Exemplary embodiments of the invention are related to a densifier. More particularly, exemplary embodiments include a densifier that has a system that facilitates cooling of mechanical components of the densifier to promote relatively prolonged or continuous use of the densifier. Exemplary embodiments of the invention also include a related method for cooling a densifier. A further exemplary embodiment relates to a system and method for adjusting a densifier such as to improve the output and/or to clean the densifier.
The amount of materials ending up in landfills is continuously increasing. As the scarcity of landfill space increases, along with more stringent environmental regulations, there have been increased efforts to reduce the amount of waste produced by individuals, in addition to an increased effort to recycle materials. Many different processes and machines have been developed to facilitate combating this ever-increasing problem.
One of the major contributing materials to landfill overflow are plastics. Additionally, certain types of lightweight plastics, such as, for example, expanded polystyrene (EPS), extruded polystyrene foam, and expanded polypropylene foam are not easily recycled because of their light weight and low scrap value. Many plastics take a very long period of time to biodegrade, if they biodegrade. These types of plastics may also be resistant to photolysis. Furthermore, certain types of lightweight plastics may not only float on water, but may also blow in the wind, causing an abundant amount of litter, especially along shores and waterways.
To combat the littering problem that comes with the use of plastics, different machines and methods of recycling have been developed. This is especially true regarding foamed plastics that typically require an extra step of densifying the foamed plastic. Different machines and methods have been developed to facilitate densification of plastics and other materials that may be recycled. Densification may facilitate the reduction of pentane gas dangers. Also, the densification process may reduce storage requirements and reduce hauling and/or handling costs.
There are currently three different types of densification methods that may be used to densify EPS and other plastics: heat extrusion, ram compaction, and screw compaction using an auger or compactor/compression screw. The known screw densifiers and related methods are less than ideal for densifying or compacting materials. One of the main problems that occur during the densifying process is that the mechanical components used to contact the plastic throughout the screw densification process may heat to undesired levels. This is especially true when known screw densifiers continuously run for extended periods of time.
Densifiers that use screw compaction have an especially inherent problem with material melt or plasticizing of the material due to the high heat. This occurs when the coefficient of friction between the material and typically the end surface of the compression screw generates high temperatures. Thus, plastics and other materials that have low melt points may be particularly vulnerable to melting during operation of known densifiers. For example, the unwanted temperature of the compression screw may be around 300 degrees Fahrenheit, which may be when the plasticizing of the material occurs. With many materials, it is highly undesirable for the materials to melt during the densification process because the melting may change the composition and/or properties of the material. For example, melting the material may change its functional properties, which may limit its future uses and hence reduce its value. Also, melting the material may change the characteristics of the output (e.g., the density or size of the log) of the densification process, which may reduce the quality of the output and/or impair the operation of the densifier. Also, plasticizing of the material may eliminate or impair the ability of the screw to transmit the force required to move the log of densified material through the compression chamber, ceasing continuous operation until the screw cools and can be cleaned of agglomerated material. Ceasing the continuous operation of the densifier may add extra time and cost to the recycling process.
Given the problems that exist with known screw densifiers, a densifier that incorporates a cooling system that minimizes the heat produced in the shaft and/or flights of the screw while operating the mechanical components of the densifier would be advantageous. Furthermore, providing a cooling system and method of cooling that provides an efficient means to cool the compression screw or other mechanical components is also desirable. Furthermore, it is desired that the cooling system and method of cooling may allow the densifier to run on a substantially continuous basis by minimizing or eliminating a buildup of solid material mass caused by melting or plasticizing that could stop or slow down the densifier. An exemplary embodiment of a densifier with a cooling system and method of cooling may satisfy some or all of these needs or preferences.
Although this application may talk about a densifier that employs the method of screw compaction to densify plastics and other materials, the cooling system and method may be used in other applications other than densifying processes. Additionally, although this application may talk about implementing the cooling system with a densifying system that includes a screw compactor, exemplary embodiments of the cooling system may be implemented with any number of densifying, condensing, or other systems that require heat reduction. It should also be noted that the cooling fluid could be replaced by or alternated with a heating fluid for other applications that require heat.
Exemplary embodiments of the cooling system and method may provide a compression screw for advancing plastic material having an interior bore and pocket chambers incorporated in at least one screw flight for the reception of fluid that is temperature controlled to maintain a temperature below that of the plasticizing or melt temperature of the material.
Exemplary embodiments of the cooling system and method may also provide increased volume output of the compression screw through increased speed of the screw, which is facilitated by temperature control of at least the distal end and/or at least one compression flight of the screw.
Further, exemplary embodiments of the cooling system and method may provide increased density of the output log or bale through additional force applied to the screw, which is facilitated by temperature control of at least the distal end and/or at least one compression flight of the screw.
Exemplary embodiments of the cooling system and method may also provide a novel combination in which a baffling apparatus is provided in the bore of the shaft and/or at least one flight, whereby circulation of temperature controlled fluids may take place in the desired bore and/or formed flight pockets.
Exemplary embodiments are directed to a densifier with a cooling system and to a method of cooling densifiers. Certain embodiments of the cooling system may be used in densifiers of multiple geometries and sizes that are used to densify different materials. Unless expressly set forth, it is not intended to limit the invention to densifying particular materials.
In accordance with exemplary embodiments of the cooling system and method for a densifier, there is provided an interior bore of the screw and a flow pocket chamber in at least one flight of the screw for temperature control where fluids are circulated so as to maintain the temperature of the screw below the melt or plasticizing temperature of the material. Also, the cooling system elements employed in conjunction with the interior bore of the screw and the flow pocket chamber in the screw flight(s) may include or be in association with thermo, speed, and/or density controls to control the circulation or lack of circulation of the fluids, temperature of the fluids, and/or volumetric output and density of the densified material produced.
In addition to the novel features and advantages mentioned above, other benefits will be readily apparent from the following descriptions of the drawings and exemplary embodiments.
As seen in
Exemplary embodiments of the densifier 10 may include a compactor module 200 that is mounted to the frame 100, as seen in
Exemplary embodiments of the grinding chamber 210 house a compression screw 230 that may be mounted to or otherwise extend generally between the distal wall and proximal wall 216 of the grinding chamber 210. In exemplary embodiments, the compression screw 230 may be secured to or otherwise in association with the grinding chamber 210 and/or frame by at least one bearing 222. In certain exemplary embodiments, the bearing 222 is contained in a bearing housing 220 that engages the proximal wall of the grinding chamber 210. The bearing housing 220 may be any number of geometries depending on the number and types of bearings used. However, the bearing housing 220 is substantially cuboid in this particular embodiment. Preferably, in some embodiments, at least a portion of the bearing housing 220 engages at least a portion of the proximal wall that may encircle the opening contained therein to assure that material does not exit the proximal end of the grinding chamber 210. In some embodiments, a gasket 224 or similar device may be placed between the bearing housing 220 and the proximal wall of the grinding chamber 210 to effectuate a seal.
In exemplary embodiments, such as seen in the examples in
The compression screw 230 may include one or more flights 240 in exemplary embodiments, such as seen in the examples of FIGS. 12C and 14A-14D. Preferably, at least one flight 240 includes a chamber 242 wherein fluid may flow through the flight 240 to cool at least the distal end of the compression screw 230. Typically, the distal end of the compression screw 230 produces the most heat during the operation of the densifier 10. Therefore, in most exemplary embodiments, the flight 240 located closest to the distal end of the compression screw 230 includes a chamber 242 that allows fluid to flow therein. However, in other embodiments, any number of flights 240 along the compression screw 230 may include a chamber 242 that allows fluid to flow therein to cool the compression screw 230. The chamber or chambers 242 contained within the flights 240 may be any number of geometries and may or may not be continuous along the entire length of the compression screw 230. In some exemplary embodiments, the chamber 242 may be substantially circular in cross-section area or any other suitable geometry to facilitate fluid flow. In some exemplary embodiments, the chamber 242 begins at a distal end portion of the flight 240, where it is in fluid association with the fluid exiting the plug 238. The chamber 242 may travel within the length of the flight 240, following the geometry of the flight 240 around the shaft 232 of the compression screw 230. The chamber 242 may then exit toward a proximal end portion of the flight 240 into the aforementioned area between the outer wall of the tubular body 234 and the inner wall of the hollowed shaft 232. In some exemplary embodiments wherein more than one flight 240 contains a chamber 242, the fluid may enter and exit multiple chambers 242 from the area between the outer wall of the tubular body 234 and the inner wall of the hollowed shaft 232 during operation of the densifier 10. Also, it should be recognized that the cooling fluid could alternatively enter a proximal end portion of a flight 240 and then exit at a distal end portion thereof. Such an embodiment could eliminate the need for a plug 238.
Unlike many types of known compression screws, the flights 240 in some exemplary embodiments that are located towards the distal end may not be conical or tapered in geometry. Instead, the flights 240 may have a flattened end 244 at the distal end in relationship with the flat end 246 of the shaft 232. The flattened ends 244 and 246 of the flights 240 and shaft 232 may help eliminate holes in bales or logs of materials produced by the densifier 10.
Exemplary embodiments of the shaft 232 of the compression screw 230 are connected with a rotary union 250 situated at the proximal end thereof that allows the fluid to flow from the rotating shaft 232 to return connections 252. One example of a rotary union 250 that may be used is the 9300 series of rotary unions fabricated by Talco, Inc. which has the website www.rotaryunions.net.
In exemplary embodiments, such as seen in the examples of
Exemplary embodiments of the rotary union 250 may also include an inlet 266 that connects with a fluid supply line 254 that is in fluid association with a heat exchanger 290 and allows cooled fluid to flow from the heat exchanger 290 through the rotary union 250 and into the tubular body 234 contained within the shaft 232 of the compression screw 230.
Exemplary embodiments of the densifier 10 may include a fluid reservoir 270 connected to the frame 100. In this particular embodiment, the fluid reservoir 270 is located on the left side at the proximal end 100a of the frame. However, in other exemplary embodiments, the fluid reservoir 270 may be located at different locations on the frame 100, depending upon design characteristics and other needs. Furthermore, in some embodiments, the fluid reservoir 270 may not be located on the frame 100. For example, the reservoir 270 could be situated adjacent to the grinding chamber 210 to allow for more ventilation in another exemplary embodiment. In some embodiments, the fluid return line 264 that is in fluid association with the fluid reservoir 270 connects with a portion of the upper surface of the fluid reservoir 270 so that the fluid flows down into the reservoir with minimal required force. However, in other embodiments, the fluid return line 264 may be connected to any location of the fluid reservoir 270. The fluid reservoir 270 may have a number of different geometries that allow suitable operation of the densifier 10. In one example, the reservoir 270 is substantially cuboid. Also, in some exemplary embodiments, the bottom inner surface of the reservoir may be concave (not shown) to facilitate collection of the cooling fluid at a certain point within the reservoir. Furthermore, exemplary embodiments of the fluid reservoir 270 may include a screening device (not shown) that may help facilitate filtration of the cooling fluid to remove any undesired debris or particulates that may enter the cooling system during use.
A pump 280 is in fluid association with the fluid reservoir 270 and the heat exchanger 290 (via a line 267). Any number of fluid pumps may be used that allow suitable operation of the densifier 10. In some exemplary embodiments, the pump 280 is mounted on the heat exchanger 290. However, in other exemplary embodiments, the pump 280 may be mounted on the frame 100 or other suitable locations associated with the densifier 10. During operation, the pump 280 pulls cooling fluid from the fluid reservoir 270 and pushes the cooling fluid through the heat exchanger 290 and the rest of the cooling system to facilitate cooling of the compression screw 230.
In exemplary embodiments, a heat exchanger 290 is in fluid association with the pump 280 and the inlet of the rotary union 250 (through supply line 268). In some embodiments, the heat exchanger 290 may be mounted to the proximal end 100a of the frame 100 on mounting brackets 104, as seen in
Such as shown in
With reference to the example in
Such as shown in the example of
Some exemplary embodiments of the densifier 10 may include an infeed hopper 500, such as seen in the examples of
With reference to
Exemplary embodiments of the extruder module 600 may include a rail section 610, as seen in
In exemplary embodiments, the pressure system 620 may include a frame 622 that engages at least a portion of the rail section 610. In some embodiments, the frame 622 may engage at least the top and bottom faces of the rail section 610. In other exemplary embodiments, the frame 622 may engage only a portion of a face of the rail section 610 or may be associated in any suitable manner with the rail section 610. Exemplary embodiments of the pressure system 620 may further include at least one spring 624 secured between the frame 622 and the rail section 610. In some embodiments, two or more springs 624 may be situated and/or secured between the outer face of each side of the rail section 610 and the corresponding inner side face of the frame 622. In some embodiments, the springs 624 may be secured between plates 626 and 627 that facilitate securement to the frame 622 and the side walls 616 of the rail section, wherein at least one of the plates 627 may slide along at least one guide rail 628 that extends substantially between the inner side face of the frame 622 and an associated plate 626 wherein the plate 627 may include an aperture that allows the guide rail 628 to pass therethrough. Such as shown in these examples, a spring 624 may be situated around a guide rail 628. With the assistance of the springs 624, the side walls 616 of the rail section may be adapted to move to allow variability in the density of the material densified. In exemplary embodiments, the extruder module 600 may further include a compression system 630 that may vary the compression applied to the side walls 616 of the rail section 610. In one example, an adjustment or compression screw 632, as seen in
An example of the compression system 630 that uses a compression screw 632 to adjust the spring compression force applied to the side walls may be environmentally friendly, when compared to other known methods of compacting materials. In other exemplary embodiments, other devices may be substituted to increase or decrease the compression force applied to the side walls 616 of the rail system 610. In one other example, a hydraulic system (not shown) may be used to vary the compression force applied to the rail system. A hydraulic system may not typically be as environmentally friendly due to the potential leakage of hydraulic fluid. In another example, a pin, clamp, or other suitable adjustable mechanism may be used to control the adjustment of the compression system 630.
Although the bales and/or logs of densified material produced by this particular embodiment are substantially rectangular in cross-section, other exemplary embodiments of the extruder module 600 may produce bales and/or logs with different cross-sectional geometries. Furthermore, although only the side walls of the rail section move in the aforementioned embodiments, other embodiments may allow all of the walls of the rail section to move in response to the pressure system 620. Other suitable variations may also be possible in light of these teachings.
It is possible to associate the densifier 10, or a portion thereof, with one or more devices that may facilitate the production of the bales and/or logs of material that have a common, desired density. In some embodiments, the devices may be automated. In one example, a speed sensor 640, such as seen in the examples of
An exemplary embodiment of an adjustment system and method may be fully or substantially automated.
In another example, the speed sensor 640 may work in conjunction with the control system 645 and other components of the extruder module 600 to produce predetermined lengths of bales or logs. The feed rate of densified material may be monitored by the speed sensor 640, wherein the input signal provides a predetermined length in whatever unit of measurement is desired, such as, for example, inches or millimeters, for the bale or log length. The predetermined length may be set within the control system 645, so that the control system may automatically stop and reverse the rotation of the compression screw 230, so as to set a break point in the baled log or bale. While or after the compression screw 230 has been reversed, the counter on the control system 645 may be reset for the next log or bale, continuing the forward operation of the compaction screw 230.
In another example, the compactor module 200 may optionally include temperature sensors 662 that may monitor the temperature of the compression screw 230 and/or the temperature of the material and/or grinding chamber 210, rotary union 250, or other components that may be prone to heat, so as to minimize the chance of melting or plasticizing the materials being densified. The temperature sensors 662 may be in electrical communication with a control system 645 (e.g., a processor or other computing device) that may vary the speed of the compression screw 230 or stop the compression screw 230 if the temperature thereof reaches an unwanted temperature.
In some examples, multiple different types of the sensors described may be used in conjunction with the control system 645 to control the material flow rate of the densified material. In some exemplary embodiments, the pressure system 620 may be used in conjunction with thermal and amperage digital input signals in the control system 645 which then provide the signal to a variable frequency drive (VFD) 320 that is in association with the electric motor 310 and is able to adjust the speed of the compression screw 230 to assure the best volume output and quality of log or bale.
In another example, a pressure system 820 may be situated at the distal end of an extruder module 800, as seen in
In this example, the pressure system 820 may include a frame 822 that engages at least a portion of a rail section 810. In some embodiments, the frame 822 may engage at least the top and bottom faces of the rail section 810. In other exemplary embodiments, the frame 822 may engage only a portion of a face of the rail section 810 or may be associated in any other suitable manner with the rail section 810. In this example, the pressure system 820 may further include at least one fluid spring 824 associated between the frame 822 and a side wall 816 of the rail section 810. In some embodiments, two or more fluid springs 824 may be associated between the outer face of each side wall 816 of the rail section 810 and the corresponding inner side face of the frame 822. Furthermore, at least one fluid spring 824 may be associated with each side wall 816 of the rail section. In one example wherein the side walls 816 form a substantially rectangular cross-section, at least one fluid spring 824 may be associated with each of the four side walls, allowing for adjustment of each of the side walls independently.
With the assistance of the at least one fluid spring 824, in one example, one or both of the side walls 816 of the rail section 810 may be adapted to move to allow variability in the density of the material densified. In exemplary embodiments, the extruder module 800 may further include a compression system 830 associated with the at least one fluid spring 824 that may increase and/or decrease the compression force applied by the at least one fluid spring 824 to the side wall 816 of the rail section 810. In one example of the compression system 830, at least one fluid spring valve 832, as seen in
In exemplary embodiments, the rail section 810 or other components of the extruder module 800 may be at least partially covered by a cover guard (not shown). As seen in
In one example of the compression system 830, at least one fluid compressor 850, as seen in
In the examples shown in
An example of the compression system 830 that uses at least one fluid spring valve 832 and/or one fluid compressor 850 to adjust the compression force applied to the side walls may be environmentally friendly, when compared to other known methods of compacting materials. The fluid utilized in exemplary embodiments of the compression system 830 may be air. However, in other embodiments, the compression system 830 may use additional or other optional fluids, such as, but not limited to: water, oils, pneumatic, hydraulic, or other fluids.
In other exemplary embodiments, other devices may be substituted to increase or decrease the compression force applied to the side walls 816 of the rail system 810. In one other example, a hydraulic system (not shown) may be used to vary the compression force applied to the rail system. A hydraulic system may not typically be as environmentally friendly due to the potential leakage of hydraulic fluid. In another example, a pin, clamp, or other suitable adjustable mechanism may be used to control the adjustment of the compression system 830.
Although the bales and/or logs of densified material produced by this particular embodiment are substantially rectangular in cross-section, other exemplary embodiments of the extruder module 800 may produce bales and/or logs with different cross-sectional geometries. Furthermore, although only the side walls 816 of the rail section 810 move in the aforementioned embodiments, other embodiments may allow all of the walls of the rail section to move in response to the compression system 830. Additionally, in the example seen in
It is possible to associate the densifier 10, or a portion thereof, with one or more devices that may facilitate the production of the bales and/or logs of material that have a common, desired density. In some embodiments, the devices may be automated. In one example, a speed sensor 840, such as seen in the examples of
In operation, in one example, the PLC 645 may take a reading from the pressure transducer 846. Depending upon the pressure reading, the PLC 645 may communicate with the at least one fluid spring valve 832 to release fluid pressure within the fluid line, which in turn reduces the amount of force applied by the at least one air spring 824 to the side wall 816. Likewise, the PLC 645 may communicate with the at least one compressor 850 to operate and add fluid pressure to the fluid line, which in turn increases the amount of force applied by the at least one air spring 824 to the side wall 816.
An exemplary embodiment of an adjustment system and method may be fully or substantially automated.
In another example, the speed sensor 840 may work in conjunction with the control system 645 and other components of the extruder module 800 to produce predetermined lengths of bales or logs. The feed rate of densified material may be monitored by the speed sensor 840, wherein the input signal provides a predetermined length in whatever unit of measurement is desired, such as, for example, inches or millimeters, for the bale or log length. The predetermined length may be set within the control system 645, so that the control system may automatically stop and reverse the rotation of the compression screw 230, so as to set a break point in the baled log or bale. While or after the compression screw 230 has been reversed, the counter on the control system 645 may be reset for the next log or bale, continuing the forward operation of the compaction screw 230.
In another example, the compactor module 200 may optionally include temperature sensors 862 that may monitor the temperature of the compression screw 230 and/or the temperature of the material and/or grinding chamber 210, rotary union 250, or other components that may be prone to heat, so as to minimize the chance of melting or plasticizing the materials being densified. The temperature sensors 862 may be in electrical communication with a control system 645 (e.g., a processor or other computing device) that may vary the speed of the compression screw 230 or stop the compression screw 230 if the temperature thereof reaches an unwanted temperature.
In some examples, multiple different types of the sensors described may be used in conjunction with the control system 645 to control the material flow rate of the densified material. In some exemplary embodiments, the pressure system 620 may be used in conjunction with thermal and amperage digital input signals in the control system 645 which then provide the signal to a variable frequency drive (VFD) 320 that is in association with the electric motor 310 and is able to adjust the speed of the compression screw 230 to assure the best volume output and quality of log or bale.
In some exemplary embodiments, the rail section 610 of the extruder module 600 may be supported by a support rail 670 that is attached to and supported by at least one support post 672. Additionally, in some exemplary embodiments, a ground body 674, as seen in
In exemplary embodiments, the ground body 674 may be adapted to be secured to various surfaces, including, but not limited to: wood, concrete, brick, and various ground terrain. In some exemplary embodiments, the support rail 670 is hingedly attached 676 to the distal end of the extruder module 600 so that the support rail 670 may be raised during the relocation of the densifier, as seen in
Exemplary embodiments of the densifier 10 may include an enclosure 700 that covers the motor 310 and/or reducer 312, the heat exchanger 290 and fluid reservoir 270, as seen in
Any embodiment of the present invention may include any of the optional or preferred features of the other embodiments of the present invention. The exemplary embodiments herein disclosed are not intended to be exhaustive or to unnecessarily limit the scope of the invention. The exemplary embodiments were chosen and described in order to explain the principles of the present invention so that others skilled in the art may practice the invention. Having shown and described exemplary embodiments of the present invention, those skilled in the art will realize that many variations and modifications may be made to affect the described invention. Many of those variations and modifications will provide the same result and fall within the spirit of the claimed invention. It is the intention, therefore, to limit the invention only as indicated by the scope of the claims.
This application claims the benefit of U.S. Provisional Application No. 61/229,527, filed Jul. 29, 2009, which is hereby incorporated by reference as if fully recited herein.
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Number | Date | Country | |
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61229527 | Jul 2009 | US |