Background of the Invention
1. Field of the Invention
The present invention relates to a screen changer assembly for screening out particulate matter in a flow of fluid and for regulating the back-pressure of the fluid. Although having general application, the present invention is more specifically directed for use with extruders of plastic material and the milling or back pressure on the material coming out of the extruder or other pump.
2. Description of the Prior Art
Screen changers for extruders coventionally comprise a pair of flat screens which are supported in the path of flow of fluid plastic material from an extruder screw substantially immediately prior to its extrusion into a definable shape. Such screens are required in order to filter out any solid particulate matter resulting from either unmelted plastic material or foreign solid objects accidentally mixed with the plastic material. Because such screens eventually become clogged with such foreign particulate matter, they must be changed and, accordingly, it is conventional to place two flat screens in tandem in a single support, so that one screen may be moved out of its screening position and be changed while the other can perform the screening operation. In such a manner, it is possible to avoid substantially shut-down in the operation of the extruder.
Such screens become clogged fairly frequently and must be replaced at frequent intervals. Therefore it has been suggested that a ribbon of filter ribbon be placed in a cassette holding a reel of screen. The screen is moved across the flow of plastics and fresh screen enters as the spent filter screen brings the impurities out of the machine. It has been further suggested to utilize a stationary spool, a transfer housing, and two filter cylinders. The spool, positioned between the extruder or other feed source and the subsequent equipment (die, spinning beam manifold, pelletizer, etc.), contains inlet and outlet passages to two filter assemblies. The filters may be sintered powder stainless tubes, sintered stainless pleated felt, or pleated stainless screens. The transfer housing, indexed around the spool, swings the filters on or off-stream. When one set of spool ports is on stream, permitting flow to and from one of the filter assemblies, the other spool ports leading to the second filter assembly are shut off from the flow. At predetermined pressures, the transfer housing shifts the filters to new positions. At the initial positions, filling and air purging commences for the new filter, which is still shut off from the outlet flow. Subsequently, however, when both filters are at equal pressures, the spent element is shut off and the new filter is placed fully on stream. The filter shift-over is now complete with a homogeneous and uninterrupted flow. The spent filter can be removed, cleaned, and readied for subsequent use.
Such prior art devices have several disadvantages. Flat screens are limited in the size of their coverage in the path of fluid flow and, therefore, require relatively frequent changing and cleaning. They further must be mounted securely in their supports against the pressure of the flowing plastic material. Furthermore, these flat screens, as well as the above-mentioned filter cylinder apparatus, tend to push solid particulate matter into the screen mesh, thereby increasing blockage of the screen. Flow rates, back pressure and temperature adjustments of the plastic material must be accomplished by accessory equipment. Another disadvantage is the relatively high cost of equipment and attention required in the servicing of such apparatus.
Summary of the Invention
The present invention overcomes and avoids these and other problems with a relatively simple apparatus comprising a housing supporting a tubular screen placed about a support. The support has radial openings therein with the incoming fluid material being off-center from the screening chamber to impart a rotational flow to the fluid material within that chamber. This rotational flow configuration presents an increased area of available screen to collect debris than previously obtainable by prior art apparatus of comparable size and also tends to push large solid particulate matter around the exterior surface of the screen so as to inbibit clogging of the screen mesh. The fluid material then flows into the interior of the support tube and out of the support tube interior through an outlet opening in the housing supporting the tube. The tube is rotational with respect to the housing; therefore, the opening between the tube outlet and the housing outlet can be varied so as to provide for a valving operation in order to adjust the back pressure of the fluid material and the pump or extruder therefor. Preferably, a pair of tubes are utilized, each with screen material therearound in order to permit one of the support tubes and its screens to perform their operation, while the other of the support tubes and its screen is outside of the housing to permit change of the screen. Temperature sensors and controls are placed directly in the housing.
It is, therefore, an object of the present invention to provide for an improved screen-changing mechanism.
Another object is to provide for increased screening capacity of such a mechanism, compared to other styles of screen changers.
Another object is to provide for increased screening capacity of such a mechanism, compared to other styles of screen changes. Another object is to provide for avoiding large particle clogging of screens in such mechanisms.
Another object is to provide for self-contained adjustment of milling or back pressure and temperature of material in and from an extruder.
Another object is to provide for such a mechanism which is simple and economical.
Another object is to provide for safety pressure relief in such a mechanism from operator error.
Another object is to provide for simplicity of the changing operation in such a mechanism.
Another object is to provide for sealing of such a mechanism from undesired flow of fluid regardless of its viscosity.
Other aims and objects as well as a more complete understanding of the present invention will appear from the following explanation of an exemplary embodiment and the accompanying drawings thereof.
Brief Description of the Drawings
FIG. 1 is a view in partial section of the changer mechanism of the present invention illustratively connected to an extruder.
FIG. 2 is an end view of the apparatus depicted in FIG. 1;
FIG. 3 is a view in partial cross section of the housing of the mechanism depicted in FIG. 1;
FIG. 4 is a view taken along lines 4--4 of FIG. 3; and
FIG. 5 is a view taken generally along the lines 5--5 of FIG. 1.
Description of the Preferred Embodiment
While the present invention has general usage, its preferred use is with an extruder of plastic material, such as for the manufacture of convoluted plastic hoses. In such extrusion of plastic material, the mechanism therefor comprises a hopper for insertion of raw material, including dyes and other additives such as lubricants, a heater for melting the raw material into a fluid, a screw for mixing and pumping or extruding the fluid material, and a die for shaping the fluid material into a definable shape. One important processing parameter in this operation relates to the milling or back pressure on the fluid material, which is the resistance of the fluid material against the screw. Increase of resistance of the fluid material results in an increase in the milling or back pressure in the screw. As the milling pressure increases, the fluid material in the screw has a tendency to move backward upon itself against the turning action of the screw, with the result of enhanced mixing. Such enhanced mixing is desired to provide more homogeneity in the material and in the plastic article being shaped by the extruder die as it passes therefrom. The present invention is specifically directed to improved control of the milling pressure, as well as to improved screening of the plastic material.
Accordingly, with reference to FIGS. 1-5, a screen changer assembly 10 comprises a housing block 12 and a plug 14. Housing block 12 is secured at its inlet end 16 to a source of fluid material, such as of molten plastic. At its outlet end 18, the housing block is connected to extruder dies contained within a housing 20 by a manifold adapter 21 and appropriate conduits 22. Although two outlets terminating in housings 20 are shown, it is to be understood that one, or more than two, housings and extruder dies may be used, as desired.
Housing block 12 is provided with a threaded internal bore 24 extending therethrough between housing ends 26 and 28. The housing is provided with an axis 30 which also coincides with the axis of plug 14; therefore, indicium 30 will refer to both the housing and plug axes. Housing 12 is provided with an outlet 32 at its outlet end 18 whose axis is substantially perpendicular to and intersects with axis 30. An inlet 34 is provided in housing inlet end 16 also for communication with bore 24. As best shown in FIGS. 3 and 4, the axis of inlet 34 lies perpendicular to a plane passing through axis 30 but is off-centered therefrom so that fluid flowing into bore 24 will be provided with a rotational flow pattern for purposes to be more fully explained hereinafter. Bore 34, as shown in FIGS. 1 and 3, is further offset along axis 30 from outlet 32.
A pair of annular grooves 36 and 38 are respectively placed in housing ends 26 and 28 about bore 24 and are closed by sealing O-rings 40 and plates 42 secured to the housing in any suitable manner to provide annular conduits having inlets 44 and outlets 46. Closed annular grooves 36 and 38 are adapted to be supplied with a coolant flowing from inlets 44 out of outlets 46 in the event that the plastic material flowing through housing 12 is of insufficient viscosity as to creep along the threaded engagement between the housing and plug 14. The coolant is adapted to make the plastic material more viscous at housing ends 26 and 28, thereby reducing or even stopping leakage. It is to be understood, of course, that if the viscosity of the plastic material is sufficiently high, it may not be necessary to utilize this cooling adjunct.
As best shown in FIG. 4, housing 12 is provided with openings 48, 50, 52, and 54 for placement therein of temperature and pressure sensing devices and heating elements. The temperature is sensed at opening 48, the temperature of the plastic material is detected at inlet 34 through opening 50, and pressure of the fluid in inlet 34 is sensed through opening 52. Housing 12 is heated through openings 54. As best shown in FIG. 2, the various sensing elements include heaters 56, pressure gauge 58, and a thermocouple 60 inserted into their respective openings of housing 12. It is, in part, because of the construction of the present invention that these various sensing devices can be placed as close to where the temperature and pressure characteristics must be taken, as distinguished from the prior art, which is not usually adapted to such ease of sensing. Thus, by means of the thermocouples in openings 48 and 50, an immediate reading of the condition of the housing and, in particular, of the temperature and viscosity of the fluid material may be obtained and controlled almost instantaneously and close to the extruder dies and die housing 20 for precise adjustment and control of the defined shape of the article to be extruded. In conjunction with precise definition of the article to be extruded, the pressure of the material can be adjusted by viewing pressure gauge 58 extending from opening 52, by cooperation between the plug and the housing, to be described shortly hereinafter. Pressure and temperature parameters may also be determined and controlled at die housing 20 by a pressure gauge 62, heaters in housings 20 controlled by wires 64, and other devices, as needed.
Referring back to FIG. 1, plug 14 preferably comprises three cylindrical portions 66, 68, and 70, each having threaded external surfaces 72 which are adapted for threaded engagement with threaded internal bore 24 of the housing. Cylindrical portions 66 and 68 are joined by a cylindrical tube support 74 while cylindrical portion 68 and 70 are joined by a second support tube 76. Both support tubes 74 and 76 have radially directed openings 78 therein extending from their outer surfaces 80 to their inner surfaces 82, the latter providing for an internal flow path 88 for the plastic material. Disposed about outer surfaces 80 are screens 84, which may comprise one or more screens of different meshes, for example, a coarse screen on each of surfaces 80 with a fine screen above the coarse screen, clipped together. Preferably, screens 84 are of rectangular configuration and, as shown in FIG. 5, are wrapped so that each leading edge 84a is disposed beneath the trailing edge 84b so that flow of material, as represented by arrows 86, will not lift the exposed edge of the screen but, rather, hold the screen in place without permitting liquid to flow within instead of through the screens.
Internal cavity 88 extends into cylindrical portions 66 and 68, and a radial bore 90 extends therefrom through threaded external surfaces 72. Cylindrical portion 70 has no interior cavity or bore but is used primarily as a further support for the plug and a closure for one of the cavities 88. An inclined surface 92 is provided as a diverter of plastic material for aiding its movement into and through bore 90.
Annular grooves 94 are formed within and extend completely about threaded external surfaces 72 of cylindrical portions 66 and 68 and communicate with radial bores 90 for effecting a pressure relief and slow flow and escape of fluid material, should radial bore 90 not otherwise be in communication with housing outlet 32. Specifically, if bore 90 were not at all aligned with outlet 32, as distinguished from the representations shown in FIGS. 1 and 2, fluid flow would follow the path provided by inlet 34, screen 84, openings 78, internal cavity 88, bore 90, annular groove 94, and outlet 32. Without the flow path provided by annular groove 94, during complete non-communication between bore 90 and outlet 32, plastic flow would be completely stopped and the resulting increase in back pressure could damage the extruder or other parts. Thus, annular grooves 94 prevent possible damage to the equipment secured to inlet end 16 from excessive back pressures.
As shown in FIG. 2, an arrow 96 is milled or otherwise formed on octagonal end 98 of plug 14 and points in the direction of exit holes or bores 90 so that an operator may visually obtain an indication of approximate alignment of bore 90 with housing outlet 32.
In operation, let it be assumed that plug 14 is engaged with housing 12 as shown in FIG. 1 so that plastic material flows through inlet 34, rotationally around screen 84, as shown in FIG. 5, through the screen and openings 78 and into internal cavity 88 of support tube 76 positioned between cylindrical portions 68 and 70. The plastic material then flows against diverting inclined surface 92 and through radial bore 90 and outlet 32 to the extruder dies. In the event that the pressure of the material must be changed, as noted by pressure gauges 58 and 62, one need only to rotate plug 14 slightly by placing a wrench on its octagonal and 98 in order to vary the coincidence of the opening of bore 90 with respect to the opening of outlet 32, the precise pressure changes also being noted on gauges 58 and 62.
Let it be assumed further that screen 84 between cylindrical portions 68 and 70 has become sufficiently clogged with particulate matter so as to require change in screens. It is only necessary, then, to rotate plug 14 by means of octagonal end 98 to screw plug through the housing so that screen 84 on tube support 74 between cylindrical portions 66 and 68 will now be within the housing and the screen between portions 68 and 70 will be outside of the housing at the right as viewed in FIG. 1. The pressure through bore 90 of cylindrical portion 66 is then adjusted by minute rotational movements of the plug. It is generally preferable to leave the plastic and the clogged first screen on the plug and utilize the screen changer until the alternate screen becomes dirty. Then, when it is necessary to change the alternate screen, the formerly dirty screen is removed and a clean screen is installed, in order to prevent the plastic in the holes to the screening chamber from oxidizing.
Although the invention has been described with reference to a particular embodiment thereof, it should be realized that various changes and modifications may be made therein without departing from the spirit and scope of the invention.