Abstract:
A self-cleaning centrifugal dryer system and method for removing surface moisture allow complete removal of plastic pellets, flakes and particles from the dryer and water-conveying or water processing system during or after each drying cycle. By eliminating plastic particulate retention in the dryer and throughout the water conveyance and processing systems whereby contamination of different type materials dried during a subsequent drying cycle is avoided. Air and water alone or in combination under pressure are discharged toward various accumulation or occlusion (“hang-up”) points in the dryer and throughout the water-conveying or processing system to remove retained plastic pellets, flakes and particles.

Description:
CROSS REFERENCE TO RELATED APPLICATION 
   This patent application is a continuation-in-part of U.S. patent application Ser. No. 10/967,305 filed Oct. 19, 2004 now U.S. Pat. No. 7,171,762, both of which are commonly owned by the same assignee. 

   FIELD OF THE INVENTION 
   The present invention generally relates to a centrifugal dryer system and more specifically to a self-cleaning dryer, water-conveying system, and/or water processing system, and method for removing surface moisture from plastic pellets, flakes, or particles discharged into the dryer in the form of a slurry in water and eliminating plastic particulate retention in the dryer and throughout the water conveyance and processing systems whereby contamination of different type materials dried during a subsequent drying cycle is avoided. Air or water alone or in combination under pressure is discharged toward various accumulation or occlusion points in the dryer and throughout the water-conveying or processing systems to remove retained plastic particles, flakes, or pellets. 
   BACKGROUND OF THE INVENTION 
   Underwater pelletizers which produce a pelletized product in the form of a slurry of pellets and water are well known for many years in the pelletizing industry as well as in patents of the assignee from as early as U.S. Pat. No. 4,123,207 issued Oct. 31, 1978. Centrifugal dryers are also well known in the prior art and have been disclosed by the assignee as early as U.S. Pat. No. 3,458,045 issued Jul. 29, 1969, and more recently in U.S. Pat. Nos. 5,265,347 (issue date Nov. 30, 1993), 6,237,244 (issue date May 29, 2001), 6,739,457 (issue date May 25, 2004), and 6,807,748 (issued Oct. 26, 2004). Details of these patents are included herein, in whole or in part, by way of reference. 
   The centrifugal pellet dryers in the prior art satisfactorily dry plastic particles, and particularly plastic pellets when properly operated. However, existing dryers have areas in which the plastic pellets and particles, and particularly plastic flakes, being dried, become lodged, form occlusions, or otherwise, accumulate. These areas are generally known as hang-up points in which pellets or plastic flakes or particles remain after a drying cycle has been completed. The pellets, flakes or particles lodged in various hang-up points may present a contamination problem in sequential drying cycles even when the same pellet slurry is supplied to the dryer. 
   Of more significant concern, a centrifugal dryer is commonly used to dry different plastic particles during sequential drying cycles. When a subsequent drying cycle is drying plastic particles different from those in a previous drying cycle, some of the particulates of the previous drying cycle that have been lodged in the hang-up points will be entrained in and mixed with different plastic pellets, flakes, or particles being dried in a subsequent drying cycle. This circumstance results in contamination of the plastic particles being dried in the subsequent drying cycle by those retained in the hang-up points during a previous drying cycle. 
   The build-up of plastic particles during water conveyance or processing may lead to hang-up points in other parts of the system other than the dryer, or may restrict flow through the system by clogging or occlusion, and may lead to downstream contamination where plastic particles are released from the hang-up points, clogs or occlusions, periodically and unpredictably. 
   The present invention is a self-cleaning dryer, water-conveying system and/or water processing system and a method of use which overcome the problems of hang-up points in prior art dryers as well as in the water conveying and processing systems similarly contaminated by hang-up points and occlusions by eliminating the particulate build-up from the hang-up points, clogs, and occlusions. Thus, contamination of plastic pellets, flakes or particles being dried in a drying cycle by residuals retained in various hang-up points, clogs, or occlusions during a previous drying cycle in which different particulates were processed is avoided. 
   SUMMARY OF THE INVENTION 
   The centrifugal dryer and water conveying and processing system in accordance with this invention includes a combination of high pressure air and/or water directed toward the hang-up points or areas of the dryer in which pellets, flakes, or particles being dried have become lodged as well as similar hang-up points, clogs or occlusions in the related water-conveyance and processing system. The self-cleaning method eliminates contamination of plastic particulates subsequently passing through the dryer by previously dried particulates that have become lodged in the afore-mentioned hang-up points, clogs, or occlusions. 
   The self-cleaning dryer and method of the present invention enable complete removal of all plastic pellets, flakes, or particles from the dryer and subsequent systems during one drying cycle thereby eliminating contamination of plastic particulates being dried in a subsequent drying cycle. The air and water pressure are discharged toward various hang-up points throughout the dryer and water systems. Timing controls operate various stages of the discharge of the pressurized air and water. As used in this specification, the term “pressurized fluid” is intended to include pressurized water or other liquid, pressurized air or other gas, or any combination of the foregoing. 
   For use in accordance with this invention, the air or other gas is preferably pressurized from about 60 psi to about 80 psi, or more, and the water or other liquid is pressurized to flow at a rate of at least 40 gallons per minute (gpm) and is preferably at 80 gpm or more. Combinations of air and water pressure for cleaning purposes herein described are pressurized similarly to the individual parameters stated above. 
   The self-cleaning centrifugal dryer in accordance with this invention includes a generally vertical housing, a substantially cylindrical foraminous membrane or screen mounted within the housing, and a slurry inlet at a lower end of the housing communicating with the lower end of the screen. The screen includes a perforated, pierced, or laser-cut peripheral wall in spaced relation to the housing. A rotor, provided with inclined radial lifting blades, is mounted inside the screen. The rotor is drivingly connected to a motor and the upper end portion of the screen is communicated with a dried particle discharge chute, and the water separated from the particulates is discharged into an underlying water tank. As used in this specification, the terms “particles” and “particulates” are intended to broadly include pellets, flakes, fines and other solids exiting in the slurry from an underwater pelletizer. 
   An agglomerate catcher and dewaterer preferably receive the slurry of water and plastic particulates in advance of the dryer. The agglomerate catcher first catches, separates and subsequently discharges agglomerated particulates before the slurry enters the dewaterer. The dewaterer then separates the bulk water from the particulates prior to entrance to the dryer screen at the lower end thereof. Once the water has been removed, the particulates still include surface moisture which is removed during elevational and centrifugal movement of those particulates by rotation of the rotor within the screen and circulation of air by a blower which removes moisture from the interior of the housing. The above described dryer and its operation are representative of well known centrifugal dryers with agglomerate catchers and dewatering devices. 
   During normal operation of the dryer, some particulates become lodged in hang-up points or areas in the dryer as well as in valves in a water box bypass of the underwater pelletizer. The removal of the particulates in these hang-up points in the self-cleaning dryer of this invention eliminates contamination from a previous drying cycle whereby particles, flakes, or pellets may subsequently be picked up and mixed with particulates of a different type being dried in a subsequent drying cycle. The elimination of this contamination is accomplished by introducing high pressure fluid into the hang-up areas at the end of each drying cycle for one type particulate, thereby cleaning any residual particulates from the dryer before commencing a subsequent drying cycle for another type particle. 
   The self-cleaning centrifugal dryer of the present invention includes the introduction of timed discharge of pressurized fluid through fixed or movable spray nozzles strategically located to purge or remove particulates lodged in the hang-up points of, or otherwise left in, the dryer and water conveyance or processing systems. Self-cleaning for the dryer is accomplished in part by spray nozzles oriented in circumferentially spaced and vertically staggered relation between the interior of the housing and the exterior of the cylindrical screen. These spray nozzles direct a high pressure fluid against the interior wall of the housing, the exterior wall of the cylindrical screen, and through the cylindrical screen to also flush the area between the rotor and inside surface of the cylindrical screen. When air or other gas is used as the pressurized fluid, dislodged particulates within the screen area are driven out through the dried particle outlet. When water or other liquid is used as the pressurized fluid, any particles lodged in the housing, outside the cylindrical screen, will be flushed to the underlying water tank. 
   Other high pressure fluid spray nozzles are strategically located to direct the pressurized fluid at other hang-up points. Such other hang-up points include the valves in a water box bypass for the underwater pelletizer, the agglomerate catcher which receives the slurry from the underwater pelletizer, the rotor, the base section of the dryer, the dryer top section, the particle diverter valve located at the end of the dried particulate discharge chute, peripherally in and around the upper walls of the water reservoir, linearly across the topmost outer edge of the fines removal screen, and peripherally spaced and vertically staggered beneath the fines removal screen, as well as peripherally around the dewatering screen or screens and baffles. Additionally, a higher volume blower is communicated with the housing. With the water tank lid open during the cleaning operation, the higher volume blower provides better air circulation through the dryer. 
   In a preferred embodiment, a water surge is directed into the dryer by injecting high pressure air into the water box bypass line through a vertically and/or positionally maneuverable head. High pressure water at a flow rate of preferably 80 gpm to 100 gpm is directed to the interior of the housing and the exterior of the cylindrical screen through a plurality of spray heads, preferably three or more, circumferentially spaced and vertically staggered around the cylindrical screen. Similarly high pressure water is directionally sprayed toward the walls of and peripherally about the water reservoir through a plurality of spray heads, preferably two or more, per side of the reservoir. Similarly placed linearly across the upper edge of the outer surface of the fines removal screen is a plurality of spray heads, preferably two or more, through which high pressure water is sprayed directionally along the upper surface of the screen. Additionally, a plurality of spray heads, preferably two per side or more, are placed peripherally around the exterior edge of the screen undersurface and optionally may be vertically staggered across that undersurface to rinse fines collected on the surface of the fines screen. Alternatively, high pressure air may be used through the spray nozzles described positionally and linearly along the topmost edge of the outer screen surface or peripherally and vertically staggered around and across the undersurface of the fines screen. 
   High pressure air is sequentially directed at the top of the rotor adjacent the dryer top section, at the bottom of the rotor adjacent the base section of the dryer and the screen support assembly, at the dried particulate discharge chute and at the diverter valve located at the end of the aforementioned discharge chute. The pressure of the air through the foregoing spray nozzles is preferably about 60 psi to about 80 psi, or more. Preferably, the high pressure air to the bottom of the rotor adjacent the base section of the dryer and screen support assembly is operated continuously inasmuch as this is a particularly vulnerable hang-up point for dried particulates. 
   Accordingly, it is an object of the present invention to provide a self-cleaning centrifugal dryer and method for removing surface moisture from plastic particulates introduced to the dryer as a slurry in water in order to eliminate contamination between different particles being dried in sequential drying cycles during operation of the dryer. 
   Another object of the present invention is to provide self-cleaning centrifugal drying by discharging pressurized fluids into particulate hang-up points or areas within the centrifugal dryer and associated water-conveyance and processing equipment. 
   A further object of the present invention is to provide a self-cleaning centrifugal dryer and method in which pressurized fluid, preferably high flow rate water, is directed onto or toward various hang-up points by spray nozzles oriented in circumferentially spaced and vertically staggered relation between the interior of the housing and the exterior of the cylindrical screen, peripherally and laterally around the topmost walls of the water reservoir, laterally across the topmost edge of the fines removal screen, and peripherally around and vertically staggered beneath the undersurface of the fines removal screen. 
   Yet another object of the present invention is to provide a self-cleaning centrifugal dryer and method in accordance with the preceding object which directs pressurized fluid, preferably high pressure air, at specific hang-up points in the dryer including: a diverter valve in the dried particulate outlet; at the top of the rotor inside the dryer top section; from inside the rotor for discharge from the lower end of the rotor toward the base section of the dryer and the screen support assembly; inside the dried particulate chute; and toward the dried particle diverter valve. 
   A final object of the present invention to be specifically set forth herein is to provide a self-cleaning centrifugal dryer and method in accordance with the preceding objects which will conform to conventional forms of manufacture and operation, and will be economically feasible, long-lasting and relatively trouble-free in use. 
   These together with other objects and advantages which will become subsequently apparent reside in the details of constructions and operation as more fully hereinafter described and claimed, reference being had to the accompanying drawings forming a part hereof, wherein like numerals refer to like parts throughout. The drawings are intended only to illustrate the present invention and should not be considered to scale. 

   
     BRIEF DESCRIPTION OF THE DRAWINGS 
       FIG. 1  is a schematic illustration of an underwater pelletizer and centrifugal dryer with water conveyance and processing system in which a self-cleaning system and method of this invention are used. 
       FIG. 2  is a schematic sectional view of one dryer embodying the present invention and illustrating the spray nozzles between the dryer housing and perforated screen as well as the slurry inlet, the dried pellet discharge chute, the water tank, the cylindrical screen, and the rotor and hollow shaft therein. 
       FIG. 3  is an enlarged detailed sectional view from  FIG. 2  showing the rotor and illustrating the hollow shaft within the rotor and apertures communicating the interior of the hollow shaft and the interior and exterior of the rotor. 
       FIG. 4  is a fragmental perspective view inside the dryer of  FIG. 2  illustrating the relationship of the dryer housing, rotor and one spray nozzle observed through a door opening in the housing. 
       FIG. 5  is a bottom view of the rotor of the dryer of  FIG. 2  illustrating the apertures in the lower end of the rotor for spraying the interior of the rotor within the base section of the dryer. 
       FIG. 6  is a schematic sectional view of another dryer embodying the present invention similar in design and scope to  FIG. 2  with an offset motor and pulley drives and stepper motor for variance positionally of the spray tubes and spray nozzles. 
       FIG. 7  is a schematic sectional view of yet another dryer embodying the present invention, similar to  FIG. 2 . 
       FIG. 8  is an enlarged detail sectional view from  FIG. 7 , similar to  FIG. 3 . 
       FIG. 9  is a schematic sectional view of still another dryer embodying the present invention, similar to  FIG. 7 , but illustrating an offset motor and pulley drives at the base. 
       FIG. 10  is a schematic sectional view of a dryer with a dewatering device in advance of the dryer in accordance with the present invention and illustrating the spray nozzle positioning. 
       FIG. 11  is a schematic sectional view showing details of the dewatering device of  FIG. 10  with spray nozzles. 
       FIG. 12  is an expanded schematic sectional view through line B in  FIG. 11  showing the vertical dewatering device detail of  FIG. 10  and  FIG. 11  with spray nozzles. 
       FIG. 13  is a schematic sectional view of a water tank and fines removal screen in accordance with the present invention and illustrating the spray nozzle positioning. 
   

   DETAILED DESCRIPTION OF THE INVENTION 
   Although preferred embodiments of the invention are explained in detail, it is to be understood that other embodiments are possible. Accordingly, it is not intended that the invention is to be limited in its scope to the details of constructions and arrangement of components set forth in the following description or illustrated in the drawings. The invention is capable of other embodiments and of being practiced or carried out in various ways. Also, in describing the preferred embodiments, specific terminology will be resorted to for the sake of clarity. It is to be understood that each specific term includes all technical equivalents which operate in a similar manner to accomplish a similar purpose. 
   Referring specifically to the drawings, a Gala centrifugal dryer modified to incorporate the structure and method of the present invention is illustrated in  FIGS. 2-5  and is generally designated by reference numeral  10 .  FIG. 1  of the drawings schematically illustrates a typical dryer  10 , associated with an underwater pelletizer generally designated by reference numeral  12  that produces and discharges a pelletized product in the form of a slurry of pellets, flakes, fines and other solids and water which is conveyed to the pellet dryer  10  through a slurry pipe  14 . The pipe  14  discharges the particulates and water slurry into an agglomerate catcher  16  which catches, removes and discharges pellet agglomerates through a discharge chute  18 . The agglomerate catcher  16  includes an angled round bar grid, perforated plate or screen  20  which permits passage of water and pellets and smaller particulates but collects agglomerated pellets and directs them toward the discharge chute  18 . The particulates and water slurry then pass into a dewaterer  22  which includes at least one vertical or horizontal dewatering foraminous membrane screen  23  containing one or more baffles  24  and/or an inclined foraminous membrane screen  28  that enables water to pass downwardly into a fines removal screen  30  and therethrough to the water reservoir  32 . The particulates which still retain moisture on their surfaces are discharged from dewaterer  22  into the lower end of the dryer  10  at a slurry inlet  29 . 
   As illustrated in  FIG. 2 , the self-cleaning centrifugal particulate dryer  10  includes but is not limited to a generally cylindrical housing  26  having a vertically oriented generally cylindrical screen  27  mounted on a cylindrical screen support  77  at the base of the screen, and a cylindrical screen support  39  at the top of the screen. The screen  27  is thus positioned concentrically within the housing  26  in radially spaced relation from the inside wall of the housing. 
   A vertical rotor  33  is mounted for rotation within the screen  27  and is rotatably driven by a motor  35  preferably mounted atop the upper end of the dryer. The motor  35  is connected to the rotor  33  by a drive connection  34  and through a bearing  36  connected with the upper end of the housing. The connection  34  and bearing  36  support the rotor  33  and guide the rotational movement of the upper end of the rotor. The slurry inlet  29  is in communication with the lower end of the screen  27  and rotor  33  through the lower screen support section  77  at connection  38 , and the upper end of the housing and rotor is in communication with a dried particulate discharge chute  40  through connection  41  in upper screen support section  39  at the upper end of the housing. A diverter plate  92  in outlet  40  can divert dried particles out of exit  97  or exit  98 . 
   The housing  26  is of sectional construction connected at a flanged coupling  42  at a lower end portion of the dryer and a flanged coupling  43  at the upper end portion of the dryer. Flange coupling  43  is connected to a top plate  47  which supports bearing structure  36  and drive connection  34  which are enclosed by a housing or guard  44 . A coupling  46  atop the housing  44  supports the motor  35  and maintains all of the components in assembled relation. 
   The lower end of the housing  26 , designated by reference numeral  48 , is connected to a bottom plate  100  on top of a water tank or reservoir  32  by a flange connection  50 . Apertures  52  communicate the lower end  48  of the dryer housing with the water reservoir  32  for discharge of water from the housing  26  into the water reservoir  32  as the surface moisture is removed from the pellets. This removal is achieved by action of the rotor which elevates the particulates and imparts centrifugal forces to the particulates so that impact against the interior of the screen  27  will remove moisture from the particulates with such moisture passing through the screen and ultimately into the water tank  32  in a manner well known in the art. 
   The self-cleaning structure of the present invention includes a plurality of spray nozzles or spray heads  54  supported between the interior of the housing  26  and the exterior of the screen  27  as illustrated in  FIG. 2 . The nozzles  54  are supported at the lower end of spray pipes  56  extending upwardly through top plate  47  at the upper end of the housing with the upper ends  60  of the spray pipes  56  being exposed. Hoses or lines  61  feed high pressure fluid, preferably water at a flow rate of at least 40 gpm, and preferably above 60 gpm, and more preferably at 80 gpm or higher to the spray nozzles  54 . The hoses  61  can optionally feed off a single manifold (not shown) mounted on the dryer  10 . 
   There are preferably at least three spray nozzles  54  and related spray pipes  56  and lines  61 . The spray nozzles  54  and pipes  56  are oriented in circumferentially spaced relation peripherally of the screen  27  and oriented in staggered vertical relation so that pressurized fluid discharged from the spray nozzles  54  will contact and clean the screen  27 , inside and out, as well as the interior of the housing  26 . Thus, any collected particulates that may have accumulated or lodged in hang-up points or areas between the outside surface of the screen  27  and inside wall of the housing  26  are flushed through apertures  52  into the water tank  32 . Similarly, leftover particulates inside the screen  27  and outside the rotor  33  are flushed out of the dryer and will not contaminate or become mixed with particulates passing through the dryer during a subsequent drying cycle in which a different type pellet is dried. 
   The region between the screen support section  77  at the lower end of the dryer and the inner wall of the housing  26  includes flat areas at the port openings and seams that connect the components of the dryer housing together. The high pressure water from the spray nozzles  54  effectively rinses this region as well. The base screen support section  77  is attached to the bottom plate  100  of the housing  26  and water tank  32  by screws  78  or other fasteners to stationarily secure the housing and screen to the water tank  32 . The base screen support section  77  is in the form of a tub or basin as shown in  FIG. 2  and  FIG. 3 . Alternatively, in other dryers the base screen support section  77  may be in the form of an inverted tub or inverted base (not shown). 
   Turning to  FIGS. 3-5 , the rotor  33  includes a substantially square tubular member  62  provided with inclined rotor blades  64  thereon for lifting and elevating the particulates and subsequently impacting them against the screen  27 . In other dryers, the rotor  33  can be round, hexagon, octagon or other shape in cross-section. A hollow shaft  66  extends through the rotor  33  in concentric spaced relation to the hollow square member  62  forming the rotor. The hollow shaft guides the lower end of the rotor as it extends through an opening  68  in a guide bushing  102  at the lower end of the rotor, as well as aligned openings  104  and  106  in bottom plate  100  and the top wall of the water tank  32 , respectively. A rotary coupling  70  is connected to the hollow shaft  66  and to a source of fluid pressure, preferably air (not shown) through hose or supply line  71  to pressurize the interior of the hollow shaft  66 . 
   The hollow shaft  66  includes apertures  72  to communicate the interior of the hollow rotor member  62  as illustrated in  FIGS. 2 and 3 . These holes  72  introduce the pressurized fluid, preferably air, into the interior of the rotor  33 . The rotor  33  in turn has apertures  76  in bottom wall  74  which communicate the bottom end of the rotor  33  with the interior of the base or tub section  77  to enable the lower end of the rotor  33  and the tub section  77  to be cleaned. Any particulates flushed from the rotor and inside screen  27  are discharged preferentially through the dried pellet outlet chute  40 . 
   The top of the rotor  33  inside top section  39  is also a hang-up point and subjected to high pressure fluid, preferably air, to dislodge accumulated particulates. As shown in  FIG. 2 , a nozzle  110  directs the high pressure air across the top  112  of the rotor  33  to drive any accumulated particulates out of the top section  39  and preferentially into the pellet outlet chute  40 . The nozzle  110  is fed by air hose or line  114  which extends through top plate  47  and is connected to a high pressure air source. 
   In addition to hang-up points or areas occurring in the dryer structure, another hang-up point occurs in a water box bypass line which includes valves  82  to bypass the water box  84  of the underwater pelletizer  12  as illustrated schematically in  FIG. 1 . This enables water flow from the pump  86  to directly enter the slurry pipe  14 . The valves  82  provide a hang-up point in the water box bypass line  80 . To alleviate collection of particulates in the water box bypass  80  the section of pipe  80  is provided with a small diameter nipple  17 , a check valve and an air hose  88  connected with an air injection port that purges any particulates out of the water box bypass  80 . This air purge also creates a high pressure water surge into the dryer which serves to clean the agglomerate catcher  16  and the base screen support section  77  within base section  48  of the dryer  10 . 
   The agglomerate catcher  16  can also be cleaned by a separate pipe or hose  90  controlled by a solenoid valve which directs high pressure fluid onto the pellet contact side of the angled agglomerate grate or catcher plate  20  to clean the bar rod grid  20  of agglomerates which are then discharged through the discharge tube or chute  18 . The air purge from the water box bypass and hose  90  flushes all agglomerated pellets from the agglomerate catcher  16 . 
   A hose  94  and nozzle  95  supply bursts of air to discharge chute or pipe  40  in a direction such that it cleans the top of the rotor  33  and the pellet discharge outlet  40 . The air discharge blows any particulates past any pipe connections and the diverter valve  92  for discharge of dried pellets and other particles out of the dryer. 
   The rotor  33  is preferably turning continuously during the full cleaning cycle. Solenoid valves are provided to supply air preferably at about 60 psi to 80 psi, or more, to the water box bypass air port, rotor air ports, top section air port, pellet outlet air port and diverter valve air port. The solenoid valves include timers to provide short air bursts, preferably about three seconds, which cleans well and does not require a lot of time. A clean cycle button (not shown) activates the cleaning cycle with the water box bypass air port being energized first to allow air to purge the bypass with a multiplicity of air bursts, preferably five or more. The top section air port  110  is then activated. This is followed sequentially with activation of the pellet outlet chute diverter valve  95 . This valve closes prior to activation of the spray nozzles  54  which wash the screen for one to ten seconds, preferably about six seconds. The blower must be deactivated during the water spray cycles and is then reactivated when the spray nozzle pump is de-energized thus completing one cleaning cycle. The cycle as herein described is not limited in scope and each component of the cycle may be varied in frequency and/or duration as necessitated to achieve appropriate removal of the residual particulates. 
   Analogous to Gala dryers exemplified in  FIGS. 2-5 ,  FIG. 6  illustrates an optional configuration with the motor  135  offset at the top of the dryer and operationally connected with a drive belt  190  to the drive pulley  192  and the rotor pulley  191 . This allows the rotary union  170  and air inlet  171  to be attached to the top of the hollow rotor  33 . Details of the drawing similarly numbered, follow those of  FIGS. 2-5 . Support platform  180  is attachedly connected to the top plate  47  on the dryer housing  26 . 
   Optionally motor  160  which is controlled electrically, hydraulically, or pneumatically, may be attached to the top plate  47  as shown or to the support platform  180 , not shown. This motor allows the adjustment of the spray tube  56  positionally to raise or lower the spray nozzle  54  enhancing the effectiveness of this component of the cleaning cycle. Motors  160  optionally are connected to each of the spray tubes and can be operated singly, multiply, or concurrently and simultaneously. The optional motors  160  described herein are applicable to all designs discussed heretofore and which follow hereinafter and are illustrated exemplary to any and all applications and designs whether illustrated or not. 
   Turning now to  FIGS. 7 and 8  of the drawings, an alternative style Gala dryer, modified to incorporate the structure and method of the present invention, is generally designated by reference numeral  210 . Where possible like parts of the dryer  210  correspond with the dryer  10  of  FIGS. 2-6 , the numbers are the same, except that the numbers are preceded by the digit “2”, or the 300 series is used for the 100 series in the  FIGS. 2-6  embodiments. New components are numbered in the 400 series. 
   The self-cleaning apparatus in the  FIGS. 7 and 8  embodiment includes three or more spray nozzles or spray heads  254  supported between the interior of the housing  226  and the exterior of the screen  228 . The screen  228  is comprised of one or more sections wherein two sections,  402  and  404  are exemplarily described herein. The nozzles  254  are supported by spray pipes  256  extending upwardly through the top plate  247  and are connected by lines  261  to a single water inlet  406 . The spray nozzles  254  preferably spray water or other liquid against the interior walls of the housing  226  and the exterior walls of the screen  228 , with the water and captured particulates exiting the dryer through drain  408 . 
   The rotor  233  is hollow and is provided with inclined rotor blades  264  around its exterior surface. A hollow shaft  266  extends through the hollow rotor  233  in concentric spaced relation thereto. The lower end of the rotor  233  is supported in bearing assembly  408 , and the hollow shaft  266  extends through the bearing assembly  408  for connection to the rotary coupling  270  for connection to a source of high air pressure through hose or line  271 . 
   The hollow shaft  266  includes apertures  272  to communicate with the interior of the hollow rotor  233 , which holes  272  introduce the pressurized air into the interior of the rotor  233 . The bottom of the rotor  233  in turn has apertures  276  in its bottom wall  274  which direct the pressurized air towards the bottom of the base or tub section  277 , thus driving any accumulated particulates outwardly and upwardly into the rotating rotor  233  and rotor blades  264 . 
   As shown in  FIG. 7 , the top of the rotor  233  is also subjected to high pressure air through nozzle  310 , which directs the high pressure air across the top  312  of the rotor  233  and underneath the top plate  247 . Hose or line  314  connects the nozzle  310  to a source of high pressure air. 
   The discharge chute or pipe  240  of the  FIGS. 7 and 8  embodiment is shown separately since it can be installed either on the front or back of the dryer  210 , as shown in  FIG. 7 . In this embodiment, there are separate nozzles for the discharge pipe  240  and the diverter valve  292 . Specifically, air hose  410  feeds a nozzle which directs high pressure air down the discharge chute  240 , and air hose  412  directs high pressure air directly at the diverter valve  292 . 
   Analogous to dryers exemplified in  FIGS. 7-8 ,  FIG. 9  illustrates an optional configuration with the motor  335  offset at the bottom of the dryer and operationally connected with a drive belt  390  to the drive pulley  392  and the rotor pulley  391 . This allows the rotary union  370  and air inlet  371  to be attached to the top of the hollow rotor  233 . Details of the dryer shown in  FIG. 9 , similarly numbered, follow those of  FIGS. 7-8 . 
   Based upon the foregoing description, taken together with the patent drawings, one skilled in the art should readily be able to establish a time cleaning sequence for the high pressure water and high pressure air flushing of any particular centrifugal pellet dryer. However, for further guidance, a self-cleaning process in accordance with the present invention utilizing the  FIGS. 7 and 8  embodiment will hereafter be described. 
   The operator would start the self-cleaning process by pressing a “Start Cleaning Cycle” button associated with the programmable logic controller or PLC. Not intending to be limited, an exemplary cleaning cycle is illustrated as follows: 
   Step 1: the water box bypass piping solenoid would energize the valve to air hose  88  to pulse air on for three seconds to create a high pressure water surge into the dryer, and then turn the air supply off for three seconds. This on/off sequence should be repeated five times; 
   Step 2: the top section solenoid is then energized pulsing air through nozzle  310  for three seconds and then off for three seconds. This sequence is repeated five times; 
   Step 3: the pellet resin outlet solenoid is then energized to pulse air through line  410  for three seconds and then off for three seconds; this sequence repeated five times; 
   Step 4: the pellet diverter valve solenoid is then energized to pulse air through line  412  for three seconds and then off for three seconds; this sequence also repeated five times; 
   Step 5: the blower motor for blower  304  is de-energized; 
   Step 6: the cleaning pump motor for delivering high pressure water to the spray nozzles  254  is energized, thus causing high pressure water spray to exit spray nozzles  254 , for a period of six seconds; 
   Step 7: the blower motor for blower  304  is then re-energized; and 
   Steps 1-7 are then repeated automatically for five consecutive sequences. Upon completion of the fifth sequence, the cleaning cycle is complete. 
   As mentioned previously, the rotor  233  is rotating during the complete cleaning process, as well as during the normal drying process. Hence, the rotor is on continuously, thus causing very little down time for the dryer. It is only necessary to run the cleaning cycle (while the rotor  233  is continuing to turn) when switching over to a new pellet material to be dried. As is reasonable to one skilled in the art, the cleaning process herein described is applicable to operation at any time throughout operation. Similarly, number of component operations, frequency, and duration of the events within the cycle are not limited in scope as detailed by the example cited. 
   Additional areas for the self-cleaning apparatus and process of the present invention are illustrated in  FIGS. 10-13 . A self-cleaning dryer  510  of the present invention is illustrated in  FIG. 10  with a dewatering device, generally designated by reference numeral  513 . The dewatering device  513  includes two vertical dewatering screens  523 , an angle feed screen  528 , and angular baffles positionally shown as an X-configuration radially and centrally contained within the vertical dewatering screen or screens  523 . Dryers of the current invention optionally contain the feed screen  528  and one or more dewatering screens  523 .  FIG. 11  shows an expanded illustration of the dewatering device  513  with one vertical dewatering screen  523 , housing  522 , flange  529  and X-configuration baffles  524 .  FIG. 12  shows a cross-section of the dewatering screen  523 , along line B-B of  FIG. 11 , indicating the screen connector  521 . Spray nozzles  554  are attached to spray pipes  556  which connect through the top of the dewaterer housing  522  to communicate with a pressurized water source through piping  560  and  561 . The spray nozzles  554  effectively clean the inside and outside of the dewatering screen or screens  523  and baffles  524 . The feed screen  528  is cleaned by high water pressure or high air pressure introduced to the spray nozzles  610  through hoses  562  directly communicated thereto and affixed to the side wall of the dewatering housing  522  at the upper end of the angled feed screen  528  and angled in parallel with the feed screen. 
     FIG. 13  illustrates a water tank or reservoir, generally designated by reference numeral  632 , in accordance with the present invention. The water tank  632  includes optional heating element  637 , lid  639 , raised as illustrated, and fines removal screen  630 . Spray nozzles  654  are peripherally positioned linearly along the upper wall  655  of the reservoir and in the housing  631  above the upper surface of the fines removal screen  630 . Spray nozzles  654  are affixedly attached to the walls and connected directly to pressurized water through pipe  660  for the tank  632  and pipe  661  for the screen housing  631 . Two or more spray nozzles described above are located on each side and peripherally around the tank  632  and fines removal screen housing  631 . Pressurized water or pressurized air is introduced through hose  662  to spray nozzles  710  positionally arrange peripherally around the underside of the fines removal screen  630  and fixedly attached to the screen housing  631 . Two or more spray nozzles are arranged on each side of the housing as illustrated. 
   Screens for the present invention as identified throughout the embodiments herein described include cylindrical stand alone, hinged cylindrical, or wrap around styles and may be plastic, wire-reinforced plastic, or metal compositionally and structurally which may be molded, punched, pierced, perforated, slotted or woven in one or more similar or different layers. The layers may be unattachedly connected or may be adhered by chemical bonding, thermal bonding, welding, soldering, brazing, resistance welding, sintering or diffusion bonding or equivalent adhesional technique known to those skilled in the art. The plastic may include polyethylene, polypropylene, nylon or polyamide, polyester, polyurethane or structurally sound material. The metal compositionally may include copper, brass, bronze, tin, iron, steel, aluminum or aluminum alloys, zinc or zinc alloys, nickel steel, stainless steel or alloys, titanium or titanium alloys, platinum or analogous metal appropriate to chemical compatibility requirements of the plastic particles being processed. The structural components of the screen may be wire, rod, or bar and may be round, oval, square, rectangular, triangular or wedge-shaped, hexagonal, or polygonal in cross-section. Structural dimensions are limited dimensionally only through requirements related to the percent open area needed to effect the necessary dewatering, drying, or fines removal. 
   While the invention has been described specifically with respect to centrifugal pellet dryers, for which it is especially preferred, the cleaning apparatus and method of this invention can also be adapted to dryers associated with other forms of pelletizers, such as strand, dice, water ring, and hot face pelletizers as well as to other plastic particulates including flakes not limited to production or manufacture by pelletization. It is not intended that the present invention be limited specifically to centrifugal pellet dryers. 
   The foregoing is considered as illustrative only of the principles of the invention. Further, numerous modifications and changes will readily occur to those skilled in the art, it is not desired to limit the invention to the exact construction and operation shown and described, and, accordingly, all suitable modifications and equivalents may be resorted to, falling within the scope of the invention.