[0001] The present invention concerns a method and an apparatus for the treatment of aerosols,
especially aerosols generated during treatment of liquid suspensions or liquid solutions
in, for example, a nuclear power station.
Background to the invention
[0002] During treatment of radioactive waste in suspension in water or as a water solution
in a waste disposal plant, certain processes generate aerosols which can contain varying
amounts of radioactive products. In waste disposal plants in nuclear power stations,
the waste water can come from different processes, for example in the form of system
drainage, cleaning water, floor drain drainage, and chemical drainage. Especially
in a number of nuclear power stations there occurs a large amount of radioactive filtering
substances in water suspension, which before final storage are treated in a special
drying process. The process may include many different machines, for example pumps,
separators, centrifuges, etc. which because of their construction and function generate
larger or smaller amounts of aerosols. From a safety and environmental point of view
it is important to prevent the aerosols leaving the process unchecked.
[0003] According to prior art certain of such machines can be constructed hermetically sealed.
With some types of machines it is however impossible to achieve complete sealing with
respect to the surroundings, for example with machines with rotating shafts there
is typically shaft seal leakage or other seal leakage. In that case, a reduced pressure
is instead arranged in the machine. According to the state of the art the casing of
the machine is for this reason connected to a ventilation system with fans which suck
out through a filter any air which may have leaked into the machine. The leaks in
the machine as a consequence of its construction entail in this case a leakage of
air in from the surroundings, and the process atmosphere is prevented from leaking
out to the surroundings. A disadvantage with this method is that the filter accumulates
aerosols and becomes more and more radioactive. This requires the installation of
radiation shields and in general makes the handling and disposal of the filter considerably
more difficult.
[0004] It is an object of the present invention to accomplish the evacuation of aerosols
from machines, which are not gastight, for the treatment of materials where aerosols
and liquids occur, in such a manner that the spread of the aerosols to the surroundings
and the treatment of such aerosols can be eliminated. It is also an object to eliminate
the necessity for filters during the evacuation of the aerosols. A comprehensive object
is accordingly to convert aerosols which arise into a solution or suspension in a
liquid.
[0005] The above mentioned and other objects and advantages are achieved according to the
invention by a method of the type mentioned, which shows the characteristic features
which are mentioned in the characterising part of claim 1 together with an apparatus
according to claim 5.
Summary of the invention
[0006] The method according to the invention accordingly concerns the treatment of aerosols
occurring during the treatment of materials where liquid is to be found, in a machine
included in the treatment process. A reduced pressure is arranged in said machine
so that in the case of a possible leakage the surrounding atmosphere can leak into
the machine. The method is characterised in that a reduced pressure is arranged through
liquid being pumped out of the machine, that a liquid suction device is driven by
the pumped out liquid, that aerosols and surrounding atmosphere that may possibly
have leaked in are sucked out of the machine by means of said liquid suction device,
whereby the aerosols are taken up in said liquid.
[0007] Said treatment process can especially be included in the treatment of waste in a
waste disposal plant at a nuclear power station in which a large amount of waste can
be a suspension of water and radioactive filtered substances. During treatment of
the radioactive suspensions radioactive aeosols arise in said machine.
[0008] Before the machine is taken out of service it is flushed with pure liquid. During
the flushing, process atmosphere is sucked out of the machine until any possible aerosols
which could be a danger to the surroundings have been removed. Subsequently extraction
is effected by means of a per se known ventilation system and then the machine is
taken out of service.
[0009] The apparatus, according to the invention for the treatment of aerosols occurring
during the treatment of materials where a liquid is present, is applied to a machine
which is included in a treatment process. A reduced pressure is arrangable in the
device so that in the case of a leak the surrounding atmosphere is able to leak into
the device. The apparatus is characterised in that a liquid pump is arranged for pumping
out liquid from the said machine. The liquid pump is coupled as a power source to
a liquid suction device, so that the liquid suction device's driving pressure is able
to be produced by means of the liquid pumped out of the machine. The machine is also
coupled to the liquid suction device's suction inlet so that the reduced pressure
in the machine is achieved by means of the liquid suction device. Both surrounding
atmosphere which may have leaked into the machine and aerosols produced during the
treatment are introducable into the liquid suction device for mixing with liquid,
so that said aerosols are able to be taken up in the liquid.
[0010] In a preferred embodiment of the invention said liquid pump is included in the process
machine. Said machine can be a separator, for example a decanting centrifuge, for
separating radioactive filter substances which are suspended in water.
[0011] The invention will now be described in more detail with the help of a working example
and with reference to the figures. In figure 1 is shown an outline diagram of one
embodiment of the invention arranged in a process machine in the form of a decanting
centrifuge, in figure 2a a preferred embodiment of a suction arrangement according
to the invention, and in figure 2b a side view of the suction arrangement according
to figure 2a.
Description of an embodiment
[0012] In figure 1 is shown fundamentally the principles of one embodiment of the invention,
arranged in a process machine 2, which in this example is an already known decanting
centrifuge. The decanting centrifuge is used in the embodying example to separate
by sedimenting solid particles and liquid from a pumpable slurry, which divides up
into a dry phase and a liquid phase during the centrifuging. The slurry is led in
a known manner from a sludge tank into a decanting centrifuge, via a pipe 4, through
slurry inlet 18, and is centrifuged in a conical rotor, after which the solid phase
of the slurry is removed through a dry phase outlet 8 and is fed, for example, to
a drying arrangement via a dry phase pipe 9. The liquid phase is pumped out through
a liquid phase outlet 16 by a liquid phase pump 14 built into the decanting centrifuge
2. In the embodiment shown in the figures the liquid phase pump is built in the decanting
centrifuge, but in other process machines a corresponding pump can be arranged separately.
During treatment of the slurry in the decanting centrifuge aerosols are produced,
which are removed through an aerosol outlet 20.
[0013] In accordance with the invention a liquid suction device, in this embodiment in the
shape of an ejector 22, which can be regarded as being known in principle, is arranged
coupled to liquid phase outlet 16 and aerosol outlet 20. During use ejector 22 is
driven by the liquid pumped out of the decanting centrifuge, whereby aerosols together
with any air which may have leaked into the decanting centrifuge are sucked into the
ejector through its suction inlet. In the ejector aerosols are combined with the liquid
and returned to the process liquid while at the same time the reduced pressure in
the decanting centrifuge is maintained. The liquid is then fed further via pipe 26
to some other process machine, to a chemical tank or back to the slurry tank where
it is blended to a homogenous liquid. The aerosols can also be led by means of an
adjustable valve 23 to, for example, a fan driven ventilation system. The ventilation
system is used to maintain a reduced pressure in the decanting centrifuge when it
is not in use and also functions as a reserve evacuating arrangement. There is preferably
a non-return valve in the liquid phase outlet. Liquid, which in this embodiment can
be deionised water, for cleaning the decanting centrifuge can be led in via pipe 10
and distributed via spray nozzles 12 and can also after being introduced through liquid
inlet 18 be flushed through rotor 6. A number of adjustable valves 11 are arranged
for controlling the cleaning liquid. After separating has finished the decanting centrifuge
2 is cleaned by means of cleaning liquid until it is free of radioactive aerosols.
Valve 23 is then set so that the reduced pressure in the decanting centrifuge is maintained
by means of the ventilation system, and subsequently liquid pump 14 and the liquid
flow can be switched off.
Ejector
[0014] Figure 2a shows a plan view and figure 2b a side view of a preferred embodiment of
an, in principle, already known ejector 22, comprising an ejector inlet 28, an ejector
outlet 30, a suction inlet 32 as well as a diffuser 34. The process liquid pumped
out of a process machine is led into ejector inlet 28 and is dispersed by diffuser
34 in ejector 22 so that a suction effect is produced at the suction inlet. Aerosols
which enter through suction inlet 32 are mixed with process liquid in the ejector
and are carried further through the ejector outlet. The liquid flow required through
the ejector is dependent on the process machines function and size. In this example
the liquid flow sometimes reaches 1.5 kg/s. The ejector's suction power can be adjusted
by changing the diffusers nozzle diameter and nozzle angle.
[0015] According to the preferred embodiment the ejector 22 is very simply designed and
gives a weak but controllable reduced pressure in the process machine. By regulating
the power of the liquid pump, the ejector's suction power can be controlled and thereby
the reduced pressure in the process machine can be regulated. The power of the ejector
can also be varied by the use of different diffuser nozzles. The ejector is preferably
mounted vertically, with the ejector inlet 28 and the suction inlet 32 in its upper
end.
[0016] The method and apparatus according to the invention is used in the preferred embodiment
for treating radioactive aerosols during the cleaning of waste water in a nuclear
power station. The invention, however, can also be used in any other process where
aerosols are present, or condensable or absorbable vapours or gases which one wishes
to return to a process liquid. It can, for example, be a matter of mixers, mills or
screwfeeds. It is also possible to use a separate circulation flow of liquid as the
drive source for the liquid suction device and collecting liquid for the aerosol or
the gas. In the case of gases or vapours, these are dissolved or condensed in the
fluid which flows through the ejector.
1. Method for the treatment of aerosols produced during the treatment of materials where
liquids are present, in a separator included in the treatment process, wherein a reduced
pressure is arranged in said separator to prevent the escape of contaminants from
the separator,
characterised in that:
- the reduced pressure is arranged by pumping liquid out of the separator,
- that a liquid suction device is powered by the pumped out liquid,
- aerosols and any of the surrounding atmosphere which may have leaked into the separator,
are sucked out of the separator by means of said liquid suction device, whereby the
aerosols are absorbed into said liquid.
2. Method according to claim 1, characterised in that said treatment process is included in the treatment of waste in a waste treatment
plant in a nuclear power station.
3. Method according to claim 1 or 2, characterised in that said liquid is a suspension of water and radioactive filtering substances, and
that radioactive aerosols are produced in said separator during said material treatment.
4. Method according to any of claims 1-3, characterised in that said separator, before it is taken out of service, is flushed with pure liquid,
that during flushing aerosols are sucked out of the separator until any possible aerosols
which pose a hazard to the surroundings have been removed, that subsequently said
sucking out is brought about by an in itself known ventilation system and that then
the separator is taken out of service.
5. Apparatus for the treatment of aerosols produced during treatment of materials where
a liquid is present, in a separator included in the treatment process, wherein a reduced
pressure is able to be arranged in the separator in order to prevent the release of
contaminants from the separator, characterised in that a liquid pump is arranged for pumping out liquid from said separator, said liquid
pump is connected as a power source to a water suction device so that the water suction
device's driving pressure is able to be generated by means of the liquid pumped out
of the separator, that the separator is coupled to the water suction device's suction
inlet so that a reduced pressure is brought about in the separator by means of the
liquid suction device, whereby any surrounding atmosphere which has leaked into the
separator as well as any aerosols arising from the treatment are able to be introduced
into the water suction device for mixing with the liquid, so that said aerosols are
able to be taken up in the liquid.
6. Apparatus according to claim 5, characterised in that said fluid pump is included in said separator.
7. Apparatus according to claim 5 or claim 6, characterised in that said separator is devised for the separating of radioactive filter substances
which are suspended in water.
8. Apparatus according to any of claims 5-7, characterised in that said separator is a decanting centrifuge.