METHOD FOR PRODUCING A GLASS PRODUCT AND GLASS PRODUCT OBTAINED BY THE METHOD

Abstract

A method for producing a glass product having a low bubble content from a melt is provided, wherein the melt at least partly comes into contact with a noble metal-comprising component.

Claims

1. A method for producing a glass product having a low bubble content from a melt, comprising: contacting the melt with a noble metal-comprising component at a location, the melt having a temperature-dependent oxygen partial pressure that varies locally over a volume of the melt up to a critical value; and implementing, at the location where the noble metal-comprising component is in contact with the melt, at least one measure, only locally, on the noble metal-comprising component, the at least one measure being selected from the group consisting of: coating a side of the noble metal-comprising component that faces away from the melt; exposing the side of the noble metal-comprising component that faces away from the melt to a water-containing atmosphere; and increasing a thickness of the noble metal-comprising component.

2. The method as claimed in claim 1, wherein the coating is a glass.

3. The method as claimed in claim 1, wherein the water-containing atmosphere is a water-containing protective gas atmosphere.

4. The method as claimed in claim 1, wherein the water-containing atmosphere comprises N.sub.2 and/or noble gas.

5. The method as claimed in claim 1, wherein the critical value is between 0.8 bar and 1.2 bar.

6. The method as claimed in claim 1, wherein the critical value is between 0.9 bar and 1.1 bar.

7. The method as claimed in claim 1, further comprising initially identifying the location at the noble metal-comprising component where the oxygen partial pressure locally reaches the critical value.

8. The method as claimed in claim 1, wherein the noble metal-comprising component comprises a stirring crucible having a tubular inlet and an outlet, and wherein the step of implementing the at least one measure is performed at the inlet and/or at the outlet.

9. The method as claimed in claim 1, wherein the noble metal-comprising component comprises one or more noble metals selected from the group consisting of platinum, rhodium, iridium, osmium, rhenium, ruthenium, palladium, gold, silver, and mixtures or alloys thereof.

10. The method as claimed in claim 1, further comprising adjusting a dew point in the water-containing atmosphere to between 20° C. and 90° C.

11. The method as claimed in claim 1, further comprising adjusting a dew point in the water-containing atmosphere to between 20° C. and 70° C.

12. The method as claimed in claim 1, further comprising adjusting a dew point in the water-containing atmosphere to between 30° C. and 65° C.

13. The method as claimed in claim 1, wherein the water-containing atmosphere has a temperature-dependent oxygen partial pressure of less than 0.1 bar.

14. The method as claimed in claim 1, wherein the water-containing atmosphere has a temperature-dependent oxygen partial pressure of less than 0.01 bar.

15. The method as claimed in claim 1, wherein the water-containing atmosphere has a temperature-dependent oxygen partial pressure of less than 0.001 bar.

16. The method as claimed in claim 1, further comprising forming the melt so that the glass product is a product selected from the group consisting of a glass tube, a glass rod, and a sheet glass.

17. The method as claimed in claim 1, further comprising forming the melt so that the glass product comprises a glass selected from the group consisting of a borosilicate glass, an alkaline earth-free or an alkaline earth-containing borosilicate glass, an alkali-alkaline earth silicate glass, a boron-free glass, a boron-free neutral glass, a low-alkali glass, an alkali-free glass, a low-arsenic glass, and an arsenic-free glass.

18. The method as claimed in claim 1, further comprising forming the melt so that the glass product comprises a glass pharmaceutical package.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0063] The invention will now be explained in more detail with reference to drawings, wherein:

[0064] FIG. 1 schematically illustrates water decomposition at the interface between noble metal-comprising component and glass;

[0065] FIG. 2a shows local critical oxygen partial pressures for the transition region from the trough to the crucible and in the crucible for a specific production system;

[0066] FIG. 2b shows local oxygen partial pressures as contour lines for the transition region from the trough to the crucible and in the crucible for a specific production system; and

[0067] FIG. 3 shows the profile of oxygen partial pressure at the component-crucible interface when flushed with different carrier gases.

DETAILED DESCRIPTION

[0068] FIG. 1 schematically illustrates the process of water decomposition at the interface between a component comprising noble metal and a glass melt. Both thermodynamic and kinetic factors must be considered.

[0069] By way of example, the gas chamber 1 located on the side of the noble metal-comprising component 2 facing away from the glass melt is illustrated on the left, and also illustrated is the zone of glass melt 3. For example, the noble metal-comprising component may comprise platinum or may be made of platinum.

[0070] In terms of thermodynamics, the driving force of water decomposition is determined by the contents of oxygen and water, both in the gas and in the melt. The locally prevailing actual oxygen partial pressure is thereby substantially influenced by the diffusion properties of the relevant components in the glass melt, for example the redox-active components, and by the diffusion of hydrogen through the noble metal-comprising component. If, owing to the complex processes which result from the particle flows of, e.g., water, the redox-active components, oxygen, and hydrogen, the oxygen partial pressure becomes too high locally, oxygen bubbles will arise locally.

[0071] FIGS. 2a and 2b illustrate, by way of exemplary schematic views, the local oxygen partial pressures arising in a glass melt at a noble metal-comprising component. Here, the case of producing glass tubes from an alkaline earth-containing borosilicate glass was considered, by way of example.

[0072] In this exemplary case, the noble metal-comprising component is provided in the form a stirring crucible having a lateral inlet and an outlet at the bottom. The stirrer shaft and stirring blades are not shown. By way of example, a glass composition according to Exemplary Embodiment 7 was considered.

[0073] More generally, however, without being limited to the example of the glass tube made of alkaline earth-containing borosilicate glass which is considered here, the method of the present invention is likewise useful for producing sheet glass or glass rods. Other glasses, for example boron-free, alkali-free, and/or alkaline earth-free glasses, can also be produced by the present method.

[0074] FIG. 2a illustrates regions 4 of critical oxygen partial pressures. Here, the regions 4 at the component, in which the oxygen partial pressure assumes critical values are indicated by arrows.

[0075] FIG. 2b is a further view of the noble metal-comprising component. Here, the oxygen partial pressures prevailing on the noble metal-comprising component are shown by way of example, with regions of equal pressures being marked by “contour lines” as shown by the scale on the right side of FIG. 2b.

[0076] It can be clearly seen from both views that a critical increase in oxygen partial pressure is existent only at a few locations in the present example. Therefore, an appropriate countermeasure for reducing water decomposition and hence the oxygen bubbles resulting therefrom has to be taken only at these sites.

[0077] It is particularly advantageous if gases are used which include no H.sub.2 at all. Otherwise, in noble metals which exhibit high H.sub.2 resorption capability, for example platinum or platinum-containing alloys, the hydrogen, through diffusion processes, could even reach the locations at the component-glass melt interface where no critical oxygen concentrations are prevailing. A drawback thereof would be that hydrogen could react with redox-active substances in the melt, such as iron or sulfur impurities or oxidic refining agents such as SnO.sub.2, and could cause alloying of the noble metal especially at locations of the component which are non-critical in terms of oxygen bubble formation, which alloying would reduce the service life of the component.

[0078] The preferred countermeasure for suppressing locally limited oxygen bubble formation consists in glazing of the noble metal-comprising component. If this is not possible for reasons of mechanical stability, the preferred countermeasure consists in a locally limited supply of water on the outer surface of the noble metal-comprising component. In this case, it is particularly preferred to utilize a carrier gas that is moisturized in controlled manner, i.e. a gas with a dew point adjusted in controlled manner. By selectively adjusting the dew point, the effect of the supplied water can be controlled selectively, and on the other hand it is possible to minimize the formation of volatile noble metal oxides by controlling the oxygen content. For this purpose, the O.sub.2 content of the carrier gas can be monitored using an atmosphere sensing ZrO.sub.2 probe.

[0079] FIG. 3 shows, by way of example, the profile of oxygen partial pressure at the component-glass melt interface during flushing with different carrier gases.

[0080] The left y-coordinate represents the oxygen partial pressure at the noble metal-comprising component. Curve 5 shows the oxygen partial pressure in the melt at the interface between component and glass melt as a function of time indicated along the x-axis.

[0081] Curve 6 gives the temperature profile at the component-glass melt interface over time, the temperature being represented by the right y-coordinate, in ° C.

[0082] It can clearly be seen that moistened air may lead to a non-critical oxygen partial pressure of less than 0.1 bar at the component-glass melt interface, when the dew point is appropriately high (see sections 51 of curve 5). In the present example, the dew point was set to 60° C. When flushing is changed from moistened air to moistened nitrogen and the dew point remains the same, i.e. also 60° C. in the present case by way of example, the oxygen partial pressure at the interface between the component and the glass melt will further decrease markedly, as can be seen from section 52 of curve 5.

[0083] This illustrates that the use of a moistened carrier gas which itself does not contain molecular oxygen has two advantages. On the one hand, the lowering of the local oxygen partial pressure at the interface between component and glass melt is more pronounced. On the other hand, oxidation of the at least one noble metal in the noble metal-comprising component is drastically reduced on the outer surface of the component, that is on the side facing away from the melt. This results in a longer service life.

[0084] If the locally delimited sites at the noble metal-comprising component which have to be appropriately protected are known, the use of the moistened carrier gas can be limited to these locations. In addition, the noble metal may be further protected locally at these sites by particularly effective coatings or by a locally limited increase of the wall thickness. If the increase in wall thickness has to be provided only locally, however, even cost-effectiveness of such a measure is given.

[0085] Thus it is possible according to the method to both reduce or even completely suppress the formation of oxygen bubbles and on the other hand maximize the service life of the noble metal-comprising component, by a combination of determining the locally delimited sites at which a critical increase of the oxygen partial pressure arises and therefore increased bubble formation occurs, and the countermeasures which then only have to be implemented locally.

LIST OF REFERENCE NUMERALS

[0086] 1 Gas chamber [0087] 2 Noble metal-comprising component [0088] 3 Glass melt zone [0089] 4 Regions of glass melt with oxygen partial pressure critical for bubble formation [0090] 5 Curve of oxygen partial pressure at the component-glass melt interface versus time [0091] 51 Section of curve 5 with air as the carrier gas [0092] 52 Section of curve 5 with nitrogen as the carrier gas [0093] 6 Curve of temperature at the component-glass melt interface versus time