The present invention relates to an annular burner assembly.
Such a burner assembly is employed, for example, in a Stirling engine in which the burner is arranged to surround the head of a Stirling engine.
The burner is supplied with a gas/air mixture which is ignited at a burner mesh. The gas is typically natural gas, biogas or some other methane rich fuel. The flow of the mixture of gas/air which is supplied is turbulent in nature which will impair its flow to the burner mesh. Also, the burner mesh must be maintained at a temperature at which the material of which it is constructed does not degrade (typically at around 1050° C.). In addition, by keeping the burner cool, emissions can be minimised, particularly those of oxides of nitrogen.
According to a first aspect of the present invention there is provided an annular burner assembly centred on a main axis, the assembly comprising an annular burner mesh, an annular gas/air supply duct to supply a combustible gas/air mixture to the burner mesh in a substantially axial direction, and a flow modifier in the vicinity of the burner and having a plurality of fins each extending in a substantially radial plane to define a plurality of axially extending passages arranged circumferentially around the supply duct to substantially laminarise the gas/air mixture, the fins providing a thermal link from the burner to a location radially away from the burner.
By providing a flow modifier in the vicinity of the burner, the flow to the burner is substantially laminarised. Also, the fins provide a thermal link from a position adjacent to the burner mesh to a location radially away from the burner thereby promoting the flow of heat away from the surface of the burner helping to maintain the burner at an acceptable temperature.
The flow modifier may either be positioned in substantially the same radial plane as the burner mesh. Alternatively, it may be positioned immediately upstream of the burner mesh. Alternatively, the flow modifier may be arranged in an intermediate position which is partly in the same radial plane as the burner mesh and partly upstream of the burner mesh.
The flow modifier may be formed as an outer ring to which the fins are fixed in order to provide the plurality of passages. However, preferably, the flow modifier is formed of a single corrugated member. This greatly simplifies the structure of the distribution ring.
If the distribution ring is axially offset from the burner, then the exact configuration of the corrugations is relatively unimportant as the gas/air mixture can pass either side of the corrugated member. However, when the flow modifier is positioned in substantially the same radial plane as the flow burner mesh, the space on the radially outwardly facing side of the corrugated member is dead space as the gas/air in this space cannot directly reach the burner mesh. Therefore, preferably, the corrugations are arranged such that the space between adjacent corrugations on the radially outwardly facing side of the corrugated member is minimised. Ideally, this space is eliminated. With such a configuration, the corrugated member will generally resemble an annular member with radially inwardly extending fins as mentioned above.
Preferably, a perforate flow distribution ring is provided at the radially innermost edge of the plurality of passages and in close proximity to the radially outer surface of the burner mesh. This further ensures the even distribution of the gas/air mix to the burner mesh.
Examples of burner assemblies in accordance with the present invention will now be described with reference to the accompanying drawings, in which:
In order to laminarise the generally turbulent flow in the annular duct 3, a flow modifier is provided. This may either be in the same radial plane as the burner mesh 4 as depicted at 7A in
The configuration of the flow modifiers is described in more detail with reference to
In use, the heated gas/air mixture flows axially along passages 11 between fins 9 and out through distribution ring 10 to the burner mesh 4. The fins 9 serve a dual function of laminarising the flow immediately upstream of the burner, and also serving to convey heat from the burner mesh radially outwardly towards the outer wall of the inlet duct 3.
In common with
Number | Date | Country | Kind |
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0522309.4 | Nov 2005 | GB | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/GB2006/004039 | 10/27/2006 | WO | 00 | 3/20/2009 |