U.S. patent application number 11/888745 was filed with the patent office on 2007-11-22 for method and a device for the refining of glass.
This patent application is currently assigned to PLAYTEX PROCUCTS, INC.. Invention is credited to Wolfgnag Schmid Bauer, Werner Kiefer, Erich Rodek, Hilgegard Romer, Gunter Weidmann.
Application Number | 20070266737 11/888745 |
Document ID | / |
Family ID | 7653754 |
Filed Date | 2007-11-22 |
United States Patent
Application |
20070266737 |
Kind Code |
A1 |
Rodek; Erich ; et
al. |
November 22, 2007 |
Method and a device for the refining of glass
Abstract
A device for the refining of a glass melt at high temperatures
according to the skull pot principle is provided. The device
includes a skull crucible having walls that are constructed from a
plurality of pipes, a high-frequency coil for coupling electrical
energy into the contents of the skull crucible, and an inlet and an
outlet of the skull crucible being arranged in a melt surface
region of the glass melt, wherein the inlet and the outlet are
essentially arranged lying opposite one another.
Inventors: |
Rodek; Erich; (Mainz,
DE) ; Bauer; Wolfgnag Schmid; (Mainz, DE) ;
Romer; Hilgegard; (Karben, DE) ; Weidmann;
Gunter; (Flonheim, DE) ; Kiefer; Werner;
(Mainz, DE) |
Correspondence
Address: |
CHARLES N.J. RUGGIERO;OHLANDT, GREELEY, RUGGIERO & PERLE, L.L.P.
10th FLOOR
ONE LANDMARK SQUARE
STAMFORD
CT
06901-2682
US
|
Assignee: |
PLAYTEX PROCUCTS, INC.
|
Family ID: |
7653754 |
Appl. No.: |
11/888745 |
Filed: |
August 2, 2007 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
|
|
10362396 |
Jul 16, 2003 |
|
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PCT/EP01/08148 |
Jul 14, 2001 |
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11888745 |
Aug 2, 2007 |
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Current U.S.
Class: |
65/346 |
Current CPC
Class: |
C03B 5/021 20130101;
C03B 5/225 20130101; C03B 5/205 20130101; C03B 2211/71
20130101 |
Class at
Publication: |
065/346 |
International
Class: |
C03B 5/225 20060101
C03B005/225 |
Foreign Application Data
Date |
Code |
Application Number |
Aug 25, 2000 |
DE |
100 41 757.4-45 |
Claims
1. A device for the refining of a glass melt at high temperatures
according to the skull pot principle, comprising: a skull crucible
having walls that are constructed from a plurality of pipes; a
high-frequency coil for coupling electrical energy into the
contents of the skull crucible; and an inlet and an outlet of the
skull crucible being arranged in a melt surface region of the glass
melt, wherein the inlet and the outlet are essentially arranged
lying opposite one another.
2. The device according to claim 1, further comprising two or more
skull crucibles connected in series.
3. The device according to claim 1, further comprising a bridge
barrier provided in the melt surface region.
4. The device according to claim 3, wherein the skull crucible is
mushroom-shaped and has a lower part of relatively small diameter
as well as an upper part of relatively large diameter, and wherein
the inlet and the outlet are connected in the upper part of the
skull crucible.
5. The device according to claim 3, further comprising two or more
skull crucibles connected in series.
6. The device according to claim 1, wherein the skull crucible is
mushroom-shaped and has a lower part of relatively small diameter
as well as an upper part of relatively large diameter, and wherein
the inlet and the outlet are connected in the upper part of the
skull crucible.
7. The device according to claim 6, further comprising two or more
skull crucibles connected in series.
Description
CROSS REFERENCE TO RELATED APPLICATIONS
[0001] This application is a divisional application of U.S.
application Ser. No. 10/362,396 filed Jul. 16, 2003, now pending,
which is a national stage entry of International Application No.
PCT/EP01/08148 filed on Jul. 14, 2001, which claims the benefit of
German Application No. DE 100 41 757.4-45 filed on Aug. 25, 2000,
the entire contents of all of which are incorporated by reference
herein.
BACKGROUND OF THE INVENTION
[0002] 1. Field of the Invention
[0003] The invention concerns the production of glass in general
from waste glass or glass batches. The three essential stations of
the production process comprise melting, then refining and finally
homogenizing.
[0004] 2. Description of Related Art
[0005] The production of high-value special glasses requires the
process step of refining after melting, in order to remove the
residual bubbles from the melt. The prior art comprises the
refining of glasses by addition of refining agents such as redox
refining agents or evaporating refining agents. One speaks here of
chemical refining, since the release of gases form the melt is
utilized in order to inflate small bubbles that are present and
thus to facilitate the rise of these bubbles.
[0006] Along with the methods of chemical refining, alternatively
or additionally, physical effects are utilized, as described in the
literature, for expelling bubbles and thus for refining, such as,
for example, centrifugal force (U.S. Pat. No. 3,893,836) or the
reduction of the bath depth and thus the rise of bubbles to the
surface of the melt is facilitated (DE 197 10 351 C1).
[0007] It is known that refining is promoted by increasing the
temperature of the melt. However, when refractory material is used
for the refining tank, limits are imposed. If ceramics with high a
zirconium content are used, then temperatures of a maximum
16,500.degree. C. can be produced.
[0008] It is known also to conduct refining in an apparatus that
operates according to the so-called skull pot principle. See EP 0
528,025 B1. Such a device comprises a crucible, the walls of which
are formed from a ring or collar of metal pipes, which can be
connected to a cooling medium, with slots between the metal pipes
adjacent to one another. The device also contains an induction
coil, which surrounds the walls of the crucible and by means of
which high-frequency energy can be coupled into the contents of the
crucible. This direct heating of the glass melt by means of
irradiation of high-frequency energy is conducted at a power of 10
kHz to 5 MHz.
[0009] Such a crucible permits essentially higher temperatures than
a vessel made of refractory material. The advantage of
high-temperature refining in comparison to all other physical
refining processes is that it is very effective and rapid due to
the high temperatures. The processes take place clearly more
rapidly at high temperatures, so that very small, rapid aggregate
modules can be prepared for the process of refining.
[0010] DE 2,033,074A describes an arrangement for the continuous
melting and refining of glass. A refining device is provided
therein, which operates according to the skull pot principle. The
melt from the bottom region of the melting vessel reaches the
refining vessel via a connection channel. It enters in the bottom
region of the latter. The glass flow in the refining vessel thus
rises upward from the bottom. This has the advantage that the flow
has the same direction as the lifting force of the bubbles. The
bubbles to be removed reach the hot surface of the melt and are
discharged from the latter.
[0011] A disadvantage of this embodiment consists of the fact that
the connection channel between the melting-down basin and the
high-frequency refining device is subject to intense wear and tear
due to the high flow velocities.
BRIEF SUMMARY OF THE INVENTION
[0012] The object of the invention is to develop a system in which
the good refining results remain, based on an upward flow of the
glass melt, but in which also the melt remains hot at the surface
in the region where the bubbles are discharged, so that all bubbles
can burst at the surface, and in which the problematic connection
channel between the melting vat and the refining device can be
omitted.
[0013] The inventor has recognized the following: If the inlet as
well as the outlet of the high-frequency crucible is arranged in
the upper region and in fact in such a way that the two of these
lie opposite one another, then a very good and effective refining
results. One would have expected that with such a structure, an
essential part of the melt would be unheated and unrefined and led
along directly to the outlet in the short circuit from the inlet at
the surface. However, this is not the case. Rather, a defined flow
is set up based on the differences in density in different melt
regions. If the expansion coefficient of the melt is sufficiently
high and the heating of the melt in the crucible is assured
appropriately, the laterally introduced cold glass does not
directly reach the crucible outlet via short-circuit currents, but
is first pulled to the bottom of the crucible and from here is led
to the surface and to the outlet via convection rollers according
to circular movements of variable length.
[0014] The inlet and outlet should essentially lie diametrically
opposite each other. This is not absolutely necessary, however;
certain deviations are admissible. Also, the crucible should be
dimensioned correctly, but this is an optimizing problem, which can
be solved by the person of average skill in the art.
[0015] The connection channel between the melting vat and the
refining crucible, which is known from the prior art, will be
avoided. Instead of this, the melt can overflow from the melting
vat into an open channel to the refining crucible.
[0016] It may be appropriate to configure the refining crucible
according to DE 2,033,074 A. The crucible comprises a lower part of
relatively small diameter, and an upper part of relatively large
diameter.
BRIEF DESCRIPTION OF THE SEVERAL VIEWS OF THE DRAWINGS
[0017] The invention is explained in more detail on the basis of
the drawing. The following are shown individually therein:
[0018] FIG. 1 shows a set-up for the production of glass.
[0019] FIG. 2 shows a refining crucible according to the invention
in a vertical section.
[0020] FIG. 3 shows another embodiment of a set-up for the
production of glass.
[0021] FIG. 4 shows a cooled bridge barrier in the skull crucible,
in schematic representation.
[0022] FIG. 5 illustrates the integration of the bridge barrier
into a skull crucible.
[0023] FIG. 6 shows a set-up for the melting of glass with two
refining stations.
DETAILED DESCRIPTION OF THE INVENTION
[0024] The set-up shown in FIG. 1 comprises a melting-down basin 1
with an introduction device 1.1. The glass batch 1.2 which has been
introduced is retained by a bridge barrier 1.3 to keep it from
flowing further to the stations connected downstream.
[0025] An overflow channel 2 is connected to the melting-down basin
1. This is open at the top. The crude melt reaches a refining
device 3 via the overflow channel 2.
[0026] This refining device comprises a skull crucible and also a
high-frequency coil, which is not shown here. The actual refining
is conducted here at temperatures of 1750 to 3,000.degree. C.,
depending on the glass synthesized and the requirements for glass
quality.
[0027] After the refining, the melt is free of bubbles. It reaches
a homogenizing device 5, which in turn comprises a stirring
crucible and a stirrer, via a conventionally heated channel system
4.
[0028] The structure of the skull crucible can be recognized in
detail in FIG. 2. This involves a so-called mushroom skull crucible
according to DE 2,033,074 A. The skull crucible has a lower
crucible part 3.1 of a relatively small diameter, and in addition
an upper crucible part of a relatively large diameter. The upper
crucible part also contains the inlet 3.2 and the outlet 3.3 for
the melt. The arrows indicate the flow of the melt. As is seen, the
cold glass introduced laterally through the inlet 3.2 first falls
downward to the bottom of the crucible 3.4, then rises again upward
in order to once more flow downward and then upward again. As is
seen, the lower part 3.1 of the skull crucible is surrounded by a
high-frequency coil 3.5.
[0029] The set-up shown in FIG. 3 is the refining device 3 equipped
with an additional, cooled bridge barrier 3.6. This has the
following task: If the glass arriving in the skull refining
aggregate is very foamy or the expansion coefficient of the melt as
a function of temperature is very small, then the danger exists
that a small portion of the melt is drawn over the surface. This
can be prevented either by a clear increase in the temperature
difference between the melt flowing in and the melt in the core of
the crucible in the skull crucible module or by incorporating the
bridge barrier 3.6.
[0030] The bridge barrier 3.6 may be comprised of either a
gas-cooled or liquid-cooled ceramic material or of a water-cooled
metal material. Modifications of cooled metal components lined with
ceramics are also conceivable. If the bridge barrier has metal
components, which lie above the surface of the melt and come into
contact with the burner atmosphere, then it may be helpful to coat
the bridge barrier with a thin layer of Teflon (<150.mu.) in
order to prevent a corrosion of the metal surface due to the
aggressive burner atmosphere. The bridge barrier 3.6 can either be
positioned centrally in the refining module or can be laterally
displaced to inlet 3.2. The latter modification has the advantage
that the hot zone where the bubbles rise can be made as large as
possible. If the bridge barrier is constructed of metal material,
then it should be electrically connected to the metal skull
crucible, so that no induced voltages build up between the metal
corset and the barrier, since these can lead to arcing and thus to
the disruption of the metal wall. If an electrical connection
cannot be produced, then all components must be operated in an
electrically free-floating manner--i.e., not grounded. This is
particularly possible if the melt tends toward intense
crystallization, since In this case a stable puncture-proof
intermediate layer is formed, which reliably stops the arcing.
[0031] An example of embodiment of such a bridge barrier 3.6 is
shown in FIG. 4. The incorporation of such a barrier 3.6 can be
seen in FIG. 5. Here, the barrier 3.6 is positioned below the
surface of the melt. This has the advantage that there are no cold
metal components in the upper furnace space. The condensation of
burner off-gases is particularly problematical on cold components.
It is a disadvantage in this type of assembly that large
fluctuations in the glass level cannot be allowed, since in order
to assure that no liquid melt flows over the barrier, the immersion
depth should be a maximum of 1 cm below the surface of the
melt.
[0032] A barrier assembly can be made possible with the edge of the
barrier above the upper edge of the glass bath by lining the metal
barrier either with Teflon or ceramic materials or by raising the
glass level first higher at the beginning of the process--and in
fact raising it over the upper edge of the barrier--and then again
lowering the glass level to the normal level in operation. In this
case, a glazing of the barrier is achieved, which protects the
barrier from attacks due to burner off-gases. In addition to the
embodiment of the barrier that is shown here, simpler embodiments,
for example, a simple ceramic stone barrier or even a cooled metal
rod which runs crosswise over the crucible is conceivable.
[0033] An electrical connection 3.7 of the crucible 3 with the
barrier 3.6 as well as a crucible short-circuit ring 3.8 can be
seen in detail in FIG. 5.
[0034] A cascade refining is provided In the set-up shown in FIG.
6. The introduced glass batch 6 as well as a bridge barrier 7 can
also be recognized again here.
[0035] Several refining modules are connected one after the other
and they connect with one another simply in the upper region. The
connection sites can be heated conventionally, for example, with
burners. In this case, complicated connection channels that are
sensitive to disruption and consume a great deal of energy can be
omitted. An example with two refining modules connected one after
the other is shown in FIG. 6. Of course, any number of refining
modules connected one after the other is conceivable.
[0036] With respect to geometry--particularly diameter--,
HF-frequency and HF voltage are adapted to the conductivity of the
glass to be melted in each case. If different types of glass with
clearly different electrical conductivities are to be melted in the
same vat and are to be refined by means of HF heating, then this is
not possible without retrofitting measures (connection of another
generator with adapted frequency region, connection of an adapted
coil, possible change of the melting diameter, adaptation of the
capacities in the HF generator). Of course, as in FIG. 6, two or
more aggregates can be connected one after the other, and thus each
individual module can be adapted to different electrical melting
properties. The HF energy is only turned on in the HF refining
module adapted to the respective melt, whereas the other modules
are not heated with HF energy, but only with conventional
energy--such as, for example, burners in the upper furnace space.
The melt flows over the modules that are not turned on and is drawn
into and heated only in the HF-heated module. In order to configure
the exchange of glass in such an aggregate in a simpler and quicker
manner, it is helpful if each module has an additional bottom
outlet 9, which is opened for a short time in the glass exchange
phase. Such a bottom outlet can also be of use in the case of the
simple structure with only one HF-module--particularly if exchanges
of glass in the vat are considered--but also if bottom residues
should deposit thereon.
[0037] Another advantage of the invention is the very good
"emergency running properties" of the set-up if there are
disruptions in the HF range. If the high-frequency heating
apparatus fails for any reason whatever, then there exists the
danger of a freezing up of the continuous flow in the case of the
continuous-flow crucible with introduction from below, whereby the
glass flow is interrupted. The danger does not exist in principle
in the present invention, since the glass flow can be assured in
each case by utilizing the upper heat of the burner.
* * * * *