
Parent | 13182653 | Jul 2011 | US |
Child | 14261940 | US | |
Parent | 10597966 | Aug 2006 | US |
Child | 13182653 | US |