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Title:
SOLAR ENERGY COLLECTOR
Document Type and Number:
WIPO Patent Application WO/1998/011393
Kind Code:
A1
Abstract:
A solar energy collector (10) has a generally planar panel (12). The generally planar panel has upper (16) and lower (20) generally planar surfaces, first and second end regions, and a planar portion (20) formed with a plurality of passages (22) extending up from one of the end regions of the other for receiving a solar energy-absorbing liquid. A respective end closure (14) is coupled to each or the end regions for conducting the solar energy-absorbing liquid to and from the passages. At least one of the end closures has means (42) enabling communication of at least one cavity with atmosphere. Each end closure has upper (26) and lower (28) limbs for sealingly gripping upper and lower surfaces of the panel (34). A kit of parts for a solar energy collector is also provided.

Inventors:
JOHNSON RICHARD (GB)
HADLUM PAUL (GB)
Application Number:
PCT/GB1997/002504
Publication Date:
March 19, 1998
Filing Date:
September 12, 1997
Export Citation:
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Assignee:
UNIV COVENTRY (GB)
JOHNSON RICHARD (GB)
HADLUM PAUL (GB)
International Classes:
F24J2/46; F24S10/70; (IPC1-7): F24J2/24; F24J2/46
Domestic Patent References:
WO1993015368A11993-08-05
Foreign References:
US4114597A1978-09-19
DE2709801A11978-09-14
DE2826937A11980-01-03
DE4241133A11994-06-09
Other References:
None
Attorney, Agent or Firm:
Hallam, Arnold Vincent (5 The Quadrant, Coventry CV1 2EL, GB)
Download PDF:
Claims:
What is claimed is :
1. A method for coextruding multiple polymer plastic materials as for injecting through a gate region into a mold cavity to produce a molded article, that comprises, coextrusively flowing streams of polymer plastic materials with at least one interior stream that is to serve as an interior core of a resulting molded plastic article within inner and outer streams of plastic material that serve as covering wall plastic material layers for the core; forcing the flowing streams to flow along concentric annular flow paths within and along a longitudinally extending tubular extruder nozzle to the cavity gate region; adjusting the flow streams initially to cause the core stream to start to flow at a region of substantially zero gradient in the transverse flow velocity profile of the extrusion ; thereupon varying the relative volumetric flow ratio of the inner and outer layer streams after the zerogradient flow of the core layer has started, in order to offset the core layer flow from the zero gradient and to shift the core layer closer to one of the inner or outer annular flow boundaries, thereby to produce a molded article wherein the major portion of the core layer is closer to one of the inner or outer article walls than the other.
2. The method of claim 1 wherein the relative thickness of the inner or outer layers is correspondingly varied substantially in said ratio.
3. The method of claim 1 wherein, prior to the termination of the extrusion, the flow ratio of the inner and outer layers is varied to shift the terminal end of the interior core stream back along substantially said zero gradient.
4. The method of claim 1 wherein the inner and outer stream ratio is varied after a few percent of the core layer stream flow has initially flowed.
5. The method of claim 1 wherein the adjusting of the flow stream initially causes the inner and outer streams to start to flow with substantially equal volumetric flow rates.
6. The method of claim 1 wherein said forcing is effected by disposing a longitudinal pin within and along the extruder to force the combined streams into said concentric annular flow paths.
7. The method of claim 1 wherein the relative volumetric flow ratio of the inner and outer streams is controlled by relatively restricting the respective flow channels of the streams within the extruder.
8. The method of claim 7 wherein the timing of said relative flow restricting is controlled to coincide with one or both of (1) a short time after the start of the flow of the core stream, and (2) near the termination thereof.
9. The method of claim 7 wherein the timing of said relative flow restricting is controlled intermediate the flow of the streams to the mold cavity.
10. The method of claim 7 wherein the relative flow restricting is effected by inserting a flow restrictor into the inner or outer flow stream within the extruder.
11. The method of claim 7 wherein the inner, outer and core layer flow streams are fed into respective entry channels in the extruder nozzle from respective material sources, and the flow restrictor is inserted into one of either a source flow channel, or near a nozzle entry channel.
12. The method of claim 11 wherein a plurality of similar nozzles are similarly simultaneously fed from respective material sources, with flow restrictors inserted near corresponding inner or outer layer entry flow channels in each nozzle or in common feed channels from said sources.
13. The method of claim 1 wherein the inner and outer layer streams are fed from the same plastic material source and the plastic core material stream from a different source, and the annular coextensive streams of the core material stream encased by the inner and outer layer streams are combined near said gate region and laterally injected in opposite transverse directions into the mold cavity.
14. The method of claim 13 wherein the molded article thereby formed is a hollow plastic container in which the interior core layer encased by inner and outer container walls is of material that serves as a barrier layer for such purposes as resisting the flow of gases through the container walls and/or scavenging oxygen.
15. The method of claim 1 wherein a threematerial plastic article is to be molded comprising inner and outer layers and two interior or core layer materials and wherein the inner and outer layer material streams are divided within the nozzle to form the inner and outer annular covering wall layers, one of the interior layer streams being directed within the nozzle to form an interior annular layer adjacent said inner layer, and the other interior stream being directed within the nozzle to form an interior annular layer adjacent the outer layer.
16. A method for coextruding multiple plastic materials as for injecting through a gate region into a mold cavity to produce a molded article having an interior core layer encased within inner and outer wall layers, that comprises, co extrusively flowing inner and outer layer streams of plastic material encasing an interior core layer to inject the same though the gate region into the mold cavity; initially starting the flow with a substantially 50 : 50 ratio of inner and outer layer stream volumetric flows to cause the interior core stream to flow at a midplane region of substantially zero gradient in the transverse flow velocity profile of the extrusion ; thereupon, for the major portion of the flow, varying the relative volumetric flow ratio of the inner and outer layer streams to offset the core layer stream from the midplane and shift the core layer closer to one of the inner or outer flow boundaries, thereby to produce a molded article wherein the major portion of the core layer within the article is closer to the inner or outer article wall.
17. The method claimed in claim 16 wherein said flow ratio is varied back to substantially 50: 50 near the terminal end of the flow into the cavity.
18. The method claimed in claim 16 wherein the ratio is varied after a few percent of the core layer stream flow has initially flowed.
19. The method in claim 16 wherein the ratio is further varied during the continued flow to the gate region, and into the mold.
20. The method of claim 19 wherein said ratio is varied back to substantially 50: 50 near the terminal end of the flow to reestablish the interior core stream flow back along substantially said zero gradient.
21. The method of claim 16 wherein the core layer stream material is selected for barrier function characteristics such as at least one of gas permeation control, gasscavenging, and electromagnetic shielding.
22. Apparatus for coextruding multiple plastic materials as for injecting through a gate region into a mold cavity to produce a molded article having an interior core layer encased within inner and outer wall layers, the apparatus having, in combination, a longitudinally extending extruder nozzle for receiving plastic material from sources thereof and coextrusively flowing the material as inner and outer layer streams of plastic material encasing an interior core layer to inject the same through the gate region into the mold cavity; flow control means for initially starting the flow with a substantially 50: 50 ratio of inner and outer layer stream volumetric flow rates to cause the interior core stream to flow at a mid plane region of substantially zero gradient in the transverse flow velocity profile of the extrusion; means for thereupon, for the major portion of the flow, adjusting the flow control means to change the relative volumetric flow ratio of the inner and outer layer streams to offset the core layer stream from the mid plane and shift the core layer closer to one of the inner or outer flow boundaries, thereby to produce a molded article in the cavity wherein the major portion of the core layer within the article is closer to one of the inner or outer article wall.
23. The apparatus claimed in claim 22 wherein the flow control means is adjusted to vary the flow ratio back to substantially 50: 50 near the terminal end of theflow into the cavity.
24. The apparatus claimed in claim 22 wherein the flow control means is operated to change the ratio after a few percent of the core layer stream flow has initially flowed.
25. The apparatus claimed in claim 22 wherein the flow control is adjusted to further vary the ratio during the continued flow to the gate region.
26. The apparatus of claim 25 wherein the flow control means is adjusted to vary said ratio back to substantially 50: 50 near the terminal end of the flow to re establish the interior core stream flow back along substantially said zero gradient.
27. The apparatus of claim 22 wherein the core layer stream material is selected for barrier function characteristics such as at least one of humidity control, gas permeation, gas scavenging and electromagnetic shielding.
28. Apparatus for co extruding multiple plastic materials as for injecting through a gate region into a mold cavity to produce a molded article, having, in combination, a longitudinally extending tubular extrusion nozzle provided with entry channels for receiving plastic materials from sources thereof and co= extensively flowing the materials as inner and outer layer streams with one interior stream that is to serve as an interior core of a resulting molded plastic article within inner and outer streams of plastic material that serve as covering wall plastic material layers for the core; a longitudinal throttle means for forcing the streams to flow along concentric annular flow paths within and along a longitudinally extending tubularextruder nozzle to the cavity gate region; means for adjusting the flow streams initially to cause the core stream to start to flow at a region of substantially zero gradient in the transverse flow velocity profile of the extrusion; means operable thereupon for varying the relative volumetric flow ratio of the inner and outer layer streams after the zerogradient flow of the core layer has started in order to offset the core layer flow from the zero gradient and to shift the core layer closer to one of. the inner or outer flow boundaries, thereby to produce a molded article wherein the major portion of the core layer is closer to one of the inner or outer article walls than the other.
29. The apparatus of claim 28 wherein the relative thickness of the inner or outer layers is correspondingly varied substantially in said ratio.
30. The apparatus of claim 28 wherein, prior to the termination of said extrusion, the adjusting means is controlled to vary the flow ratio of the inner and outer layers to shift the terminal end of the interior core stream back along substantially said zero gradient.
31. The apparatus of claim 28 wherein the adjusting means varies the inner and outer stream ratio after a few percent of the core layer stream flow has initially started.
32. The apparatus of claim 28 wherein the adjusting means initially causes the inner and outer streams to start with substantially equal volumetric flow rates.
33. The apparatus of claim 28 wherein said adjusting means comprises an axial pin for forcing the combined streams into said concentric annular flow paths.
34. The apparatus of claim 28 wherein the relative volumetric flow ratio of the inner and outer streams is controlled by restrictors disposed in the respective flow channels of the streams within the extruder.
35. The apparatus of claim 34 wherein means is provided for controlling the timing of the relative restricting by the restrictors to coincide with one or both of shortly after the start of the flow of the core stream, and near the termination of the core stream flow.
36. The apparatus of claim 35 wherein means is provided for controlling the timing of the relative flow restricting intermediate the flow of the streams to themold cavity.
37. The apparatus of claim 35 wherein the relative flow restricting is effected by means for inserting a flow restrictor into one of the inner or outer flow streams.
38. The apparatus of claim 28 wherein the inner, outer and core layer flow streams are fed into respective entry channels in the nozzle from respective material sources, and the flow restrictor is inserted into one of (1) a source flow channel or (2) near a nozzle entry channel.
39. The apparatus of claim 28 wherein a plurality of similar nozzles is provided, the nozzles of which are similarly simultaneously fed from respective material sources, with flow restrictor means inserted in corresponding inner or outer layer entry flow channels in each nozzle or in common feed channels from said sources.
40. The apparatus of claim 28 wherein the inner and outer layer streams are fed from the same plastic material source and the plastic core material stream from a different source, and the annular co extensive streams of the core material stream encased by the inner and outer layer streams are combined near said gate region and laterally injected in opposite transverse directions into the mold cavity.
41. The apparatus of claim 40 wherein the molded article thereby formed is a hollow plastic container in which the interior core layer is of material that serves as a barrier layer for such purposes as resisting the flow of humidity and or gases through the container walls and/or scavenging oxygen through chemical combination therewith.
42. The apparatus of claim 28 wherein a 3material plastic article is to be molded comprising inner and outer layers and two interior or core layer materials, and wherein the inner and outer layer material streams are divided within the nozzle to form the inner and outer annular covering wall layers, one of the interior layer streams is directed within the nozzle to form an interior annular layer adjacent said inner layer, and the other interior stream is directed within the nozzle to form an interior annular layer adjacent the outer layer.
43. The method of claim 1 wherein a plurality of similar extruder nozzles is provided similarly simultaneously fed from respective material sources, and with flow restriction inserted in corresponding inner and outer layer entry flow channels into each nozzle or in common feed channels from said sources.
44. The method of claim 1 wherein two interior streams are flowed within said inner and outer streams, with the flow of one of the interior stream started before the flow of the other interior stream and with its leading edge starting on saidzero gradient, and the subsequent initiation of the flow of said other interior stream offsetting the laterflowing portions of said one interior stream flow from said zero gradient, and with the completing of the injecting of the other interior stream before the completion of the injecting of said one interior stream through said gate region and into said mold cavity, and finishing the injecting of said interior stream on said zero gradient.
45. The method of claim 44 wherein the materials of the inner, outer and interior streams constitute three molding materials forming a fourlayer molded article.
46. The method of claim 45 wherein the relative thickness and position of each of the interior streams is chosen to enhance the properties of the molded article.
47. The method of claim 46 wherein the innermost of the interior streams is of gas scavenging material in order to reduce the permeation rate of gas through said outer wall of the molded article, and to increase the rate of gas scavenging from the contents of the article if the scavenger material is intended to absorb gas permeating from the exterior of the article.
48. The method of claim 46 wherein the outermost of the interior streams is of humidity sensitive gas barrier material in order to position such barrier at a position within the molded article that is closer to the exterior atmosphere surrounding the article.
49. The method of claim 44 wherein the article is one of a cylindricalshaped hollow container, such as a bottle, and a flatshaped article.
50. The apparatus of claim 22 wherein said inner core layer comprises a pair of interior core streams, with said adjusting means enabling one of the interior streams to start flow before the other of the pair of interior streams and with its leading edge starting on said zero gradient, and enabling the subsequent initiation of the flow of said other interior stream offsetting the laterflowing portions of said one interior stream through said gate region and into said mold cavity, with the finishing of the injecting of said one interior stream lying on said zero gradient.
51. The apparatus of claim 50 wherein the materials of the inner, outer and interior streams constitute three molding materials forming a fourlayer molded article.
52. The apparatus of claim 51 wherein the relative thickness and position of each of the interior streams is chosen to enhance the properties of the molded article.
53. The apparatus of claim 52 wherein the innermost of the interior streams is of gas scavenging material in order to reduce the permeation rate of gas through said outer wall of the molded article, and to increase the rate of gas scavenging from the contents of the article if the scavenger material is intended to absorb gas permeating from the exterior of the article.
54. The apparatus of claim 52 wherein the outermost of the interior streams is of humidity sensitive gas barrier material in order to position such barrier at a position within the molded article that is closer to the exterior atmosphere surrounding the article.
55. The apparatus of claim 50 wherein the article is one of a cylindricalshaped hollow container, such as a bottle, and a flatshaped article.
56. A molded plastic material article having an interior plastic core layer encased within inner and outer plastic wall layers wherein the major portion of the core layer within the article is closer to one of the inner or outer article walls.
57. The molded article of claim 56 wherein the article is hollow and bounded by the coreencased inner and outer walls.
58. The molded article of claim 57 wherein the initial portion the core layer lies substantially on the centerline of the coreencased inner and outer article walls.
59. The molded article of claim 58 wherein said initial portion constitutes a few percent of the length of the core layer.
60. The molded article of claim 59 wherein the core layer near its terminal end again lies substantially on said centerline.
61. The molded article of claim 59 wherein the core layer material is selected for barrier function characteristics such as at least one of humidity control, gas permeation, gas scavenging and electromagnetic shielding.
62. The molded article of claim 59 wherein the inner and outer walls and the core are of three molding materials forming a fourlayer molded article.
63. A preform for a hollow molded plastic material article having an interior plastic core layer encased within inner and outer plastic wall layers wherein the major portion of the core layer within the preform is closer to one of the inner and outer article walls.
64. The preform of claim 63 wherein the initial portion of the core layer lies substantially on the centerline of the coreencased inner and outer article walls.
65. The preform of claim 64 wherein said initial portion constitutes a few percent of the length of the core layer.
66. The preform of claim 65 wherein the core layer near its terminal end again lies substantially on said centerline.
67. The preform of claim 65 wherein the core layer material is selected for barrier function characteristics such as at leas'tone of humidity control, gas permeation, gas scavenging and electromagnetic shielding.
Description:

TITLE: Solar Energy Collector

Field of the Invention

This invention relates to solar energy collectors.

Description of the Prior Art

Conventionally a solar energy collector comprises a panel having a number of passages through which a liquid passes so that it is heated by absorbing solar energy. The heated liquid may be used in a number of ways, for example it may be supplied to a heat exchanger forming part of a domestic water heating system.

One of the difficulties facing designers of solar energy collectors is that in order to be economic, particularly in the United Kingdom where there is much less solar energy available in the Winter than in the Summer, a collector must be efficient and also simple and inexpensive to manufacture install and maintain.

It has previously been proposed to use extruded plastic panels having a plurality of side-by- side passages for the flow of solar energy-absorbing liquid through the panel but it is thought that the thermal efficiency of such panels could be improved.

Summary of the Invention

According to the present invention there is provided a solar energy collector comprising:

a generally planar panel having:

upper and lower generally planar surfaces;

first and second end regions;

a first planar portion formed with a plurality of passages extending from said one of said end regions to the other for receiving a solar energy-absorbing liquid;

and a respective end closure coupled to each of said end regions of said panel for conducting said solar energy-absorbing liquid to and from said passages;

and wherein each said end closures has upper and lower limbs for sealingly gripping said upper and lower surfaces of said panel.

In a preferred form of the invention said first planar portion is a lower planar portion and said panel further comprises an upper planar portion adapted to allow the passage therethrough of solar radiation and formed with at least one cavity extending from one of said end regions to the other for containing a heat-insulating fluid.

Advantageously, at least one of said end closures has means enabling communication of said at least one cavity with atmosphere. This has the advantage that an accumulation of condensation within the cavity is substantially reduced.

The present invention also provides a kit of parts for a solar energy collector comprising:

a generally planar panel having:

upper and lower generally planar surfaces;

first and second end regions;

a planar portion formed with a plurality of passages extending from said one of said end regions to the other for receiving a solar energy-absorbing liquid;

and a respective end closure adapted to be coupled to each of said end regions of said panel for conducting said solar energy-absorbing liquid to and from said passages;

and wherein each said end closure has upper and lower limbs for sealingly gripping said upper and lower surfaces of said panel.

Preferably, said first planar portion is a lower planar portion;

and said panel further comprises an upper planar portion adapted to allow the passage therethrough of solar radiation and formed with at least one cavity extending from one of said end regions to the other for containing a heat-insulating fluid.

A collector panel of this form can be manufactured relatively inexpensively, particularly as an extruded plastics moulding, and in use the heat-insulating fluid, which is conveniently air, reduces heat loss from the solar energy-absorbing liquid beneath it.

The lower planar portion of the panel preferably has a single group of passages arranged side- by-side. The idea is that in use the panel is installed with the passages extending vertically or at inclination to the vertical, and preferably the solar energy-absorbing liquid is caused to flow upwardly through the passages, for example by pumping it through a pressurised system.

The liquid is conveniently water which may be coloured to provide shade, for example when the panel forms part of a roof.

A further advantage of providing a coloured liquid such as coloured water is that in general the darker the colour of the liquid, the more heat absorbent the liquid will be.

In the examples where a coloured liquid is used, once substantially all the liquid has drained back from the passages in the collector, the collector will be substantially clear. Thus, by switching a pump on or off, an operator can determine whether the collector provides shade

and absorbs heat, for example in the heat of the day, or whether the collector substantially does not provide shade, allowing the majority of the light to pass through, for example, in the early morning or the evening.

A control system comprising valves may be used to permit liquid to flow through all or only some of the passages.

The upper planar portion of the panel is preferably formed with a similar group of passages providing a plurality of the cavities referred to above.

The end closure preferably comprises a channel-section member which is formed or constructed so that when fitted over an end of the panel its limbs grip the panel, the member being provided with an opening arranged to communicate with the passages in the panel to provide an inlet or outlet, as the case may be, for the solar energy-absorbing liquid.

The end closures may be attached to the panel by adhesive, which acts as a sealant for the passages in the panel, in which case the grip exerted by its limbs on the panel enhances the reliability of the attachment.

Preferably, the channel-section member is formed as an extrusion of a resiliently deformable plastics material so that the limbs of the member grip the panel by virtue of their inherent resilience.

The means enabling communication of said at least one cavity with atmosphere prevents distortion of the panel as a result of expansion or contraction of the fluid in said at least one cavity, and condensation. Such means also allow the escape of any gases produced by the sealant.

Conveniently the passages are coupled via the end closures to a reservoir so that the passages communicate with the reservoir allowing flow of the solar energy-absorbing liquid between

the passages and the reservoir.

The reservoir is preferably large enough to store substantially all of the solar energy- absorbing liquid. The coupling of the reservoir to the passages provides a drain back system. Thus, when the pump is switched off, the solar energy-absorbing liquid is allowed to drain back from the passages in the collector to the reservoir.

Brief Description of the Drawings

The invention will now be described, by way of example, with reference to the accompanying drawings, in which:-

Figure 1 is a perspective view from below showing one end of a solar energy collector panel and its manifold or end closure embodying the invention;

Figure 2 is a sectional view showing the end closure fitted to the panel;

Figure 3 is a side view of another form of end closure according to the invention;

Figure 4 shows a solar energy collector according to the invention coupled to a reservoir to form a drainback system, as applied in a greenhouse;

Figure 5 shows a solar energy collector according to the invention coupled to a reservoir to form a drainback system as applied in a conservatory;

Figure 6 shows a graph of the temperature variation for the preferred form of collector panel; and

Figure 7 shows a graph of the efficiency of the collector.

Description

Figures 1 and 2 show a solar energy collector 10 which comprises a generally rectangular panel 12 provided at its ends with manifolds or end closures 14.

The panel 12 is an extruded plastics moulding, for example of polycarbonate, having an upper generally planar portion 16 formed with a series of parallel longitudinal cavities 18, and a lower generally planar portion 20 formed with a corresponding number of similar parallel longitudinal passages 22.

The end closures 14, of which only one is shown in the drawings, each comprises a channel- section member 24 formed as an extrusion of a preferably resiliently deformable plastics material. The member 24 has upper and lower limbs 26, 28 which are relatively thin compared with the thickness of the base 30 of the member. As shown in Figure 2, the member 24 is pushed over the relevant end of the panel 12 and the resilience of the limbs 26, 28 causes them to grip the upper and lower faces 32, 34 of the panel. The member 24 is of such a width that it does not cover the side margins of the upper and lower surfaces 32, 34 of the panel so that glazing bars can engage these margins to mount the panel 12 in position. It also leaves the longitudinal ends of the outermost passages 22 exposed as these are not used. A strip of sealant 36 is provided across the inner face of the upper limb 26 in contact with the upper face 32 of the panel and sealant 37 is provided over the whole of the inner face 46 of the lower limb 28 in contact with the lower face 34 of the panel 12 and also over the internal face of the base 30 of the member 24. The sealant seals the ends of the cavities and passages in the panel to the end closure.

Each end closure 14 is further provided with an opening 38 in its lower limb 28 forming an inlet or outlet port 40, as the case may be, for solar energy-absorbing liquid flowing through the lower portion 20 of the panel 12. The walls of the panel forming the passages 22, except those immediately adjacent to the outermost passages, are cut away as shown in Figure 1 so that all these passages 22 communicate with the inlet or outlet port 40.

Each end closure 14 also incorporates a piece of porous material such as foam plastics material 42 which is located in a groove 44 in the inner face 46 at the base 30 of the closure member 24 so as to be in contact with the ends of all the cavities 18 in the upper portion 16 of the panel 12 except, perhaps, the outermost cavities 18. The foam plastics material 42 connects with atmosphere and serves as breather foam which connects the cavities 18 with atmosphere. It allows the cavities to breathe in order to help prevent condensation.

The base 30 of each end closure forms a substantially U-shaped section with the upper and lower limbs which are substantially planar and formed by the arms of the U. The end closure is of substantially rectangular cross-section and has a thickness approximating to that of the panel thereby to form a generally flat profile with the panel.

In use the solar energy collector is mounted, for example, in the roof of a building so that the passages 22 extend vertically. The intention is that solar energy-absorbing liquid, conveniently water, will flow upwardly through the passages 22. Therefore the opening 38 in the lower closure member constitutes an inlet port and is connected to a pumped supply of water, the opening 38 in the upper closure member constituting an outlet port arranged to return the water to the supply. Preferably the water is coloured, for example by the addition of an appropriate amount of black ink to it, so as to provide shade for the interior of the building. The air in the cavities 18 in the upper portion 16 of the panel provides heat insulation for the liquid flowing through the passages 22 in the lower portion 20, these cavities 18 being allowed to "breathe" through the foam plastics material 42 in each end closure.

Figure 3 of the drawings shows another form of end closure 50 which, like the closure 14, has a member 51 with side limbs 26, 28 and a base 30 to be provided with sealant 36 and 37. In this case, however, the base 30 is formed in two parts 52 and 54 which are joined together by an integral hinge portion 56. As the closure member 51 is made of a resiliently deformable plastics material, the hinge portion 56 enables the closure to be transformed from an open position as shown in full lines in Figure 3 to a closed position as shown in dotted

lines in which the limbs 26, 28 grip the relevant end of the panel 12. The opposite faces of the portions 52 and 54 of the base 30 of the member are formed respectively with a transverse groove 60 and a projecting rib 62 arranged when the member is closed to engage the groove 50 with a snap-in fit, thereby locking the side limbs 26, 28 of the member in position gripping the panel 12.

Alternatively, the base may be formed in two separate parts which are not joined by an integral hinge. The two parts may then be secured in the closed position, for example, by use of securing means such- as screws, or a snap-fit arrangement, so that the side limbs are locked in position gripping the panel.

In the collector as described above with reference to the drawings, the upper and lower surfaces of the panel 12 are generally planar and parallel. This enables the manifold 14 to be manufactured by extrusion and cut to the desired length to be slid onto the end of the panel 12. The manifold 14 seals the end of the panel 12 except for the breather foam 42 which allows the cavities 18 to breath and therefore helps prevent condensation, and the outermost cavities 18 and passages 22 as explained earlier.

The solar energy collector has a low, flat profile which facilitates assembly and entry into roof areas. The manifold is of simple design and clamps both upper and lower surfaces of the panel 12.

Referring to Figure 4 this shows the application of a multi-wall polycarbonate solar collector, 71 similar to that described above, in a greenhouse.

Greenhouses, due to their construction, overheat in hot weather and cool down rapidly requiring night time heating and day time shading and/or ventilation. The design of the collector of the present invention can help to overcome these problems to some extent, replacing the glazing fully or as a retrofit below the existing glazing.

The collector 71, when filled with an ink/water mixture, shades the interior of the greenhouse and at the same time absorbs solar energy in the fluid. The collector is fed by means of small bore flexible tubing 72, through a pump 73. The system is a "drain back" system and has a reservoir 74 large enough to store all of the fluid within the system, when the pump is switched off to allow the fluid to drain back from the collector 71. An outlet tube 75 feeds heated fluid to a pebble bed 76, which may comprise 8mm pebbles and is typically 3 metres long x 600mm wide x 120mm deep topped up with water. Further tubing loops 77 forming a heat exchanger convey the warm fluid around the pebble bed to heat it up. The pebble bed 76 rests on a layer of insulation 78 to minimise heat losses. The upper surface of the pebble bed has a layer of black plastics covering it. This is tucked around grow bags which in the early season have the local warmth from the system to promote plant growth. The black plastics also absorbs a little extra heat, and prevents the growth of algae.

At the height of the summer when there is no need for the pebble bed to be heated but there is still need to shade the plants, the flow can be diverted by closing valve VI and opening valve V2, so diverting the warm fluid along a tube 79 into a standard high gain insulated storage cylinder 80 and returning fluid to the system by way of a tube 81.

Referring to Figure 5, multi-wall polycarbonate solar collectors 85 (only one shown) according to the invention can also be used as an integral part of a conservatory roof. Conservatories also tend to overheat in hot weather and cool down rapidly requiring night time heating and day time shading and/or ventilation. The collector can help to overcome these problems to some extent, replacing the glazing fully or as a retrofit below the existing glazing.

The system of Figure 5 is similar to that of Figure 4 and has the or each collector 85 coupled through small bore flexible tubing 86, 89 and pump 87 to a reservoir 88 which is large enough to store all of the fluid within the system. When the pump is switched off it allows the fluid to drain back from the collector 85. The outlet tube 89 feeds warm water to a heat exchanger coil 90 in a high gain fully insulated storage cylinder 91 and thence back to the

reservoir 88. Expansion of the fluid is allowed by an expansion pipe 92 and the system is controlled by a room thermostat 93 inside the conservatory.

In the situations where the collector is to be used as a retrofit below existing glazing, the upper cavities 18 may be absent.

With regard to the system of Figure 5, Figure 6 shows the variation of temperature with time for the fluid at the panel inlet, the fluid at the panel outlet, the inside air and the external air. A collector of an area of 0.8 sqm with an estimated flow rate of 1.1 L per minute for the fluid was used.

Figure 7 shows the collector efficiencies characteristics where Ti is the inside temperature and the Ta is the external, ambient temperature.