[0001] The invention relates to an apparatus for the removal of gasses from electrolysis
cells by suction comprising a branch duct for each electrolysis cell, a main duct
connecting the branch ducts to a gas treatment centre and a central suction fan providing
for at least part of the suction.
[0002] During the electrolysis process gasses are produced that can be harmful for the environment
and that could provide unacceptable working conditions. Especially in the aluminium
electrolysis process harmful gasses containing fluorides and fluoride particles are
emitted. The last decades major improvements have been implemented to reduce the emission
of both fluoride particles and gasses containing fluorides. Today in most plants the
emission of the fluoride particles through the chimney stack of the plant is, because
of an efficient adsorption system, at a level that no significant further improvement
seem to be possible.
[0003] However, emission directly from the shielded electrolysis cells or pots into the
potroom and subsequently from the potroom through the roof to the outside environment
is an area wherein improvement is still possible. Proper shielding of the electrolysis
cells and the suction of the gasses from the electrolysis cells adequately prevent
that gasses enter the potroom. However, during the tapping of molten aluminium from
the electrolysis cells, maintenance around the electrolysis cells or the change of
anodes, for which the hoods of the electrolysis cells have to be lifted, still a considerable
emission of gasses into the potroom occurs. Also defect covers of the hood will contribute
to the emission in the potroom.
[0004] In order to reduce the emission of gasses during the change of anodes several systems
are known that provide for boosted suction during the change of anodes to prevent
these emissions. Although these systems seem to provide a good solution to the problem,
the major disadvantage of these systems is that the systems all involve large investments
due to the necessity of a secondary duct system required for the boosted suction.
A secondary system is also difficult to install in older plants due to lack of space.
A secondary duct system is connected to each branch duct of each pot and is activated
by closing and opening valves during anode change only. Separate fans in the secondary
system provide the boost capacity.
[0005] With the normal operation of an electrolysis cell is meant the electrolysis process
in operation with all hoods of the electrolysis cells closed.
[0006] However, taking the covers of the hood off the electrolysis cells for tapping and
changing of anodes and putting the covers back again will result after a period of
use that not all electrolysis cells close off as well as originally designed to do.
Most common damages to these covers are bends and holes through spilling of molten
aluminium with a tapping operation. This will result in a larger open area between
the covers and this will increase the ventilation of the potgas to the potroom, stimulating
the emission.
[0007] It is an object of the present invention to provide an apparatus for the removal
of gasses from a number of electrolysis cells by suction wherein the suction is adjusted
to a level needed to minimize emissions from the electrolysis cells.
[0008] It is a further object of the invention to provide an apparatus for the removal of
gasses from a number of electrolysis cells by suction wherein for all levels of suction
only one duct system is used.
[0009] It is a further object of the present invention to provide an apparatus for the removal
of gasses from a number of electrolysis cells by suction wherein the pressure in each
of the electrolysis cells or in the branch duct downstream of the electrolysis cell
is kept at a predetermined pressure.
[0010] It is a further object of the present invention to provide an apparatus for the removal
of gasses from a number of electrolysis cells by suction wherein the temperature of
the gasses provides additional information and or in combination with the pressure
and calculated flow present the heat load leaving the pot.
[0011] It is a further object of the present invention to provide an apparatus for the removal
of gasses from a number of electrolysis cells by suction that is easier to build,
use and maintain than the existing apparatuses.
[0012] It is a further object of the present invention to provide an apparatus for the removal
of gasses from a number of electrolysis cells that is cheaper to build than the existing
apparatuses.
[0013] According to a first aspect of the invention one or more of these objects are realized
by providing an apparatus for the removal of gasses from electrolysis cells by suction
comprising a branch duct for each electrolysis cell, a main duct connecting the branch
ducts to a gas treatment centre and a central suction fan providing for at least part
of the suction, wherein control means to control the supplementary suction means and
pressure monitor means are provided, wherein the control means are adapted to control
the supplementary suction means in dependence from changes in the monitored pressure
with respect to a reference pressure.
[0014] With the supplementary suction means and control means therefore the flow from each
electrolysis cell may be adjusted to have the pressure in the electrolysis cell or
in the branch duct correspond to a predetermined pressure, wherein the predetermined
pressure is such that under all conditions the removal of gasses from an electrolysis
cell is sufficient to minimize emission of the gasses from the electrolysis cell into
the potroom. This will mean that with normal operation the flow of gasses from the
electrolysis cells will be at a minimum but for each electrolysis cell adapted to
the degree of leakage from that electrolysis cells to the potroom. The invention relates
to an apparatus to control pot emission dedicated for each pot and independent of
the operational status and shielding condition of the pot. A clear advantage is that
for all electrolysis cells the emission is reduced to a minimum providing a working
environment for the workers on the floor as safe as possible without the chance as
with the know suction systems that one of the electrolysis cells unexpectedly has
a far larger emission into the potroom than the other electrolysis cells.
[0015] Another advantage is that since there is no need to generate a large predetermined
common gas flow that will be sufficient for all electrolysis cells the total flow
of gasses with the apparatus according the invention will be lower than with the known
apparatuses. This results in an important further advantage that more electrolysis
cells can be connected to a single gas treatment centre which allows for further expansion
of the plant without the need to have to provide for a further gas treatment centre,
which will be far more capital-intensive.
[0016] The reference pressure with respect to which the supplementary suction means are
controlled dependent on changes in a monitored pressure can be a predetermined pressure
in the electrolysis cells or a pressure linked in a known manner to that predetermined
pressure. For instance the pressure at the outlet of an electrolysis cell is monitored
wherein a reference pressure at said outlet has a known ratio to said predetermined
pressure in the electrolysis cell. In the same manner it is possible to monitor a
pressure drop over a part of a branch duct between the electrolysis cell and the supplementary
suction means for that cell and compare the pressure drop with a reference pressure
drop which in its turn has a known ratio to the predetermined pressure in the electrolysis
cells.
[0017] In an analogous manner it is possible to monitor the flow in a part of a branch duct
between the electrolysis cell and the supplementary suction means for that cell, wherein
the measured flow corresponds to a difference in pressure which in its turn has a
known ratio to the predetermined pressure in the electrolysis cells.
[0018] The supplementary suction means operate in combination with the central suction fan
and since part of the suction is realized by the supplementary suction means the central
fan does not need to be as powerful as in the known suction systems.
[0019] Another advantage is that since the flow from the electrolysis cells is controlled
with the supplementary suction means there is no need for valves or other flow restriction
devices in the branch duct as with the known suction systems. Although this will mean
a reduction in costs with new suction systems, the main advantage in both new and
upgraded existing systems is that misbalance in the suction system by incorrect settings
of these valves can be prevented since these valves or restriction devices are no
longer needed.
[0020] In the known suction systems, despite the flow restriction devices, boosted suction
of an electrolysis cell will influence the normal suction of electrolysis cells which
connect to the main duct close to the branch duct of said electrolysis cell and misbalance
of the system might occur. With the apparatus according the invention any misbalance
is avoided since the pressure in the other electrolysis cells is kept at the predetermined
pressure with the supplementary suction means and the control means therefore. The
obvious advantage of avoiding any misbalance in the suction system is that the emission
of gasses in the potroom is kept at a minimum at all times.
[0021] According to a further aspect of the invention the supplementary suction means comprise
air injection means. To control the air injection means the control means control
feed means with which pressurized air is fed to the air injection means.
[0022] According a first embodiment air is injected in a branch duct therewith increasing
the flow of the gasses in the branch duct.
[0023] According to a second embodiment the air injection means comprise an air amplifier,
also known as an air driven positive displacement pump. An air amplifier increases
the gas pressure at point of use therewith increasing the flow through the device.
With such an air amplifier less pressurized air is needed than with the direct injection
of air in a branch duct to control the flow. By adjusting the amount of pressurized
air fed to the air amplifier the pressure difference over the air amplifier and therewith
the gas flow can be adjusted accurately over a wide range.
[0024] Another embodiment provides that the supplementary suction means comprise a suction
fan, wherein the control means control the speed of the motor of the suction fan.
[0025] The invention also provides a method to control the removal of gasses from electrolysis
cells by suction wherein the gasses are removed through branch ducts connected to
the electrolysis cells and a main duct connecting the branch ducts to a gas treatment
centre, a central suction fan providing for at least part of the suction, wherein
for each of a number of electrolysis cells supplementary suction is provided for by
means of supplementary suction means provided for in the branch ducts of each of said
electrolysis cells in dependence of changes of a monitored pressure with respect to
a reference pressure.
[0026] The suction of the gasses from the electrolysis cells is controlled by keeping the
pressure at the outlet of the electrolysis cells or the pressure or drop in pressure
in the branch ducts connecting the electrolysis cells to the main duct at a reference
pressure by means of the supplementary suction means in the branch ducts.According
to a further aspect the supplementary suction is realized by means of injection of
a fluid medium in a branch duct. Preferably the fluid medium is pressurized air.
[0027] The pressurized air can be fed directly in the branch duct therewith entraining the
gasses from the electrolysis cell. By controlling the amount of pressurized air fed
to the branch duct the flow can be controlled. However, it is preferred to feed the
pressurized air to an air amplifier in the branch duct since less pressurized air
is needed while the flow of gasses can be controlled more accurately and over a wide
range.
[0028] According to a further embodiment of the invention it is provided that the temperature
of the gasses coming from each of the electrolysis cells is monitored. To this end
temperature measurement means are provided in the electrolysis cell and/or in the
part of the branch duct between the electrolysis cell and the supplementary suction
means. By monitoring the temperature of the gasses important information of the process
in each of the electrolysis cells is obtained on basis of which the process can further
be controlled. For instance a rise in temperature can be controlled or temporarily
controlled by increasing the suction for that particular electrolysis cell to get
the temperature down.
[0029] The temperature measurement means can be connected directly or via a central control
system to the control means of the supplementary suction means to be able to control
the temperature of the gasses by increasing the suction in an electrolysis cell.
[0030] With the monitor and measurement means also connected to a central control and monitor
system an easy overview of each of the electrolysis cells can be obtained, also facilitating
separate action for a electrolysis cell for instance if the process temperature starts
to rise.
[0031] The invention is further explained on hand of the embodiments given by way of example
in the drawing, wherein
fig.1 shows schematically an arrangement of a row of electrolysis cells with a suction
system according to the invention,
fig.2 shows schematically an embodiment of supplementary suction system using pressurized
air, and
fig.3 shows schematically an embodiment of supplementary suction system with a suction
fan.
[0032] In fig.1 rows 1 of electrolysis cells 2 are shown, wherein each electrolysis cell
2 connects by means of a branch duct 3 to a main duct 4. The main duct 4 is connected
to a gas treatment centre 5 downstream of which a central suction fan 6 is provided.
The central suction fan 6 in its turn connects to chimney 7. The number of electrolysis
cells 2 in a row 1 may amount to well over a hundred and the number of rows 1 may
be up to ten in a single plant. The central suction fan 6 may consist of a single
fan or a number of separate suction fans.
[0033] In each of the branch ducts 3 supplementary suction means 8 are provided with control
means 9 to control the supplementary suction means 8.
[0034] Fig.2 shows in more detail a number of electrolysis cells 2. Each of the electrolysis
cells 2 are provided with hoods 10 to be able to locally open an electrolysis cell
2 for tapping molten aluminium, to change anodes and for maintenance of the cells.
In branch ducts 3 supplementary suction means 8 are provided with control means 9.
The control means 9 comprise pressure monitor means 11 such as a pressure sensor in
branch duct 3 upstream of supplementary suction means 8, a microcontroller 12 connected
to the pressure monitor means 11 and to a valve 13 in a supply pipeline 15 for pressurized
air.
[0035] The supplementary suction means 8 preferably comprise an air amplifier because this
is a simple device without any moving parts and with which the pressure drop over
the air amplifier and therewith the gas flow can be controlled over a considerable
range without having to use a lot of pressurized air. It is also possible to only
use pressurized air as supplementary suction means 8 but this will require much more
pressurized air than when using an air amplifier as supplementary suction means 8.
[0036] In the branch duct 3 of each electrolysis cells 2 temperature measurement means 14
are provided to monitor the electrolysis process in each of the cells 2.
[0037] The pressure in the main duct 4 will be less in downstream direction towards the
gas treatment centre 5 resulting in that the pressure drop over the supplementary
suction means 8 in each successive branch duct 3 connecting to main duct 4 further
downstream will have to be less to get the desired suction and therewith the desired
gas removal from the electrolysis cells 2. With the supplementary suction means 8
and control means 9 the suction and therewith the pressure in the electrolysis cell
will be automatically controlled and kept within a narrow range around the predetermined
pressure. This will also be the case if for one of the electrolysis cells 2 the normal
suction for that electrolysis cell is changed to a level of boosted suction when one
or more of the hoods 10 have to be lifted for tapping or to change anodes. The locally
increased pressure in main duct 4 will automatically be compensated for with the supplementary
suction means 8 and control means 9.
[0038] In fig.3 an embodiment is shown wherein a suction fan 16 is used as a supplementary
suction means. In this configuration the control means 9 comprise pressure monitor
means 11 such as a pressure sensor in branch duct 3 upstream of suction fan 16, a
microcontroller 12 connected to the pressure monitor means 11 and to a variable speed
drive 17 for motor 18 of suction fan 16.
[0039] The balancing of the pressure in each of the electrolysis cells and therewith the
suction from each of the electrolysis cells is with this embodiment in principle the
same as with the previous embodiment. The only difference is that the control is done
by means of an electric circuit and that consequently no pressurized air system is
needed.
1. Apparatus for the removal of gasses from electrolysis cells by suction comprising
a branch duct for each electrolysis cell, a main duct connecting the branch ducts
to a gas treatment centre and a central suction fan providing for at least part of
the suction, wherein one or more of the branch ducts are provided with supplementary
suction means and wherein control means to control the supplementary suction means
and pressure monitor means are provided, wherein the control means are adapted to
control the supplementary suction means in dependence from changes in the monitored
pressure with respect to a reference pressure.
2. Apparatus according to claim 1, wherein the pressure monitor means are provided in
the electrolysis cell and/or in the part of the branch duct between the electrolysis
cell and the supplementary suction means.
3. Apparatus according to one or more of claims 1-2, wherein the supplementary suction
means comprise air injection means.
4. Apparatus according to claim 3, wherein the control means control feed means with
which pressurized air is fed to the air injection means.
5. Apparatus according to claim 3, wherein the air injection means comprise an air amplifier.
6. Apparatus according to claim 1 or 2, wherein the supplementary suction means comprise
a suction fan and wherein the control means control the motor of the suction fan.
7. Apparatus according to one or more of the claims 1-6, wherein temperature measurement
means are provided in the electrolysis cell and/or in the part of the branch duct
between the electrolysis cell and the supplementary suction means.
8. Apparatus according to claim 8, wherein the temperature measurement means are connected
to the control means for the supplementary suction means
9. Apparatus according to one or more of the claims 1-8, wherein central control means
are provided to which pressure monitor means, control means for the supplementary
suction means and the temperature measurement means are connected.
10. Method to control the removal of gasses from electrolysis cells by suction wherein
the gasses are removed through branch ducts connected to the electrolysis cells and
a main duct connecting the branch ducts to a gas treatment centre, a central suction
fan providing for at least part of the suction, wherein for each of a number of electrolysis
cells supplementary suction is provided for by means of supplementary suction means
provided for in the branch ducts of each of said electrolysis cells in dependence
of changes of a monitored pressure with respect to a reference pressure.
11. Method according to claim 10, wherein the pressure is monitored in the electrolysis
cell or in the part of the branch duct between the electrolysis cell and the supplementary
suction means.
12. Method according to claim 10 or 11, wherein the supplementary suction is realized
by means of injection of a fluid medium in a branch duct.
13. Method according to claim 12, wherein the fluid medium is pressurized air.
14. Method according to one or more of claims 10-13, wherein the temperature of the gasses
is monitored in the electrolysis cell and/or in the part of the branch duct between
the electrolysis cell and the supplementary suction means.
15. Method according to claim 14, wherein the temperature of the gasses is used in the
control of the supplementary suction means.