Device and process for the remelting of glass

Abstract

The invention relates to a device for the remelting of glass bars:

Description

[0001] The invention relates to a device and to a process for the remelting of glass semifinished products. It is a matter here of glass semifinished products that are present in the form of bars. The bars have mostly a circular cross section. The remelting of such glass semifinished products is necessary for the further processing. It is associated mostly with a portioning of glass.

[0002] In principle glass--either pre-portioned or in relatively large quantities--can be melted with the necessity of a subsequent portioning.

[0003] The process of the remelting of portioned glass is problematical. From a certain temperature onward, namely, there occurs an adhesion of the glass to the underlayer or, respectively, to the forming tool. The co-called adhesion temperature (1010 dPas) lies below the softening temperature (107.6 dPas), so that in the remelting there occurs a adhesion of the glass to the wall of the melting vessel.

[0004] There could be considered cooling the wall, so that in the wall zone the adhesion temperature is not reached. But in the heating-up process the cooling cannot be strong enough for the contact temperature to remain below the adhesion temperature. Furthermore, there occur excessively great inhomogeneities of the temperature.

[0005] As remedy, work is being done with separating agents of various type. These lead, however, to undesired alterations of the glass surface.

[0006] The other possibility lies then in melting larger quantities and then portioning them. There the glass semifinished product is usually prepared not in the form of regular bodies, but it can be melted-up in the crucible as glass fragments. In the first place, however, this process is in general a discontinuous one; continuous processes require special measures and therewith special expenditures. In the second place, here in all cases hollow-space forms, which are filled with air or another gas. To the glass fragments adsorbed gas adheres. When the fragment surfaces pass into the melt, then the adsorbed gas is released from the fragment surfaces, and bubbles form. In order to remove these bubbles again from the melt, a strong increase of the melt temperature to refining temperature is necessary. This means that the melting processes must be run through once again. This is highly unfavorable and uneconomical energy-wise.

[0007] It is also possible, when using glass bars, to heat up the free bar end and therewith to do the melting. There, to be sure, the above-mentioned problems do not arise. Here, however, there occurs a continuous run-off of the glass in the form of a downward-tapering glass stream. A drop-portioning is not possible.

[0008] JP 63/236729A shows a device with which a glass fiber is drawn. At the outlet of a revolving nozzle there arises a “draw onion” (Ziehzwiebel). This device, therefore, does not serve for the remelting and portioning of glass bars.

[0009] Underlying the invention is the problem of providing steps with which a remelting and portioning of glass semifinished material is possible without there arising the problems of adhesion, of alteration of the glass surface, or of the gas inclusion; further, an energy-wise and economically favorable process is to be given, with which semifinished material can be rewarmed and made available for the shaping.

[0010] This problem is solved by the independent claims. The solution is very simple and requires a relatively slight expenditure.

[0011] One proceeds, accordingly, from a receiving shell which has an upper receiving opening for the introduction of a glass bar, and a lower outlet opening. To the shell there is assigned a crucible. The crucible is open at the top, so that the shell can plunge, at least in a part of its length, into the space enclosed by the crucible wall. The crucible has a runoff in its lower region. There, any type of crucible heating is possible, for example a resistance heating and a radiation heating. An advantageous form of execution is the providing of a coil which surrounds the wall of the crucible in a known manner. The coil serves for the coupling of electric energy into the crucible contents.

[0012] The shell is suitably designed and dimensioned in such manner that its inner contour corresponds to the outer contour of the glass bars to be processed. The shell does not absolutely have to be vertical. It can also be slanted with respect to the vertical. Furthermore, instead of one shell there can also be provided several shells.

[0013] By corresponding allocation of shell and crucible it is achieved that the glass bar in the shell melts at its lower end. In the crucible itself there was previously melted up a glass bath. The glass bar melts off slowly at its lower end. The melting-off and flowing-off material passes continuously into the bath mentioned, present in the crucible.

[0014] When energy costs play no role, then the semi-finished products can simply be melted up again below, refined at low viscosities and then fed to the shaping operation. This heating to melting or refining temperature can be eliminated by the invention. The advantage becomes clear if one considers that the refining temperature can lie at ca. 1600° C., for the shaping, however, only temperatures on the order of 1100° C. are necessary.

[0015] What is essential for the device in its general form is merely that the receiving shell be arranged over a container that contains a glass melt. The glass melt is portioned-- possibly only after further transport. Also an intermediately engaged homogenization step is conceivable. This becomes necessary if the introduced glass is a glass other than that which is present in the container.

[0016] An essential advantage of the process of the invention for the remelting and portioning is the continuity through the steady following-up of the glass bars. There the shape of the glass bar ends to be added to one another is decisive in respect to the avoiding or minimizing of bubble inclusions.

[0017] Untreated bar ends, by reason of shrinkage in the production, have a concave curvature. The setting on one another of two such ends would lead to a gas inclusion in the cavity arising between the ends, which would later become visible in the feeder as bubble thrust, therefore spoilage.

[0018] A bar end is easily influenceable by the casting mold used for the production. The shaping of the (other) bar end must occur by mechanical reworking and is expensive. But at least it is possible, if necessary, to free it from the concave curvature in this way. As suitable pairs of bar ends there have proved the combinations in which the gas to be expelled can escape and is not trapped.

[0019] If the same amount of melt that is removed in a portioned manner is added to the crucible, then the volume of the melt in the crucible remains constant. The level of the melt, therefore, likewise remains constant. If these conditions are maintained, then no level re-setting of the receiving shell is necessary.

[0020] For reasons of energy saving the volume of the crucible should be just as great as that of the required portions being processed. Any increase of this volume is unfavorable in respect to the energy saving of the process.

[0021] The invention is explained in detail with the aid of the drawing. The drawing shows in vertical section an arrangement for the remelting of glass bars.

[0022] There is perceived in particular the following:

[0023] A receiving shell 1 is provided. This is vertically arranged in the present case. It is open at the top for the reception of a glass bar 2. At its lower end it is first tapered into a truncated conical part 1.1 and then goes over into a cylindrical part 1.2.

[0024] A crucible 3 is further provided. The crucible is pot-shaped. It has a bottom 3.1 as well as a cylindrical wall 3.2. The crucible has in its bottom a runoff in the form of a runoff shell 3.3. To the runoff shell 3 there is assigned a heating arrangement 4.

[0025] The cylindrical wall 3.2 of the crucible 3 is surrounded by a medium frequency coil 5. Over this coil electric medium-frequency energy is coupled into the crucible contents. Through the warmed crucible wall and the warmed glass bath the receiving shell 1 is warmed by heat radiation over the crucible wall and the glass bath, especially its lower region.

[0026] The receiving shell 1 is produced in the present case from platinum with a wall thickness of 1 mm. The receiving shell is adjustable in its height. The melt-off amount is regulated over the height adjustment of the receiving shell 1.

[0027] The device of the invention operates as follows:

[0028] Into the receiving shell 1 there is introduced a glass bar 2. The inner contour of the receiving shell 1 and the outer contour of the gas bar are such that the glass bar 2 is snugly enclosed by the receiving shell 1. The temperature generated by the coil 5 in the crucible 3 is controlled in such manner that the glass bar 2 melts at its lower end and supplies the melt bath 7 setting in a controlled manner with after-flowing glass. There the lower end of the receiving shell, especially the zone of the truncated conical part 1.1 and of the cylindrical part 1.2 is heated by the radiant heat from the wall 3.2 of the crucible 3 as, well as by the liquid level surface 7.1 of the melt bath. Also the receiving shell 1 can be adjusted in its height. The under edge of the receiving shell will have, as a rule, a distance of 1 to 2 cm from the surface 7.1 of the melt bath. Even a plunging of the cylindrical part 1.2 into the melt bath 7 is thinkable. In accordance with the distance, the melt-off performance and therewith the throughput can be varied.

[0029] The glass bar 2 sinks by its own weight deeper and deeper into the receiving shell 1, until it is largely melted up. Before it is completely melted up, a following glass bar can be introduced from above into the receiving shell 1. The glass melt can thereby continuously be provided with glass. The runoff shell 3.3 of the crucible may be equipped with a needle feeder arrangement. Therewith it is possible to control the glass throughput throughout the device in a desired manner. The runoff shell 3.3 may also be provided with a shearing device in order to generate glass drops for the following production steps.

[0030] The device can be used everywhere where, for a following hot-shaping process there is needed glass which must be brought to high temperatures lying above the adhesion temperature. With the device there are avoided all the problems of the state of the art. There does not occur any adhesion of glass to the walls of a shaping arrangement. No separating agent is needed. The glass surface is subject to no alteration. No after-engaged refining process is needed.

[0031] The device represented comprises a needle feeder 6.

[0032] The crucible represented in the present case is a platinum crucible. The induction heating has a power of 10 kHz. Instead of this there would also be conceivable a 50 Hz resistance heating or a radiation heating.

Claims

1. Device for the remelting of glass bars (2); 1.1 with at least one receiving shell (1) which has an inlet at its upper end for the receiving of the glass bar (2), and an outlet at its other end for the running-off of the melt; 1.2 with a crucible (3) which is located underneath the receiving shell (1), is open at the top and has a runoff (3), at its bottom; 1.3 with a heating arrangement (5) for heating the crucible contents; 1.4 the under-edge of the receiving shell (1) is located, for the avoidance of a tapering of the glass stream, at the height of the liquid level (7.1) of the melt bath (7) or above it; 1.5 following the crucible (3) there is engaged a runoff shell (3.3); 1.6 to the runoff shell (3.3) there is assigned an arrangement for the generation of drops (needle or suction feeder).

2. Device according to claim 1, characterized in that the heating arrangement for the heating up of the crucible contents comprises a coil (5) for the coupling-in of electric energy.

3. Device according to claim 1 or 2, characterized in that the receiving shell (1) and the crucible (33) are arranged relatively to one another in such manner that the receiving shell (1) is enclosed by the crucible wall (3.2) at least on the lower part of its length.

4. Device according to one of claims 1 to 3, characterized in that the outlet zone (1.1, 1.2) of the receiving shell (1) is tapered continuously or abruptly in the running out direction.

5. Device according to one of claims 1 to 4, characterized in that the cross section contour of the inner surface of the receiving shell (1) is at least approximately equal to the cross section contour of the outer surface of the glass bar (2).

6. Device according to one of claims 1 to 5, characterized in that the heating arrangement (4) is assigned to the runoff shell (3.3.).

7. Device according to one of claims 1 to 6, characterized in that the runoff shell (3.3) is offset with respect to the receiving shell (1).

8. Device according to one of claims 1 to 7, characterized in that the receiving shell (1) is adjustable i n its position relatively to the crucible (3), especially in its height.

9. Process for the remelting of glass bars, with the following features: 9.1 A glass bar (2) is introduced into the upper end of a receiving shell (1); 9.2 underneath the receiving shell (1) there is made available a molten bath (7) with a surface (7.1); 9.3 the receiving shell (1) is positioned in such manner that its lower edge is located at the height of the surface (7.1) or above it; 9.4 the lower end of the glass bar (2) is heated to a temperature above the softening temperature of the glass; 9.5 the melt-off process is controlled in such manner that a continuous melt stream enters the molten bath (7) with avoidance of a constriction; 9.6 melt is drawn off from the molten bath (7) by means of an arrangement for drop generation.

10. Process according to claim 9, characterized in that the melting-off of the glass bar (2) is performed by the coupling of electric energy into the crucible unit or by radiation heating elements, or by burner (blowpipe) heating.

11. Process according to claim 9 or 10, characterized in that the glass throughput is controlled by the means that at least one of the following parameters is altered: by the amount of the supplied energy; by the spacing between the under edge of the receiving shell (1) and the liquid surface (7.1) of the molten bath (7); by a choking of the glass stream emerging from the bath (7).

12. Process according to one of claims 9 to 11, characterized in that the glass bars (2) used have in each case at least one end which closes off with a convex form (for example a cone, a hemisphere) or with a flat surface, in order to avoid an inclusion of gas at the bar-to-bar impact point.