Patent Publication Number: US-9849468-B2

Title: Cyclonic separator having stacked cyclones

Description:
REFERENCE TO RELATED APPLICATION 
     This application claims priority of United Kingdom Application No. 1318815.6 filed Oct. 24, 2013, the entire contents of which are incorporated herein by reference. 
     FIELD OF THE INVENTION 
     The present invention relates to a cyclonic separator having stacked cyclones. 
     BACKGROUND OF THE INVENTION 
     Vacuum cleaners which utilise cyclonic separators are well known. Cyclonic separators typically comprise a first cyclone stage and a second cyclone stage downstream of the first cyclone stage. The first cyclone stage, which is intended to remove larger dirt and debris, typically comprises a relatively large cyclone chamber, whereas the second cyclone stage, which is intended to remove finer dirt that is able to pass through the first cyclone stage, typically comprises a number of smaller cyclone bodies connected in parallel. 
     The smaller cyclone bodies are usually arranged in a ring around a longitudinal axis of the cyclonic separator. Through providing a plurality of relatively small cyclones in parallel instead of a single relatively large cyclone, the separation efficiency of the second cyclone stage (i.e. the ability to separate entrained particles from an air flow) can be increased. This is due to an increase in the centrifugal forces generated within the smaller cyclone bodies which cause dust particles to be thrown from the air flow. 
     Increasing the number of parallel cyclones can further increase the separation efficiency. However, when the cyclone bodies are arranged in a ring this can increase the external diameter of the cyclonic separator, which in turn can undesirably increase the size of the vacuum cleaner. While this size increase can be ameliorated through reducing the size of the individual cyclones, the extent to which the cyclone bodies can be reduced in size is limited. Very small cyclones can become rapidly blocked and can be detrimental to the rate of the air flow through the vacuum cleaner, and thus its cleaning efficiency. 
     In order to be able to increase the number of cyclone bodies in a cyclonic separator without increasing its external diameter, a recent trend has been to stack the cyclone bodies in two or more layers. Such a configuration is described in GB2475313. 
     Even when stacked in two or more layers, the cyclone bodies remain connected in parallel. In order that air reaches all layers of cyclones, a system of conduits, or ducts, is provided within the second cyclone stage. By way of example,  FIG. 1  shows a schematic representation of stacked cyclone bodies  10  according to a known configuration which shows sets of conduits  16  and  18  that convey air to the cyclone bodies  10 , and a further set of conduits  20  that convey air from the cyclone bodies  10 . Two layers of cyclone bodies are provided, a lower layer L and an upper layer U, each cyclone body  10  comprising an inlet  12  and a vortex finder  14  that serves as an outlet. Sets of inlet conduits  16  and  18  are provided to convey air from the first cyclone stage to the cyclone bodies  10  of the second cyclone stage. One set of these inlet conduits  16  is configured to convey air to the cyclone bodies  10  on the lower layer L, and the other set of conduits  18  is configured to convey air to the cyclone bodies  10  on the upper layer U. The vortex finders  14  of each of the cyclone bodies  10  on both the upper and lower layers L, U then feed into one of a number of outlet conduits  20  which convey the cleaned air downstream to a next stage in the cyclonic separator. 
     As can be seen from  FIG. 1 , the fluid paths through the conduits are different. This can lead to uneven loading of the air supply on the cyclone bodies  10 . For example, some cyclone bodies, through which an easier fluid path is available, will be under a greater load than other cyclone bodies that provide a more tortuous fluid path for the air to take. This creates inefficiency within the cyclonic separator, and can reduce the overall efficiency of the vacuum cleaner. 
     SUMMARY OF THE INVENTION 
     This invention provides a cyclonic separator comprising a first cyclone stage; and a second cyclone stage comprising a plurality of cyclone bodies arranged in parallel, each cyclone body comprising an inlet and an outlet, the plurality of cyclone bodies being divided into at least a first layer and a second layer; wherein the second cyclone stage further comprises a first plenum common to the cyclone bodies, the first plenum extending from the outlet of the first cyclone stage to the inlets of each of the cyclone bodies of the second cyclone stage. 
     As a result, air that enters the cyclone bodies is drawn from a single common volume, and so a more even loading of the air supply on the cyclone bodies can be achieved. If the cyclone bodies are loaded more evenly, this can help the cyclonic separator to separate dust and dirt from the air passing through it more efficiently, and may in turn result in a more efficient vacuum cleaner. 
     The second cyclone stage may further comprise a second plenum common to the cyclone bodies and extending from the outlet of each of the cyclone bodies. The second plenum makes it possible for all air leaving the cyclone bodies to be deposited into a single common volume, this in addition to the first plenum can go even further to achieve a more even loading of the air supply on the cyclone bodies, which can lead to a better separation efficiency and a more efficient vacuum cleaner. 
     The second plenum may substantially surround the first plenum. This allows the first plenum to extend to the inlets of the cyclone bodies in the second layer, while at the same time the second plenum can extend from the outlets of the cyclone bodies in the first layer. By having the second plenum substantially surround the first plenum, both plenums are able to be common to each of the cyclone bodies, and may help to prevent a need to increase the size of the cyclonic separator. 
     The cyclonic separator may comprise a further stage located downstream of the second cyclone stage, the second plenum may extend from the outlets of the cyclone bodies to the further stage, and the further stage may be one of a cyclone stage, a filter stage and a chamber comprising an outlet of the cyclonic separator. By having the second plenum extend from the outlets of the cyclone bodies to the further stage, the second plenum can take advantage of the maximum volume available to it which can go further to help even out the load of the air supply between the cyclone bodies. 
     The second and/or first plenum may be substantially annular. This can allow the plenum(s) to extend around to reach the whole ring of cyclone bodies, but at the same time also allows other components and stages within the cyclonic separator to be housed within the area surrounded by the plenum(s). 
     The inlet to the first plenum may be substantially annular. This allows air to be drawn into the first plenum from substantially the whole way around the inner circumference of the first cyclone stage. This can further aid to even the loading of the air supply on each of the cyclone bodies. 
     Each inlet may have the same size and dimensions as all the other inlets, and each outlet may have the same size and dimensions as all the other outlets. If all inlets to the cyclone bodies are the same size and have the same dimensions, this stops any uneven loading on the cyclone bodies due to differences in the inlets. The same applies to having all the outlets the same size and of the same dimensions to each other. 
     This invention further provides a cyclonic separator as herein described with reference to and as shown in the accompanying drawings. 
     This invention further provides a vacuum cleaner comprising a cyclonic separator as described in any one of the preceding statements. 
    
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
       In order that the present invention may be more readily understood, embodiments of the invention will now be described, by way of example, with reference to the accompanying drawings, in which: 
         FIG. 1  is a schematic representation of a known configuration of stacked cyclone bodies in a cyclonic separator; 
         FIG. 2  is a cylinder vacuum cleaner; 
         FIG. 3  is a cyclonic separator for a vacuum cleaner; 
         FIG. 4  is a plan view of the cyclonic separator of  FIG. 3 ; 
         FIGS. 5, 6   a  and  6   b  are schematic representations of cyclone bodies in the cyclonic separator of  FIG. 3 ; 
         FIG. 7  is a cross section through the cyclonic separator of  FIG. 3  along the line A-A; 
         FIG. 8 a    is a second cross section through the cyclonic separator of  FIG. 3  along the line B-B; 
         FIG. 8 b    shows a portion of  FIG. 8   a;    
         FIG. 9  is a cross section through the cyclonic separator of  FIG. 4  along the line C 6 -Y; and 
         FIG. 10  is a second cross section through the cyclonic separator of  FIG. 4  along the line D-D. 
     
    
    
     DETAILED DESCRIPTION OF THE INVENTION 
       FIG. 2  illustrates an external view of a cleaning appliance in the form of a vacuum cleaner  22 . The vacuum cleaner  22  is of the cylinder or canister type which typically has a body  24  which is pulled behind a hose and wand assembly  26  during use. Although  FIG. 2  shows a cylinder type vacuum cleaner, the presently claimed invention can be incorporated within any style of vacuum cleaner that comprises a cyclonic separator with stacked cyclones, other examples of which may be upright or handheld vacuum cleaners. 
     The body  24  comprises a cyclonic separator  28  for separating dirt and dust from an airflow, and a chassis  30 . The cyclonic separator  28  is received within the chassis  30  such that it is at least partially nested or docked within the chassis  30 . In use, a motor and fan unit located within the chassis  30  draws dust laden air into the vacuum cleaner  22 . The dirty air enters the body  24  from the hose and wand assembly  26  via an inlet duct, and into the cyclonic separator  28 . Dirt and dust particles entrained within the air flow are separated from the air and retained in the cyclonic separator  28 . The clean air then passes from the cyclonic separator into the chassis  30  and is subsequently expelled through air outlets in the body  24 . The cyclonic separator  28  is removable from the chassis  30  such that any dirt collected by the cyclonic separator  28  may be emptied. 
       FIG. 3  shows the cyclonic separator  28 . The cyclonic separator  28  comprises a first cyclone stage  32  and a second cyclone stage  34  located downstream of the first cyclone stage  32 . The first cyclone stage  32  is intended to remove relatively large dirt and debris, and the second cyclone stage  34  is intended to remove finer dirt that is able to pass through the first cyclone stage  32 . A handle  56  is provided at the top of the cyclonic separator  28  for carrying the cyclonic separator  28  and the body  24 . 
     The first cyclone stage  32  comprises an outer wall  36 , an inner wall  38 , a shroud  40  and a base  42 , which collectively define a cyclone chamber  44  and a first dirt collection chamber  46 . An inlet (not shown) to the cyclone chamber  44  is provided and arranged so as to introduce air into the cyclone chamber  44  in a substantially tangential direction in order to encourage the air to flow in a spiral or helical manner around the cyclone chamber  44 . The shroud  40  comprises a mesh  48  secured to an upper portion  50  and a lower portion  52 . Partially cleaned air exits the cyclone chamber  44  through the mesh  48  and is then directed towards the second cyclone stage  34 . 
     The second cyclone stage  34  comprises a second dirt collection chamber and a plurality of cyclone bodies  54  arranged in two layers about a longitudinal axis (shown as dotted line Y-Y in  FIG. 3 ) of the cyclonic separator  28 . The second cyclone stage  34  illustrated in the figures comprises two layers of cyclone bodies  54 . However, other alternative embodiments may contain more than two stacked layers of cyclone bodies  54 . 
     Although only a lower section of the inner wall  38  is visible in  FIG. 3 , it extends beneath the shroud  40  and joins to the base of the cyclone bodies  54  at the top of the first cyclone stage  32 . The inner wall  38  defines an inner cavity that is the second dirt collection chamber. The finer dirt captured by the second cyclone stage  34  is collected in the second dirt collection chamber. Both the first and second dirt collection chambers are closed at the lower end by the base  42 . The base  42  can be opened to allow both the first and second dirt collection chambers to be emptied. For example, the base  42  may be pivotably attached to the outer wall  36  by a hinge and can be held in a closed position by a catch which engages a lip located on the outer wall  36 . 
     A plan view of the cyclonic separator  28  is shown in  FIG. 4 . The handle  56  has been omitted from  FIG. 4  to show more clearly the arrangement of the cyclone bodies  54  in the second cyclone stage  34 . The embodiment of the figures shows a cyclonic separator  28  that has two layers of cyclone bodies, each layer comprising twelve cyclone bodies. The cyclone bodies extend nearly the entire way around the Y-Y longitudinal axis. It will be understood that in alternative embodiments, the cyclone bodies may be arranged differently within the layers, for example they may extend fully around the Y-Y longitudinal axis. Furthermore, different numbers of cyclone bodies may also be provided within the layers of the second cyclone stage  34 . The cyclone bodies  54  positioned in line with the dotted lines C1 to C6 are shown in the schematic representations of  FIGS. 5, 6   a  and  6   b.    
       FIG. 5  shows twelve cyclone bodies  54 . Each cyclone body  54  comprises an air inlet  60  and an air outlet in the form of a vortex finder  62 . The bottom end of each cyclone body  54  is open and extends into the second dirt collection chamber (not shown) such that any dust and dirt separated from the air within the cyclone body can be deposited into the second dirt collection chamber. The second dirt collection chamber is sealed so air can only exit the cyclone bodies  54  through the vortex finders  62  located at the top of each of the cyclone bodies  54 . Partially cleaned air arriving from the first cyclone stage  32 , shown as arrows T, enters a first plenum  64  in the second cyclone stage  34 . This first plenum  64  extends from the outlet of the first cyclone stage  32  to the inlets  60  of all of the cyclone bodies  54  in the second cyclone stage  34 , regardless of which level the cyclone bodies are on. Therefore the first plenum  64  acts as a common feed to all cyclone bodies  54  in the cyclonic separator  28 . As indicated by the arrows U, air is able to pass around the cyclone bodies  54  of the lower layer L within the first plenum  64 . As such, air located at any point within the first plenum  64  can potentially be drawn into any one of the cyclone bodies  54  within the second cyclone stage  34 . 
     Arrows V show the airflow pathway within the first plenum at the level containing the inlets for the lower layer L. Some of the air is drawn into the inlets  60  of the lower layer cyclone bodies C 1L , C 2L , C 3L , C 4L , C 5L  and C 6L , while the remainder of the air continues to progress up the first plenum towards the inlets of the cyclones in the upper layer U. 
     The air that does not enter the cyclone bodies of the lower level L is drawn into the inlets  60  of the upper layer cyclones C 1U , C 2U , C 3U , C 4U , C 5U  and C 6U . As air is drawn into the cyclone bodies  54 , more air continues to be drawn into the first plenum  64  from the first cyclone stage  32  to replace it. 
     As air passes through a cyclone body  54 , it spirals around and any dust that is entrained in the air is separated by centrifugal forces which cause the dust particles to be thrown from the air. The dust then passes through an opening in the bottom of the cyclone body  54  from which it is deposited into a second dust collection chamber, whereas the air passes back up the cyclone body towards the vortex finder  62 . 
     Once the air has passed through the vortex finders  62 , it then enters a second plenum  66 . The second plenum  66  is separate from the first plenum  64 , but is also common to all of the cyclone bodies  54  of the second cyclone stage  34 . The second plenum  66  extends from the outlet of each of the cyclone bodies  54  to an inlet of a further stage in the cyclonic separator  28 . In the present embodiment, the further stage is a filter stage. However, the further stage could equally be a further cyclone stage, or a chamber having an outlet of the cyclonic separator. The second plenum  66  therefore acts as a common volume into which the air from all of the cyclone bodies  54  is unloaded. The arrows X and Y show air exiting the vortex finders of the lower layer L and upper layer U cyclone bodies respectively and entering the second plenum  66 . 
     In order that the two plenums can more easily be distinguished, the schematic representation of  FIG. 5  is repeated in  FIGS. 6 a  and 6 b   . In  FIG. 6 a    the first plenum  64  has been highlighted using a first hatch pattern, and in  FIG. 6 b    the second plenum  66  has been highlighted using a second hatch pattern. These two hatch patterns are used uniformly throughout the figures to indicate the location of the first and second plenums  64 , 66 . 
     While passing through the second cyclone stage  34 , the air is not required or restricted to pass through any conduits or ducts. The air feeding into all the cyclone bodies comes from a single common volume, and this ensures that each of the cyclone bodies has an equal load of air supply passing through it. Although the representations of  FIGS. 5, 6   a  and  6   b  contain arrows that suggest the air takes specific pathways through the second cyclone stage  34 , it should be understood that the arrows merely indicate examples of the general airflow, and that, in practice, air within the first and second plenums is not restricted to following any particular pathway. 
     As can be seen in the figures, the inlet  60  and outlet  62  for each cyclone body  54  is the same as for all other cyclone bodies  54 . In other words, the sizes and dimensions of all inlets  60  are the same. In addition, the sizes and dimensions of all outlets  62  are the same. Consequently, there is no preferential loading of air supply on any of the cyclone bodies  54 . 
       FIG. 7  shows a cross section through the cyclonic separator  28  of  FIG. 3  which passes through the lower layer L of cyclone bodies  54 , denoted by dotted line A-A in  FIG. 3 . The first plenum  64  forms a ring between the cyclone bodies  54  and an inner wall  70 . The inner wall defines a chamber that houses a filter through which air is passed after leaving the second cyclone stage  34 . Inlets  60  of the cyclone bodies  54  are open to the first plenum  64  such that they are able to draw air into the cyclone bodies  54  from the first plenum  64 . Each of the inlets  60  opens directly onto the first plenum, therefore no ducting or conduits are required to direct the air towards the inlets  60 . No part of the second plenum  66  is visible at this level. For simplicity, the upper level U of cyclone bodies have been removed from view in this figure, but the first plenum  64  extends around the cyclone bodies of the upper level U which pass through the first plenum  64  at an angle inclined towards the longitudinal axis Y. 
       FIG. 8 a    shows a cross section through the cyclonic separator  28  of  FIG. 3  which passes through the upper layer U of cyclone bodies  54 , denoted by dotted line B-B in  FIG. 3 . The first plenum  64  is still visible and forms a ring around the inner wall  70 . The first plenum  64  extends to the inlets  60  of each of the cyclone bodies  54  in the upper layer U. In addition, the second plenum  66  can also be seen, and is located between the cyclone bodies  54  and the first plenum  64 . The second plenum appears, when viewed in cross-section at this level, to be a multiplicity of individual volumes. However, these seemingly separate volumes are all connected at other levels to form one plenum. In order to more easily view the first and second plenums  64 , 66  of  FIG. 8 a   , they have been reproduced in  FIG. 8 b    without the cyclonic separator visible. The second plenum  66  generally surrounds the first plenum  64 . 
       FIG. 9  shows a cross section through one half of the cyclonic separator along the line C 6 -Y shown in  FIG. 3 . This cross-section passes directly through the cyclone bodies C 6U  and C 6L . Each of cyclone bodies C 6U  and C 6L  has an outlet in the form of a vortex finder  62 . At the lower end of the cyclone bodies is an opening  72 . These openings  72  are open to an annular chamber which forms part of the second dirt collection chamber  74 . The dust that is separated by each of the cyclone bodies C 6U  and C 6L  is deposited through the openings  72  and will pass into the second dirt collection chamber  74 . Located around the outside of the second dirt collection chamber  74  is the shroud  75 . The shroud  75  has a wall having a multiplicity of through-holes, for example a mesh, and an inlet to the first plenum  64  (not visible in  FIG. 9 ) is located behind the wall of the shroud  75 . The cross section of  FIG. 9  passes through the first plenum  64  in two areas on the inner side of both cyclone bodies C 6U  and C 6L . The cross section of FIG.  9  also passes through the second plenum  66  in two places: one on the outer side of the upper cyclone body C 6U  at the opening of the vortex finder of C 6L , and the other above the cyclone bodies at the opening of the vortex finder of C 6U . The second plenum  66  has an annular outlet  76  at its uppermost point that feeds air into a filter stage  78  in the cyclonic separator  28 . 
       FIG. 10  shows a full cross section through the cyclonic separator  28  along the line D-D shown in  FIG. 3 . This cross-section passes between the cyclone bodies at C 6  and C 5 . This cross section clearly shows the two separate plenums, with the second plenum  66  substantially surrounding the first plenum  64 . The inlet  80  to the first plenum  64  is visible and is positioned behind the wall of the shroud  75  at the lowest point of the chamber that defines the first plenum  64 . 
     Whilst particular embodiments have thus far been described, it will be understood that various modifications may be made without departing from the scope of the invention as defined by the claims.