Patent Application
20200158429
Applicant hereby incorporates by reference United States patent publication US 2018-0264684 A1; U.S. Pat. Nos. 7,234,247 and 8,776,392 and United States reissue patents Re45,501 and Re45,408.
Not applicable—this invention was conceived and developed entirely using private source funding; this patent application is being filed and paid for entirely by private source funding.
Vacuum dryers for drying granular plastic resin material, prior to that material being molded or extruded into a finished product, are known. One commercially successful vacuum dryer, as disclosed in U.S. Pat. No. 6,154,980, uses a powered, rotating carousel to move granular plastic resin material among three stations, at which the granular plastic resin material is heated, dried by vacuum, and stored. Another approach to vacuum drying of granular plastic resin material is disclosed and claimed in U.S. Pat. No. 8,776,392.
This invention uses gravity to move granular plastic resin material in a vacuum dryer. The granular plastic resin material preferably is heated in a top heating hopper. The granular plastic resin material is then preferably dropped into a vacuum chamber. From the vacuum chamber the granular plastic resin material is preferably dropped into a retention hopper.
A plastic product manufacturing process, either molding or extrusion, can preferably draw dry granular plastic resin material from the retention chamber as required, while the heating hopper and the vacuum chamber preferably continuously prepare subsequent batches of granular plastic resin material. The preferable straight down processing and drying of granular plastic resin material results in a much lower cost dry granular plastic resin material as compared to granular plastic resin material dried using known vacuum dryers.
In a preferred embodiment of this invention, preferably at least one slide gate allows and blocks granular plastic resin material downward flow from part of the dryer to another. Costs are reduced by about forty percent and drying capacity is actually higher in the advantageously small footprint dryer embodying this invention. The small footprint afforded by the vertical, “stacked” configuration of this dryer is advantageous in that space in a plastic manufacturing processing plant, whether an extrusion operation or a molding operation, is often at a premium.
The vacuum chamber of the granular plastic resin material dryer is preferably closed with at least one slide gate having a vacuum tight seal. The slide gate preferably closes and seals against an o-ring to provide a vacuum tight seal. Use of the slide gate avoids vacuum leakage that could occur from the contamination that is present everywhere in a plastic molding or extrusion facility. With the slide gate, plastic dust, flakes, and pellets of granular plastic resin material do not interfere with the vacuum tight seal.
The invention introduces dry air into the vacuum chamber periodically. As moisture is released from the granular plastic resin material while under vacuum, a vacuum pump preferably continues to pull the resulting air-water vapor mixture from the vacuum chamber. Over several minutes, this mixture changes to become a very high percentage of water vapor relative to the air remaining in the chamber.
If the moisture in the form of water vapor is not purged, when vacuum is released from the vacuum chamber, the resulting “thin” but moisture-laden air would reenter the pellets of granular plastic resin material resident within the chamber and reverse the effect of the drying that has occurred. To prevent this, the invention preferably purges the vacuum chamber of moisture several times while vacuum is present. The invention preferably permits very dry purge air to enter the vacuum chamber and then draws the resulting mix of the very dry air and the water vapor-laden air, laden with moisture drawn out of the resin pellets, out of the chamber.
When drying polyethyleneterephthalate (“PET”), used conventionally for beverage bottles, it is essential that moist ambient air not enter the vacuum chamber at the end of a vacuum cycle. The dry air purge allows effective drying of PET pellets.
To supply such dry purge air, the invention preferably uses a separate dry air source. Suitable dry air can be obtained in several ways. Desirably in the practice of the invention in the preferred manner, the invention utilizes compressed air, which passes through at least one oil separator coalescing filter and a compressed air membrane dryer so that the air exiting the oil separator coalescing filter and the compressed air membrane dryer is extremely dry. This dry air is desirably heated to a desired level for introduction into the vacuum chamber. Since only a relatively small amount of dry air is required for purging the vacuum chamber, the compressed air membrane dryer can be very small and of very low capacity.
In the invention, the hopper in which the granular plastic resin material is initially heated is preferably designed such that hot air enters the bottom of the hopper, passes upwardly through the granular plastic resin material resident in the hopper, and exits the hopper at the top. As the hot air is passing through the heating hopper, granular plastic resin material may be dropped from the bottom of the hopper into the vacuum chamber, while new granular plastic resin material is added at the top of the hopper. The heating hopper preferably holds sufficient granular plastic resin material to provide from three to five hours of residence time for the granular plastic resin material before exiting the bottom of the heating hopper. In this way, the granular plastic resin material is exposed to hot, dry air for from three to five hours, which is the time required for the granular plastic resin material to flow downwardly through the heating hopper.
The invention does not dry the granular plastic resin material using “hot” air in the conventional sense. Hot air is used only to bring the granular plastic resin material up to a desired temperature. By carefully controlling the speed of a blower that moves the hot air, air flow is adjusted so that the invention provides the hot air at the correct rate to heat the granular plastic resin material. Viewed differently, most of the useful heat, in terms of calories or BTUs, is removed from the hot or “heating” air before the heating air arrives at the upper surface of the granular plastic resin material in the heating chamber and is allowed to escape.
In the instant invention, since the invention is not concerned with heating during the drying stage, namely the stage during which the pellets are exposed to vacuum in the vacuum chamber, is as short as possible, and may be as little as fifteen or twenty minutes, as contrasted to three to five hours in a conventional desiccant dryer. There is no air filter for the heating air in the invention. The heating air is used only once and is vented to the atmosphere after it has been used for heating and has given up most of its heat. The hearing air is not recirculated.
The single pass flow of heating air and the elimination of the need for a filter for the heating air is unique to this invention. Earlier vacuum dryer designs involved recirculation of air with filtering being required. This invention eliminates the need for a filter by having the “heating” air pass through the granular plastic resin material only once. The invention further regulates the speed of the blower forcing the air through the material to avoid, to the extent possible, loss of unused, residual heat remaining in the “heating” air leaving the heating hopper. Blower speed is adjusted so that only enough heated air, at a desired temperature for the resin material prior to drying, is fed to the heating hopper at the bottom so that the bottom potion of resin in the heating hopper reaches the desired final temperature to meet the appetite of the process machine, namely the molding machine or extruder, for dry granular plastic resin material to be molded or extruded.
In one of its aspects, this invention provides a method for drying granular resin material prior to processing of the granular resin material by molding or extrusion that includes heating granular resin material in a heating hopper, monitoring air temperature at the top of the heating hopper, and regulating introduction of heat to the hopper bottom based on monitored air temperature at the top of the heating hopper.
The method may further proceed by releasing heated granular resin material from the heating hopper for flow downwardly into a vacuum chamber while replenishing the heating hopper from above with fresh resin material, preferably in an amount substantially equal to that released into the vacuum chamber. The method preferably proceeds by drawing vacuum in the vacuum chamber, periodically purging the vacuum chamber interior with dry air while the chamber is under vacuum, draining resin material from the vacuum chamber into a retention hopper, and blanketing dried resin material in the retention hopper with dry air so long as the material is resident therein.
Heating the granular resin material preferably further includes introducing dry heating air into the heating hopper at the heating hopper bottom.
In another aspect of the invention, there is provided an improved method for drying granular resin material prior to processing thereof by molding or extrusion by loading granular resin material into a heating hopper from above the hopper, introducing heated air into the hopper at the hopper bottom, monitoring the temperature of the air leaving the hopper at a position above the resin material, and regulating the rate of heated air introduction into the hopper so that monitored temperature of air leaving the hopper does not exceed a preselected level.
In still another one of its aspects, this invention provides apparatus for drying granular resin material prior to molding or extrusion processing of the material. Desirably the apparatus includes a heating hopper, a vacuum chamber positioned below the heating hopper, and a retention hopper positioned below the vacuum chamber. A blower is provided for pumping heating air upwardly through the retention hopper.
The following detailed description is merely exemplary in nature and is not intended to limit the described embodiments of the invention or uses of the described embodiments. As used herein, the words “exemplary” and “illustrative” mean “serving as an example, instance, or for illustration.” Any implementation or embodiment or abstract disclosed herein as being “exemplary” or “illustrative” is not necessarily to be construed as preferred or advantageous over other implementations, aspects, or embodiments. All of the implementations or embodiments described in the detailed description are exemplary implementations and embodiments provided to enable persons of skill in the art to make and to use the implementations and embodiments as disclosed below, to otherwise practice the invention, and are not intended to limit the scope of the invention, which is defined by the claims.
Furthermore, by this disclosure, there is no intention on the part of the Applicant to be bound by any express or implied theory presented in the preceding materials, including but not limited to the summary of the invention or the description of the prior art, or in the following detailed description of the invention. It is to be understood that the specific implementations, devices, processes, aspects, and the like illustrated in the attached drawings and described in the following portion of the application, usually referred to as the “specification,” are simply exemplary embodiments of the inventive concepts defined in the claims. Accordingly, specific dimensions and other physical characteristics relating to the embodiments disclosed herein are not to be considered as limiting as respecting the invention unless the claims or the specification expressly state otherwise.
Referring to
Heating hopper 12, vacuum chamber 14, and retention hopper 16 are all preferably independently supported by a support frame designated 20 and shown only schematically in
Similarly, vacuum chamber 14 is independently supported by support frame 20 so that none of the weight of vacuum chamber 14 is transferred to or borne by retention hopper 16. While support frame 20 has been depicted in
The vertically aligned “stacked” arrangement of heating hopper 12, vacuum chamber 14, and retention hopper 16, as depicted generally in
Air for heating granular plastic resin within heating hopper 12 is supplied by a centrifugal blower 22 that draws in ambient air and forces that ambient air through an air heating chamber 23, which preferably includes a heating element 24 positioned within an open ended cylindrical housing 25. The open ended cylindrical housing 25 is preferably a 6 inch diameter, 6 inch length stainless steel cylinder having suitable insulative material around the exterior thereof. Voltage applied to heating element 24 within cylindrical housing 25 causes heating element 24 to rise in temperature. Air passing along heating element 24, as blown through air heating chamber 23 by centrifugal blower 22, is heated by heating element 24 and exits air heating chamber 23 at the top of chamber 23 and travels via a hot air conduit 74 to heating hopper 12, where the hot air enters heating hopper 12 at the bottom thereof for upward passage through granular plastic resin residing in heating hopper 12. A variable frequency drive 30 is provided for centrifugal blower 22 to modulate the speed of blower 22 and thereby control and adjust the amount of heating air, and therefore the amount of heat, that is introduced into heating hopper 12.
Vacuum chamber 14 is mounted on support frame 20 with one or more load cells 36 between vacuum chamber 14 and support frame 20. Load cell 36 provides data to controller 76 as to the weight of vacuum chamber 20 and any granular plastic resin material being dried therein.
Similarly, retention hopper 16 is mounted on support frame 20 using one or more load cells 38 to provide data to controller 76 as to the weight of dried granular plastic resin material resident within retention hopper 38.
Temperature sensors are provided to monitor air temperature at the inlet connecting conduit 74 to heating hopper 12 and at the top of heating hopper 12, where the heated air, having given up most of its heat, is exhausted. The temperature sensor at the hot air inlet to heating hopper 12 is designated 44 in the drawings, while the temperature sensor at the outlet, at the top of heating hopper 12 where heated ambient air is exhausted, is designated 46.
A material level sensor 42 is provided in heating hopper 12. Level sensor 42 provides a signal indicating excessively low level of material in heating hopper 12. Controller 76 receives a signal from heating hopper level sensor 42 and in response to a low material level signal, controller 76 either actuates apparatus to provide granular resin material for replenishing heating hopper 12 or if no material is available, controller 76 shuts down the air purge dryer 10.
A temperature sensor 56 within retention hopper 16 senses the temperature of the dry purge air with which dried granular resin in retention hopper 16 is blanketed. A granular resin material temperature sensor 58 may be provided at the bottom, close to the material outlet from retention hopper 16, to sense the temperature of the resin material being supplied from retention hopper 16.
Controller 76 desirably has two display screens. The upper screen 82, which desirably has a red background, shows actual temperatures and set point temperatures. The lower screen 84, which desirably has a blue background, shows various running mode information, set up information, and dryer configuration information, as selected by the operator by touch controls that are a part of controller 76 and are associated with the two screens.
One or more oil separator coalescing filters 32 are provided to remove entrained oil and some moisture from the compressed air supply. A compressed air membrane dryer 34 further dries the air and provides very dry purge air for vacuum chamber 14 and a dry air blanket for maintenance of dry conditions for granular resin material in retention hopper 16.
As operation of the air purge dryer begins, material in heating hopper 12 is brought up to temperature. The time for preheating is determined by a specified preheat time, which may be entered by an operator into controller 76, or by an automatic set-up option in controller 76 which establishes an inlet-to-outlet temperature difference for the air input to and exhausted by heating hopper 12, and a minimum preheat time. Once resin material in heating hopper 12 is up to temperature, as determined by the inlet-to-outlet temperature difference as measured by temperature sensors 44 and 46, and the temperature difference is supplied to controller 76, approximately one-third of the resin material in heating hopper 12 is dispensed into vacuum chamber 14. Once this occurs, a first vacuum cycle begins. Each vacuum cycle, namely the time a batch of resin material remains in vacuum chamber 14 under vacuum, has a minimum time that the material is under vacuum. This time may be set by an operator using the inputs available on controller 76 or a default time of 20 minutes may be used.
During normal operation, vacuum in vacuum chamber 14 is brought to a level of about 700 mm Hg and held to about a plus or minus 20 mm Hg differential for the vacuum cycle time. A typical vacuum cycle lasts from 15 to 20 minutes, depending on the material being dried.
As vacuum chamber 14 receives the heated granular resin material through first conduit 102 through operation of material flow control gates 60 and 62 and the vacuum cycle begins, a suitable loader, either human or mechanical, loads heating hopper 12 with new replenishment material, desirably concurrently with the start of the vacuum cycle. Granular resin material loaded into heating hopper 12 remains in heating hopper 12 for a minimum of the time for a vacuum cycle in vacuum chamber 14. After a vacuum cycle in vacuum chamber 14, granular resin material that has been dried in vacuum chamber 14 is dispensed downwardly through second conduit 104, via operation of material flow control gates 64 and 66, into retention hopper 16 and is ready for use. Dried granular resin material residing in retention hopper 16 and not immediately removed therefrom for molding or extrusion is blanketed with dry air so long as that granular resin material remains in retention hopper 16. The dry air blanketing the dried granular resin material remaining in retention hopper 16 is maintained under positive pressure and is desirably slightly heated so as to be warm.
The rate of consumption of dried granular resin material from retention hopper 16 dictates the time granular resin material will be heated in heating hopper 12 and dried under vacuum in vacuum chamber 14. For example, if thirty (30) minutes are required to deplete retention hopper 16, the vacuum cycle in vacuum chamber 14 will run past the normal twenty (20) minute set point and will last thirty (30) minutes. This is normal operation and does not in any way degrade the granular plastic resin that has been dried in vacuum chamber 14. However, if retention hopper 16 is depleted in fifteen (15) minutes and the time for a vacuum cycle in vacuum chamber 14 has been set to twenty (20) minutes, a five (5) minute window will result when no granular resin material is available. This indicates that the throughput capacity of the dryer has been exceeded for the particular granular resin material being dried. Upon such occurrence, controller 76 senses that retention hopper 16 is empty, that vacuum chamber 14 is still drying material, and with no material being available in retention hopper 16, controller 76 sounds an alarm.
Vacuum chamber load cell(s) 36 and retention hopper load cell(s) 38 allow controller 76 to always have in memory the current weight of material in the vacuum chamber and the current weight of material in the retention hopper. This permits calculation by controller 76 of throughput of granular resin material in pounds of resin material per hour.
Venturi vacuum generator 28 requires an operating air pressure of about 80 psi. The pressurized air is desirably supplied by an in-house air system.
A purge air inlet temperature sensor 56 is provided in retention hopper 16. A granular resin material outlet temperature sensor 58 is provided at the bottom of retention hopper 16. Both sensor 56 and sensor 58 provide temperature data to controller 76.
The desired temperature of air being outlet from the top of heating hopper 12 may be set in controller 76 such that once the temperature of air escaping from the top of heating hopper 12 reaches a desired level, centrifugal blower 22 and heating element 24 will shut down for a predetermined time period specified by an operator and programmed into controller 76 or until a vacuum cycle, which is under way, ends, whichever event comes first.
The fill and the fill rate for vacuum chamber 14 are controlled and may be adjusted by material flow control gates 60 and 62 above vacuum chamber 14 as actuated and controlled by controller 76. Similarly, material dump and material dump rate from vacuum chamber 14 can be controlled and adjusted by material flow control gates 64 and 66 below vacuum chamber 14 as actuated and controlled by controller 76. These parameters, namely vacuum chamber fill and fill rate and vacuum chamber dump and dump rate are programmable into controller 76. Similarly, the timing by which dry purge air is introduced into vacuum chamber 14 is desirably adjusted and controlled by controller 76. Typically during a twenty (20) minute vacuum cycle, purge air will be introduced into vacuum chamber 14 six (6) times.
Controller 76 controls and allows adjustment to the heat output provided to heating hopper 12. While the vacuum dryer of the invention produces dried material in batches, the dryer is a continuous supplier of suitably dry material for molding or extrusion. Dry material may be withdrawn from retention hopper 16 on a continuous basis. Vacuum chamber 14 processes one batch of material every 20 minutes, which is sufficient to keep retention hopper 16 and any process machine being fed by retention hopper 16 supplied on a continuous basis.
The vacuum dryer of the invention uses fresh air without recycling any air in the dryer. The air coming into the dryer is used once and goes out of the dryer; there is no recycling of air.
The load cells, together with controller 76, facilitate tracking throughput of granular resin material by the vacuum dryer of the invention, permitting optimization of manufacturing parameters in the plastic molding or extrusion facility in which the dryer of the invention is located.
During the course of operation of the invention, vacuum is drawn by venturi vacuum generator 28 from vacuum chamber 14 via vacuum drawing conduit 90.
Incoming compressed air from the plastics molding or extrusion facility is supplied to pressure regulator 100 as indicated in the drawing. This regulated pressurized air, with pressure regulated to a required level, is then supplied via regulated pressure air line 106, which splits as illustrated in
Purge air is provided via purge air supply line 94 which exits compressed air membrane dryer 34 and supplies purge air in very dry form after exiting dryer 34 to both retention hopper 16 and to vacuum chamber 14. Introduction of purge air to retention hopper 16 is controlled by valve 96, which in turn is actuated by controller 76. Introduction of purge air to vacuum chamber 14 is controlled by vacuum chamber purge air valve 98, which in turn is also controlled by controller 76. The wiring for connection of valves 96, 98 and the other components to controller 76 is not illustrated in the drawing to enhance the drawing clarity.
Flow of granular plastic resin material downwardly from heating hopper 12 to vacuum chamber 14 is desirably through a first conduit 102. Flow of dried granular resin material from vacuum chamber 14 to retention hopper 16 is desirably through a second conduit 104. Conduits 102, 104 are respectively mechanically connected, preferably substantially air tightly, respectively to heating hopper 12, vacuum chamber 12 and retention hopper 16.
Gates 60, 62, 64, and 66 have been illustrated positioned respectively in the bottom of heating hopper 60, at the top and at the bottom of vacuum chamber 14, and at the top of retention hopper 16. These gates may desirably be positioned in respective first and second conduits 102, 104 according to the manner of selected construction for the flow through vacuum dryer.
It is desirable to have two gates, such as gates 60, 62, above vacuum chamber 14 to control downward flow of resin from heating hopper 12, with an upper gate 60 providing gross, course control and a lower gate 62 providing air tight vacuum sealing of the vacuum chamber. Use of the two gates, 60, 62, with course control afforded by upper gate 60, minimizes the possibility of resin material becoming stuck in gate 62 and thereby precluding gate 62 from making the vacuum tight seal required for effective operation of vacuum chamber 14 during the drying phase. Desirably, gate 62 is a slide gate providing vacuum tight seal using a rubber gasket with the movable slide portion of the gate closing against the rubber gasket and moving first in a direction laterally across with respect to the direction of downward flow of resin and then vertically parallel with the direction of downward flow of resin, with such horizontal and then vertical movement of the gate effectuated by the shape of the slot in which the slide gate moves.
Material gate 64 may similarly be a slide gate or may be a pivoting gasket-equipped gate actuated by an air cylinder with the gate pivoting downwardly to effectuate downward flow of dried plastic resin material out of vacuum chamber 14 upon the conclusion of the vacuum cycle. Use of a pivoting-type gate at gate 64 reduces cost over the cost of a slide gate since gravity will carry any residual granules of plastic resin material downwardly through second conduit 104 into retention hopper 16. Gates 60 and 66 may be of any suitable type, desirably actuated by air cylinders controlled by controller 76.
All components illustrated in
Although schematic implementations of present invention and at least some of its advantages are described in detail hereinabove, it should be understood that various changes, substitutions and alterations may be made to the apparatus and methods disclosed herein without departing from the spirit and scope of the invention as defined by the appended claims. The disclosed embodiments are therefore to be considered in all respects as being illustrative and not restrictive with the scope of the invention being indicated by the appended claims rather than by the foregoing description. All changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein. Moreover, the scope of this patent application is not intended to be limited to the particular implementations of apparatus and methods described in the specification, nor to any methods that may be described or inferentially understood by those skilled in the art to be present as described in this specification.
As disclosed above and from the foregoing description of exemplary embodiments of the invention, it will be readily apparent to those skilled in the art to which the invention pertains that the principles and particularly the compositions and methods disclosed herein can be used for applications other than those specifically mentioned. Further, as one of skill in the art will readily appreciate from the disclosure of the invention as set forth hereinabove, apparatus, methods, and steps presently existing or later developed, which perform substantially the same function or achieve substantially the same result as the corresponding embodiments described and disclosed hereinabove, may be utilized according to the description of the invention and the claims appended hereto. Accordingly, the appended claims are intended to include within their scope such apparatus, methods, and processes that provide the same result or which are, as a matter of law, embraced by the doctrine of the equivalents respecting the claims of this application.
As respecting the claims appended hereto, the term “comprising” means “including but not limited to”, whereas the term “consisting of” means “having only and no more”, and the term “consisting essentially of” means “having only and no more except for minor additions which would be known to one of skill in the art as possibly needed for operation of the invention.” The scope of the invention is, therefore, indicated by the appended claims rather than by the foregoing description and all changes which come within the range of equivalency of the claims are to be considered to be embraced within the scope of the claims. Additional objects, other advantages, and further novel features of the invention will become apparent from study of the appended claims as well as from study of the foregoing detailed discussion and description of the preferred embodiments of the invention, as that study proceeds.
This patent application is a 35 USC 120 continuation of co-pending U.S. patent application Ser. No. 14/693,951, filed 23 Apr. 2015 in the names of Stephen B. Maguire and Michael E. Gera, Jr., and assigned to Maguire Products, Inc. The '951 application claimed the priority under 35 USC 119 and 120 of pending U.S. provisional application Ser. No. 61/986,266 entitled “Vacuum Dryer for Granular Plastic Resin Material” filed 30 Apr. 2014 in the name of Stephen B. Maguire. This patent application similarly claims the benefit of the filing date of the '266 application through the '951 application, pursuant to 35 USC 120. The '951 application is issuing today as U.S. Pat. No. 10,539,366. This patent application is entitled to and claims the benefit of the filing date of the '951 application under the authority of Immersion Corp. v. HTC Corp., 826 F.3d 1357, 119 USPQ2d 1083 (Fed. Cir. 2016).
| Number | Date | Country | |
|---|---|---|---|
| 61986266 | Apr 2014 | US |
| Number | Date | Country | |
|---|---|---|---|
| Parent | 14693951 | Apr 2015 | US |
| Child | 16747938 | US |
