The invention relates to a tip plate for a bushing for receiving a high temperature melt and a corresponding bushing. The term “receiving” includes all kinds of preparing, storing and treating melts. In particular the bushing and its tip plate are intended for use in the production of fibres, such as glass fibres, mineral fibres, basalt fibres etc.
Prior art and the invention will be described hereinafter in more detail with reference to the production of and an apparatus for producing glass fibres, including textile glass fibres, although not limited to such use.
Glass fibres have been manufactured from a glass melt by means of bushings for more than 100 years. A general overview may be derived from “Design and Manufacture of Bushings for Glass Fibre Production”, published by HVG Hüttentechnische Vereinigung der Deutschen Glasindustrie, Offenbach in connection with the glasstec 2006 exhibition in Dusseldorf.
A generic bushing may be characterized as a box like melting vessel (crucible), often providing a cuboid space and comprising a bottom, the so called tip plate, as well as a circumferential wall.
A generic tip plate comprises a body between an upper surface and a lower surface at a distance to the upper surface as well as a multiplicity of so-called tips (also called nozzles and/or orifices), extending between the upper surface and the lower surface and through said body, through which tips/nozzles/orifices the melt may leave the bushing, in most cases under the influence of gravity.
The tip plate requires high temperature resistant and thus expensive materials like precious metals to withstand the high temperature melt (e.g. up to 1700° C.). The design and arrangement of the nozzles in a generic tip plate varies and depends on the local conditions in a glass fibre plant and on the target product. While the tips often have an inner diameter of 1-4 mm and a length of 2-8 mm, the number of tips of one tip plate may be up to a few thousand. In various embodiments the tips protrude the lower surface of the tip plate—in the flow direction of the melt, being the z-direction during use—.
Several attempts have been made in the past to arrange as many tips as possible per unit area to reduce the quantity and thus the costs of the precious metals required to manufacture a tip plate with a certain number of tips. The number of tips (with corresponding flow-through openings) per unit area has been referred to in prior art as the “packing density” of the tip plate.
To realize a high packing density U.S. Pat. No. 5,062,876 A discloses a tip plate, wherein the lower end of the tips is substantially a regular polygon in shape. The realization of regular polygonal shapes in connection with tips welded to a tip plate is difficult with conventional manufacturing techniques, leads to an irregular flow of a glass melt through such orifices and causes difficulties in heat dissipation.
For example: the speed of the fibres drawn from such an orifice (tip, nozzle) downwardly may be around 1000 meters per minute and allows the formation of very thin continuous glass fibre filaments with diameters of even less than 50 μm, often 4 to 35 μm.
It is an object of the invention to overcome as much as possible of the known drawbacks and in particular to provide a tip plate with a high packing density (and thus a favorable relation: number of tips/required precious metal mass), an excellent service life and/or allowing a glass fibre production of high uniformity and quality.
The invention is based on the following findings:
One limiting factor to achieve higher packing densities (of tips) compared with prior art tip plates is the arrangement of nozzles (tips) and thus the arrangement of the flow-through openings at the upper surface of the tip plate. This is true in particular if the tips are fixed to the tip plate by welding or punching. In its use position this upper surface is fully covered by the glass melt and the hydrostatic pressure is high as the bushing comprises a certain volume of said glass melt.
Typically the tips are arranged one behind the other in a row, i.e. side by side with their central longitudinal axes intersecting a common virtual straight line. At least a further multiplicity of tips is arranged along at least one further (common) virtual straight line in a further row and the lines (rows) extend parallel to each other, altogether forming a group of tips. A third, fourth etc. similar arrangement may be added. Several groups are spaced to each other so that a so called cooling fin may be arranged at the lower surface of the tip plate and between adjacent groups. The tips may also be arranged as double, triple, quadruple etc. rows with intermediate cooling fins.
To allow high melt flow rates through the tips of the tip plate, relatively large flow-through orifices at the upper surface of the tip plate may be used. To avoid a contact between melt particles (drops) deriving from adjacent tips at their opposite (lower, exit) end, the respective distance between adjacent tips at their lower end (in the operating position) should be as large as possible. A larger distance at the melt outlet end of the tips further allows an improved cooling around the tips. The combination of these design features at both ends of the tips leads to a synergetic behavior with respect to production rate and production reliability, melt flow characteristic and fibre quality. A corresponding design also leads to a high packing density and a high flow rate of the melt through the tips.
While the minimum distance between adjacent virtual straight lines at the upper surface of the tip plate is defined by an arrangement wherein adjacent orifices touch each other at corresponding points at their outer periphery, the maximum distance must be smaller than the diameter of the respective orifices at the upper surface. Correspondingly orifices which are arranged along different virtual lines but adjacent to each other lead to an “overlap” as will be described in further detail hereinafter.
Due to manufacturing reasons (notwithstanding manufacturing tolerances or limits) and the required quality of glass fibres it is assumed that the majority of tips (>50%, often >70%, >80%, >90%) are of substantially same dimensions, especially their flow through openings are of the same design and cross-section. This is in particular true for the tips arranged along a central section of the tip plate.
There is a geometric relation between the distance of adjacent lines of tips (orifices), the diameter of the tips (orifices), in particular at the upper surface of the tip plate, and the distance of adjacent tips. For example: if the distance between the virtual straight lines mentioned is larger than the diameter of the tips at the upper surface, the packing density worsens characteristically. The same is true if the distance between adjacent tips of one line is enlarged to an extent that the same distance to a tip of the adjacent line would require a distance between the two lines of larger than the diameter of the tips at the tip plate surface.
The volumetric flow through a cylindrical pipe (here: the flow-through opening of a tip) can be calculated according to the Hagen-Poiseuilles equation for laminar flow:
wherein
Correspondingly the mass flow rate Ps of the melt is calculated as
with
In case of a non circular cross section of the pipe (flow-through opening) the following geometry factor Q replaces D4/L:
for frustums, wherein d1 defines the larger diameter, d2 the smaller diameter and L is again the length of the tip, all in m (Meter).
Notwithstanding that external effects like temperature, environmental turbulences etc. are not regarded in this equation it may be used for the calculation of tips according to the invention.
With respect to the present invention an important finding is to set the distance of the central longitudinal axes of the tips in relation to the mass flow rate, in other words: to make the distance as small as possible while keeping the mass (melt) flow rate constant.
In its most general embodiment the invention relates to a tip plate for a bushing for receiving a high-temperature melt, comprising—in its operational position—an upper surface, which extends in two directions (x,y) of the coordinate system, a lower surface at a distance to the upper surface and a body in between, as well as a multiplicity of tips with flow-through openings of substantially circular cross-section in the x-y-directions and their largest diameter (dmax) adjacent to the upper surface of the tip plate, which tips extend from the upper surface through the body and protrude the lower surface and through which the high-temperature melt may leave the tip plate in a third (z) direction of the coordinate system, wherein
A distance dL=0,866 dmax and distances dT1 and dT2=1 dmax define an arrangement with which adjacent tips touch each other at one point on their outer periphery.
A distance dL=dmax defines the farthest distance between two adjacent virtual lines which allow at least a point contact between adjacent tips of two lines.
Upper limits of dL may also be set at <1.0, <0.97 or <0.95.
While the invention refers to tips with flow-through openings featuring a substantially circular cross section in an x-y-direction, this includes exactly circular cross sections and in an embodiment flow through openings featuring slightly different cross sectional profiles but with a substantially overall circular profile, e.g. polygonal profiles, which will work as well. In this context the dimensions of a typical tip plate are of importance:
As far as the invention refers to “substantially circular cross-section”, this is not to be understood in an exact geometric sense but technically. In case of a slightly non-circular cross section the (one) “diameter” will be replaced by the so called diameter equivalent.
With respect to the arrangement of the tips along a virtual straight line it may be understood that a distance of central longitudinal axes of adjacent tips of slightly less than 1.0 dmax (in particular down to a minimum of 0.9 dmax) are possible as well, although this leads to a certain intersection of adjacent circular openings of adjacent tips at the upper surface of the tip plate and thus to certain irregularities in the melt's flow behavior along respective cross sections of such tips (nozzles).
The invention also provides a manufacturing technique, namely additive manufacturing, which allows high precision designs and a further flexibility and freedom with respect to tip geometry. In particular the tip plate may be manufactured as one monolithic part, i.e. with tips (nozzles) which are shaped together with the tip plate body. This has considerable advantages over welding or punching technologies to shape the tips.
Optional features of the invention include the following, either individually or in connection with other features as long as technically feasible:
Finally the invention also relates to a bushing for receiving a high-temperature melt and comprising a tip plate in its broadest embodiment and optionally including one or more features as mentioned before. The bushing may also be made partly or completely by additive manufacturing.
Further features of the invention may be derived from the sub-claims and the other application documents. The inventions will now be described with reference to the attached drawing, showing in a very schematic way in
The tips TI extend downwardly from the upper surface US, thereby penetrating a body BO of the tip plate TP (of thickness d) and protruding downwardly from a lower surface LS of the tip plate TP as shown in
The embodiment of
In the upper part of
In the lower part of
Between the upper and lower part of
All tip plates TP and associated parts have been manufactured by additive manufacturing, using a PtRh 90/10 alloy to provide a monolithic tip plate TP.
Number | Date | Country | Kind |
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102020005323.8 | Aug 2020 | DE | national |
Filing Document | Filing Date | Country | Kind |
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PCT/EP2021/073063 | 8/19/2021 | WO |