The present invention relates to a forehearth or working-end for a glass furnace and a procedure for the extraction of fumes from said forehearth.
Forehearths and working-ends are thermal machines that cool and condition the glass exiting the furnace in order to bring it to the maximum thermal homogeneity at the forehearth exit (“feeder”), where the gob is created which will be subsequently fed to the automatic forming machines that mold glass objects.
The glass exiting the furnace is at a temperature of around 1350° C., whereas at the forehearth exit it has a temperature of around 1100° C.
To determine the validity of the thermal homogeneity, use is conventionally made of the “thermal efficiency” parameter, i.e. a number, expressed as a percentage, which depends on the temperature gradients in the final section of the forehearth. Temperatures are normally measured by 9 thermocouples disposed in a grid and the differences between one value and another are calculated. The smaller these differences are, the closer the thermal efficiency is to the ideal value of 100%.
The lower the temperature gradients are, the better will be the uniformity of viscosity in the gob that enters the moulds, with consequent savings in terms of the material used and a reduction in rejects.
Thermal homogeneity of the glass gob is thus pursued because it is directly linked to the homogeneity of viscosity, lacking which the products moulded from said gob could have structural defects (e.g. non-uniform walls in the case of glasses or bottles) such that they must be rejected, or would require a larger quantity of material and thus entail a higher cost (due principally to the energy consumed to produce the glass).
According to the prior art, the forehearth comprises an understructure and a superstructure in refractory material, between which the molten glass flows, in addition to combustion and cooling systems and a supporting structure.
In particular, there exist lateral burners which heat the lateral parts of the stream of molten glass, while the central part is cooled by a flow of air, so as to seek to achieve thermal homeogeneity between the central and lateral zones of the molten glass stream. In fact, the lateral zones would tend to cool more rapidly than the central zone if there were no lateral burners and if there were no central air cooling.
The forehearth is composed of various sections, i.e. independent, mutually interconnected cooling units, each of which normally comprises the same sequence of elements.
The present forehearths present, however, some significant drawbacks.
In fact, the efficiency achieved in the best glass factories for white soda-lime glass is around 95-96% and for coloured glass it is 93%-94%, whereas it would be desirable to come closer to the limit of 100%.
Another drawback is due to the fact that cracks sometimes form in the superstructure, which over the years may lead to a failure thereof, with consequent damage to production.
Another drawback is related to the fact that the cost of refractories is high, approximately proportional to the total weight of the refractory used in the specific forehearth, and in the known embodiments considerable use is made of refractory material.
Furthermore, the cost of installing refractories is high, considering the time it takes to assemble them on site. Each day of on-site work is a lost production day. Finally, the superstructure is made up of a large number of pieces. In the best performing forehearths, in each section, besides the superstructure block, which is not standardised (it must be assembled according to a particular order defined at the “pre-installation” stage), the following types of accessories are present (in respect whereof specific reference is made to
The cost of the combustion and cooling systems is also high, because in the case of the best performing forehearths the following pipes (not illustrated) arrive in each section:
Each pipe is electronically and/or manually controlled by means of what are called combustion and cooling ramps. The cost of the electronic controller and hardware for each ramp is considerable and is approximately proportional to the ducts leading into the forehearth.
In this context, the technical task at the basis of the present invention is to provide a forehearth that overcomes the drawbacks of the above-mentioned prior art and to achieve a better extraction of fumes.
In particular, it is an object of the present invention to make available a forehearth capable of obtaining a greater thermal homogeneity of the glass.
A further object of the present invention is to provide a forehearth in which the risk of cracks in the superstructure is reduced and in which the overall use of refractory material is reduced.
Another object is to facilitate assembly of the superstructure by decreasing the number of different elements of which it is composed.
The defined technical task and the specified objects hereof are substantially achieved by a forehearth and a fume extraction procedure comprising the technical characteristics described in one or more of the appended claims.
Further characteristics and advantages of the present invention will become more apparent from the following approximate, and hence non-restrictive, description of a preferred, but not exclusive, embodiment of a forehearth, as illustrated in the appended drawings, in which
With reference to the figures, 1 indicates a forehearth or working-end for a glass furnace, in the sense that it can be used either as a working-end immediately downstream of the furnace, or as a forehearth (or number of forehearths) leading from the working-end.
Therefore, when reference is made solely to the forehearth in the description, it shall be understood to mean forehearth or working-end.
Neither the combustion and cooling systems, nor the supporting structure of forehearth are illustrated in the figures, since they are of a known type.
The forehearth 1 comprises a number of sections or modules 2, which can be of a rectilinear or curvilinear type (see
The forehearth 1, and hence the modules 2 making it up, comprise an understructure 3 in which is defined a vat 4 (preferably in high-density alumina or electro-fused refractory or refractory containing zirconium) into which molten glass flows, and a covering superstructure 5 (preferably in mullite or sillimanite).
The understructure 3 is formed of several layers of insulating material disposed in such a way that, starting from the innermost layer in contact with the vat 4 and proceeding outwardly, the layers are increasingly insulating and increasingly less resistant to high temperatures.
The understructure 3 preferably comprises at least 50 mm of microporous panel.
At the sides of the vat 4, situated immediately above the latter, there are burners (not illustrated) housed inside burner blocks, preferably chosen from among standard ones with a minimum height of 64 mm, which have the purpose of heating the lateral parts of the molten glass stream in order to maintain thermal homogeneity with the central zone, which in the meantime is cooled by introducing cooling air.
The superstructure, via protuberances 6 which extend downward, innovatively, until practically touching the surface of the molten glass, being at a distance of only 1-2 mm therefrom (unlike in the prior art, where they remain at a distance of over 50 mm from the molten glass), enables three substantially separate areas to be created: two lateral areas 7 for the combustion fumes and a central area 8 for the cooling air.
For each module 2, the superstructure 5 is substantially composed of the following elements:
The blocks 9, 10 and 11 are very similar to one another and differ substantially in that the initial block 9 is provided with an initial closing element 14 of the duct defining an air inlet opening 15, whereas the end block 11 is analogously provided with an end closing element 16 of the duct 13 defining an air outlet opening 17.
The “C” shaped elements 12 forming the duct 13 are applied on the intermediate blocks 10.
The cooling air duct 13 communicates with the central area 8 through a plurality of vertical air channels 18.
Each lateral area 7 communicates, through a plurality of vertical fume channels 19, with a corresponding fume duct 20 (right and left) defined in the blocks 9, 10 and 11.
21 indicates a hole for introducing a pyrometer or thermocouple, not illustrated, for measuring the temperature of the molten glass, according to known methods, so that there is in actual fact no passage either of air or fumes through the hole 21.
With reference to
All of the blocks 9, 10 and 11 have original lateral chamfers 24 that extend for about 30-50% of the total height of the intermediate block 10 and about 10-25% of the size of the blocks diagonal to the forehearth 1.
The innovative incorporation of the fume ducts 20 in the blocks 9, 10 and 11 of the superstructure 5, as well as the innovative presence of the chamfers 24, advantageously permit a reduction in the refractory material used—the length of the forehearth being equal—and thus cost savings; moreover, a better and more homogeneous distribution of the stresses inside the blocks is achieved (smaller variation in bending moment), with a consequent decrease in the formation of cracks and in the possibility of the superstructure collapsing.
In particular, the lateral chamfers 24 allow the removal of material from the superstructure where high mechanical strength is not required.
The central part of the blocks in fact has a greater height (compared to prior art solutions), the bending moment being equal.
Furthermore, in order to improve the distribution of internal stresses, the fume ducts 20 are defined in each initial 9, intermediate 10 or end 11 block, in the upper part of the block itself, i.e. the distance (d1) between an upper edge of the fume ducts 20 and an immediately upper edge of each block, is less than the distance (d2) between a lower edge of the fume ducts 20 and an immediately lower edge of each block.
The “Venturi block” 22 illustrated in
Inside the Venturi block 22 there is defined a chute 23 for conveying cooling air toward to the air outlet opening 17 present in the duct 13.
The Venturi block is in fact open at the top to create a continuity between the duct 13 (defined by the “C”-shaped elements 12) and the outlet opening 17 defined in the end closing element 16 of the end block 11.
Furthermore, at the upper opening of the Venturi block 22 there is defined a lateral slit 25 communicating with the chamber 26 that joins the fume ducts 20.
As a result, the air that exits through the opening 17 will automatically entrain the fumes as well, and the extraction of fumes will increase as the degree of cooling increases.
Thanks to this solution, it is possible to eliminate the fume and air pressure control systems of traditional forehearths and to eliminate the air and fume chimneys, as well as the associated air curtains, i.e. it is possible to dispense with the elements A, B, C and D of
Advantageously, the forehearth of the present invention can achieve an efficiency of up to 98% for coloured soda-lime glass and 99% for white glass.
This efficiency is the consequence of a variety of factors:
The present invention also achieves a reduction in cracks (as a result of the improved distribution of internal stresses) and in the use of refractory material (the fume ducts 20 having been incorporated in the blocks 9, 10 and 11), and thus a reduction in costs as well.
Moreover, the superstructure is extremely easy to assemble, being composed of only three types of blocks (initial, intermediate and end) and a smaller number of accessory components (“C”-shaped elements, Venturi block), without there being any need to use air chimneys, fume chimneys, “L”-shaped blocks, fume duct closing triangles or air duct closing rectangles, all of which are envisaged by the prior art.
The combustion and cooling equipment is also reduced, because the only pipes arriving at the forehearth are the cooling air duct and combustion mixture pipes, the air curtain pipes envisaged by the prior art being no longer necessary.
Number | Date | Country | Kind |
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PR2008A000050 | Aug 2008 | IT | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/IB09/53290 | 7/29/2009 | WO | 00 | 1/26/2011 |