Cyclonic Separating Apparatus
The invention relates to cyclonic separating apparatus. Particularly, but not exclusively,
the invention relates to cyclonic separating apparatus suitable for use in vacuum
cleaners.
Vacuum cleaners which utilise cyclonic separating apparatus are well known.
Examples of such vacuum cleaners are shown in EP 0042473, US 4,373,228, US
3,425,192, US 6,607,572 and EP 1268076. In each of these arrangements, first and
second cyclonic separating units are provided with the incoming air passing sequentially
through each separating unit. In some cases, the second cyclonic separating unit
includes a plurality of cyclones arranged in parallel with one another.
None of the prior art arrangements achieves 100% separation efficiency (ie the ability
reliably to separate entrained dirt and dust from the airflow), particularly in the context
of use in a vacuum cleaner. Therefore, it is an object of the invention to provide
cyclonic separating apparatus which achieves a higher separation efficiency than the
prior art.
The invention provides cyclonic separating apparatus comprising a first cyclonic
separating unit including at least one first cyclone; a second cyclonic separating unit
located downstream of the first cyclonic separating unit and including a plurality of
second cyclones arranged in parallel; and a third cyclonic separating unit located
downstream of the second cyclonic separating unit and including a plurality of third
cyclones arranged in parallel; characterised in that the number of second cyclones is
higher than the number of first cyclones and the number of third cyclones is higher than
the number of second cyclones.
Cyclonic separating apparatus according to the invention has the advantage that, when
the apparatus is considered as a whole, it has a separation efficiency which is improved
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as compared to the individual separation efficiencies of the individual cyclonic
separating units. The provision of at least three cyclonic separation units in series
increases the robustness of the system so that any variations in the airflow presented to
the downstream units have little or no effect on the ability of those units to maintain
their separation efficiency. The separation efficiency is therefore also more reliable as
compared to known cyclonic separating apparatus.
It will be understood that, by the term "separation efficiency", we mean the ability of a
cyclonic separating unit to separate entrained particles from an airflow and that, for
comparison purposes, the relevant cyclonic separation units are challenged by identical
airflows. Hence, in order for a first cyclonic separating unit to have a higher separation
efficiency than a second cyclonic separating unit, the first unit must be capable of
separating a higher percentage of entrained particles from an airflow than the second
unit when both are challenged under identical circumstances. Factors which can
influence the separation efficiency of a cyclonic separating unit include the size of the
inlet and outlet, the angle of taper and length of the cyclone, the diameter of the cyclone
and the depth of the cylindrical inlet portion at the upper end of the cyclone.
The increasing number of cyclones in each successive cyclonic separating unit allows
the size of each individual cyclone to decrease in the direction of the airflow. The fact
that the airflow has passed through a number of upstream cyclones means that the larger
particles of dirt and dust will have been removed which allows each smaller cyclone to
operate efficiently and without risk of blockage.
Preferably, the first cyclonic separating unit comprises a single first cyclone and, more
preferably, the or each first cyclone is substantially cylindrical. This arrangement
encourages larger particles of dirt and debris to be reliably collected and stored with a
relatively low risk of re-entrainment.
Embodiments of the invention will now be described with reference to the
accompanying drawings, in which:
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Figures 1 and 2 show cylinder and upright vacuum cleaners respectively incorporating
cyclonic separating apparatus;
Figure 3 is a sectional side view through the cyclonic separating apparatus forming part
of either of the vacuum cleaners shown in Figures 1 and 2;
Figure 4 is a sectional plan view of the cyclonic separating apparatus of Figure 3
showing the layout of the cyclonic separating units;
Figure 5 is a sectional side view of cyclonic separating apparatus according to the
invention;
Figure 6 is a sectional plan view of the cyclonic separating apparatus of Figure 5
showing the layout of the cyclonic separating units;
Figure 7 is a schematic diagram of first alternative cyclonic separating apparatus
according to the invention and suitable for forming part of either of the vacuum cleaners
shown in Figures 1 and 2; and
Figures 8 and 9 are schematic diagrams ■ of second and third alternative cyclonic
separating apparatuses according to the invention and suitable for forming part of either
of the vacuum cleaners of Figures 1 and 2.
Figure 1 shows a cylinder vacuum cleaner 10 having a main body 12, wheels 14
mounted on the main body 12 for manoeuvring the vacuum cleaner 10 across a surface
to be cleaned, and cyclonic separating apparatus 100 also mounted on the main body 12.
A hose 16 communicates with the cyclonic separating apparatus 100 and a motor and
fan unit (not shown) housed within the main body 12 for drawing a dirty airflow into
the cyclonic separating apparatus 100 via the hose 16. Commonly, a floor-engaging
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cleaner head (not shown) is coupled to the distal end of the hose 16 via a wand to
facilitate manipulation of the dirty air inlet over the surface to be cleaned.
In use, air drawn into the cyclonic separating apparatus 100 via the hose 16 has
entrained dirt and dust separated therefrom in the cyclonic separating apparatus 100.
The dirt and dust is collected within the cyclonic separating apparatus 100 while the
cleaned air is channeled past the motor for cooling purposes before being ejected from
the vacuum cleaner 10 via an exit port in the main body 12.
The upright vacuum cleaner 20 shown in Figure 2 also has a main body 22 in which a
motor and fan unit (not shown) is mounted and on which wheels 24 are mounted to
allow the vacuum cleaner 20 to be manoeuvred across a surface to be cleaned. A
cleaner head 26 is pivotably mounted on the lower end of the main body 22 and a dirty
air inlet 28 is provided in the underside of the cleaner head 26 facing the floor.
Cyclonic separating apparatus 100 is provided on the main body 22 and ducting 30
provides communication between the dirty air inlet 28 and the cyclonic separating
apparatus 100. A handle 32 is releasably mounted on the main body 22 behind the
cyclonic separating apparatus 100 so that the handle 32 can be used either as a handle or
in the manner of a wand. Such an arrangement is well known and will not be described
any further here.
in use, the motor and fan unit draws dirty air into the vacuum cleaner 20 via either the
dirty air inlet 28 or the handle 32 (if the handle 32 is configured for use as a wand). The
dirty air is carried to the cyclonic separating apparatus 100 via the ducting 30 and
entrained dirt and dust is separated from the airflow and retained in the cyclonic
separating apparatus 100. The cleaned air is passed across the motor for cooling
purposes and then ejected from the vacuum cleaner 20 via a plurality of outlet ports 34.
The present invention relates solely to the cyclonic separating apparatus 100 as will be
described below and so the detail of the remaining features of the vacuum cleaners 10,
20 are comparatively immaterial.
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The cyclonic separating apparatus 100 forming part of each of the vacuum cleaners 10,
20 is shown in Figures 3 and 4. The specific overall shape of the cyclonic separating
apparatus 100 can be varied according to the type of vacuum cleaner in which the
apparatus 100 is to be used. For example, the overall length of the apparatus can be
increased or decreased with respect to the diameter of the apparatus, or the shape of the
base can be altered so as to be, for example, frusta-conical.
The cyclonic separating apparatus 100 shown in Figures 3 and 4 comprises an outer bin
102 which has an outer wall 104 which is substantially cylindrical in shape. The lower
end of the outer bin 102 is closed by a base 106 which is pivotably attached to the outer
wall by means of a pivot 108 and held in a closed position (illustrated in Figure 3) by a
catch 110. In the closed position, the base is sealed against the lower end of the outer
wall 104. Releasing the catch 110 allows the base 106 to pivot away from the outer
wall 104 for purposes which will be explained below. A second cylindrical wall 112 is
located radially inwardly of the outer wall 104 and spaced therefrom so as to form an
annular chamber 114 therebetween. The second cylindrical wall 112 meets the base 106
(when the base is in the closed position) and is sealed thereagainst. The annular
chamber 114 is delimited generally by the outer wall 104, the second cylindrical wall
112, the base 106 and an upper wall 116 positioned at the upper end of the outer bin
102.
A dirty air inlet 118 is provided at the upper end of the outer bin 102 below the upper
wall 116. The dirty air inlet 118 is arranged tangentially to the outer bin 102 (see Figure
4) so as to ensure that incoming dirty air is forced to follow a helical path around the
annular chamber 114. A fluid outlet is provided in the outer bin 102 in the form of a
shroud 120. The shroud 120 comprises a cylindrical wall 122 in which a large number
of perforations 124 are formed. The only fluid outlet from the outer bin 102 is formed
by the perforations 124 in the shroud. A passage 126 is formed between the shroud 120
and the second cylindrical wall 112, which passage 126 communicates with an annular
chamber 128.
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The annular chamber 128 is arranged radially outwardly of the upper end of a tapering
cyclone 130 which lies coaxially with the outer bin 102. The cyclone 130 has an upper
inlet portion 132 which is generally cylindrical in shape and in which two air inlets 134
are formed. The inlets 134 are spaced about the circumference of the upper inlet portion
132. The inlets 134 are slot-like in shape and communicate directly with the annular
chamber 128. The cyclone 130 has a tapering portion 136 depending from the upper
inlet portion 132. The tapering portion 136 is frusto-conical in shape and terminates at
its lower end in a cone opening 138.
A third cylindrical wall 140 extends between the base 106 and a portion of the outer
wall of the tapering portion 136 of the cyclone 130 above the cone opening 138. When
the base 106 is in the closed position, the third cylindrical wall 140 is sealed
thereagainst. The cone opening 138 thus opens into an otherwise closed cylindrical
chamber 142. A vortex finder 144 is provided at the upper end of the cyclone 130 to
allow air to exit the cyclone 130.
The vortex finder 144 communicates with a plenum chamber 146 located above the
cyclone 130. Arranged circumferentially around the plenum chamber 146 are a
plurality of cyclones 148 arranged in parallel with one another. Each cyclone 148 has a
tangential inlet 150 which communicates with the plenum chamber 146. Each cyclone
148 is identical to the other cyclones 148 and comprises a cylindrical upper portion 152
and a tapering portion 154 depending therefrom. The tapering portion 154 of each
cyclone 148 extends into and communicates with an annular chamber 156 which is
formed between the second and third cylindrical walls 112, 140. A vortex finder 158 is
provided at the upper end of each cyclone 148 and each vortex finder 158
communicates with an outlet chamber 160 having an exit port 162 for ducting cleaned
air away from the apparatus 100.
As has been mentioned above, the cyclone 130 is coaxial with the outer bin 102. The
eight cyclones 148 are arranged in a ring which is centred on the axis 164 of the outer
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bin 102. Each cyclone 148 has an axis 166 which is inclined downwardly and towards
the axis 164. The axes 166 are all inclined to the axis 164 at the same angle. Also, the
angle of taper of the cyclone 130 is greater than the angle of taper of the cyclones 148
and the diameter of the upper inlet portion 132 of the cyclone 130 is greater than the
diameter of the cylindrical upper portion 152 of each of the cyclones 148.
In use, dirt-laden air enters the apparatus 100 via the dirty air inlet 118 and, because of
the tangential arrangement of the inlet 118, the airflow follows a helical path around the
outer wall 104. Larger dirt and dust particles are deposited by cyclonic action in the
annular chamber 114 and collected therein. The partially-cleaned airflow exits the
annular chamber 114 via the perforations 124 in the shroud 122 and enters the passage
126. The airflow then passes into the annular chamber 128 and from there to the inlets
134 of the cyclone 130. Cyclonic separation is set up inside the cyclone 130 so that
separation of some of the dirt and dust which is still entrained within the airflow occurs.
The dirt and dust which is separated from the airflow in the cyclone 130 is deposited in
the cylindrical chamber 142 whilst the further cleaned airflow exits the cyclone 130 via
the vortex finder 144. The air then passes into the plenum chamber 146 and from there
into one of the eight cyclones 148 wherein further cyclonic separation removes some of
the dirt and dust still entrained. This dirt and dust is deposited in the annular chamber
156 whilst the cleaned air exits the cyclones 148 via the vortex finders 158 and enters
the outlet chamber 160. The cleaned air then leaves the apparatus 100 via the exit port
162.
Dirt and dust which has been separated from the airflow will be collected in all three of
the chambers 114, 142 and 156. In order to empty these chambers, the catch 110 is
released to allow the base 106 to pivot about the hinge 108 so that the base falls away
from the lower ends of the cylindrical walls 104, 112 and 140. Dirt and dust collected
in the chambers 114,142, 156 can then easily be emptied from the apparatus 100.
It will be appreciated from the foregoing description that the apparatus 100 includes
three distinct stages of cyclonic separation. The outer bin 102 constitutes a first

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cyclonic separating unit consisting of a single first cyclone which is generally
cylindrical in shape. In this first cyclonic separating unit, the relatively large diameter
of the outer wall 104 means that, primarily, comparatively large particles of dirt and
debris will be separated from the airflow because the centrifugal forces applied to the
dirt and debris are relatively small. Some fine dust will be separated as well. A large
proportion of the larger debris will reliably be deposited in the annular chamber 114.
The cyclone 130 forms a second cyclonic separating unit. In this second cyclonic
separating unit, the radius of the second cyclone 130 is much smaller than that of the
outer wall 104 and so the centrifugal forces applied to the remaining entrained dirt and
dust are much greater than those applied in the first cyclonic separating unit. Hence the
efficiency of the second cyclonic separating unit is higher than that of the first cyclonic
separating unit. The performance of the second cyclonic separating unit is also
enhanced because it is challenged with an airflow in which a smaller range of particle
sizes is entrained, the larger particles having been removed by the cyclonic separation
which has already taken place in the first cyclone of the first cyclonic separating unit.
The third cyclonic separating trait is formed by the eight smaller cyclones 148. In this
third cyclonic separating unit, each third cyclone 148 has an even smaller diameter than
the second cyclone 130 of the second cyclonic separating unit and so is capable of
separating finer dirt and dust particles than the second cyclonic separating unit. It also
has the added advantage of being challenged with an airflow which has already been
cleaned by the first and second cyclonic separating units and so the quantity and average
size of entrained particles is smaller than would otherwise have been the case. This
reduces any risk of blockage of the inlets and outlets of the cyclones 148.
The separation efficiency of the first cyclonic separating unit is thus lower than the
separation efficiency of the second cyclonic separating unit and the separation
efficiency of the second cyclonic separating unit is lower than the separation efficiency
of the third cyclonic separating unit. By this, we mean that the separation efficiency of
the first cyclone is lower than the separating efficiency of the second cyclone and the

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separating efficiency of the second cyclone is lower than the separating efficiency of all
eight third cyclones taken together. Hence, the separation efficiency of each successive
cyclonic separating unit increases.
Cyclonic separating apparatus 200 according to the invention is shown in Figures 5 and
6. The apparatus 200 is similar in structure to the embodiment shown in Figures 3 and
4 and described in detail above in that it is suitable for use in either of the vacuum
cleaners 10, 20 shown in Figures 1 and 2 and it comprises three successive cyclonic
separating units.
As described above, the first cyclonic separating unit consists of a single, cylindrical
first cyclone 202 which is delimited by an outer cylindrical wall 204, a base 206 and a
second cylindrical wall 212. A dirty air inlet 218 is provided tangentially to the outer
wall 204 to ensure that cyclonic separation occurs in the first cyclone 202 and larger
particles of dirt and debris are collected in the annular chamber 214 at the lower end of
the cyclone 202. As before, the only exit from the first cyclone 202 is via the
perforations 224 in the shroud 222 into a passage 226 located between the shroud 222
and the second cylindrical wall 212.
In this embodiment, the second cyclonic separating unit consists of two tapering second
cyclones 230 arranged in parallel with one another. The second cyclones 230 are
located side by side inside the outer wall of the apparatus 200 as can be seen in Figure
6. Each second cyclone 230 has an upper inlet portion 232 in which at least one inlet
234 is provided. Each inlet 234 is orientated for tangential introduction of air into the
upper inlet portion 232 and communicates with a chamber 228 which, in turn,
communicates with the passage 226. Each second cyclone 230 has a frusto-conical
portion 236 depending from the upper inlet portion 232 and terminating in a cone
opening 238. The second cyclones 230 project into a closed chamber 242. Each second
cyclone 230 has a vortex finder 244 located at the upper end thereof and communicating
with a chamber 246.
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The third cyclonic separating unit consists of four third cyclones 248 arranged in
parallel. Each third cyclone 248 has an upper inlet portion 252 which includes an inlet
250 communicating with the chamber 246. Each third cyclone 248 also has a frusto-
conical portion 254 depending from the inlet portion 252 and communicating with a
closed chamber 256 via a cone opening. The chamber 256 is closed with respect to the
chamber 242 by means of a pair of walls 270 (see Figure 6). Each third cyclone 248 has
a vortex finder 258 located at the upper end thereof and communicating with an outlet
chamber 260 having an exit port 262.
The first cyclone 202 has an axis 264, each, second cyclone 230 has an axis 265 and
each third cyclone has an axis 266. In this embodiment, the axes 264, 265 and 266 lie
parallel to one another. However, the diameters of the first, second and third cyclones
202, 230, 248 decrease to provide increasing separation efficiencies in successive
cyclonic separating units.
The apparatus 200 operates in a manner similar to the operation of the apparatus 100
shown in Figures 3 and 4. Dirt-laden air enters the first cyclone 202 of the first cyclonic
separating apparatus via the inlet 218 and circulates around the chamber 214 so that
larger dirt particles and debris are separated by cyclonic action. The dirt and dust
collects in the lower portion of the chamber 214 whilst the cleaned air exits the chamber
214 via the perforations 224 in the shroud 222. The air passes through the passage 226
to the chamber 228 and then to the inlets 234 of the second cyclones 230. Further
cyclonic separation takes place in the second cyclones 230, which operate in parallel.
Dirt and dust separated from the airflow is deposited in the chamber 242 whilst the
further cleaned air exits the second cyclones 230 via the vortex finders 244. The air
then enters the third cyclones 248 via the inlets 250 and further cyclonic separation
takes place therein with separated dirt and dust being deposited in the chamber 256.
The cleaned airflow exits the apparatus 200 via the chamber 260 and the exit port 262.
Each cyclonic separating unit has a separation efficiency which in greater than that of
the previous cyclonic separating unit. This allows the second and third cyclonic

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separating units to operate more effectively because they are challenged with an airflow
in which a smaller range of particles is entrained.
Each of the cyclonic separating units can consist of different numbers and different
shapes of cyclone. Figures 7 to 9 illustrate schematically three further alternative
configurations which fall within the scope of this invention. In these illustrations, all
detail will be omitted other than the number and general shape of the cyclones which
make up each cyclonic separating unit.
Firstly, in Figure 7, the apparatus 300 comprises a first cyclonic separating unit 310, a
second cyclonic separating unit 320 and a third cyclonic separating unit 330. The first
cyclonic separating unit 310 comprises a single first cyclone 312 which is cylindrical in
shape. The second cyclonic.separating unit 320 comprises two frusto-conical second
cyclones 322 arranged in parallel and the third cyclonic separating unit 330 comprises
eight frusto-conical third cyclones 332, also arranged in parallel. In this embodiment,
the dimensions of the third cyclones 332 are much smaller than those of the second
cyclones 322 and the separating efficiency of the third cyclonic separating unit 330 is
higher than that of the second cyclonic separating unit 320.
In the arrangement shown in Figure 8, the apparatus 400 comprises a first cyclonic
separating unit 410, a second cyclonic separating unit 420 and a third cyclonic
separating unit 430. The first cyclonic separating unit 410 comprises a single first
cyclone 412 which is cylindrical in shape. The second cyclonic separating unit 420.
comprises three cylindrical second cyclones 422 arranged in parallel and having
diameters which are considerably smaller than the diameter of the first cyclone 410.
The third cyclonic separating unit 430 comprises twenty-one frusto-conical third
cyclones 432, also arranged in parallel. The dimensions of the third cyclones 432 will
be very much smaller than those of the second cyclones 422 and so the separating
efficiency of the third cyclonic separating unit 430 will be higher than that of the second
cyclonic separating unit 420

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In the arrangement shown in Figure 9, the apparatus 500 comprises a first cyclonic
separating unit 510, a second cyclonic separating unit 520 and a third cyclonic
separating unit 530. The first cyclonic separating unit 510 comprises two, relatively
large first cyclones 512 which are frusto-conical in shape. The second cyclonic
separating unit 520 comprises three frusto-conical second cyclones 522 arranged in
parallel but having diameters which are considerably smaller than the diameter of the
first cyclones 510. The third cyclonic separating unit 530 comprises four frusto-conical
third cyclones 532, also arranged in parallel. The dimensions of the third cyclones 532
will be smaller again than those of the second cyclones 522 and so the separating
efficiency of the third cyclonic separating unit 530 will be higher than that of the second
cyclonic separating unit 520.
The arrangements illustrated in Figures 7 to 9 are intended to show that the number and
shape of the cyclones forming each cyclonic separating unit can be varied. It will be
understood that other arrangements are also possible. For example, another suitable
arrangement is to use a first cyclonic separating unit comprising a single cyclone, a
second cyclonic separating unit comprising two cyclones in parallel and a third cyclonic
separating unit comprising eighteen cyclones in parallel.
It will be understood that further cyclonic separating units can be added downstream of
the third cyclonic separating unit if desired. It will also be understood that the cyclonic
separating units can be physically arranged to suit the relevant application. For
example, the second and/or third cyclonic separating units can be arranged physically
outside the first cyclonic separating unit if space permits. Equally, if any one of the
cyclonic separating units includes a large number of cyclones, the cyclones can be
arranged in two or more groups or include cyclones of different dimensions.
Furthermore, the cyclones included within a multi-cyclone separating unit can be
arranged such that their axes lie at different angles of inclination to the central axis of
the apparatus. This can facilitate compact packaging solutions.

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We claim:
1. Cyclonic separating apparatus comprising: a first cyclonic separating unit
including at least one first cyclone; a second cyclonic separating unit located
downstream of the first cyclonic separating unit and including a plurality of second
cyclones arranged in parallel; and a third cyclonic separating unit located downstream
of the second cyclonic separating unit and including a plurality of third cyclones
arranged in parallel; characterised in that the number of second cyclones is higher than
the number of first cyclones and the number of third cyclones is higher than the number
of second cyclones.
2. Cyclonic separating apparatus as claimed in claim 1, wherein the first cyclonic
separating unit comprises a single first cyclone.
3. Cyclonic separating apparatus as claimed in claim 1 or 2, wherein the or each
first cyclone is substantially cylindrical.
4. Cyclonic separating apparatus as claimed in any one of claims 1 to 3, wherein
the second cyclones are substantially identical to one another and the third cyclones are
substantially identical to one another.
5. Cyclonic separating apparatus as claimed in any one of the preceding claims,
wherein each second and third cyclone is tapering in shape.
6. Cyclonic separating apparatus as claimed in claim 5, wherein each second and
third cyclone is frusto-conical.
7. Cyclonic separating apparatus as claimed in claim 6, wherein the angle of taper
of each second cyclone is greater than the angle of taper of each third cyclone.

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8. Cyclonic separating apparatus as claimed in any one of the preceding claims,
wherein each second cyclone has at least two inlets which communicate with the first
cyclonic separating unit.
9. Cyclonic separating apparatus as claimed in claim 8, wherein the inlets to each
second cyclone are circumferentially spaced about an axis of the relevant second
cyclone.
10. Cyclonic separating apparatus as claimed in any one of the preceding claims,
wherein each cyclonic separating unit has a collector which can be emptied
simultaneously with the other collectors.
11. Cyclonic separating apparatus as claimed in any one of the preceding claims and
further comprising additional cyclonic separating units downstream of the third
separating unit, the or each additional cyclonic separating unit including a plurality of
further cyclones arranged in parallel and the number of further cyclones being greater
than the number of cyclones included in the cyclonic separating unit immediately
upstream thereof.
12. Cyclonic separation apparatus substantially as hereinbefore described with
reference to any one of the embodiments shown in the accompanying drawings.
13. A vacuum cleaner incorporating cyclonic separation apparatus according to any
one of the preceding claims.
Dated this 27th day of November, 2007.
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Cyclonic separating apparatus according to the invention comprises a first cyclonic
separating unit (310, 410; 510) including at least one first cyclone (102; 202; 312; 412;
512), a second cyclonic separating unit (320; 420; 520) located downstream of the first
cyclonic separating unit (310, 410; 510) and including a plurality of second cyclones
(130; 230; 322; 422; 522) arranged in parallel, and a third cyclonic separating unit (330;
430; 530) located downstream of the second cyclonic separating unit (320; 420; 520) and
including a plurality of third cyclones (148; 248; 332; 432; 532) arranged in parallel.
The number of second cyclones (130; 230; 322; 422; 522) is higher than the number of
first cyclones (102; 202; 312; 412; 512) and the number of third cyclones (148; 248; 332;
432; 532) is higher than the number of second cyclones (130; 230; 322; 422; 522). This
provides an apparatus which achieves a higher separation efficiency than known
separation apparatus.