AU776759B2 - Low pressure dryer - Google Patents

Description

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AUSTRALIA

Patents Act COMPLETE SPECIFICATION

(ORIGINAL)

Class Int. Class Application Number: Lodged: Complete Specification Lodged: Accepted: Published: Priority Related Art: oe

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o°° Name of Applicant: Maguire Products, Inc.

Actual Inventor(s): Stephen B Maguire Address for Service: PHILLIPS ORMONDE FITZPATRICK Patent and Trade Mark Attorneys 367 Collins Street Melbourne 3000 AUSTRALIA Invention Title: LOW PRESSURE DRYER Our Ref 649551 POF Code: 457434/224709 The followinq statement is a full description of this invention, including the best method of performing it known to applicant(s): -1- LOW PRESSURE

DRYER

The present application is a divisional application from Australian patent application number 93971/98, the entire disclosure of which is incorporated herein by reference.

This invention relates to drying granular or powdery material, preferably granular resin material, prior to processing thereof into intermediate or finished products, preferably by extrusion or molding.

Plastic resins are initially granular materials and are produced in pellets. These pellets are processed by extrusion or other means in which the granular resin pellets are heated until the pellets melt and may then be molded or extruded into a desired shape. Typically granular resins melt at elevated temperatures, for example from 300-400 0 F, which is well above the boiling point of water.

Many granular resins have affinity for moisture.

These hydroscopic resins absorb moisture and cannot be properly processed by molding or extrusion until dried.

If processed before dry, moisture in the plastic boils 20 at or approaching the high plastic molding or extrusion process temperatures, leaving bubbles and perhaps other imperfections in the finished product. Hence, S. hydroscopic granular resins must be dried prior to molding or extrusion.

Some granular resin materials are extremely hydroscopic and become unprocessable by molding or extrusion in ten minutes or less after exiting a dryer, due to the rapid absorption of moisture by the granular resin material.

It is known to dry granular resin material by placing the granular resin material pellets on large shallow trays to a depth of one or two inches, and putting those trays into ovens for sveal hoJ 1. nui this approach to granular resin material drying, resin temperatures of 150-180.F, but no higher, can be used since many granuiar resin materials begin to soften at 200-210 0

F.

During the drying process, the granular resin material cannot be permitted to soften, since it becomes unmanageable. Once granular resin material begins to soften, at temperatures above the boiling point of water, the granular resin material pellets stick together in lumps or even melt into useless masses of solid plastic, making it impossible to further process the resin material into a useful article.

The above discussion of documents, acts, materials, devices, articles and the like is included in this specification solely for the purpose of providing a context for the present invention. It is not suggested or represented that any of these matters formed part of the prior art base or were common general knowledge in the field relevant to the present invention as it existed in Australia before the priority date of each claim of this application.

In one of its aspects, this- invention provides a low pressure granular or powdery granular material dryer. The dryer preferably includes a rotatable preferably vertical shaft, a plurality of preferably vertically-oriented, open-ended preferably cylindrical hoppers which are preferably equiangularly positioned and rotatable about a vertical axis, which is preferably defined by the shaft, serially among material filling and heating, vacuum drying and dispensing positions.' The dryer preferably further includes a pin S"extending vertically and radially displaced from the axis, a preferably triangular preferably horizontal plate rotatably receiving the pin proximate the center of the plate, a preferably horizontal link pivotally connecting said shaft and the plate, and a plurality of preferably pneumatic piston-cylinder combinations equiangularly operatively connected to the plate for rotating the shaft by sequentially moving the plate relative to the shaft thereby to move the hoppers among the filling and heating, vacuum drying and dispensing positions.

The dryer yet preferably includes preferably pneumatic piston-cylinder actuated means for sealing the cylindrical hoppers at the vacuum drying station.

3 In another of its aspects, this invention provids a hopper for use in a low pressure granular resin material or powdery material dryer where the hopper includes a preferably vertically-oriented preferably cylindrical shell having open ends with the shell preferably adapted to be sealingly closed by selectably contacting top and bottom plates thereagainst, thereby enabling vacuum to be drawn within the shell wlhen desired. The hopper further preferably includes a funnel within the cylindrical shell and located proximate the shell bottom. The hopper further preferably includes an internal material flow control plate in the form of a dump flap located within the shell beneath the funnel. The dump flap is preferably pivotally connected to the shell for movement about the connection point away from a downwardly opening discharge orifice of the funnel, thereby to selectably release granular resin material from the hopper.

In yet a further aspect of the invention, top and bottom plates preferably selectably seal the cylindrical shell thereby allowing vacuum to be drawn therewithin.

Pneumatic piston-cylinder means may be provided for urging the top and bottom plates into sealing contact with the shell.

The shell is desirably adapted to selectably dispense granular or powdery material stored therewithin at a dispense position, when the shell is at that ~position. The dispense position is preferably removed from the vacuum drying position.

The hopper is further preferably adapted to effectuate material dispensing upon contact by an upwardly moving rod of a pneumatic piston-cylinder combination, thereby permitting downward flow from the funnel of material with the material thereby flowing out of the cylindrical shell.

In yet another of its aspects, this invention provides a method for continuously drying granular or 4 r-rT,vder- Tn+m- 1 A extruding or other processing of that material. The method preferably includes supplying granular or powdery material to a vertically-oriented cylindrical shell at a fill and heat position and heating the material within the shell by introduction of heated air into the cylindrical shell while at the fill and heat position.

The method yet further preferably includes moving the vertically-oriented cylindrical shell through an arc about a vertical axis outboard of the shell periphery to a vacuum drying position and sealing open ends of the shell at such position.

The method still yet further preferably includes drawing a preselected level of vacuum within the sealed shell for a time sufficient to evaporate moisture from the heated material within the shell to a desired degree of dryness.

The method even yet further preferably includes bringing the shell to a material discharge position at 20 which the bottom of the shell is open and then discharging the dried material from the cylindrical shell responsively to action of a preferably pneumatic piston-cylinder combination inserting a rod into the shell interior from below to move a material discharge 25 gate proximate the bottom of the shell.

The method preferably still yet even further includes moving the shell through an arc about the vertical axis to the fill and heat position and sequentially repeating the steps of supplying material to the shell, heating the material within the shell, moving the shell to the vacuum drawing position, drawing a sufficient level of vacuum within the shell to evaporate moisture from the material within the shell and moving the shell to a discharge position, for so long as the material is to be continuously dried.

5 In yet another of its aspects, this IVert provides a method for continuously supplying dried granular resin material for processing from a supply of material which is excessively moist where the method preferably includes substantially simultaneously performing the steps of heating a portion of the moist granular resin material to a selected temperature at which the moisture evaporates from the granular resin material at a preselected level of vacuum, drawing and maintaining the preselected vacuum for a second portion of the granular resin material which has been heated to the selected temperature for time sufficient to cause the moisture to evaporate therefrom and result in the second portion of granular resin material being at the preselected dryness and supplying to granular resin material processing equipment a third portion of the granular resin material which was dried to the preselected dryness by evaporation in the preselected level of vacuum after having been heated to the selected temperature.

Brief Description of the Drawings Figure 1 is a front elevation of part of the low pressure granular or powdery material dryer showing a cylindrical hopper portion of the dryer at a material 25 filling and heating position prior to supply of heated air to the hopper interior, in accordance with the 4. preferred embodiment of the invention.

.Figure 2 is a plan view of the supply plenum portion of the low pressure dryer at the heating and 30 filling station, taken at arrows 2-2 in Figure 1.

Figure 3 is a front elevation of part of the low ,resrirr dryer showing a hoDper portion of the dryer at the material filling and heating position, as illustrated generally in Figure I, configured for supply of heated air to the hopper.

6 Figure 4 is a partially sectioed, sce i elevation of a vertically-oriented open ended cylindrical hopper, forming a part of the low pressure dryer, showing the hopper at a vacuum drying position with the hopper open so that pressure within the hopper is ambient.

Figure 5 is a partially sectioned, schematic elevation of the vertically-oriented open ended generally cylindrical hopper illustrated in Figure 4, with top and bottom plates sealing the hopper, thereby allowing vacuum to be drawn within the hopper and further illustrating the hopper connected to a vacuum pump.

Figure 6 is a broken front schematic elevation of the lower interior of a vertically-oriented open ended generally cylindrical hopper as illustrated generally in Figures 4 and 5, showing two material discharge funnels within the hopper, with the hopper illustrated at the material dispensing position.

Figure 7 is a broken front schematic elevation of the lower interior of a vertically-oriented open ended "generally cylindrical hopper as illustrated in Figure 6, at the same material dispensing position illustrated in Figure 6, illustrating the material dispensing piston- 25 cylinder combination actuated, thereby actuating a discharge flap beneath the discharge funnels within the hopper permitting material flow out of the hopper.

Figure 8 is a broken schematic side elevation of the lower interior of a vertically-oriented open ended generally cylindrical hopper as shown in Figures 6 and 7, taken looking from the right in Figure 7 illustrating the material dispensing piston-cylinder combination c. hv r nv mrna a discharge flap beneath the material discharge funnels depicted in dotted lines within the hopper, to dispense material from the hopper.

Figure 9 is a top view of low pressure dryer illustrated in Figures i through 8.

-7- Figure 10 is a front elevationl the low prcssure dryer illustrated in Figures 1 through 9.

Figure 11 is a top view, similar to Figure 9, schematically illustrating a portion of the low pressure dryer.

Description of the Preferred Embodiment and _Best Mode Known for Practicing the Invention Referring to the drawings in general and to Figures 9, 10 and 11 in particular, a low pressure granular..material dryer manifesting aspects of the invention is designated generally 10 and includes a plurality of cylindrical hoppers, preferably three, each of which has been designated generally 12. Each hopper 12 preferably includes a cylindrical shell 14 and is preferablY substantially vertically-oriented with the axis of the cylinder extending substantially vertically in order to be rotatable preferably unitarily with the other hoppers about a substantially vertical axis defined by a preferably vertical shaft 24.

Dryer 10 includes a frame, designated generally 22, on and within which vertical shaft 24 is rotatably mounted for rotation relative to frame 22, the details of which are discussed below. Cylindrical hoppers 12 rotating unitarily with vertical shaft 24 preferably move serially among a material fill and heat position designated generally 100, a material vacuum drying position designated generally 102 and a material dispensing position designated generally 104. Hoppers 12 move when and as required among fill and heat position 100, vacuum drying position 102 and dispensing position 104. The three hoppers 12 start and stop toaether as reauired; they do not move continuously in a merry-go-round fashion among positions 100, 102 and 104.

Referring principally to Figures 9 and 10, frame 22 is formed of a plurality of vertically and horizontally 8 extending preferably angle iron members which collectively define what appears as the edges of a rectangular parallelepiped. As visible in Figure frame 22 includes preferably four substantially vertical members 160, only two of which are visible in Figure the remaining two substantially vertical members 160 are hidden behind the two members 160 visible in Figure Frame 22 further includes four upper substantia-Ily horizontally extending members 162 which collectively define the outer periphery of a square in geometrical terms; the four upper substantially horizontally extending members 162 are visible in Figure 9; not all of members 162 are visible in Figure Frame 22 further yet preferably includes four lower horizontally extending members 164, one of which is visible in Figure 10. The remaining lower members 164 lie immediately under the corresponding upper horizontally extending members 162 illustrated in Figure 9. The four lower horizontally extending members 164 20 define the base of frame 22 for contacting a floor or other weight supporting structure on which dryer rests.

At least one and preferably a plurality of suspension members 166 extend laterally across the upper end of dryer 10, between selected upper horizontal members 162. One of such suspension members 166 is illustrated in Figure 10. A hopper top sealing pistoncylinder combination designated generally 44, serving to seal the top of a hopper 12 at the vacuum drying position, is supported by one of horizontally extending suspension members 166 as illustrated in Figure Similarly, a hopper upper closure piston-cylinder rnmhi.nation 98 located at material fill and heat position 100, which piston-cylinder combination is used to close an upper end of a cylindrical hopper 12 at the fill and heat position 100, is supported by one of 9 horizontally extending suspension members 166 as also illustrated in Figure First, second and third driving rotation pistoncylinder combinations 34, 36, 38 are preferably pivotally connected to selected ones of upper horizontal members 162 of frame 22 as illustrated in Figure 10. In the case of first driving rotation piston-cylinder combination 34, a triangular or cantilever extension may be provided from the proximate upper horizontal member 162 where the triangular extension has been designated generally 182 in Figure 9. Connections of driving rotation piston-cylinder combinations 34, 36 and 38 to frame 22 are denoted as pivotal connections 180 in the drawings.

Connection of generally triangular plate 28 with vertically-oriented shaft 24 is effectuated by means of a pin connector 168 which is vertically-oriented and resides rotatably slidably within an aperture formed at the center of horizontal central portion 30 of generally triangular plate 28. Pin connector 168 fits rotatably not only within triangular plate 28 but also fits rotatably within an aperture in one end of a plate-pin connection arm 116 best shown in Figure 9. While platepin connection arm preferably lies under triangular plate 28 as is apparent from Figure 10, plate-pin connection arm 116 has been illustrated in solid lines in Figure 9 to facilitate understanding.

Plate-pin connection arm 116 is fixedly connected to vertical shaft 24 at the upper end thereof.

In this arrangement movement of triangular plate 28, as effectuated by any of first, second or third driving rotation piston-cylinder combinations 34, 36 or 'o -eti-ul i- in cr r rn r R t-ranslating such motion to plate-pin connection arm 116. Rotation of plate-pin connection arm 116, being fixedly connected to shaft 24, results in shaft 24 rotating. As shaft 24 rotates, it carries hoppers 16 among the fill and heat position 100, 10 vacuum drying position 102 and material dispense position 104. Hoppers 16 move this way unitarily with shaft 24 as a result of hoppers 16 being fixedly connected to shaft 24 by cantilever connecting rods 110, illustrated in phantom lines in Figure Shaft 24 is journaled in suitable bearings mounted on upper and lower shaft suspension plates 112 to define upper and lower shaft bearing: -assemblies 114 as indicated in Figure 10. Upper shaft suspension plate 112 is connected to a horizontally extending suspension member 166 by suitable nut and bolt combinations which have not been numbered but are clearly visible in Figure lower shaft suspension plate 112 is connected to a lower horizontal member 164 as indicated generally in Figure 10, again by suitable nut and bolt combinations which have not been numbered in the drawings.

Referring to Figures 1 through 3 illustrating the fill and heat position 10O.-of lower pressure dryer at fill and heat position 100 a moist material supply hopper 64 has a supply of moist granular or powdery material, which is to be dried resident therein. A butterfly valve at the bottom of hopper 64 is within a conduit 144 and is operated by a piston-cylinder combination 146 as clearly visible in Figures 1 and 3.

Conduit 144 includes a telescoping portion 148 for connecting moist material supply hopper 64 with a hopper top sealing plate 150 at fill and heat position 100.

Positioned around the outer periphery of hopper top sealing plate 150 is an annular lip 152. An aperture 30 154 is within hopper top sealing plate 150 and facilitates communication between telescoping portion 148 of conduit 144 and the interior of a hopper 14 when fill mnn heat nosition.

Still referring to Figures 1 and 3, a hopper 14 is illustrated in position as a result of having been rotated to that position by rotation of vertical shaft 11 24 1 .nraspcr. ci st r second and third driving rotation piston-cylinder combinations 34, 36 and 38.

At material fill and heating position 100, a blower 76 facilitates recirculation of heated air through material 74 resident within hopper 14 to heat material 74. Blower 76 has an intake aperture 78 and an exhaust aperture 80. Exhaust aperture 80 connects to conduit 156 within which there are a- pl.uralTy of heater elements 82 to heat air exhausted from blower 76 prior to flow through material within hopper 12. Conduit 156 includes a telescoping portion 158 connecting with and exhausting into a supply plenum designated generally 86 via a plenum inlet 90 which is visible in both Figures 1 and 2.

plenum 86 includes an outlet screen 88 mounted at the upper end thereof, as illustrated generally in Figure 2. Outlet screen 92 has a plurality of apertures 184 formed therein with apertures 184 concentrated towards the central portion of outlet screen 92 as 20 illustrated in Figure 2. Apertures 184 serve to concentrate upward flow of the heating air about the central portion or central axis of hopper 14 which is desirable since this is where the majority of the material is concentrated to the shape of dispensing funnels 94, 96. A preferably silicon annular gasket 88 on plenum 86 provides tight sealing between supply plenum 86 and the open bottom of hopper 12 at the material fill and heat position illustrated in Figures and 3.

A pneumatic piston-cylinder combination 106 is mounted on a suitable cross-member, not illustrated in the drawings but forming a part of frame 22. When actuated, piston-cylinder combination 106 serves to close the bottom of hopper 12 in the fill and heat position by moving supply plenum 86 vertically upwardly, from the position illustrated in Figure 1 to the position illustrated in Figure 3, thereby effectuating 12 ti2a Seal AJ4:Wa oula P -uvm 86an hov.i -v 12 to facilitate passage of heated air through granular or powdery material in hopper 14.

Heated air, having passed through granular or powdery material within hopper 14, exhausts from hopper 14 via telescoping portion 148 of conduit 144. A butterfly valve 66 having closed conduit 144 so that heated air passing through telescoping portion 148 of conduit 144 cannot escape through supply hopper 64, causes the heated, moist air to f low into heated air recirculator 70 at heated recirculation intake 72. A thermocouple 68 positioned at heated air recirculation intake 72 senses temperature of heated air leaving hopper 14. A second thermocouple 84 is positioned proximate the outlet of the heated air supplied by blower 76, after the heated air has passed along heating elements 82. When the temperature sensed by thermocouples 68 and 84 are substantially equal, this is indicative of the granular or powdery material within 20 hopper 14 faying reached the desired temperature, namely the selected temperature of the air entering into supply ***plenum 86 after having been heated by heating elements 82.

~:During material heating at the fill and heat position, hopper top sealing plate 150 is lowered into position against the upper extremity of hopper 14 by action of a pneumatic piston-cylinder combination 98 which is connected to a suitable cross-member extending across the top of frame 22.

30 Referring to Figures 4 through 8 in particular, each preferably cylindrical hopper 12 preferably includes a cylindrical shell designated generally 14.

Each cylindrical shell 14 is preferably defined by an inner cylindrical tube referred to as a vacuum tube and designated 52 in the drawings and a concentric outer cylindrical tube referred to as an insulation tube and designated 54 in the drawings. Annular space between 13 tubes 52 and 54, wi'chj* sc is cgcz generally in the drawings, is preferably filled with thermal insulation to minimize heat transfer and heat loss out of cylindrical shell 14.

A pair of downwardly opening material dispensing funnels designated 94 and 96 respectively are secured within each cylindrical shell 14 of cylindrical hopper 12 proximate the bottom.-of hopper 12. The higher of the two material dispensing funnels is referred to as an upper material dispensing funnel and is designated 94 in the drawings. The lower of the two material dispensing funnels is referred to as the lower material dispensing funnel and is designated generally 96 in the drawings.

Material dispensing funnels 94 and 96 are preferably fixedly secured, by suitable sheet metal screws or other fastening means, to a lower portion of vacuum tube 52 at the positions generally indicated in the drawings.

Material dispensing funnels 94 and 96 preferably share a common funnel angle such that the sloped sides S 20 of the respective funnels are essentially parallel one with another. The sloped surface or side of upper .*.material dispensing funnel is designated generally 122 in the drawings while the sloped side of lower dispensing funnel 96 is designated generally 124 in the drawings.

As further apparent from the drawings, particularly Figures 6 through 8, upper dispensing funnel 94 is configured as an extremely truncated cone such that the downwardly dispensing opening of upper material dispensing funnel 94, which is designated 126 in the drawings, is substantially larger than a corresponding downwardly dispensing opening 128 of lower material dispensing funnel 96. This results from lower dispensing funnel 96 being less truncated in the vertical direction than upper dispensing funnel 94, as is illustrated in the drawings.

14 Use of two dispensing funnels such as dispensing funnels 94, 96 facilitates circulation of heated drying air around material in hopper 14 at filling and heating position 100 and further facilitates drying of the material in hopper 14 when the hopper is at vacuum drying position 102.

Each hopper 14 preferably further includes a dump ,flap designated generally 20 located below downwardly dispensing opening 128 of lower funnel 96. Dump flap is pivotally connected to vacuum tube 52 by suitable screw connections which are illustrated in the drawings, particularly in Figures 4, 5 and 8, and are numbered 140 and 170 respectively.

Dump flap 20 includes a central portion 172 which is generally planar in configuration as illustrated in the drawings, particularly Figures 6, 7 and 8, and has a weight 130 located at one side thereof, offset from the point of pivotal connection between dump flap 20 and dump actuator 62, which point of pivotal connection is denoted 132 in the drawings, and also offset from the pivotal connection of dump flap 20 with vacuum tube 52 of hopper shell 14 as effectuated by screw-nut connection 170 and offset from pivotal connection 140 of pivoting arm 134 to the interior surface of vacuum tube 52. Weight 130 helps to cause dump flap 20 to return to the position illustrated in Figure 6 in response to **gravitational force after material dispensing pistoncylinder combination 108 has been deactuated.

Dump actuator 62 engages a generally vertical arm 134 forming a part of dump flap 20. Dump actuator 62 includes a vertically movable arm 136, also illustrated 0 00 in Figure 7. Vertically movable arm 136 is mounted for 1W~ rr vrtirca1. movement alona the interior surface of vacuum tube 52 of horizontal shell 14. The extent of vertical movement of vertically movable arm 136 is controlled by a pin 174 illustrated in Figure 7, which is preferably mounted fixedly to and extending radially 15 fv-^ m the orr of vacuum tube 52. A vertical slot 176, similarly visible in Figure 7, in vertically movable arm 136 receives pin 174.

Interference between pin 174 and the ends of slot 176 limits vertical travel of movable arm 136.

Movement of arm 136 upwardly in Figures 6, 7 and 8 results from actuation of material dispensing pistoncylinder combination 108, which is preferably a pneumatically powered piston-cylinder combination. When piston-cylinder combination 108 is actuated, a piston rod 178 extending from piston-cylinder combination 108 contacts a horizontal tabular extension portion of vertically movable arm 136. This horizontal tabular extension of vertically movable arm 136 is designated 138 and is shown in Figure 8. There tabular extension 138 is illustrated in solid lines in the "at rest" or unactuated position and in dotted lines in the position assumed by tabular extension 138, and hence vertically movable arm 136, when material dispensing pneumatic 20 piston-cylinder combination 108 has been actuated and the piston rod associated therewith extends therefrom.

Actuation of material dispensing piston-cylinder combination 108 moves vertically movable arm 136 *upwardly, to the position illustrated in solid lines in Figure 8; the movement of arm 136 is from the position illustrated in Figure 6 to the position illustrated in Figure 7.

Vertically movable arm 136 is pivotally connected to an arm 134 portion of dump flap Arm 134 connects the horizontal part of dump flap to the inside of vacuum tube 52 via a pivotal connection identified as 140 in Figures 6, 7 and 8. Arm 134 is pivotally connected not only to the interior vacuum tube 52 at connection 140 but is also pivotally connected to vertically movable arm 136 at a pivotal connection 132. As a result, upward movement of vertically movable arm 136 causes pivotal movement of 16 pivoting arm 134 about pivotal connection 140. Since pivotal connections 140 and 170 are horizontally aligned along a common axis, pivotal movement of arm 134 about this axis moves the horizontal part of dump flap 20 away from the dispensing aperture of lower funnel 96 thereby permitting granular or powdery material contained within hopper 12 to float downwardly outwardly therefrom when dump flap 20 is in the position illustrated in Figure 7.

Once preferably pneumatic hopper dispensing pistoncylinder combination 108 has been deactuated, gravitational force acting with weight 130 tends to rotate dump flap 20 back to the horizontal, hopper closed, position illustrated in Figures 6 and 8. This causes vertically movable arm 136 to drop downwardly, from the position illustrated in Figure 7 to the position illustrated in Figure 6. This further causes arm 134 to rotate counterclockwise from the position illustrated in Figure 7 to the position illustrated in Figure 6, about pivotal connection point 140. This returns dump flap 20 to the horizontal position illustrated in Figure 6 where granular material in hopper 12 cannot flow outwardly downwardly therefrom through the open bottom of hopper 12.

The horizontal portion 172 of dump flap 20 is positioned sufficiently close to and sufficiently Soverlaps downwardly dispensing opening 128 of lower funnel 96 about the periphery of dispensing opening 128 that the angle of repose of any granular or powdery material within hopper 12 is sufficient to prevent downward flow of material through the gap between horizontal portion 172 of dump flap 20 and dispensing opening 128 of lower funnel 96.

Material dispensina piston-cylinder combination 108 is preferably mounted either on a portion of frame 22 below dryer 10 or on some other stable member such as the floor of an installation where dryer 10 may be used.

In either case, material dispensing piston-cylinder 17 combination T108 the sense that pistoncylinder combination 108 does not rotate with hoppers 12 as they are moved among fill and heat position 100, vacuum drying position 102 and material dispense position 104; hopper dispensing piston-cylinder combination 108 remains at material dispense position 104.

As apparent from Figure 8, dump fltip 20 h11clndes two arms 134, 134A. Arm 134A which is located at the side of dump flap 20 remote from material dispensing piston-cylinder combination 108 is pivotally connected directly to vacuum tube 52, preferably by screw-nut combination 170 as illustrated in Figures 4 and 5, for pivotal movement as dump flap 20 is actuated.

In Figures 4 and 5 one of hoppers 12 is illustrated at vacuum drying position 102. Figure 4 illustrates hopper 12 at vacuum drying position 102 prior to movement of hopper top and bottom vacuum sealing plates 42 into position to seal cylindrical shell 14 so 20 that a vacuum may be drawn therewithin.

Hopper top and bottom vacuum sealing plates 40, 42 are preferably respectively connected to unnumbered piston rod extensions which are connected to and are parts of hopper top and bottom sealing piston-cylinder combinations 44, 46 respectively. Piston-cylinder combinations 44, 46 are preferably pneumatically actuated; the cylinder portions thereof are preferably fixedly connected to horizontally extending crossmembers of frame 22 as indicated generally in Figures 4 and Hopper top and bottom vacuum sealing plates 40, 42 are most preferably of dome-like shape, as illustrated in Figure 4, and have upper and lower vacuum sealing gaskets 58, 60 positioned running circumferentially around the unnumbered preferably circular lips of preferably dome-like hopper top and bottom vacuum sealing plates 40, 42 respectively.

18 When a hopper 12 is located at vacuum_ dring position as illustrated in Figure 4, pneumatic actuation of respective hopper top and bottom sealing pistoncylinder combinations 44, 46 respectively causes respective dome-like hopper top and bottom vacuum sealing plates 40, 42 to move vertically towards cylindrical hopper shell 14. Arrows A in Figure 4 denote the vertical movement of hopper top and bottom vacuum sealing plates 40, 42 respectively.

When hopper cylindrical shell 14 is located at vacuum drying position 102, actuation of respective piston-cylinder combinations 44, 46 moves top and bottom sealing plates 40, 42 downwardly and upwardly respectively to effectuate an airtight, vacuum maintaining seal between the preferably circular periphery of top and bottom sealing plates 40, 42, where S.vacuum gaskets 58 and 60 are preferably located and the preferably circular circumferential top and bottom edges S.of vacuum tube 52. The hopper top and bottom vacuum 20 sealing plates 40, 42 in this position, with gaskets 58, 60 in sealing connection with the circumferential circular top and bottom edges of vacuum tube 52, as illustrated in Figure Top vacuum sealing plate 40 preferably includes a fitting, not numbered in the drawings, selectably connectingly receiving a preferably flexible vacuum line which is preferably connected to a vacuum pump depicted schematically in Figure 5 and designated 48.

When hopper top and bottom vacuum sealing plates 40, 42 30 have been engaged with cylindrical shell 14 as illustrated in Figure 5 and vacuum pump 48 is actuated, vacuum is drawn within hopper 12 at this vacuum drying position. As pressure drops within hopper 12 at this vacuum drying position, moisture rapidly evaporates from granular resin material within hopper 12.

Once moisture has been evaporated from resin material within hopper 12 when located at vacuum drying 19 position 102 and the resin material has reached a desired degree of dryness, hopper top and bottom sealing piston-cylinder combinations 44, 46 are permitted to return to their default positions illustrated in Figure 4. This retracts hopper top and bottom vacuum sealing plates 40, 42 away from and out of contact with cylindrical shell 14, thereby permitting air once again to enter cylindrical shell 14 ard permitting cylindrical shell 14, having the now-dried granular resin material therewithin, to be moved to the material dispensing position.

The time during which vacuum is drawn within hopper 12 while located at vacuum drying position 102 may be adjusted by microprocessor control means connected to and associated with the low pressure granular material dryer. Similarly, the level of vacuum drawn in hopper 12 at vacuum drying position 102 may be adjusted.

Furthermore, air withdrawn from hopper 12 by vacuum pump S- 48 may be monitored for moisture content and vacuum pump 20 48 may be halted once the desired low level of moisture of the material within hopper 12 has been attained. The microprocessor control means controls operation of the low pressure dryer, including operation of the pneumatic piston-cylinder combinations, the blower, the vacuum pump, etc.

Referring to Figures 9, 10 and 11, plate-pin connection arm 116 is rotatably connected to a generally horizontal plate 28 by pin connector 168. Pin connector facilitates rotation of plate 28 respecting plate-pin 30 connection arm 116 and hence respecting pin-like extension 26 and vertical shaft 24.

Plate 28 includes a horizontal central portion and downwardly projecting lips 32 extending from the periphery of plate 28.

Three preferably pneumatically actuated pistoncylinder combinations 34, 36 and 38 are designated respectively first, second and third piston-cylinder 20 and are vpiP^_+- =I I -Frame 22, specifically to upper horizontally extending members 162 of frame 22, as generally illustrated respecting second and third piston-cylinder combinations 36, 38 in Figure 9. The pivotal connections are designated 180 in Figure 9.

To facilitate rotation of plate 28 about an axis defined by vertical shaft 24, first, second and third piston-cylinder combinations 34, 36, 38 are actuated as needed. Each piston-cylinder combination 34, 36, 38 has a piston rod extension which fits loosely within a respective aperture formed in a respective portion of a downwardly projecting lip 32, with the piston rods being retained in position within those apertures by nuts threaded on the piston rod extremities as illustrated generally in Figures 9 and 11.

With this arrangement, as piston-cylinder combinations 34, 36, 38 are actuated to move their associated piston rods, from extended positions in which 20 the piston rods of piston-cylinder combinations 36, 38 are illustrated in Figure 11 to the retracted position in which the piston rod extension of piston-cylinder combination 34 is illustrated in Figure 11. As a result plate 28 and hence, vertical shaft 24 and cylindrical hoppers 12 attached thereto rotate about the axis of vertical shaft 24, thereby moving hoppers 12 serially among the material fill and heat, vacuum drying and material dispense positions 100, 102, 104 respectively as illustrated in Figures 9 and 11.

For example, referring to Figure 9, upon actuation of first driving rotation piston-cylinder combination 34 to extend the piston shaft therefrom forwardly out of the retracted position illustrated in Figure 9 and actuation of third driving rotation piston-cylinder combination 38 to cause the piston shaft associated therewith to retract to within piston-cylinder combination 38, plate 28 rotates counterclockwise as 21 considering Figure 9, in the arrow A, with such rotation of plate 28 being about pin connector 168 and as illustrated in Figure 11 and indicated by arrow B.

As plate 28 rotates about pin connector 168 in the direction indicated by arrow A, plate 28 together with pin connector 168 rotate with horizontally extending plate-pir. connection arm 116 pivotally about the axis defined by vertical shaft 24 thereby rotating shaft 24.

This rotation results from plate-pin connection arm 116 being fixedly connected to shaft 24. Hence, as first, second and third driving rotation piston-cylinder combinations 34, 36 and 38 respectively are actuated in a sequential manner, plate 28 rotates about pin connector 168 and plate 28, pin connector 168 and platepin connection arm 116 all rotate about the vertical axis defined by shaft 24 thereby to rotate shaft 24.

The vertically-oriented cylindrical sides of hopper shells 14 defined by vacuum tubes 52 and insulation tubes 54 are connected to shaft 24 for rotation therewith by cantilever connecting rods 110 as best illustrated in Figure 10. Each cylindrical shell 14 of *a cylindrical hopper 12 may be removable from its associated cantilever connecting rods 110 if desired; preferably two cantilever connecting rods 110 are provided for each hopper 12, with one rod 110 connecting hopper 112 to vertical shaft 24 at positions relatively close to but removed from the vertical extremities of hoppers 12, as illustrated in Figure Figure 9 has been drawn without depiction of moist material supply hopper 64, exhaust plenum 142 and the structure associated therewith, to enhance drawing clarity. Similarly, hopper dispensing piston-cylinder 108 has been depicted in Figure 9 even though it is to be understood that such piston-cylinder combination would not be visible in the view from above dryer since when a hopper 12 is at material dispense position 22 104, piston-cylinder combination 106 is blocked from view from above.

Arrow B in Figure 11 depicts the preferred direction of rotation of vertical shaft 24 and hoppers 12 so as to move hoppers 12 serially from the material fill and heat position 100 to material vacuum drying position 102, then to material dispense position 104 and then to material fill and heat position 100, dhere this cycle may repeat.

At the material vacuum drying position, the heated material is preferably subjected to a vacuum of about 27.5 millimeters of mercury or greater. This lowers the evaporation point or boiling point of water to only 120 0 F, thereby causing the moisture within the heated material to evaporate and be drawn off through the vacuum pump drawing vacuum within hopper 12 at the vacuum drying position 102. Once the vacuum drying Sprocess is sufficiently complete, piston-cylinder "combinations 44, 46 retract hopper top and bottom sealing plates 40, 42 so that hopper 12 may move from the vacuum drying position to the material dispense position.

Blower 70 is preferably a one horsepower blower.

Preferably two heater elements 82 are utilized, as illustrated in the drawings. Air flow through supply plenum 86 is preferably restricted to 4.5 ounces of pressure.

As depicted schematically in the drawings by line 74 indicating the angle of repose of within hopper 12, an air space is permitted to remain within hopper 12 to accommodate material spillage during movement of hoppers 12 and cycling of the drying process.

The material fill and heat and vacuum drying functions may each take approximately twenty minutes.

Accordingly, in one hour, all three hoppers 12 preferably cycle through material fill and heat position 100, material vacuum drying position 102 and material 23 ,C Vt 12 s dispense position 104. If each 12 is approximately 10 inches in diameter and 24 inches high, each hopper 12 will hold about one cubic foot of granular resin material, which is about thirty-five pounds of granular resin material. With such configuration, dryer 10 embodying the invention can provide about 100 pounds per hour of dried granular resin material for subsequent processing by plastic injection molding or extrusion equipment.

As is apparent from the drawings, hoppers 12 are preferably provided equally spaced around vertical shaft 24 with hoppers 12 1200 apart.

ee o

Claims (36)

1. A low pressure dryer for granular or powdery material, including: a. a plurality of hoppers rotatable about a common vertical axis serially among material filling and heating, vacuum drying and material discharge positions; b. a plurality of pneumatic piston-cylinder combinations for rotating said hoppers about said axis among said filling and heating, vacuum drying and discharge positions; c. means for heating contents of a hopper at said filling and heating position; d. means for sealing a hopper at said vacuum drying position; e. means for drawing vacuum within a hopper at said vacuum drying position; f. means for selectably permitting downward flow of dried granular or powdery material out of a hopper at said discharge position.

2. Apparatus of claim 1 further including: 20 a. a vertical shaft defining said vertical axis; b. said pneumatic piston-cylinder combinations being equiangularly positioned about said shaft for rotating said shaft and thereby said hoppers.

3. Apparatus of claim 1 wherein said hoppers are open-ended, generally vertically oriented cylindrical configuration and equiangularly positioned respecting a vertical axis.

4. A hopper for use in a low pressure granular or powdery material dryer including: a. a vertically-oriented cylindrical shell having open ends, adapted to be sealingly closed by selectably contacting top and bottom plates thereagainst, enabling vacuum to be drawn within said shell when said shell is at a vacuum drawing position; b. a funnel within said cylindrical shell proximate the bottom thereof; c. an internal material flow control plate located within said cylindrical shell beneath said funnel, pivotaiiy connected to said cyiindricai shell for movement about said connection away from a downwardly opening discharge orifice in said funnel to a position permitting downward granular resin material flow from said hopper; Apparatus of claim 4 further including: a. top and bottom plates for selectively sealing said cylindrical shell allowing vacuum to be drawn therein; b. pneumatic piston-cylinder means for urging said top and bottom plates into sealing contact with said shell; said shell being adapted to selectively dispense granular material stored therein at a dispense position removed from said vacuum drawing position.

6. A method for continuously drying granular or powdery material preparatory to mixing, molding, extruding or other processing of that ~material, including the steps of: a. supplying granular or powdery material to a vertically-oriented cylindrical shell at a fill and heat position and heating said material within said shell by introduction of heated air into said cylinder; b. moving said first vertically-oriented cylindrical shell through an arc .**about a vertical axis outboard of the shell periphery to a vacuum 25 drying position and sealing open ends of said shell thereat; c. drawing a preselected level of vacuum within said sealed shell for time sufficient to evaporate moisture from said heated material to a desired degree of dryness; d. moving said shell to a discharge position at which said shell is open; e. discharging said dried maieriai iWIII bdiu Uyhi! IIIi 6Ih6II responsively to a pneumatic piston-cylinder combination actuating a material discharge gate proximate the bottom of said shell; and -26- f. moving said shell through an arc about said vertical axis to a fill and heat position and sequentially repeating steps through (d) or so long as such granular plastic material is to be continuously dried.

7. A method for continuously supplying dried granular resin material for processing from a supply of material which is excessively moist, including, substantially simultaneously performing the steps of: a. heating a portion said moist material to a selected temperature at which said moisture evaporates therefrom at a preselected level of vacuum; b. drawing and maintaining said preselected level of vacuum for a second portion of said material which has been heated to said selected temperature for a time sufficient to cause said moisture to evaporate therefrom and result in said second portion of material being at a preselected dryness; and c. supplying to granular resin material processing equipment a third portion of said material which has been dried to said preselected dryness by evaporation in said preselected level of vacuum after S 20 being heated to said selected temperature.

8. The method of claim 7 wherein respective ones of said portions are serially supplied. 0 0ll .000 s e 0*O@ @0SS 0 S @0 S *5 @0 00 @0 0 0S@ 0

9. A low pressure dryer for granular or powdery material, including: a. a plurality of hoppers movable at least between material heating and vacuum drying positions; b. means for moving said hoppers at least between said heating and vacuum drying positions; c. means for heating contents of a hopper at said heating position; d. means for sealing a hopper at said vacuum drying position; e. means for drawing vacuum in a hopper at said vacuum drying position; and f. means for selectably permitting downward flow of dried granular or powdery material out of a hopper upon said material reaching an acceptable level of dryness at said vacuum drying position.

10. Apparatus of claim 9 further including; a. a vertical shaft having said hoppers connected thereto; b. said means for moving said hoppers comprising pneumatic piston- cylinder combinations connected to said shaft for rotating said shaft and thereby moving said hoppers.

11. Apparatus of claim 9 or 10 wherein said hoppers are open-ended, of generally vertically oriented cylindrical configuration and are equiangularly positioned respecting said shaft. 25 12. A hopper for use in a low pressure granular or powdery material dryer including; a. an upwardly-oriented shell having open ends, adapted to be sealingly closed by selectably contacting upper and lower plates thereagainst, enabling vacuum to be drawn within said shell when said shell is at a vacuum drawing position; b. a iuritlIl i w lllll zldIu CyiiI lu idi ,c II pr X ,,ii ata 111 iLir... i. *eve 0050 0 0 0@SO 0 OOSS W:\SHARONndreW\.PCTCOMP73328DNi l.dC C. an internal material flow control plate located within said shell beneath said funnel, pivotally connected to said shell for movement about said connection away from a downwardly opening discharge orifice in said funnel to a position permitting downward granular resin material flow from said hopper.

13. Apparatus of clilm1 2 futher including: a. upper and lower plates for selectably sealing said shell allowing vacuum to be drawn therein; b. means for urging said upper and lower plates into sealing contact with said shell; said shell being adapted to selectively dispense granular material stored therein when at a dispense position upon completion of a vacuum drawing operation within said shell.

14. A method for drying granular or powdery material preparatory to mixing, molding, extruding or other processing of that material, including the steps of: a. supplying granular or powdery material to a shell at a heat position and heating said material within said shell by introduction of heated air thereinto; moving said shell along a path to a vacuum drying position and sealing said shell thereat; C. drawing a preselected level of vacuum within said sealed shell for time sufficient to evaporate moisture from said heated material to a desired degree of dryness; di. discharging dried material from said shell through a material discharge gate proximate the bottom of said shell; and e restoring said shell to said heat position and sequentially repeating steps (a) through for so long as such material is to be continuously dried. A method for continuously supplying dried granular resin material for processing from a supply of material which is excessively mojSt,including SUbStanialY simultaneously performing the steps of: a. heating a portion said moist material to a selected temperature at which said moisture evaporates at a preselected level of vacuum; b. drawing and Maintaiing said preselected level of vacuum over a second portion of said material which has been heated to *Said selected temperaturte for a time sufficient to cause said moisture to evaporate therefrom and result in said second portion of material being at a preselected dryness; and C. supplying to granular resin material processing equipment a third portion of said material which has been dried to said preselected dryness by evaporatiot in said preselected level of vacuum after being heated to said selected temperature.

16. The method of claim 15 wherein respective ones of said portions are serially supplied.

17. A low pressure dryer for granular or powdery material, i n clu d i ng a hopper moveable between heating and vacuum drying positions; b. means for moving said hopper at least between said heating and vacuum drying positions; C. means for heating contents of said hopper at said Miling and heating position; d. means for sealing said hopper at said vacuum drying position; e. means for drawing vacuum within said hopper at said vacuwm drying position; arnd f. means for selectably permitting downward flow of dried granular or powdery material out of a hopper upon said material reaching an acceptable level of dryness at said vacuum drying position. *18. ApparatUs of claimi 17 wherein said means for moving said hopper further in cIu d es: a. a shaft defiing an axis; b. at least one pneumatic piston-cylinder combination for rotating said shaft and thereby moving said hopper. Ig. A orf r-Inim 1 R wherein said hopper is open-ended and of generally cylindrical configuration with the axis substantially parallel with said shaft. A method for continuously drying granular or powdery material preparatory to mixing, molding, extruding or other processing of that material, including the steps of: a. supplying granular or powdery material to at least one of a plurality of shells at a fill and heat position and heating said material within said filled shells by introduction of heated air thereinto; b. moving said shells along a path defined in part by an arc to del iver said filled shell to a vacuum drying position and sealing open ends of sai shell thereat while delivering at least one remaining shell to a fill and heat position; C. drawing a preselected, level of vacuum within said sealed shell for time sufficient to evaporate moisture from said heated material to a desired degree of dryness-, d. moving said shell with said dried material therein from said vacuum drying position while moving said shell filled with said heated material to said drying position; e. discharging said dried material from said shell by actuating a material discharge gate proximlate the bottomn of said shell; and moving said now-empty shell through an arn to said fill and beat position and :sequentially repeating steps through for so long as such granular plastic material is to be continuously dried.

21. A low pressure dryer for granular or powdery material, including: at least one hopper movable among material heating and vacuum drying positions; means for moving said hopper among said heating and vacuum drying positions; means for heating hopper contents at said heating position; means for drawing vacuum within at least one hopper at said vacuum drying position; and means for selectably discharging dried granular or powdery material out of a hopper.

22. The dryer of claim 21 wherein said hopper has an opening on at least one end.

23. A hopper for use in a low pressure granular or powdery material dryer including; a shell having at least one opening in at least one end, adapted to be sealingly closed by selectably movably contacting sealing means thereagainst, enabling vacuum to be drawn within said shell when said shel is at a vacuum drawing position; an apertured baffle within said shell proximate the bottom thereof for positioning material within said shell; an internal material flow control plate located within said shell beneath said baffle, pivotally connected to said shell for movement about said connection away from a downwardly opening discharge orifice in said baffle to a position permitting downward granular resin material flow from said hopper. 2 4. The hopper of claim 2 3 wherein said shell is cylindrical. A method for drying granular or powdery material preparatory* to mixing, molding, extruding or orber processing of that material,including. the Steps Of: supplying granular or powdery material to a shell and heating said material within said shell by introduction of heated air thereto; moving said shell to a vacuum drying position and sealing said shell thereat; drawing vacuum within said sealed shell for time sufficient to evaporate moisture from said heated material to a desired degree of dryness; discharging said dried material from said cylbidrical shell; and sequentially repeating steps through for so long as granular plastic material isto b dried.

26. The method of claim 24 wherein moving said shell is performed by moving said shell through an arc.

27. Thenmethod of claim25Z or 26 wherein said shell is cylindrical.

28. The method of claim 26 wherein said shells have convex exterior surface portions.

29. The method Of claim' 27 wherein said shells are upwardly oriented. A method for continuously supplying dried granular resin material for processing from a supply which is excessively moist,including substantially simultaneously performing the steps of: heating a portion said moist material to a temperature at which said moisture evaporates at a preselected level of vacuum; drawing and maintaining at least said preselected level of vacuum over a second portion of said material heated to said temperature for time sufficient to evaporate moisture therefrom to a preselected dryness; and supplying to granular resin material processing equipment a third portion of said material evaporated to said preselected dryness after being heated.

31. The method of claim 30 wherein said portions are serially supplied.

32. A method for continuously drying granular or powdery material in batches preparatory to mixing, molding, extruding or other processing of that material, including the Steps Of: supplying granular or powdery material to a closeable shell; heating said material within said shell by introduction of heated air* thereinto; drawing a preselected level of vacuum within said shell for time sufficient to evaporate moisture from said heated material to a desired degree of dryness; discharging said dried material from said shell; and siequentially repeating steps through for so long as said granular plastic material is to be continuously dried in batches.

33. The method of claim 32 wherein said heating further includingintroducing air into said shell at a desired material temperature, measuring temperature of said air as it exits said sheji, comparing said exit air temperature to taid desired temperature and halting heating when said eit air reaches said desired temperature.

34. The method of claim 32 wherein said heating further including capturing heating air leaving said shell for recycling through said shell. The method of claim 32 wherein said heating further including Capturg heating air leaving said shell for recycling through said shell. :36. A low pressure dryer for granular or powdery material, including a shell; means for moving said shell at least among material heating and vacuum drying positions; means for heating contents of said shell at said heating position; means for drawing vacuum over contents within said shell at said vacuum drying position; and means for evacuating dried granular or powdery material from said shell.

37. The dryer of claim 3 6further i n cIu d ing;

38. Thedryerofclaim 36 or 37 further including a plurality of shells. S

39. A low pressure dryer for granular or powdery material, including: a. a plurality of shells individually movable among at least material heating and vacuum drying positions; b. means for moving said shells serially simultaneously among at least said heating and vacuum drying positions; c. means for heating contents of a shell at said heating position; d. means for drawing vacuum within a shell at said vacuum drying position; and e. means for selectably permitting flow of dried granular or powdery material out of a shell at a position selected for shell discharge. The dryer of claim 39 further including: a. means for sealing one or more shells at said vacuum drying position.

41. A dryer of claim 39 or 40 wherein said shells are collectively movable among material heating and drying positions.

42. A low pressure dryer for granular or powdery material, including: a. a plurality of shells collectively movable among positions where material loading, heating, drying and/or discharge may occur; b. means for moving said shells among said positions; c. means for heating shell contents; d. means for drawing vacuum within said shells; and e. means for removing dried granular or powdery material from said shells.

43. The dryer of claim 42 wherein the shells are movable serially.

44. A low pressure dryer for granular or powdery material, including: a plurality of shells movable around a circuit along which said shells are filled, emptied, heated and vacuum dried; means for moving sad shells around said circuit for filling and emptying said shells aid heating and vacuum drying material in said shells; means for loading said shells with material; means for heating material within said shells prior to drying; means for drawing vacuum within said shells to effectuate drying; and means for removing dried granular or powdery material from said shells after drying. A method for drying granular resin material including: heating said material to a temperature at which moisture evaporates at a preselected level of vacuum; and drawing said preselected level of vacuum around said heated material sufficiently to cause moisture to evaporate from said miaterial resulting in said material reaching a preselected level of dryness.

46. A granular material dryer including: a shell for holding granular material to be dried; means for heating granular material in said shell to a temperature at which moisture evaporates at a preselected level of vacuum; and c. means for drawing said preselected level of vacuum around said heate-d material within said sheai suffic I iently o eapVOrate moisture in said material to a selected level of dryness.

47. A low pressure dryer substantially as herein described with reference to the accompanying drawings.

48. A hopper substantially as herein described with reference to the accompanying drawings.

49. A method substantially as herein described with reference to the accompanying drawings. 15 50. A granular material dryer substantially as herein described with reference to the accompanying drawings. 9099 DATED: 3 August 2001 PHILLIPS ORMONDE FITZPATRICK 20 Attorneys for: MAGUIRE PRODUCTS, INC. 0*6 D W.SHARON\An rew\PCTCOMP\733028Dvisionaldoc