The device is in the field of laundry appliances, and more specifically, laundry appliances having a lint removal system that requires a minimal amount of user intervention for removing lint from the laundry appliance.
In at least one aspect, a laundry appliance includes a drum for processing laundry. A blower delivers process air through an airflow path that includes the drum. A lint filter is positioned within the airflow path that separates particulate matter from the process air. A lint disposal mechanism removes entrapped lint particles from a surface of the lint filter.
In at least another aspect, a laundry appliance includes a rotating drum for processing laundry. An airflow path is in communication with the rotating drum. A blower is positioned proximate the airflow path wherein the blower moves process air through the rotating drum and the airflow path for capturing moisture and particulate material from the laundry within the rotating drum. A lint separator is positioned within the airflow path that removes the particulate material from the process air to define captured particulate material. A lint disposal mechanism removes the captured particulate material from the lint separator.
In at least another aspect, a laundry appliance includes a drum for processing laundry. A blower delivers process air through an airflow path that includes the drum. The process air transports particulate material from the drum and into the airflow path. A lint separator is positioned within the airflow path that separates the particulate material from the process air. A lint disposal mechanism removes entrapped lint particles from the lint separator.
These and other features, advantages, and objects of the present device will be further understood and appreciated by those skilled in the art upon studying the following specification, claims, and appended drawings.
In the drawings:
For purposes of description herein the terms “upper,” “lower,” “right,” “left,” “rear,” “front,” “vertical,” “horizontal,” and derivatives thereof shall relate to the device as oriented in
With respect to
The lint disposal mechanism 28 is configured to operate continuously or substantially continuously throughout a particular drying cycle of the appliance 12. Through this continuous operation, the surface 44 of the lint filter 26 is allowed to remain substantially unobstructed by entrapped lint 32. Lint particles 30 that become entrapped within the lint filter 26 are removed by the lint disposal mechanism 28 shortly thereafter. Accordingly, portions of the lint filter 26 are continuously cleaned so that the process air 20 can move relatively freely through the lint filter 26 throughout the drying cycle. The continuous operation of the lint disposal mechanism 28 also provides for a maintenance-free lint removal system 10 of the appliance 12 that requires little, if any, customer intervention in the form of maintenance.
As exemplified in
As exemplified in
Referring again to
Studies related to the incinerating mechanism 40 have shown that the incinerating temperature 68 for incinerating lint particles 30 into the gas byproduct 42 can be approximately 900° C. This temperature can fluctuate depending upon the composition of the lint particles 30, the amount of entrapped lint 32 disposed on the lint filter 26, the speed at which the lint filter 26 operates with respect to the incinerating mechanism 40, and other considerations. The heater 60 causes a thermal degradation of the lint particles 30 that can be converted into the gas byproduct 42. The gas byproduct 42 may also include ash particles that typically have a greatly decreased mass with respect to the entrapped lint 32 that has been incinerated. After the gas byproduct 42 is formed through operation of the incinerating mechanism 40, the gas byproduct 42 can be vented away from the incinerating area 62 using natural thermodynamic venting that moves the gas byproduct 42 through a secondary air path 82. This thermodynamic venting can be a result of the hot gas byproduct 42 being drawn through the flue 84 and toward the lower temperature gas that is present at the end of the flue 84. In various aspects of the device, a secondary blower 80 may be incorporated within the lint disposal mechanism 28 as part of the secondary air path 82 that is adapted to move the gas byproduct 42 from an incinerating area 62 that houses the incinerating mechanism 40. The secondary air path 82 moves the gas byproduct 42 from the incinerating area 62 through an air outlet or flue 84 of the laundry appliance 12. Typically, the flue 84 will deliver the gas byproduct 42 to a separate area within the cabinet of the appliance 12. This gas byproduct 42 may then ultimately dissipate to areas outside of the appliance 12. Accordingly, operation of the thermodynamic venting, or, where applicable, the secondary blower 80, can conveniently move the gas byproduct 42 through the secondary air path 82 and through a separate portion of the appliance 12 or to areas outside of the appliance 12. Incorporation of the secondary air path 82 substantially prevents the gas byproduct 42 from entering into the primary airflow path 22 and the drum 16.
When the heater 60 is used as the incinerating mechanism 40, typically a small localized portion 52 of the lint filter 26 is exposed to the heater 60. Because very high temperatures are experienced within the incinerating area 62, the lint filter 26 is moved away from the incinerating area 62 so that the process air 20 can cool the heated localized portions 52 of the lint filter 26 after leaving the incinerating area 62. As discussed above, only a small portion of the lint filter 26 is typically exposed to the incinerating mechanism 40. Additionally, the lint filter 26 and the incinerating mechanism 40 typically operate at a relatively slow pace with respect to one another. During operation of the incinerating mechanism 40, the lint filter 26 is rotationally operable with respect to the incinerating mechanism 40, or vice versa. According to the various embodiments, the lint filter 26 can rotate at a speed of from approximately one revolution per minute to as slow as approximately 0.1 revolutions per minute (or one revolution every 10 minutes). Typically, the lint filter 26 or the incinerating mechanism 40 operates at a rate of approximately 1 revolution per minute or less. Other speeds of the lint filter 26 can also be used in conjunction with the incinerating mechanism 40. The speed ranges listed above are exemplary in nature. Faster or slower operating speeds can also be used for moving the lint filter 26 with respect to the incinerating mechanism 40. Alternating or varying speeds can be used to move the lint filter 26 in a wide range of conditions where varying amounts of entrapped lint 32 may be held within the surface 44 of the lint filter 26.
By way of example, and not limitation, during laundry cycles that may produce greater amounts of lint particles 30, the lint filter 26 may be operated at a faster speed so that the greater amounts of entrapped lint 32 can be processed by the incinerating mechanism 40. Slower speeds may also be used in instances of greater amounts of entrapped lint 32 so that the incinerating mechanism 40 has a greater amount of time to oxidize the entrapped lint 32 into the gas byproduct 42. In this manner, the surface 44 of the lint filter 26 can be maintained at a substantially unobstructed state 90. During laundry cycles where lesser amounts of lint particles 30 are typically generated, the lint filter 26 may operate at faster or slower speeds depending on the design of the appliance 12, the particular laundry cycle being performed and other considerations. One consistent speed of the lint filter 26 may be utilized during all laundry cycles.
Various aspects of the device can include an automatic and/or manual override that may cause the lint filter 26 to selectively and intermittently rotate at a faster speed in conditions where large amounts of entrapped lint 32 may be held within the surface 44 of the lint filter 26 in an unexpected laundry operating condition. Various sensors can be used in conjunction with a processor to indicate when large quantities of entrapped lint 32 are disposed on the surface 44 of the lint filter 26. In these atypical or unexpected conditions, the processor can cause the motor 50 to operate at a faster speed so that the entrapped lint 32 can be processed by the incinerating mechanism 40 and maintain the lint filter 26 in the substantially unobstructed state 90.
According to various aspects of the device, as exemplified in
Where the incinerating mechanism 40 is a heater 60, the heater 60 can take the form of a ceramic heating element that can be used to generate the incinerating temperatures 68 necessary for incinerating the entrapped lint 32 into the gas byproduct 42. Other electrically resistive heating elements can be used, as well as gas-based or gas-powered heating elements. The various types of heating elements are typically used for generating the incinerating temperature 68 within the incinerating area 62.
Typically, the lint filter 26 can be a stainless steel mesh that is positioned to separate the lint particles 30 from the processed air emanating from the drum 16. The lint disposal mechanism 28 can be located upstream of the blower 18 and consists of the incinerator housing 100 and includes the incinerating mechanism 40. Typically, the incinerating mechanism 40 takes the form of a heater 60 and can include one or more heating elements, such as ceramic heating elements. As discussed above, these heating elements can be used to heat the air within the incinerating area 62 to the appropriate incinerating temperature 68. The incinerating mechanism 40 is adapted to act on a relatively small and localized portion 52 of the lint filter 26. In this manner, the heat 102 generated by the heater 60 can be focused on the localized area of the lint filter 26 that is disposed within the incinerating area 62. By concentrating the heat 102 generated by the incinerating mechanism 40 at this localized area, power consumption can be minimized during use of the incinerating mechanism 40. Using these high temperatures also has the benefits of minimizing or preventing the production of smoke and also minimizing production of offensive solid byproducts. The use of the heater 60 also enables rapid degradation of the entrapped lint 32 from the surface 44 of the lint filter 26.
Referring again to
By heating air within the incinerating area 62 to these high temperatures, natural thermal draft may cause an updraft of the air within the incinerating area 62 to be directed through the flue 84 into a separate area of the appliance 12 or out of the appliance 12 altogether. This process may be performed with or without the assistance of the secondary blower 80. The updraft through the incinerating area 62 is also assisted through a combustion inlet 110 where combustion air 112 is directed from outside of the appliance 12. The temperature difference between the cooler combustion air 112 and the heated gas byproduct 42 creates a draft through the incinerating area 62. The dry airstream of cooler combustion air 112 can be used in this manner to move the gas byproduct 42 from the incinerating area 62 and through the flue 84. This combustion air 112 from the combustion inlet 110 can also be used to cool the areas of the lint screen 132 that have just been heated while moving through the incinerating area 62. Typically, the use of the cooler combustion air 112 will cool the localized area of the lint filter 26 to temperatures of approximately 100° C. According to various aspects of the device, this combustion air 112 can also be reclaimed and recirculated back into the incinerating area 62 or to another portion of the appliance 12 so that the heat 102 can be reused to warm other aspects of the appliance 12. In this manner, the reclaimed heat 102 can be used to increase the efficiency of the various heating mechanisms and air-conditioning mechanisms 24 of the appliance 12. By way of example, and not limitation, the heat 102 can be reused within the incinerating area 62 so that the incinerating mechanism 40 can efficiently operate using less electrical power or fuel. In various embodiments of the device, after the combustion air 112 cools the lint screen 132, this combustion air 112 may be preheated within the incinerating area 62. This preheated combustion air 112 can then be recirculated back to the localized area of the lint screen 132 being acted upon by the incinerating mechanism 40 within the incinerating area 62. This preheated combustion air 112 can also be used to heat the process air 20 within the airflow path 22. Various temperature sensors within the incinerating area 62 can cooperate with the heater 60 within the incinerating mechanism 40 to accurately operate the heater 60 to achieve the desired incinerating temperature 68 within the incinerating area 62. After the gas byproduct 42 is generated by the incinerating mechanism 40, the gas byproduct 42 can be directed by the combustion air 112 through the flue 84. A supplemental heater 120 can be disposed within the flue 84 to further decompose all undesirable solids and gasses that may be present within the gas byproduct 42 and the combustion air 112.
Referring again to
The incinerator housing 100 is typically made of a refractory material in areas where there is heat generated. By way of example, and not limitation, the incinerator housing 100 can be made from non-metallic materials that may have a low heat capacity to avoid absorbing and conducting the heat 102 generated by the incinerating mechanism 40. To further assist in the operation of the lint filter 26, a seal 140 can be disposed around the outer edge 142 of the lint filter 26. This outer edge 142 of the lint filter 26, near the seal 140, can include various indentations 144 that can cooperate with the flue 84 of the lint disposal mechanism 28. In such an embodiment, when a particular filtering section 146 of the lint filter 26 that is bound by adjacent ribs 130 is disposed within the incinerating area 62, the indentations 144 within the outer edge 142 of the lint filter 26 can form a portion of the secondary air path 82 that allows for movement of the combustion air 112 through the incinerating area 62 and up through the flue 84 of the lint disposal mechanism 28. As the lint filter 26 rotates, at least one of the indentations 144 is aligned within the secondary air path 82 to promote the flow of combustion air 112 and the gas byproduct 42 carried therein.
Typically, the rotation of the lint filter 26 can be operated through the use of a motor 50, such as a stepper motor, pulley-driven motor, direct drive motor, servo motor, and other similar motors. While rotational operation of the lint filter 26 is described, the lint filter 26 may also be configured for other directional movement with respect to the incinerating mechanism 40. Such movements of the lint filter 26 can be linear movements.
As exemplified in
In various aspects of the device, it is contemplated that the incinerating mechanism 40 can be moved with respect to the lint filter 26. In such an embodiment, the lint filter 26 may be stationary and the incinerating mechanism 40 can operate in a rotational or linear path within the airflow path 22. Typically, it is the lint filter 26 that will operate with respect to the lint disposal mechanism 28.
As exemplified in
Referring again to
In various aspects of the device, it is also contemplated that the individual electrodes 170 can be moved within the incinerating area 62. By way of example, and not limitation, the various electrodes 170 can be moved within the incinerating area 62 in a generally recirculating path to achieve the most complete coverage by the arcing electrical current 172 with respect to the surface 44 of the lint filter 26. The recirculating path can be in the form of a reciprocating linear motion, an elliptical motion, a generally arcuate motion, and other similar movements of the electrodes 170 within the incinerating area 62. In various aspects of the device, the electrodes 170 may also take the form of one or more bar electrodes 170, as well as other electrodes 170 having various shapes, sizes and configurations.
Where the incinerating mechanism 40 includes the plurality of electrodes 170, the housing can include the combustion inlet 110 that allows combustion air 112 from the exterior of the appliance 12 to move through the incinerating area 62 and up through the flue 84 of the lint disposal mechanism 28. Combustion air 112 serves to eliminate the various byproducts, including the gas byproducts 42, that are generated through the use of this incinerating mechanism 40 from the airflow path 22. Again, the flue 84 can include a supplemental heater 120 that can be used to decompose the gas byproducts 42, and other byproducts that may be present, into carbon dioxide or other similar non-nuisance gasses that can be responsibly directed back into the surrounding environment.
As exemplified in
In the various embodiments, the lint disposal mechanism 28 utilizing the plurality of electrodes 170, the lint filter 26 is typically a stainless steel mesh or other similar metallic mesh that can be used in conjunction with electrodes 170 to generate the arcing electrical current 172. The plurality of electrodes 170 are typically spaced relatively close to the surface 44 of the lint filter 26. In this manner, the arcing electrical current 172 can be conveniently generated between the electrodes 170 and the surface 44 of the lint filter 26. When the electrodes 170 generate arcing electrical current 172, lint particles 30 that are aligned beneath or adjacent to the electrodes 170 are incinerated or electrolyzed. By electrolyzing the entrapped lint particles 30, the arcing electrical current 172 serves to decompose these lint particles 30 into various byproducts that typically include gas byproducts 42. Again, these gas byproducts 42 can be further decomposed through the supplemental heater 120 that is disposed within the flue 84 of the lint disposal mechanism 28.
While the term gas byproduct 42 is used in the various embodiments to describe the remnants left of the lint particles 30 after being acted upon by the incinerating mechanism 40, various ash, and other ultra-fine particulate matter may also be generated as a byproduct. The byproducts generated during operation of the incinerating mechanism 40 are typically light enough that the combustion air 112 conveniently moves these byproducts along with the gas byproduct 42 from the incinerating area 62 and through the flue 84 of the lint disposal mechanisms 28. As discussed above, a supplemental heater 120 can be included within the flue 84 to further degrade the various byproducts.
Referring now to
As exemplified in
As exemplified in
The amount of compressive force 240 exerted by the compactor 212 can be a consistent compressive force 240 that can achieve the non-rebounding or substantially non-rebounding formation of the compressed lint pellet 218. This compressive force 240, based upon testing performed on various aspects of the lint disposal mechanism 28, has been shown to be from approximately 6.5 pounds per square inch to approximately 9.8 pounds per square inch to achieve the compressed lint pellets 218 using various compositions of lint. These compressive forces 240 can be used to achieve a density of the compressed lint pellet 218 that is from approximately 3 grams per cubic centimeter to approximately 9 grams per cubic centimeter. This range in density has been shown to achieve the non-rebounding or substantially non-rebounding configuration of the compressed lint pellets 218.
As exemplified in
According to various aspects of the device, the holding compartment 220 can be adapted to be a non-removable chamber that receives the formed compressed lint pellet 218 through the life of the appliance 12. Stated another way, the holding compartment 220 can be configured to not be emptied during the life of the appliance 12. According to various aspects of the device, the holding compartment 220 can also be configured to be periodically removed and emptied by a user of the appliance 12.
Where the compressed lint pellets 218 are disposed within a holding compartment 220 that is not removed but is added to over the life of the product, studies have shown that the size of the compressed lint pellets 218 that may be accumulated over approximately 5,000 drying cycles may require approximately 2,300 cubic centimeters of space. Larger or lesser amounts of space may be needed depending upon the amount of cycles and the nature of the lint being compressed into the compressed lint pellets 218. However, studies have shown that the amount of lint that may be accumulated over the life of the appliance 12 will typically not exceed a volume of approximately 7,500 cubic centimeters, which is approximately the size of twelve soda cans.
The various compactors 212 that can be used within the lint disposal mechanism 28 can take the form of an operable piston 260, rolling compactors, folding-type compactors, combinations thereof, and other similar compacting mechanisms. During the process of compacting the removed lint 216 into the compressed lint pellet 218, the removed lint 216 can be compressed in a dry state where no moisture is added to the removed lint 216. It is also contemplated that the removed lint 216 can be combined with various amounts of moisture to assist in compaction of removed lint 216 into the compressed lint pellets 218.
As exemplified in
In various aspects of the device, the cyclonic separator 230 can also take the form of a fluid spray that saturates various lint particles 30 entrapped within the process air 20. These saturated lint particles 30 can then be dropped into a compaction chamber for compression into the compressed lint pellets 218. The fluid spray can act as a lint filter 26 of the appliance 12 or can operate in conjunction with a separate lint filter 26.
According to various aspects of the device, the removed lint 216 disposed within the compacting chamber 214 as well as the compressed lint pellets 218 disposed within the holding compartment 220 can also be acted upon by at least one of the incinerating mechanisms 40 described herein. In such an embodiment, lint particles 30 can be placed into one of these separate compartments. Within this compartment, the compacting chamber 214 and/or the holding compartment 220, the incinerating mechanism 40 can be placed adjacent thereto so that the incinerating mechanism 40 can act upon the removed lint 216 to incinerate the removed lint 216 into the gas byproduct 42. In such an embodiment, the compacting chamber 214 and/or the holding compartment 220 can be configured as a separate and substantially heat-resistant compartment within which the incinerating temperatures 68 can be reached or the arcing electrical current 172 can be used to degrade the lint particles 30 into the gas byproduct 42. The flue 84 can also be coupled with the compacting chamber 214 or holding compartment 220 so that the gas byproduct 42 can be further degraded by the supplemental heater 120 and removed from the appliance 12.
According to various aspects of the device, the lint disposal mechanism 28 can be used within various appliances 12. Such appliances 12 can include, but are not limited to, heat pump dryers, exhaust dryers, combination washing/drying appliances, appliances that incorporate a heat pump system, appliances 12 that incorporate an air-to-air heat exchanger, refrigerating appliances, freezers, combinations thereof, and other similar appliances. It is also contemplated that various aspects of the lint disposal mechanism 28 can be included within air handling systems, such as air conditioners, furnaces, air filtration devices, air sanitizers, combinations thereof and other similar air-handling systems.
It will be understood by one having ordinary skill in the art that construction of the described device and other components is not limited to any specific material. Other exemplary embodiments of the device disclosed herein may be formed from a wide variety of materials, unless described otherwise herein.
For purposes of this disclosure, the term “coupled” (in all of its forms, couple, coupling, coupled, etc.) generally means the joining of two components (electrical or mechanical) directly or indirectly to one another. Such joining may be stationary in nature or movable in nature. Such joining may be achieved with the two components (electrical or mechanical) and any additional intermediate members being integrally formed as a single unitary body with one another or with the two components. Such joining may be permanent in nature or may be removable or releasable in nature unless otherwise stated.
It is also important to note that the construction and arrangement of the elements of the device as shown in the exemplary embodiments is illustrative only. Although only a few embodiments of the present innovations have been described in detail in this disclosure, those skilled in the art who review this disclosure will readily appreciate that many modifications are possible (e.g., variations in sizes, dimensions, structures, shapes and proportions of the various elements, values of parameters, mounting arrangements, use of materials, colors, orientations, etc.) without materially departing from the novel teachings and advantages of the subject matter recited. For example, elements shown as integrally formed may be constructed of multiple parts or elements shown as multiple parts may be integrally formed, the operation of the interfaces may be reversed or otherwise varied, the length or width of the structures and/or members or connector or other elements of the system may be varied, the nature or number of adjustment positions provided between the elements may be varied. It should be noted that the elements and/or assemblies of the system may be constructed from any of a wide variety of materials that provide sufficient strength or durability, in any of a wide variety of colors, textures, and combinations. Accordingly, all such modifications are intended to be included within the scope of the present innovations. Other substitutions, modifications, changes, and omissions may be made in the design, operating conditions, and arrangement of the desired and other exemplary embodiments without departing from the spirit of the present innovations.
It will be understood that any described processes or steps within described processes may be combined with other disclosed processes or steps to form structures within the scope of the present device. The exemplary structures and processes disclosed herein are for illustrative purposes and are not to be construed as limiting.
It is also to be understood that variations and modifications can be made on the aforementioned structures and methods without departing from the concepts of the present device, and further it is to be understood that such concepts are intended to be covered by the following claims unless these claims by their language expressly state otherwise.
The above description is considered that of the illustrated embodiments only. Modifications of the device will occur to those skilled in the art and to those who make or use the device. Therefore, it is understood that the embodiments shown in the drawings and described above is merely for illustrative purposes and not intended to limit the scope of the device, which is defined by the following claims as interpreted according to the principles of patent law, including the Doctrine of Equivalents.
This application claims priority to and the benefit under 35 U.S.C. § 119(e) of U.S. Provisional Patent Application No. 62/563,304, filed on Sep. 26, 2017, entitled LAUNDRY APPLIANCE HAVING A MAINTENANCE FREE LINT REMOVAL SYSTEM, the entire disclosure of which is hereby incorporated herein by reference.
Number | Date | Country | |
---|---|---|---|
62563304 | Sep 2017 | US |