Abstract:
The cylindrical or conical shaped particle separator operates based on cyclone-induced flow sweeping the face of the cylindrical separator screen, creating inertial separation of suspended particles. The separator screen comprises of multitude of parallel, evenly spaced, asymmetrically profiled, linear, screen elements arranged in a cylindrical or conical grid-like shape parallel with the axis of the cylinder or cone. The cyclone effect is created by the rotational, helical path of the fluid inside or outside of the cylindrical or conical separator screen. The spinning, rotating fluid sweeps the inner or outer side of the stationary or rotating screen, passing approximately perpendicularly over the linear grid-like elements and gaps between the elements. The screen elements may be wires, bars, narrow strips, airfoil vanes or other similar linear elements with a flow separation edge on the trailing end of the profile of the element.

Description:
TECHNICAL FIELD 
     The present application relates generally to inertial separation of particulates suspended in or carried by fluids and specifically to, air filters, dust separators, clarifiers, cyclones, vacuum cleaners, precipitators, sifting screens, decanters, demisters, gaseous and fluid filtration devices alike. 
     BACKGROUND OF THE INVENTION 
     Separation of suspended particulates from fluids is a common filtration engineering task. Solid, semi-solid or gel-like particulates may be suspended or carried in a gases or liquids in motion. Small water droplets, spray-mist, sea salt, dust etc, may be suspended in the ambient air, carried by wind or blown by ventilation systems. Fly ash and unburned coal dust may be exhausted in the hot fumes of industrial boilers and combustors. Intakes of water treatment systems, desalination systems may have sand and suspended silt in the raw water. Wastewater and storm water may also carry large quantities of suspended solids. Various chemical, petrochemical and pharmaceutical processes may have liquids that have suspended bubbles of insoluble liquids (emulsion droplets) or small blobs of coagulated matter mixed in with the carrying liquid. The present application has a solution for the problem of efficient separation of such particles and droplets from fluids by means of inertial separation. In inertial separation technologies, local acceleration is used to induce inertial forces to the suspended particles required for separation. The concentration of particles is low or close to zero in the filtrate stream and high in the concentrate stream. The efficiency of separation is commonly expressed as the ratio of particle concentration in filtrate stream over the particle concentration in the feed stream. There are several known inertial separation technologies. Demister vanes, marine vane separators, inertial spin or swirl tubes, tuyere separators, centrifuges, variety of cyclones, etc. 
     Cyclone separation technology is widely used for removal of particulate matter from fluids without the use of filters. Cyclones are devices that create high speed rotating flow—or spinning field of fluid—in a cylindrical and conical vessel by inducing the fluid tangentially to the circumference of the cylinder. Centrifugal force and gravity are used to separate mixtures of solids and fluids. Air flows in a spiral pattern, beginning at the top (wide end) of the cyclone and ending at the bottom (narrow) end before exiting the cyclone in a straight stream through the center of the cyclone and out at the top. Larger and denser particles in the rotating stream have too much inertia to follow the curvature of the stream and strike the outside wall, falling then to the bottom of the cyclone where they can be removed. In a conical system, as the rotating flow moves towards the narrow end of the cyclone the radius of the stream curvature is reduced, separating smaller and smaller particles. Larger particles will be removed with a greater efficiency and smaller particles with a lower efficiency. The disadvantage of the currently known cyclone technology is that it has limited minimum streamline curvature (i.e. how small the curvature can be). The streamline curvature is largely defined by the radius of the cylindrical portion of the cyclone. As smaller curvature generally results in better separation efficiency, therefore the current cyclone technology has limited efficiency because the curvature of the cyclone is limited to the radius of its cylinder. The present application has improved separation efficiency over the current cyclones. 
     Various separation screens are also widely used in the field of liquid and gas filtration. There are several known inertial separator technologies such as demister vanes, marine vane separators, tuyere separators, water intake screens, etc. Few of these recently developed separator systems employ sweeping flow to facilitate and improve the separation of suspended matter. The sweeping flow is tangential to the surface of the separator while the pass-through flow is perpendicular to the surface. These recently introduced sweeping flow technologies utilize wedge wire screens for inertial separation, such as described in US20100224570. Wedge shaped wire screens are preferred for their low-maintenance operation. 
     The present application is the continuation of the inertial separation concept described in the Patent Application titled “Wedge Bar for Inertial Separation” U.S. Ser. No. 12/924,003 Asymmetrical separators elements are utilized, promoting small curvature accelerated flow across the linear gaps of the screen—separated from the flow sweeping the face side of the screen. 
     SUMMARY OF THE INVENTION 
     The present application describes a particle separator based on a cyclone induced sweeping flow. This cylindrical or conical shaped separator screen operates based on inertial separation of suspended particles in fluids. The separator screen comprises of multitude of parallel, evenly spaced, asymmetrically profiled, linear elements arranged in a cylindrical or conical shape parallel with the axis of the cylinder or cone. In one embodiment, the fluid mixed with particulates enters tangentially at the top end of the cylinder or cone through a high velocity jet. The cyclone effect is created by the rotational, helical path of the fluid inside of the cylindrical or conical separator screen. The spinning, rotating fluid sweeps the inner side of the separator, passing approximately perpendicularly over the linear elements and gaps between the elements. Part of the fluid will pass through the gaps of the separator to a collector-space that is an outer space, approximately coaxial with the separator-screen. The streamlines of the fluid passing through the gaps of the separator have sharp curvatures creating the acceleration conditions required for inertial separation of particulates. The particulates even those that are smaller than the openings of the separator screen—separate from the streamlines of the pass-through flow and continue on the helical path inside the cylinder. The pass-through fluid is clean while the rotating vortex flow inside the separator-screen is concentrated with particles. The spiraling flow sweeps the particles along the inner portion of the separator-screen and they are collected at the bottom cone and released from the cyclone. The separated, clean fluid leaves the cyclone from the coaxial collector space. The separator-screen elements may be wires, bars, narrow strips, blades, airfoils or other similar linear elements with a flow separation edge on the trailing end of the profile of the element. The separation edge facilitates a formation of sharply curved streamlines of the flow passing through the gaps of the separator-screen for high acceleration and effective inertial separation of particles. The protruding separation edge also facilitates a formation of gently curved un-separated sweeping streamlines that provide bridge effect, taking the particles over the gaps of the separator. 
     In another embodiment, the fluid mixed with particulates enters tangentially at the top end of the cylindrical vessel into the coaxial space between the inertial separator screen and the wall of the cylinder vessel. The cyclone effect is created by the rotational, helical path of the fluid imposed by wall of the cylinder vessel. The rotating fluid sweeps the outer side of the separator screen, passing over the linear elements. Part of the fluid will pass through the gaps of the separator to the central collector-space that is inside the separator-screen. The sharply curved streamlines of the fluid passing through the gaps of the separator-screen have the acceleration conditions required for inertial separation of particles. The particles—even though some are smaller than the screen openings—separate from the streamlines of the pass-through flow and continue on the helical path in the coaxial space outside the separator. The pass-through fluid is clean while the rotating vortex flow outside the separator screen is concentrated with particles. The spiraling cyclone-flow sweeps the particles along the outer portion of the separator-screen and they are collected at the bottom cone and released from the cyclone. The separated, clean fluid leaves the cyclone from the central collector space through an outlet pipe and port, located in the centerline of the apparatus. 
     In another embodiment, the inertial separation screen is a rotating (non-stationary) component of the system. The separation screen is rotating around of its cylindrical axis, in counter direction of the rotation of the tangentially entered mixed-fluid. The counter directional rotation enhances the inertial separation effect of the system. The fluid mixed with particulates enters tangentially at the top end of the cylindrical vessel into the coaxial space between the rotating inertial separator screen and the wall of the cylinder vessel. The rotating fluid sweeps the outer side of the rotating separator screen, passing over the linear elements that are moving in counter direction. Part of the fluid will pass through the gaps of the separator to the central collector-space that is inside the separator-screen. The particles separate from the streamlines of the pass-through flow and continue on the helical path in the coaxial space outside the separator. The pass-through fluid is clean while the rotating vortex flow outside the separator screen is concentrated with particles. The spiraling cyclone-flow sweeps the particles along the outer portion of the separator-screen and they are collected at the bottom cone and released from the cyclone. The separated, clean fluid leaves the cyclone from the central collector space through an outlet pipe and port, located in the centerline of the apparatus. 
     These and other features of the present application will become apparent to one of ordinary skill in the art upon review of the following detailed description when taken in conjunction with the several drawings and the appended claims. 
    
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         FIG. 1  shows one preferred embodiment of the cyclone induced sweeping flow separator. This embodiment is primarily for low pressure fluids. It has a single stage sweeping flow separator screen. The mixed fluid enters to the cyclone tangentially; the clean fluid leaves tangentially through a volute shaped collector space, while the separated particles are removed from the bottom. 
         FIG. 2  shows a two-stage sweeping flow separator screen. Two sweeping flow separators are installed in series in a single cyclone. The apparatus cleans the inlet fluid and separates the particulate matter into coarser and finer particles. The mixed fluid enters into the cyclone tangentially at the top and the clean fluid leaves tangentially through a volute collector space. The coarser and finer particles are removed from two solid outlets at the bottom of the cyclone. 
         FIG. 3  depicts another embodiment of the cyclone separator-screen. It is a single stage, high pressure device, where the inlet port and the two outlet ports are arranged conventionally as in the known cyclones. The mixed fluid tangentially enters the upper portion of the cyclone and creates a sweeping vortex flow along the internal surface of the cylindrical screen. The clean fluid passed through the separator-screen is collected in the outer, cylindrical portion of the vessel and leaves the system through the port at the top center. The concentrate with separated particles leaves at the bottom center. 
         FIG. 4  illustrates another embodiment of the cyclone induced sweeping flow separator screen. This apparatus is an integrated system with conventional cyclone action as well as sweeping flow separator action. The clean fluid is collected from the cylindrical outer portion as well as through the central collector tube from the bottom portion of the cyclone. The ratios of the flows from these two sources are balanced through a balancing valve and an ejector located in the upper extraction port. 
         FIG. 5  depicts four of multitude of possible profiles of the sweeping flow separator screen. The linear grid of screen elements creates sharply curved streamlines required for inertial separation of particles that are swept across the internal surface of the screen. The flow of clean fluid with curved streamlines passes through the gaps of the separator screen. 
         FIG. 6  depicts another embodiment of the cyclone induced sweeping flow separator. The direction of the flow through the separator screen is inward-radial from the perimeter to the center of the cyclone. The mixed fluid enters to the cyclone tangentially into the outer coaxial space and passes through the separator screen into the central collector space, while the separated particles are removed from the bottom of the outer space. 
         FIG. 7  depicts another embodiment of the cyclone induced sweeping flow separator. The rotational separator screen is rotating in counter direction of the tangentially entered inlet flow of fluid mixed with particles. The flow through the separator screen is inward-radial from the perimeter to the center of the cyclone. The mixed fluid enters to the cyclone tangentially into the outer coaxial space and passes through the separator screen into the central collector space, while the separated particles are removed from the bottom of the outer space. 
     
    
    
     DETAILED DESCRIPTION 
     Referring now to the drawings, in which like numerals indicate like elements,  FIG. 1  shows cross sectional views and details of one preferred embodiment of the cyclone induced sweeping flow separator screen. Multitude of parallel, asymmetrically profiled linear elements  101  are evenly spaced, separated by gaps  102  to form the linear grid of the cylindrical or slightly conical face of the separator-screen  103 . The mixed flow of fluid (gas or liquid) and particles enters the apparatus through the inlet port  104  at the top portion of the device. The inlet nozzle  105  accelerates and directs the flow tangentially to the face of the screen. This tangential entry generates a spinning, rotating, swirling motion of the fluid  106  inside the separator-screen that is also referred as cyclone effect. The rotating fluid sweeps the cylindrical face of the screen perpendicularly crossing  107  its linear grid elements  101 . Some of the fluid will pass through the gaps of the separator screen, with sharply curved streamlines  108  around the edges of the grid elements. The inertia of the particles in the mixed fluid will separate them from the curved streamlines of the fluid  108  passing through the separator screen and they will remain inside of the screen swept along the rotating cyclone flow  106 —even if they are smaller than the screen gaps. The sweeping cyclone flow and the gravity will carry the particles to the bottom portion of the device. The particles will collect in the bottom, cone shaped space  109  and are removed through the outlet port  110 . The separated fluid passed through the separator screen and enters in the clean-fluid collector space  111 . The clean fluid collector space is spiral shaped volute  112  formed around the separator screen. The volute has an outlet port  113  for the clean fluid. 
       FIG. 2  generally depicts the principle of operation of multi-stage sweeping flow separator screen and specifically one preferred embodiment of a two-stage sweeping flow separator screen. The multi-stage apparatus cleans the inlet fluid from particulates and separates the particulate matter into multitude of coarser to finer particles bins. The description of operation of the two stage separator shown on  FIG. 2  is as follows: The coarser flow separator  202  is embedded inside of the second finer flow separator  203 . They are connected in series as the fluid flows through the inner separator  202  first and the outer separator  203  second. The separator screens are mounted in the same cyclone-housing  212 . The fluid mixed with particles enters into the cyclone tangentially at the top through the inlet port  201  and is accelerated through the inlet nozzle  204 . The fluid is forced to a spinning rotational flow  207  along the inner, cylindrical wall of the coarser screen. This rotational-flow pattern is also referred to as cyclone effect. Asymmetrically profiled, vertically oriented linear elements  210  form the wall of the cylinder of the screen. The multitude of parallel, evenly spaced, linear elements separated by gaps form the linear grid of the cylindrical face of the separator screen. The rotational spinning flow sweeps across the screen-grid elements perpendicular to their longitudinal axis. Some of the fluid passes through the gaps of the separation screen  209 . The streamlines of the passing fluid are sharply curved. The larger, high-velocity particles are separated from the screened flow by their inertia and swept along, inside the cylinder of the separator screen. The particles pulled by gravity, travel on a helical path  211  down to the bottom inner collector cone  213  and are removed through a coarse-particle outlet port  214 . The fluid passed through the coarse inner screen is collected in a volute space  205  and guided by a spiral shaped wall  208 , through a tangential nozzle into the outer separator screen  216 . The outer screen is finer in that the linear screen-bar elements have a smaller pass-through gap. The mechanism of inertial separation of finer particulates in the outer screen is similar to the inner screen described above. The particles travel on a helical path  217  inside of the  216  downwards into the fine collector cone  218  and are removed through the fine particle outlet port  219 . The cleaned flow that passed the second stage separator-screen is collected in a spiral volute  206 —shaped by spirally formed outer wall  212  and leaves the device through the clean fluid outlet port  220 . 
       FIG. 3  presents another preferred embodiment of the cyclone separator-screen. The depicted device is a single stage separator, constructed for high pressures. The mixed fluid enters through the inlet port  301  and is accelerated through a converging nozzle  302 . The fluid jet enters tangentially into the vertically oriented, cylindrical or slightly conical cyclone  303 . The fluid is forced in a rotational helical downward path  304 . The fluid sweeps perpendicularly over the linear elements of the separator-screen  305 . Some of the fluid passes through the gaps of the screen forced on sharply curved streamlines  308 . The inertial forces acting on the particles separate them from the pass-through flow and they continue to be swept along the rotational path inside the cylinder of the separator-screen. The particles gradually fall down to the bottom collector cone  310  and are removed through the particulate outlet port  311 . The cleaned flow passed through the separator-screen, is collected in the cylindrical outer sleeve  306  and it flows upward  309  to the outlet port  312  located on the top of the system. Despite the similar external geometry, the embodiment presented on  FIG. 3  is substantially different than the known conventional cyclone separators because the applied principle of inertial separation: The present application utilizes the inertial separation forces on a small scale due to the sharply curved streamlines around the asymmetric profile of the linear screen grid elements. The rotational cyclone flow is only induced to maintain the sweeping flow over the cylindrical separator-screen. The known conventional cyclones use the inertial forces on the macro scale as the curvature of the streamlines are determined by the radius of the cylinder of the cyclone. In comparison the radius of curvature of the streamlines of the present application is smaller by several orders of magnitude compared to the radius of curvature of streamlines of known cyclone technologies. 
       FIG. 4  depicts another embodiment of the cyclone induced sweeping flow separator screen. This device is an integrated system with conventional cyclone action combined with sweeping flow separation-screen action. The mixed fluid enters the device through the inlet port  401  and is accelerated to a jet through a converging nozzle  402 . The jet enters tangentially into the cylindrical cyclone  403  of the separation screen  404  described in the previous paragraphs of this application. The fluid is forced to a helical downward path  405 . The fluid sweeps perpendicularly over the linear elements of the screen  404 . Portion of the fluid passes through the separation screen on sharply curved streamlines  407 . Inertial forces separate the particles from the pass-through flow and are swept along inside the cylinder of the screen. The cleaned flow passed through the separation-screen, is collected in the cylindrical outer sleeve  411  and it flows upward  412  to the outlet port  413  located on the top of the apparatus. The particles are carried down to the bottom portion of the cyclone toward the collector cone  408 . The following portion of the process is a conventional cyclone separation effect of the known technologies. In the converging cone the angular (rotational) speed of the spinning fluid increases—such that the inertial momentum of the fluid can be preserved. The increased rotational speed results in an increased centrifugal force. The particles are concentrated near the wall of the cone by centrifugal forces. The clean fluid is removed through the collector tube located at the center of the bottom portion of the cyclone  409 . The particles—separated by the combined inertial screen and conventional cyclone effect—are collected at the bottom of the cone and removed through the particulate outlet port  410 . There are two streams of clean fluid: one collected in the outer sleeve  412 , the other through the central collector tube  409 . The two streams are combined through an ejector  414  located in the outlet port  413 . The ratios of the flows from these two sources are balanced through a balancing valve  415  and an ejector  414 . The balancing valve also serves as a control device that may influence the efficiency of the separation for variable particle sizes. 
       FIG. 5  depicts four of multitude of possible profile geometries of the linear grid elements of the sweeping flow separator screen. The primary common objective and unique property of the grid element geometry is creation of sharply curved streamlines of the flow  502  passing through the gaps between the elements. In general: smaller the radius of the curvature of the streamline is, the smaller the size of the particle that will be separated from the pass-through flow and will remain on the face or concentrated side of the separator-screen. The secondary common objective and unique property of the grid element geometry is creation of least obstructed-low drag-flow conditions for the sweeping flow on the face side  503  of the screen. The separated particles remain on the swept side of the separator-screen and they must travel along the face of the screen with the seeping flow  501  with the least amount of resistance. In order to achieve these objectives all of the considered profiles must be asymmetrical with low-drag streamlined properties in direction of the sweep flow and must provide a highly curved streamlines for the flow passing through the gaps between the elements. For the purposes of this application the following nomenclature is applied to describe the orientations, directions and sides of the screen elements: The face side  503  is from where the mixed concentrated flow approaches the separator-screen. The clean side of the screen  504  is where the cleaned flow leaves the screen. Leading side  505  is facing the sweeping flow and trailing or after is side  506  where the sweeping flow leaves the profile. Consistent with this naming convention there are four quadrants of the profile: Leading-Face  507 , Leading-Clean  508 , Trailing-Face  509  and Trailing-Clean  510 . 
     The geometry of the linear grid screen element depicted on  FIG. 5 a    is a square profile with an attached, fastened, adhered, welded or otherwise secured lip or edge on the trailing-face quadrant of the element. The trailing edge is protruding into the sweeping flow on the face side of the separator-screen at an angle so the edge is leaning in the direction of the sweeping flow.  FIG. 5 b    illustrates a complex wedge-like solid-bar profile of the linear grid screen element with the protruding edge on the trailing-face quadrant of the profile. The angle of the protrusion of the edge tilts the edge in direction of the sweeping flow such that it is streamlined for small drag against the sweeping flow. The sharp protruding edge (lip) facilitates the small curvature streamlines of the passing through flow. The profile of the linear elements of the separator screen depicted on  FIG. 5 c    and  FIG. 5 d    may be fabricated out of sheet metal or plate material. The profiles form a sharply curved path between two adjacent elements thereby enhancing particle separation from the pass-through flow. The shape of the profile is streamlined for the sweeping flow across the separator screen face. The protruding edge—on the profile depicted on  FIG. 5 d   —has minimal resistance. The sizes and proportions of the linear screen elements and gaps may vary with the specific application. The approximate range of the gap-size may be from 0.2 mm to 100 mm. The gap-size is larger than the separated particle size. The approximate width size of the linear screen element may be from 0.8 mm to 250 mm. 
       FIG. 6  shows cross sectional views and details of another preferred embodiment of the cyclone induced sweeping flow separator. The direction of the flow through the separator screen with this embodiment is the opposite of direction of the previously described embodiments. The direction of the flow-through is inward-radial that is from the perimeter toward the center of the cyclone. The mixed fluid enters the cyclone tangentially into the outer coaxial space and passes through the separator screen into the central collector space, while the separated particles are removed from the bottom of the outer space. The mixed flow of fluid (gas or liquid) and particles enters the apparatus through the inlet port  601  at the top portion of the device. The inlet nozzle  602  accelerates and directs the flow tangentially into the coaxial cylindrical sleeve-like space  606  between the separator screen  605  and the outer wall of the cyclone  607 . This tangential entry generates a spinning, rotating, swirling motion of the fluid  604  that is also referred as cyclone effect. The rotating fluid sweeps the outer face of the cylindrical separator, perpendicularly crossing its linear grid elements  605 . As the fluid circulates around the separator screen, the fluid will gradually pass through the gaps of the separator, with sharply curved streamlines  608  around the edges of the grid elements  605 . The inertia of the particles in the mixed fluid will separate them from the curved streamlines of the fluid  608  passing through the separator and they will remain outside of the separator screen—despite the fact that the particles are smaller than the openings of the screen—and are swept along the rotating cyclone flow  604 . The sweeping cyclone flow and the gravity will carry the particles to the bottom portion of the device. The particles will collect in the bottom, cone shaped space  610  and are removed through the outlet port  611 . The separated fluid passes through the separator and it enters in the clean-fluid collector space  603  located in the center of the device. The clean fluid will be collected through a collector tube or pipe  613  located in the center line of the apparatus and exits the apparatus through port  612 . The efficiency of the conventional cyclone is significantly improved by the inertial separator screen because the sharply curved, small-scale streamlines formed around the elements and the gaps enhance the particle separation. 
       FIG. 7  shows cross sectional views and details of another preferred embodiment of the sweeping flow separator. This embodiment is different than the previously described ones in that the inertial separator screen is not stationary. The cylindrical/conical separator screen is turning around it longitudinal axis thereby providing a rotational motion to the separation elements and gaps. The direction of its rotation is opposite to the direction of the rotating cyclone flow, thus enhancing the particle separation efficiency of the system. The mixed fluid  701  enters the cyclone tangentially into the outer coaxial space  704  and passes through the separator screen into the central collector space, while the separated particles are removed from the bottom of the outer space  703 . The mixed flow of fluid (gas or liquid) and particles enters the apparatus through the inlet port  701  at the top portion of the device. The inlet nozzle  702  accelerates and directs the flow tangentially into the coaxial cylindrical sleeve-like space  706  between the separator screen  705  and the outer wall of the cyclone  707 . This tangential entry generates a spinning, rotating, swirling motion of the fluid  704 . The separator screen is mounted on bearings  715  and driven through a drive mechanism  716 . The direction of the rotation of the screen  714  is the opposite to the rotational direction of the fluid  704 . The rotating fluid sweeps the outer face of the rotating cylindrical separator at an increased sweeping speed as the tangential velocity of the rotating fluid is superimposed (added) to the tangential speed of the screen. The increased sweeping velocity enhances the acceleration of the fluid as it is perpendicularly crossing its linear grid elements  705  through the gaps. This enhanced acceleration improves the separation efficiency of the particles forcing them to remain in the coaxial space  706 . As the fluid circulates around the separator screen, the fluid will gradually pass through the gaps of the separator, with sharply curved streamlines  708  around the edges of the grid elements  705 . The inertia of the particles in the mixed fluid will separate them from the curved streamlines of the fluid  708  passing through the separator and they will remain outside of the separator screen. The sweeping cyclone flow and the gravity will carry the particles to the bottom portion of the device. The particles will collect in the bottom, cone shaped space  710 , and are removed through the outlet port  711 . The separated fluid passes through the separator and it enters in the clean-fluid collector space  703  located in the center of the device. The clean fluid will be collected through a collector tube or pipe  713  located in the center line of the apparatus and exits the apparatus through port  712 . The efficiency of the conventional cyclone is significantly improved by the inertial separator screen because the sharply curved, small-scale streamlines formed around the elements and the gaps enhance the particle separation.