(57) The invention relates to refractory materials being used in aluminum reduction cells
such as structural parts, mortars, grouts and shaped lining products.
It was dicovered that - if the aluminum cell refractory material consists of more
than 50% of silicon metal remains solid at the operating temperatures of aluminum
electrolysis cells up to 1000°C.
A process for the manufacture of solid aluminum cell refractory material in the form
of tiles, slabs and bricks is characterized in that a dry aggregate composition of
- Dust fraction
- 0-0.5mm = 30%
- Particle fraction
- 0-1mm = 20%
- Particle fraction
- 1-2mm = 20%
- Particle fraction
- 2-4mm = 30%
is mixed with a binder of a colloidal silica solution or with a high-softening coal-tar
pitch, the mix is formed to bricks, slabs and tiles which are further treated to form
a dense, highly cryolith resistant material, having extremely low electrical and moderate
thermal conductivity.
[0001] The invention relates to innovative materials being used in aluminium reduction cells
such as structural parts, mortars, grouts, and shaped lining products.
[0002] A basic prerequisite of materials which are suitable in the lining of electrolytic
reduction cells for aluminium production is a good resistance against the constituents
of cryolitic melts. According to the invention it was found that silicon metal meets
this requirement, especially under reducing conditions. Thermodynamic experiments
showed that there is an extremely low probability for the reaction of silicon with
cryolite or its constitutional compounds sodium and aluminium fluoride. Silicon also
behaves inert against other ingredients of the electrolytic melt such as calcium,
magnesium and lithium fluorides as well as against metallic sodium that occurs in
the cathodic region of electroytic reduction cells. It was found that silicon used
as a lining material has to be kept away only from large amounts of liquid aluminium.
[0003] If prepared under the conditions described below the new pot lining or embedding
material remains solid at the operating temperatures of aluminium electrolysis cells
up to 1000°C (melting point above 1400°C) and can be considered to be electrically
non-conductive. Other favourable features of the new silicon material are its fairly
low thermal conductivity and good oxidation resistance forming a basis for its use
as a superior refractory lining material.
[0004] The properties of the new silicon pot lining material which are briefly characterised
above open up a number of useful applications in aluminium reduction cells which can
be grouped as follows:
1. Structural, shaped parts of the new silicon material which are either directly
cast or machined (cutting, drilling) from blocks or lumps of solid silicon.
2. Mortars and castables where powdery or fine, granular silicon material is used
as filler material.
3. Block, bricks or tiles where a dry aggregate of silicon material ranging from 0
to about 8 mm in particle size constitutes the basis of the formed and fired products.
[0005] The silicon particle range of "0 to about 8" means that all particles above "0" can
be used up to a particle size of about "8". A particle diameter of more than "9" mm
has certain disadvantages because it is difficult to handle such particles in a colloidal
silica solution.
[0006] Of the above-mentioned products some selected examples of preparation and application
will be given below whereby the term "silicon" should be interpreted as the new silicon
material defined in the claims.
Example 1:
[0007] Structural parts like shaped parts of pure silicon with drilled holes can be used
to control the operating temperatures of aluminium reduction cells. The new silicon
structural parts like hollow cylinders can, for instance, be either immersed from
the top in the electrolytic bath or embedded in the cathode lining as protecting sheathes
for example to protect temperatures sensors. The new silicon-protected measuring devices
allow to monitor cell temperatures continuously over medium- (weeks or months) or
long-term periods (years). The permanent recording of temperature signals represents
a great advantage in the optimisation of cell process control.
Example 2:
[0008] New silicon mortars have been made by using pulverised silicon material as filler
and a colloidal silica solution as binder. The following filler composition has shown
significant properties: 70 % silicon powder of total mortar mass 0 - 0.5 mm and 30
% silicon powder of total mortar mass 0 - 0.2 mm. About 40 % of a colloidal silica
solution are added which results to 100 % total mortar mass after a drying step. The
silicon-based mortar is applied to lay fireclay bricks in the bottom or side pier
lining of reduction cells. Many tests have shown that the joints filled with silicon-based
mortar are at least 100 times more resistant to the infiltration and attack of fluoride
melts than the fireclay bricks. If the fireclay bricks are bonded with conventional
mortars prepared from ceramic filler materials (silica, chamotte, mullite, alumina,
silicon carbide) and ceramic binders (sodium silicate, calcium aluminate cements etc.),
it is always observed that the joints are attacked and converted first by the infiltrated
fluoride bath constituents, i.e. penetration of cryolite bath moves faster and preferentially
along the joints between the refractory bricks. This phenomenon is effectively stopped
by using a silicon-based, silica-bonded mortar.
Example 3:
[0009] To manufacture slabs, bricks or tiles on the basis of silicon, silicon particle fractions
must be prepared at first. Since Silicon is very brittle it should be crushed carefully
and comminuted. According to the invention a preferred composition of the dry aggregate
is the following:
| Dust fraction |
0 - 0.5 mm = 30 % |
| Particle fraction |
0 - 1 mm = 20 % |
| Particle fraction |
1 - 2 mm = 20 % |
| Particle fraction |
2 - 4 mm = 30 % |
[0010] The silicon particles exhibit an extremely low porosity. Thus, a dense product of
low permeability can be made. Compared with a standard lining material the porosity
and permeability of the new silicon material is below 1 % measured under identically
conditions according to DIN 1306.
[0011] Various binders can be used to manufacture a shaped product from the preceding dry
aggregate. Two examples will be described below.
Example 4:
[0012] The silicon dry aggregate is mixed with a 30 % colloidal silica solution. 0.5 % of
wheat or rye flour may be added to facilitate forming. The green mix is compacted
and formed by means of a hydraulic press to bricks or tiles. The bricks and tiles
are dried or tempered, and thereafter are ready for use. Their cryolite resistance
turned out to be excellent, even after long-term periods and strong turbulence conditions
of the electrolytic bath.
Example 5:
[0013] Another bond structure of the electrolytic cell is produced by the following method:
A new silicon dry aggregate is mixed with a high-softening coal-tar pitch at 180-200°C.
One part of the silicon/pitch paste is formed to bricks, slabs and blocks by pressing
another part, by vibration moulding under vacuum. The green shaped products are baked
and calcined in an anode-carbon baking furnace under a nitrogen atmosphere up to 1200°C.
During heat-treatment in an anode baking furnace the carbon residue of the coked pitch
reacts with silicon to form β-silicon carbide as a bond matrix. This procedure was
conducted in a nitrogen atmosphere until silicon nitride was formed in the presence
of carbon monoxide which lead to partial preferably more than 30 % formation of silicon
oxicarbide and oxinitride. It was found that some nitridation and oxygenation creates
a microporosity and renders a less permeable product. The silicon-based product obtained
by the preceding process is a dense, highly cryolite-resistant material of extremely
low electrical and moderate thermal conductivity. It offers new possibilities in minimising
the heat losses from electrolytic cells in conjunction with carbon & graphite as hot
face materials.
[0014] Economic efficiency and life time of the reduction cells are noticeably improved
by the silicon-based refractory materials outlined above. For comparison with a product
made under the conditions of the prior art the following example 6 has been drawn
up:
Example 6:
[0015]
I. Comparison test of density (100 % = not permeable)
Temperature = 1000°C - pressure: 10 bar
| |
Invention |
Standard product |
| 1) |
rod of pure silicon |
fire clay brick |
| |
100% |
55% |
| 2) |
product of example 4 |
mortar |
| |
98% |
45% |
II. Comparison test of cryolite resistant
(attack in mm after 10 h)
Temperature: 1000°C
| |
Invention |
Standard product |
| 1) |
rod of pure silicon |
fire clay brick |
| |
0 mm |
18 mm |
| 2) |
product of example 4 |
mortar |
| |
1 mm |
25 mm |
III. Thermal conductivity
(standard fire clay brick = 100 %)
| |
Invention |
Standard product |
| 1) |
rod of pure silicon |
fire clay brick |
| |
18 % |
100 % |
| 2) |
product of example 4 |
mortar |
| |
21 % |
96 % |
[0016] The comparison test shows that the new innovative materials can be favourably used
in aluminium reduction cells such as structural parts, mortars, grouts, and shaped
lining products. They are principally made on the basis of silicon metal > 50 % and
are corrosion-resistant against cryolitic melts and sodium. They have a low permeability
and, compared to carbon & graphite, a very high electrical resistance and low thermal
conductivity.
1. Aluminium cell refractory material comprising structural parts, mortars, grouts and
shaped lining products
characterized in
that the refractory material consists in more than 50 % of silicon metal.
2. Aluminium cell refractory material according to claim 1,
characterized in
that the silicon metal consists of a dry aggregate having a composition as follows
| Dust fraction |
0 - 0.5 mm = 30 % |
| Particle fraction |
0 - 1 mm = 20 % |
| Particle fraction |
1 - 2 mm = 20 % |
| Particle fraction |
2 - 4 mm = 30 %. |
3. Aluminium cell refractory material according to claim 2,
characterized in
that the silicon metal consists of 65 - 75 % dry aggregate and 25 - 35 % colloidal silica
solution.
4. Aluminium cell refractory material according to claim 2,
characterized in
that the refractory material consists in a mixture of 65 - 75 % dry aggregate and 25 -
35 % high-softening coal-tar pitch.
5. Aluminium cell refractory material according to claim 4,
wherein the carbon residue of the coked pitch is reacted with silicon to β-silicon
carbide as a bond matrix.
6. Aluminium cell refractory material according to claim 4 or 5,
characterized in
that the carbon residue of the pitch is reacted with silicon in the presence of nitrogen
to silicon oxicarbide and/or oxinitride.
7. Aluminium cell refractory material according to claim 1,
characterized in
that the refractory material is a mixture of a binder and silicon metal which is a pulverised
silicon filler having the following composition:
- 60 - 75 % silicon powder of 0 - 05, mm
- 25 - 35 % silicon powder of 0 - 0,2 mm and that
- 30 - 50 % of a colloidal silica solution is used as a mortar-binder.
8. Process for the manufacture of an aluminium cell refractory material in the form of
tiles, slabs and bricks,
characterized in
that a dry aggregate composition of
| Dust fraction |
0 - 0.5 mm = 30 % |
| Particle fraction |
0 - 1 mm = 20 % |
| Particle fraction |
1 - 2 mm = 20 % |
| Particle fraction |
2 - 4 mm = 30 % |
is mixed with a binder of a colloidal silica solution to a green mixture,
the green mix is compacted and formed to bricks, slabs and tiles and
the compacted bricks, slabs and tiles are dried and tempered to receive a dense, highly
cryolith resistant material, having extremely low electrical and moderate thermal
conductivity.
9. Process for the manufacture of an aluminium cell refractory material,
characterized in
that a dry aggregate composition of
| Dust fraction |
0 - 0.5 mm = 30 % |
| Particle fraction |
0 - 1 mm = 20 % |
| Particle fraction |
1 - 2 mm = 20 % |
| Particle fraction |
2 - 4 mm = 30 %. |
is mixed with a high-softening coal-tar pitch at 180 - 200°C,
the silicon/pitch paste is formed to bricks, slabs and blocks by pressing and/or vibration
moulding under vacuum and
the green shaped products are baked and calcined under a nitrogen atmosphere with
a temperature between 1000 and 1200°C.
10. Process for the manufacture of an aluminium cell refractory material according to
claim 9,
wherein the baking and calcining step is conducted for a time sufficient to react
the carbon residue of the coked pitch with silicon to form better-silicon carbide
as a bond matrix.
11. Process for the manufacture of an aluminium cell refractory material according to
claim 9 or 10,
characterized in
that the baking step is conducted in the presence of carbon-mono-oxide to form silicon-oxicarbide
and/or silicon-oxinitride.