Refrigerator appliance with water condensing features

Information

  • Patent Grant
  • 10451320
  • Patent Number
    10,451,320
  • Date Filed
    Thursday, May 25, 2017
    7 years ago
  • Date Issued
    Tuesday, October 22, 2019
    4 years ago
Abstract
A refrigerator appliance includes a cabinet that defines a chilled chamber. The cabinet has a duct with an inlet and an outlet. The inlet and outlet of the duct is contiguous with the chilled chamber of the cabinet such that air within the chilled chamber is flowable into the duct at the inlet of the duct and air within the duct is flowable into the chilled chamber at the outlet of the duct. A heat pump system is operable to cool the chilled chamber of the cabinet. The heat pump system includes a cold side heat exchanger in thermal communication with the air within the duct. The heat pump system also includes features for condensing water vapor from the air within the duct prior to the cold side heat exchanger.
Description
FIELD OF THE INVENTION

The present subject matter relates generally to heat pumps, such as magneto-caloric heat pumps, for refrigerator appliances.


BACKGROUND OF THE INVENTION

Conventional refrigeration technology typically utilizes a heat pump that relies on compression and expansion of a fluid refrigerant to receive and reject heat in a cyclic manner so as to effect a desired temperature change or transfer heat energy from one location to another. This cycle can be used to receive heat from a refrigeration compartment and reject such heat to the environment or a location that is external to the compartment. Other applications include air conditioning of residential or commercial structures. A variety of different fluid refrigerants have been developed that can be used with the heat pump in such systems.


While improvements have been made to such heat pump systems that rely on the compression of fluid refrigerant, at best such can still only operate at about forty-five percent or less of the maximum theoretical Carnot cycle efficiency. Also, some fluid refrigerants have been discontinued due to environmental concerns. The range of ambient temperatures over which certain refrigerant-based systems can operate may be impractical for certain locations. Other challenges with heat pumps that use a fluid refrigerant exist as well.


Magneto-caloric materials (MCMs), i.e. materials that exhibit the magneto-caloric effect, provide a potential alternative to fluid refrigerants for heat pump applications. In general, the magnetic moments of MCMs become more ordered under an increasing, externally applied magnetic field and cause the MCMs to generate heat. Conversely, decreasing the externally applied magnetic field allows the magnetic moments of the MCMs to become more disordered and allow the MCMs to absorb heat. Some MCMs exhibit the opposite behavior, i.e. generating heat when the magnetic field is removed (which are sometimes referred to as para-magneto-caloric material but both types are referred to collectively herein as magneto-caloric material or MCM). The theoretical Carnot cycle efficiency of a refrigeration cycle based on an MCMs can be significantly higher than for a comparable refrigeration cycle based on a fluid refrigerant. As such, a heat pump system that can effectively use an MCM would be useful.


Challenges exist to the practical and cost competitive use of an MCM, however. In addition to the development of suitable MCMs, equipment that can attractively utilize an MCM is still needed. Currently proposed equipment may require relatively large and expensive magnets, may be impractical for use in e.g., appliance refrigeration, and may not otherwise operate with enough efficiency to justify capital cost.


Accordingly, a heat pump system that can address certain challenges, such as those identified above, would be useful. Such a heat pump system that can also be used in a refrigerator appliance would also be useful.


BRIEF DESCRIPTION OF THE INVENTION

The present subject matter provides a refrigerator appliance with a cabinet that defines a chilled chamber. The cabinet has a duct with an inlet and an outlet. The inlet and outlet of the duct is contiguous with the chilled chamber of the cabinet such that air within the chilled chamber is flowable into the duct at the inlet of the duct and air within the duct is flowable into the chilled chamber at the outlet of the duct. A heat pump system is operable to cool the chilled chamber of the cabinet. The heat pump system includes a cold side heat exchanger in thermal communication with the air within the duct. The heat pump system also includes features for condensing water vapor from the air within the duct prior to the cold side heat exchanger. Additional aspects and advantages of the invention will be set forth in part in the following description, or may be apparent from the description, or may be learned through practice of the invention.


In a first exemplary embodiment, a refrigerator appliance includes a cabinet that defines a chilled chamber and a mechanical chamber. The cabinet has a duct with an inlet and an outlet. The inlet and outlet of the duct are contiguous with the chilled chamber of the cabinet such that air within the chilled chamber is flowable into the duct at the inlet of the duct and air within the duct is flowable into the chilled chamber at the outlet of the duct. The air within the duct is flowable along an air flow path between the inlet and the outlet of the duct. A heat pump system is operable to cool the chilled chamber of the cabinet. The heat pump system includes a cold side heat exchanger positioned in thermal communication with the air within the duct. A condensing heat exchanger is positioned in thermal communication with the air within the duct and also positioned upstream of the cold side heat exchanger on the air flow path. A hot side heat exchanger is positioned within the mechanical chamber of the cabinet. A caloric heat pump includes a caloric material. A working fluid is flowable between the caloric heat pump and one or more of the cold side heat exchanger and the condensing heat exchanger and between the caloric heat pump and the hot side heat exchanger. The condensing heat exchanger is chilled by the working fluid to a water condensing temperature during operation of the heat pump system. The water condensing temperature is greater than the freezing temperature of water. The cold side heat exchanger is chilled by the working fluid to a set temperature during operation of the heat pump system. The set temperature is less than the water condensing temperature.


In a second exemplary embodiment, a refrigerator appliance includes a cabinet that defines a chilled chamber. The cabinet has a duct with an inlet and an outlet. The inlet and outlet of the duct are contiguous with the chilled chamber of the cabinet such that air within the chilled chamber is flowable into the duct at the inlet of the duct and air within the duct is flowable into the chilled chamber at the outlet of the duct. The air within the duct flowable along an air flow path between the inlet and the outlet of the duct. A heat pump system is operable to cool the chilled chamber of the cabinet. The heat pump system includes a cold side heat exchanger positioned within the duct. A condensing heat exchanger is positioned within the duct upstream of the cold side heat exchanger on the air flow path. A caloric heat pump includes a caloric material. Working fluid is flowable between the caloric heat pump and one or more of the cold side heat exchanger and the condensing heat exchanger. The condensing heat exchanger is chilled by the working fluid to a water condensing temperature during operation of the heat pump system. The water condensing temperature is greater than the freezing temperature of water. The cold side heat exchanger is chilled by the working fluid to a set temperature during operation of the heat pump system. The set temperature is less than the water condensing temperature.


In a third exemplary embodiment, a refrigerator appliance includes a cabinet that defines a chilled chamber. The cabinet has a duct with an inlet and an outlet. The inlet and outlet of the duct is contiguous with the chilled chamber of the cabinet such that air within the chilled chamber is flowable into the duct at the inlet of the duct and air within the duct is flowable into the chilled chamber at the outlet of the duct. A heat pump system is operable to cool the chilled chamber of the cabinet. The heat pump system includes a cold side heat exchanger positioned within the duct. The heat pump system also includes means for condensing water vapor from the air within the duct prior to the air within the duct flowing over the cold side heat exchanger.


These and other features, aspects and advantages of the present invention will become better understood with reference to the following description and appended claims. The accompanying drawings, which are incorporated in and constitute a part of this specification, illustrate embodiments of the invention and, together with the description, serve to explain the principles of the invention.





BRIEF DESCRIPTION OF THE DRAWINGS

A full and enabling disclosure of the present invention, including the best mode thereof, directed to one of ordinary skill in the art, is set forth in the specification, which makes reference to the appended figures.



FIG. 1 is a refrigerator appliance in accordance with an exemplary embodiment of the present disclosure.



FIG. 2 is a schematic illustration of certain components of a heat pump system positioned in the exemplary refrigerator appliance of FIG. 1.



FIG. 3 is a schematic illustration of certain components of the heat pump system of FIG. 2, with a first stage of MCM within a magnetic field and a second stage of MCM out of a magnetic field, in accordance with an exemplary embodiment of the present disclosure.



FIG. 4 is a schematic illustration of certain components of the exemplary heat pump system of FIG. 2, with the first stage of MCM out of the magnetic field and the second stage of MCM within the magnetic field.



FIGS. 5 and 6 are schematic illustrations of certain components of the heat pump system of FIG. 2, in accordance with another exemplary embodiment of the present disclosure.



FIG. 7 provides a schematic view of an exemplary caloric heat pump according to another exemplary embodiment of the present subject matter.



FIG. 8 is a schematic diagram illustrating various positions and movements there-between of MCM stages in accordance with an exemplary embodiment of the present disclosure.



FIG. 9 provides a schematic view of certain components of the exemplary caloric heat pump of the heat pump system of FIG. 2.





DETAILED DESCRIPTION

Reference now will be made in detail to embodiments of the invention, one or more examples of which are illustrated in the drawings. Each example is provided by way of explanation of the invention, not limitation of the invention. In fact, it will be apparent to those skilled in the art that various modifications and variations can be made in the present invention without departing from the scope or spirit of the invention. For instance, features illustrated or described as part of one embodiment can be used with another embodiment to yield a still further embodiment. Thus, it is intended that the present invention covers such modifications and variations as come within the scope of the appended claims and their equivalents.


The present subject matter is directed to a caloric heat pump system for heating or cooling an appliance, such as a refrigerator appliance. While described in greater detail below in the context of a magneto-caloric heat pump system, one of skill in the art using the teachings herein will recognize that other suitable caloric materials may be used in a similar manner to heat or cool an appliance, i.e., apply a field, move heat, remove the field, move heat. For example, electro-caloric material heats up and cools down within increasing and decreasing electric fields. As another example, elasto-caloric material heats up and cools down when exposed to increasing and decreasing mechanical strain. As yet another example, baro-caloric material heats up and cools down when exposed to increasing and decreasing pressure. Such materials and other similar caloric materials may be used in place of or in addition to the magneto-caloric material described below to heat or cool liquid/water within an appliance. Thus, caloric material is used broadly herein to encompass materials that undergo heating or cooling when exposed to a changing field from a field generator, where the field generator may be a magnet, an electric field generator, an actuator for applying mechanical stress or pressure, etc.


Referring now to FIG. 1, an exemplary embodiment of a refrigerator appliance 10 is depicted as an upright refrigerator having a cabinet or casing 12 that defines a number of internal storage compartments or chilled chambers. In particular, refrigerator appliance 10 includes upper fresh-food compartments 14 having doors 16 and lower freezer compartment 18 having upper drawer 20 and lower drawer 22. Drawers 20, 22 are “pull-out” type drawers in that they can be manually moved into and out of freezer compartment 18 on suitable slide mechanisms. Refrigerator 10 is provided by way of example only. Other configurations for a refrigerator appliance may be used as well including appliances with only freezer compartments, only chilled compartments, or other combinations thereof different from that shown in FIG. 1. In addition, the heat pump and heat pump system of the present disclosure is not limited to refrigerator appliances and may be used in other applications as well such as e.g., air-conditioning, electronics cooling devices, and others. Thus, it should be understood that while the use of a heat pump and heat pump system to provide cooling within a refrigerator is provided by way of example herein, the present disclosure may also be used to provide for heating applications as well.



FIG. 2 is a schematic view of various components of refrigerator appliance 10, including refrigeration compartments 30 (e.g., fresh-food compartments 14 and freezer compartment 18) and a machinery compartment 40. Refrigeration compartment 30 and machinery compartment 40 include a heat pump system 52 having a first or cold side heat exchanger 32 positioned in refrigeration compartments 30 for the removal of heat therefrom. A heat transfer fluid such as e.g., an aqueous solution, flowing within cold side heat exchanger 32 receives heat from refrigeration compartment 30 thereby cooling contents of refrigeration compartment 30.


The heat transfer fluid flows out of cold side heat exchanger 32 by line 44 to heat pump 100. As will be further described herein, the heat transfer fluid receives additional heat from magneto-caloric material (MCM) in heat pump 100 and carries this heat by line 48 to a second or hot side heat exchanger 34. Heat is released to the environment, machinery compartment 40, and/or other location external to refrigeration compartment 30 using hot side heat exchanger 34. A fan 36 may be used to create a flow of air across hot side heat exchanger 34 and thereby improve the rate of heat transfer to the environment. A pump or pumps (not shown) cause the heat transfer fluid to recirculate in heat pump system 52. Motor 28 is in mechanical communication with heat pump 100 and is operable to provide relative motion between a field generator and a regenerator housing. From hot side heat exchanger 34, the heat transfer fluid returns by line 50 to heat pump 100 where, as will be further described below, the heat transfer fluid loses heat to the MCM in heat pump 100. The now colder heat transfer fluid flows by line 46 to cold side heat exchanger 32 to receive heat from refrigeration compartment 30 and repeat the cycle as just described.


Cold side heat exchanger 32 is configured for cooling refrigeration compartments 30, e.g., fresh-food compartment 14 and/or freezer chamber 18. For example, cold side heat exchanger 32 may be positioned at or adjacent fresh-food compartment 14, and air from cold side heat exchanger 32 may cool fresh-food compartment 14, as shown in FIG. 2. In alternative exemplary embodiments, cold side heat exchanger 32 may be positioned at or adjacent freezer compartment 18, and air from cold side heat exchanger 32 may cool freezer compartment 18. Cold side heat exchanger 32 may also be configured to cool both fresh-food compartment 14 and freezer compartment 18.


As may be seen in FIG. 2, refrigerator appliance 10 includes a duct 60. Duct 60 extends between an inlet 62 and an outlet 64. Inlet 62 and outlet 64 of duct 60 are contiguous or in fluid communication with refrigeration compartment 30. Thus, air within refrigeration compartment 30 is flowable into duct 60 at inlet 62 of duct 60. In turn, air within duct 60 is flowable into refrigeration compartment 30 at outlet 64 of duct 60. The air within duct 60 is flowable along an air flow path P between inlet 62 and outlet 64 of duct 60. Inlet 62 of duct 60 may be positioned above outlet 64 of duct 60. For example, inlet 62 of duct 60 may be positioned at or adjacent a top portion of refrigeration compartment 30 while outlet 64 of duct 60 may be positioned at or adjacent a bottom portion of refrigeration compartment 30. It will be understood that fresh-food compartments 14 and freezer compartment 18 may share a common duct or may have separate ducts in various exemplary embodiments.


Cold side heat exchanger 32 is positioned or disposed in thermal communication with the air within duct 60, e.g., within duct 60 along the air flow path P. Thus, the air within duct 60 flows through cold side heat exchanger 32 between inlet 62 and outlet 64 of duct 60 during operation of heat pump system 52. The air within duct 60 is cooled by cold side heat exchanger 32 and the working fluid within cold side heat exchanger 32, in the manner describe above, during operation of heat pump system 52.


Refrigerator appliance 10 also includes features for regulating air flow along the air flow path P and across cold side heat exchanger 32 to refrigeration compartment 30. As may be seen in FIG. 2, refrigerator appliance 10 includes a fan 66. Fan 66 may be positioned at or within duct 62. Fan 66 is operable to force air flow between refrigeration compartment 30 and duct 60. Fan 66 may thus be used to create a flow of air along the air flow path P across cold side heat exchanger 32 and thereby improve the rate of heat transfer.


As may be seen in FIG. 2, heat pump system 52 also has a third or condensing heat exchanger 33. Condensing heat exchanger 33 may be separate or spaced from cold side heat exchanger 32. Condensing heat exchanger 33 is positioned or disposed in thermal communication with the air within duct 60, e.g., within duct 60 along the air flow path P. In particular, condensing heat exchanger 33 may be positioned within duct 60 upstream of cold side heat exchanger 32 on the air flow path P. Thus, the air within duct 60 flows through condensing heat exchanger 33 prior to flowing through cold side heat exchanger 32 during operation of heat pump system 52. As discussed in greater detail below, condensing heat exchanger 33 is configured to condense water vapor from air within duct 60 onto condensing heat exchanger 33 prior to the air flowing to cold side heat exchanger 32.


Operation of heat pump system 52 and fan 66 allows chilled air from cold side heat exchanger 32 to cool refrigeration compartment 30 to a set temperature of refrigeration compartment 30. The set temperature of refrigeration compartment 30 may be any suitable temperature. For example, the set temperature of refrigeration compartment 30 may be about zero degrees Fahrenheit (0° F.) or about forty degrees Fahrenheit (40° F.), depending upon whether cold side heat exchanger 32 is used to cool fresh-food compartments 14 or freezer compartment 18. As used herein, the term “about” mean within ten degrees of the stated temperature when used in the context of temperatures. As may be seen from the above, the set temperature of refrigeration compartment 30 may be selected such that cold side heat exchanger 32 suitably cools refrigeration compartment 30.


To cool refrigeration compartment 30 to the set temperature of refrigeration compartment 30, the working fluid supplied to cold side heat exchanger 32 cools cold side heat exchanger 32 to a set temperature of cold side heat exchanger 32. The set temperature of cold side heat exchanger 32 is less than the set temperature of refrigeration compartment 30. For example, the set temperature of cold side heat exchanger 32 may be about negative ten degrees Fahrenheit (−10° F.) or about thirty degrees Fahrenheit (30° F.), depending upon whether cold side heat exchanger 32 is used to cool fresh-food compartments 14 or freezer compartment 18. The set temperature of cold side heat exchanger 32 is also less than the freezing temperature of water. Thus, water vapor may condense onto cold side heat exchanger 32 and form frost on cold side heat exchanger 32 during operation of heat pump system 52. Condensing heat exchanger 33 assists with reducing the volume of water that condenses onto cold side heat exchanger 32.


Condensing heat exchanger 33 is chilled by the working fluid to a water condensing temperature during operation of heat pump system 52. The water condensing temperature is greater than the set temperature of cold side heat exchanger 32. The water condensing temperature is selected such that water vapor in the air within duct 60 condenses onto condensing heat exchanger 33 during operation of heat pump system 52. Thus, condensing heat exchanger 33 condenses water vapor from air within duct 60 onto condensing heat exchanger 33 prior to the air flowing to cold side heat exchanger 32 in order to supply drier air to cold side heat exchanger 32 and reduce the volume of water that condenses onto cold side heat exchanger 32, e.g., relative to systems without condensing heat exchanger 33. In turn, condensing heat exchanger 33 may reduce necessary defrosting of cold side heat exchanger 32 relative to systems without condensing heat exchanger 33.


The water condensing temperature is greater than the freezing temperature of water. Thus, water does not freeze onto condensing heat exchanger 33 during operation of heat pump system 52, and condensing heat exchanger 33 does not require defrosting in certain exemplary embodiments. In particular, refrigerator appliance 10 may not include an electric defrost heating element on condensing heat exchanger 33. Thus, condensing heat exchanger 33 may efficiently remove water from air within duct 60.


Condensing heat exchanger 33 may be positioned below cold side heat exchanger 32 within duct 60. In addition, a drain pan 70 may be positioned below condensing heat exchanger 33. In particular, drain pan 70 may be positioned within duct 70 at a bottom portion of duct 60. Drain pan 70 is configured to receive condensed water vapor from condensing heat exchanger 33. Thus, as water vapor condenses on condensing heat exchanger 33, the condensed water vapor may flow downwardly and collect within drain pan 70. From drain pan 70, the condensed water vapor may flow to an evaporation pan (not shown) below hot side exchanger 34 within machinery compartment 40 or to an external drain line. Thus, the condensed water vapor may flow from drain pan 70 out of refrigerator appliance 10.


Condensing heat exchanger 33 may be plumbed in series or in parallel with cold side heat exchanger 32 in heat pump system 52. When heat pump system 52 is plumbed such that the working fluid is flowable in series through cold side heat exchanger 32 and condensing heat exchanger 33, lines 44, 46 may connect cold side heat exchanger 32 and condensing heat exchanger 33 such that the working fluid flows from heat pump 100 to cold side heat exchanger 32 and condensing heat exchanger 33 in series through line 46 and such that the working fluid flows from cold side heat exchanger 32 and condensing heat exchanger 33 in series to heat pump 100 to through line 44.


When cold side heat exchanger 32 and condensing heat exchanger 33 are plumbed in series, various components or properties of condensing heat exchanger 33 may be selected or configured such that condensing heat exchanger 33 is chilled by the working fluid to the water condensing temperature during operation of heat pump system 52. For example, a surface area of condensing heat exchanger 33, e.g., that is exposed to air within duct 60, may be selected such that condensing heat exchanger 33 is chilled by the working fluid to the water condensing temperature during operation of heat pump system 52. As another example, condensing heat exchanger 33 may include insulation that is configured such that condensing heat exchanger 33 is chilled by the working fluid to the water condensing temperature during operation of heat pump system 52. Thus, condensing heat exchanger 33 sized and/or insulated for operating at the water condensing temperature.


As discussed above, cold side heat exchanger 32 and condensing heat exchanger 33 may also be plumbed in parallel. When heat pump system 52 is plumbed such that the working fluid is flowable in parallel through cold side heat exchanger 32 and condensing heat exchanger 33, lines 44, 46 may connect cold side heat exchanger 32 and heat pump 100 such that the working fluid flows from heat pump 100 to cold side heat exchanger 32 through line 46 and such that the working fluid flows from cold side heat exchanger 32 to heat pump 100 to through line 44. Conversely, lines 96, 98 may connect condensing heat exchanger 33 and heat pump 100 such that the working fluid flows from heat pump 100 to condensing heat exchanger 33 through line 98 and such that the working fluid flows from condensing heat exchanger 33 to heat pump 100 to through line 96.


It will be understood that heat pump system 52 is provided by way of example only. Other configurations of heat pump system 52 may be used as well. For example, lines 44, 46, 48, 50, 96, 98 provide fluid communication between the various components of heat pump system 52 but other heat transfer fluid recirculation loops with different lines and connections may also be employed. Still other configurations of heat pump system 52 may be used as well.


Various heat pump configurations are available to flow working fluid to both cold side heat exchanger 32 and condensing heat exchanger 33 when heat exchangers 32, 33 are plumbed in parallel. Example configurations for plumbing cold side heat exchanger 32 and condensing heat exchanger 33 in parallel are discussed in greater detail below.



FIGS. 3 through 7 illustrate various exemplary heat pumps 100 and components thereof, and the use of such heat pumps 100 with heat pump system 52, in accordance with exemplary embodiments of the present disclosure. Heat pump 100 shown in FIGS. 3 through 6 may be suitable for use within a linear reciprocating caloric heat pump while heat pump 100 shown in FIG. 7 may be suitable for use within a rotatory caloric heat pump. Thus, it will be understood that the present subject matter may be used in or with any suitable heat pump, including linear caloric heat pumps and rotary caloric heat pumps, and the example heat pumps 100 provided herein are not intended to limit the present subject matter to any particular heat pump arrangement.


Referring now to heat pump 100 in FIGS. 3 and 4 and FIGS. 5 and 6, heat pump 100 may include a plurality of stages, each of which includes a magneto-caloric material (MCM). In exemplary embodiments, such MCM stages may be provided in pairs, each of which may for example include a first stage 130 and a second stage 132. Each stage 130, 132 may include one or more different types of MCM. Further, the MCM(s) provided in each stage 130, 132 may be the same or may be different. Stages 130, 132 may be disposed within a regenerator housing 140. Regenerator housing 140 along with stages 130, 132 and optional insulative materials may collectively be referred to as a regenerator assembly. As illustrated, in exemplary embodiments, regenerator housing 140 may include two stages 130, 132. Alternatively, three, four or more stages may be provided in regenerator housing 140. In particular, as shown in FIG. 7, heat pump 100 may include a plurality of first stages 130 within regenerator housing 140, e.g., eight first stages 130 uniformly distributed about a rotation axis of heat pump 100.


Each stage 130, 132 may extend between a first end 134 and a second end 136. As discussed herein, working fluid (also referred to herein as heat transfer fluid or fluid refrigerant) may flow through stages 130, 132 during operation of heat pump 100 generally between first and second ends 134, 136 of stages 130, 132. As discussed in greater detail below, heat pump 100 includes features for drawing-off or removing the working fluid from the stage 130, 132 at various locations along a transverse direction T.


Heat pumps 100 also includes one or more magnet assemblies (not shown), each of which creates a magnetic field M (FIG. 8), or other suitable field generators. The regenerator housing 140 and magnet assembly(s) may be movable relative to each other. In exemplary embodiments as shown, for example, regenerator housing 140 is movable relative to the magnet assembly. Alternatively, however, the magnet assembly may be movable relative to regenerator housing 140. Such relative movement between regenerator housing 140 and an associated magnet assembly causes movement of each stage 130, 132 into the magnetic field M and out of the magnetic field M. As discussed herein, movement of a stage 130, 132 into the magnetic field M may cause the magnetic moments of the material to orient and the MCM to heat (or alternatively cool) as part of the magneto-caloric effect. When one of stages 130, 132 is out of the magnetic field M, the MCM may thus cool (or alternatively heat) due to disorder of the magnetic moments of the material.


For example, referring to FIGS. 3 through 6, regenerator housing 140 may be movable linearly between a first position and a second position. In the first position, regenerator housing 140 may be positioned such that first stage 130 disposed within regenerator housing 140 is within the magnetic field M and second stage 132 disposed within regenerator housing 140 is out of the magnetic field M. Notably, being out of the magnetic field M means that second stage 132 is generally or substantially uninfluenced by the magnets and resulting magnetic field M. Accordingly, the MCM of the stage as a whole may not be actively heating (or cooling) as it would if within the magnetic field M (and instead may be actively or passively cooling (or heating) due to such removal of the magnetic field M). In the second position, regenerator housing 140 may be positioned such that first stage 130 disposed within regenerator housing 140 is out of the magnetic field M and second stage 132 disposed within regenerator housing 140 is within the magnetic field M. Similarly, with reference to FIG. 7, regenerator housing 140 may also be rotatable such that one portion of stages 130 are within the magnetic field M and the remainder of the stages 130 are out of the magnetic field M in the first position and vice versa in the second position. Movement of a regenerator housing 140 may be caused by operation of motor 26. Motor 26 may be in mechanical communication with regenerator housing 140 and configured for linearly or rotatably moving regenerator housing 140 or the magnet assemblies.


Referring also to FIG. 2, in some exemplary embodiments, lines 44, 46, 48, 50, 96, 98 may facilitate the flow of working fluid between heat exchangers 32, 33, 34 and heat pump 100. In exemplary embodiments, lines 44, 46, 48, 50, 96, 98 may facilitate the flow of working fluid between heat exchangers 32, 33, 34 and stages 130, 132 of heat pump 100. For example, a line 44 (e.g., a first cold side working fluid return conduit) may extend between cold side heat exchanger 32 and regenerator housing 140, such that working fluid from an outlet of heat exchanger 32 flows through line 44 to regenerator housing 140. A line 46 (e.g., a first cold side working fluid supply conduit) may extend between regenerator housing 140 and cold side heat exchanger 32, such that working fluid from regenerator housing 140 flows through line 46 to an inlet of heat exchanger 32. A line 50 (e.g., hot side working fluid return conduit) may extend between hot side heat exchanger 34 and regenerator housing 140, such that working fluid from an outlet of heat exchanger 34 flows through line 50 to regenerator housing 140. A line 48 (e.g., hot side working fluid supply conduit) may extend between regenerator housing 140 and hot side heat exchanger 34, such that working fluid from regenerator housing 140 flows through line 48 to an inlet of heat exchanger 34. A line 96 (e.g., a second cold side working fluid return conduit) may extend between condensing heat exchanger 33 and regenerator housing 140, such that working fluid from an outlet of heat exchanger 33 flows through line 96 to regenerator housing 140. A line 98 (e.g., second cold side working fluid supply conduit) may extend between regenerator housing 140 and an inlet of condensing heat exchanger 33, such that working fluid from regenerator housing 140 flows through line 98 to heat exchanger 33.


Notably, check valves 190 may in some exemplary embodiments be provided on the various lines 44, 46, 48, 50, 96, 98 to prevent backflow there-through. Exemplary positions and orientations of check valves 190 on lines 44, 46, 96, 98 are shown in FIGS. 3 through 6. Check valves 190, in combination with differential pressures during operation of heat pump 100, may thus generally prevent flow through the improper flow path when working fluid is being actively flowed through heat pump 100, e.g., such that working fluid flows through stages 130, 132 in the manner described below in the context of FIG. 8. In particular, with reference to the exemplary embodiment shown in FIGS. 3 and 4, check valves 190 are positioned on lines 44, 46, 96, 98 to provide the flow of working fluid shown with solid lines 44, 46, 96, 98 in FIG. 3 during the compression stroke of pump 170 and to conversely provide the flow of working fluid shown with solid lines 44, 46, 96, 98 in FIG. 4 during the compression stroke of pump 172. Heat pump system 52 may also include a restriction 192 on one of lines 44, 46, 96, 98. Restriction 192 may assist with balancing working fluid flow between cold side heat exchanger 32 and condensing heat exchanger 33.


Heat pump system 52 may also include at least one pump, such as pump 170 and/or pump 172, operable to flow the working fluid through lines 44, 46, 48, 50, 96, 98. With reference to FIGS. 3 through 6, first and second pumps 170, 172 may be synchronized such that one of first and second pumps 170, 172 is on a compression stroke while the other of first and second pumps 170, 172 is on a suction stroke. Such synchronization may assist with maintaining a constant volume of working fluid within heat pump system 52. For example, in FIGS. 3 and 5, first pump 170 is shown at a bottom dead center position while second pump 172 is shown at a top dead center position. Conversely, in FIGS. 4 and 6, first pump 170 is shown at the top center position while second pump 172 is shown at the bottom center position. Thus, first and second pumps 170, 172 may be synchronized to operate completely out of phase with one another. With reference to FIG. 7, first pump 170 may also operate continuously to flow working through first stages 130 during rotation of regenerator housing 140.



FIG. 8 illustrates an exemplary method of the present disclosure using a schematic representation of associated stages 130, 132 of MCM during dwelling in and movement between the various positions as discussed herein. With regard to first stage 130, during step 200, which corresponds to the first position, stage 130 is fully within magnetic field M, which causes the magnetic moments of the material to orient and the MCM to heat as part of the magneto caloric effect. Further, pump 170 is activated to actively flow working fluid. As indicated by arrow QH-OUT, working fluid in stage 130, now heated by the MCM, can travel out of stage 130 and along line 48 to hot side heat exchanger 34. At the same time, and as indicated by arrow QH-IN, working fluid from cold side heat exchanger 32 flows into stage 130 from line 44. Because working fluid from cold side heat exchanger 32 is relatively cooler than the MCM in stage 130, the MCM will lose heat to the working fluid.


In step 202, stage 130 is moved from the first position to the second position in the first transition. During the time in the first transition, working fluid dwells in the MCM of stage 130. More specifically, the working fluid does not actively flow through stage 130.


In step 204, stage 130 is in the second position and thus out of magnetic field M. The absence or lessening of the magnetic field is such that the magnetic moments of the material become disordered and the MCM absorbs heat as part of the magnetocaloric effect. Further, pump 172 is activated to actively flow working fluid. As indicated by arrow QC-OUT, working fluid in stage 130, now cooled by the MCM, can travel out of stage 130 and along line 46 to cold side heat exchanger 32. At the same time, and as indicated by arrow QC-IN, working fluid from hot side heat exchanger 34 flows into stage 112 from line 50 when stage 130 is in the second transition. Because working fluid from hot side heat exchanger 34 is relatively warmer than the MCM in stage 130, the MCM will gain some of its heat to the working fluid. The working fluid now travels along line 46 to cold side heat exchanger 32 to receive heat and cool refrigeration compartment 30.


In step 206, stage 130 is moved from the second position to the first position in the second transition. During the time in the second transition, the working fluid dwells in the MCM of stage 130. More specifically, the working fluid does not actively flow through stage 130.


With regard to second stage 132, during step 200, which corresponds to the first position, second stage 132 is out of magnetic field M. The absence or lessening of the magnetic field is such that the magnetic moments of the material become disordered and the MCM absorbs heat as part of the magneto-caloric effect. Further, pump 170 is activated to actively flow working fluid. As indicated by arrow QC-OUT, working fluid in stage 132, now cooled by the MCM, can travel out of stage 132 and along line 46 to cold side heat exchanger 32. At the same time, and as indicated by arrow QC-IN, working fluid from hot side heat exchanger 34 flows into stage 112 from line 50 when stage 132 is in the second transition. Because working fluid from hot side heat exchanger 34 is relatively warmer than the MCM in stage 132, the MCM will gain some of its heat to the working fluid. The working fluid now travels along line 46 to cold side heat exchanger 32 to receive heat and cool the refrigeration compartment 30.


In step 202, stage 132 is moved from the first position to the second position in the first transition. During the time in the first transition, the working fluid dwells in the MCM of stage 132. More specifically, the working fluid does not actively flow through stage 132.


In step 204, stage 132 is in the second position and thus fully within magnetic field M, which causes the magnetic moments of the material to orient and the MCM to heat as part of the magneto caloric effect. Further, pump 172 is activated to actively flow working fluid. As indicated by arrow QH-OUT, working fluid in stage 132, now heated by the MCM, can travel out of stage 132 and along line 48 to hot side heat exchanger 34. At the same time, and as indicated by arrow QH-IN, working fluid from cold side heat exchanger 32 flows into stage 132 from line 44. Because working fluid from cold side heat exchanger 32 is relatively cooler than the MCM in stage 132, the MCM will lose heat to the working fluid.


In step 206, stage 132 is moved from the second position to the first position in the second transition. During the time in the second transition, working fluid dwells in the MCM of stage 132. More specifically, the working fluid does not actively flow through stage 132. It will be understood that while described above in the context of cold side heat exchanger 32, condensing heat exchanger 33 may be configured and operate in the same or similar manner to cool freezer compartment 18 as described above for cold side heat exchanger 32 to cool fresh-food compartment 14 unless otherwise stated.



FIG. 9 provides a schematic view of certain components of heat pump 100 of heat pump system 52. As discussed in greater detail below, heat pump 100 includes features for drawing working fluid from regenerator housing 140 at a plurality of locations along a length H of first and second stages 130, 132. For example, the working fluid exits regenerator housing 140 at a first location along the length H of first stage 130 to cool condensing heat exchanger 33. Conversely, the working fluid exits regenerator housing 140 at a second location (different than the first location) along the length H of first stage 130 to cool cold side heat exchanger 32. While described in greater detail below in the context of first stage 130, it will be understood that regenerator housing 140 may be configured in a similar manner at second stage 132 to allow multiple working fluid draw location along a length of second stage 132.


As may be seen in FIG. 9, first stage 130 is disposed within regenerator housing 140. In particular, first stage 130 may have a length H along a longitudinal direction O, e.g., that is parallel to the transverse direction T, within regenerator housing 140. Working fluid is flowable through first stage 130 within regenerator housing 140. Regenerator housing 140 is also connected to condensing heat exchanger 33 such that working fluid is flowable from regenerator housing 140 to condensing heat exchanger 33. In particular, regenerator housing 140 includes a first cold side connection 150. Lines 96, 98 are connected to regenerator housing 140 at first cold side connection 150. Thus, working fluid is flowable from regenerator housing 140 to an inlet of condensing heat exchanger 33 via line 98 at first cold side connection 150 (also shown in FIGS. 3 through 6 during operation of pumps 170, 172 and in FIG. 7 during operation of pump 170), and working fluid is flowable from an outlet of condensing heat exchanger 33 to regenerator housing 140 via line 96 at first cold side connection 150. The flow of working fluid through lines 96, 98 within heat pump system 52 may also be seen in FIGS. 3 through 6 during operation of pumps 170, 172 and in FIG. 7 during operation of pump 170.


In addition, regenerator housing 140 is also connected to cold side heat exchanger 32 such that working fluid is flowable from regenerator housing 140 to cold side heat exchanger 32. In particular, regenerator housing 140 includes a second cold side connection 154. Lines 44, 46 are connected to regenerator housing 140 at second cold side connection 154. Thus, working fluid is flowable from regenerator housing 140 to an inlet of cold side heat exchanger 32 via line 46 at second cold side connection 154, and working fluid is flowable from an outlet of cold side heat exchanger 32 to regenerator housing 140 via line 44 at second cold side connection 154. Thus, lines 44, 46 may be in parallel with lines 96, 98. The flow of working fluid through lines 44, 46 within heat pump system 52 may also be seen in FIGS. 3 through 6 during operation of pumps 170, 172 and in FIG. 7 during operation of pump 170.


Regenerator housing 140 is also connected to hot side heat exchanger 34 such that working fluid is flowable between regenerator housing 140 and hot side heat exchanger 34. In particular, regenerator housing 140 has a hot side connection 152. Lines 48, 50 are connected to regenerator housing 140 at hot side connection 152. Thus, working fluid is flowable from regenerator housing 140 to an inlet of hot side heat exchanger 34 via line 48 at hot side connection 152, and working fluid is flowable from an outlet of hot side heat exchanger 34 to regenerator housing 140 via line 50 at hot side connection 152. The flow of working fluid through lines 48, 50 within heat pump system 52 may also be seen in FIGS. 3 through 6 during operation of pumps 170, 172 and in FIG. 7 during operation of pump 170.


Hot side connection 152 is spaced from first and second cold side connections 150, 154 on regenerator housing 140, e.g., along the longitudinal direction O. For example, hot side connection 152 may be positioned at first end portion 144 of regenerator housing 140, and second cold side connection 154 may be positioned at second end portion 146 of regenerator housing 140. First cold side connection 150 may be positioned between hot side connection 152 and second cold side connection 154, e.g., along the longitudinal direction O. By spacing first and second cold side connections 150, 154 on regenerator housing 140, first cold side connection 150 may draw working fluid from regenerator housing 140 at a different location along the length H of first stage 130 relative to second cold side connection 154. In particular, the working fluid exits regenerator housing 140 at the first cold side connection 150 to cool condensing heat exchanger 33 to the set temperature of condensing heat exchanger 33, and the working fluid exits regenerator housing 140 at the second cold side connection 154 to cool cold side heat exchanger 32 to the set temperature of cold side heat exchanger 32.


First cold side connection 150 is closer to hot side connection 152 than second cold side connection 154, e.g., along the longitudinal direction O. Thus, the working fluid may flow through less of the length H of first stage 130 to first cold side connection 150 compared to second cold side connection 154. In such a manner cooling of the working fluid by first stage 130 may be regulated. In particular, first stage 130 may reduce the temperature of the working fluid more when the working fluid exits regenerator housing 140 at second cold side connection 154 compared to when the working fluid exits regenerator housing 140 at first cold side connection 150. It will be understood that additional cold side connections may be positioned at any other suitable location in alternative exemplary embodiments. The multiple cold side connections on regenerator housing 140 allows working fluid to be pulled-off at multiple locations when cooling the cold side heat exchanger 32 and condensing heat exchanger 33. By pulling the working fluid from one of the cold side connections, each heat exchanger 32, 33 may be cooled to a respective set temperature.


This written description uses examples to disclose the invention, including the best mode, and also to enable any person skilled in the art to practice the invention, including making and using any devices or systems and performing any incorporated methods. The patentable scope of the invention is defined by the claims, and may include other examples that occur to those skilled in the art. Such other examples are intended to be within the scope of the claims if they include structural elements that do not differ from the literal language of the claims, or if they include equivalent structural elements with insubstantial differences from the literal languages of the claims.

Claims
  • 1. A refrigerator appliance, comprising: a cabinet defining a chilled chamber and a mechanical chamber, the cabinet having a duct with an inlet and an outlet, the inlet and outlet of the duct contiguous with the chilled chamber of the cabinet such that air within the chilled chamber is flowable into the duct at the inlet of the duct and air within the duct is flowable into the chilled chamber at the outlet of the duct, the air within the duct flowable along an air flow path between the inlet and the outlet of the duct;a heat pump system operable to cool the chilled chamber of the cabinet, the heat pump system comprising a cold side heat exchanger in thermal communication with the air within the duct;a condensing heat exchanger positioned in thermal communication with the air within the duct and also positioned upstream of the cold side heat exchanger on the air flow path;a hot side heat exchanger positioned within the mechanical chamber of the cabinet;a caloric heat pump comprising a caloric material disposed within a regenerator housing, working fluid flowable between the caloric heat pump and one or more of the cold side heat exchanger and the condensing heat exchanger and between the caloric heat pump and the hot side heat exchanger, the regenerator housing between a first end portion and a second end portion,wherein the condensing heat exchanger is chilled by the working fluid to a water condensing temperature during operation of the heat pump system, the water condensing temperature being greater than the freezing temperature of water,wherein the cold side heat exchanger is chilled by the working fluid to a set temperature during operation of the heat pump system, the set temperature being less than the water condensing temperature,wherein the heat pump system is plumbed such that the working fluid is flowable in parallel through the cold side heat exchanger and the condensing heat exchanger,wherein the caloric heat pump has a first outlet connected to the cold side heat exchanger, a second outlet connected to the condensing heat exchanger, and a third outlet connected to the hot side heat exchanger, andwherein the third outlet is positioned on the regenerator housing at the first end portion of the regenerator housing, the first outlet is positioned on the regenerator housing at the second end portion of the regenerator housing, and the second outlet is positioned on the re the first and second end portions of the regenerator housing.
  • 2. The refrigerator appliance of claim 1, wherein the water condensing temperature is selected such that water vapor in the air within the duct condenses onto the condensing heat exchanger.
  • 3. The refrigerator appliance of claim 1, further comprising a drain pan positioned below the condensing heat exchanger such that condensed water vapor on the condensing heat exchanger is flowable into the drain pan.
  • 4. The refrigerator appliance of claim 3, wherein the cold side heat exchanger is positioned above the condensing heat exchanger within the duct.
  • 5. The refrigerator appliance of claim 1, wherein the cold side heat exchanger is spaced from the condensing heat exchanger within the duct.
  • 6. The refrigerator appliance of claim 1, wherein the heat pump system does not include an electric defrost heating element on the condensing heat exchanger.
  • 7. The refrigerator appliance of claim 1, wherein the second outlet is positioned closer to the first outlet on the regenerator housing than the second outlet is positioned relative to the third outlet.
  • 8. A refrigerator appliance, comprising: a cabinet defining a chilled chamber, the cabinet having a duct with an inlet and an outlet, the inlet and outlet of the duct contiguous with the chilled chamber of the cabinet such that air within the chilled chamber is flowable into the duct at the inlet of the duct and air within the duct is flowable into the chilled chamber at the outlet of the duct, the air within the duct flowable along an air flow path between the inlet and the outlet of the duct;a heat pump system operable to cool the chilled chamber of the cabinet, the heat pump system comprising a cold side heat exchanger positioned within the duct;a condensing heat exchanger positioned within the duct upstream of the cold side heat exchanger on the air flow path;a caloric heat pump comprising a caloric material disposed within a regenerator housing, working fluid flowable between the caloric heat pump and one or more of the cold side heat exchanger and the condensing heat exchanger, the regenerator housing between a first end portion and a second end portion,wherein the condensing heat exchanger is chilled by the working fluid to a water condensing temperature during operation of the heat pump system, the water condensing temperature being greater than the freezing temperature of water, and wherein the cold side heat exchanger is chilled by the working fluid to a set temperature during operation of the heat pump system, the set temperature being less than the water condensing temperature,wherein the heat pump system is plumbed such that the working fluid is flowable in parallel through the cold side heat exchanger and the condensing heat exchanger,wherein the caloric heat pump has a first outlet connected to the cold side heat exchanger, a second outlet connected to the condensing heat exchanger, and a third outlet connected to a hot side heat exchanger, andwherein the third outlet is positioned on the regenerator housing at the first end portion of the regenerator housing, the first outlet is positioned on the regenerator housing at the second end portion of the regenerator housing, and the second outlet is positioned on the regenerator housing between the first and second end portions of the regenerator housing.
  • 9. The refrigerator appliance of claim 8, wherein the water condensing temperature is selected such that water vapor in the air within the duct condenses onto the condensing heat exchanger.
  • 10. The refrigerator appliance of claim 8, further comprising a drain pan positioned below the condensing heat exchanger such that condensed water vapor on the condensing heat exchanger is flowable into the drain pan.
  • 11. The refrigerator appliance of claim 8, wherein the cold side heat exchanger is positioned above the condensing heat exchanger within the duct, the cold side heat exchanger also spaced from the condensing heat exchanger within the duct.
  • 12. The refrigerator appliance of claim 8, wherein the heat pump system does not include an electric defrost heating element on the condensing heat exchanger.
  • 13. The refrigerator appliance of claim 8, wherein the second outlet is positioned closer to the first outlet on the regenerator housing than the second outlet is positioned relative to the third outlet.
US Referenced Citations (235)
Number Name Date Kind
668560 Fulner et al. Feb 1901 A
1985455 Mosby Dec 1934 A
2671929 Gayler Mar 1954 A
2765633 Muffly Oct 1956 A
3816029 Bowen et al. Jun 1974 A
3956076 Powell, Jr. et al. May 1976 A
4037427 Kramer Jul 1977 A
4102655 Jeffery et al. Jul 1978 A
4107935 Steyert, Jr. Aug 1978 A
4197709 Hochstein Apr 1980 A
4200680 Sasazawa et al. Apr 1980 A
4259843 Kausch Apr 1981 A
4507927 Barclay Apr 1985 A
4507928 Johnson Apr 1985 A
4549155 Halbach Oct 1985 A
4554790 Nakagome et al. Nov 1985 A
4557228 Samodovitz Dec 1985 A
4599866 Nakagome et al. Jul 1986 A
4625519 Hakuraku et al. Dec 1986 A
4642994 Barclay et al. Feb 1987 A
4735062 Woolley et al. Apr 1988 A
4741175 Schulze May 1988 A
4785636 Hakuraku et al. Nov 1988 A
4796430 Malaker et al. Jan 1989 A
5091361 Hed Feb 1992 A
5156003 Yoshiro et al. Oct 1992 A
5249424 DeGregoria et al. Oct 1993 A
5336421 Kurita et al. Aug 1994 A
5351791 Rosenzweig Oct 1994 A
5465781 DeGregoria Nov 1995 A
5599177 Hetherington Feb 1997 A
5661895 Irgens Sep 1997 A
5718570 Beckett et al. Feb 1998 A
5934078 Lawton, Jr. et al. Aug 1999 A
6332323 Reid et al. Dec 2001 B1
6423255 Hoechsmann et al. Jul 2002 B1
6446441 Dean Sep 2002 B1
6467274 Barclay Oct 2002 B2
6526759 Zimm et al. Mar 2003 B2
6588215 Ghoshal Jul 2003 B1
6612816 Vanden Brande et al. Sep 2003 B1
6668560 Zimm et al. Dec 2003 B2
6826915 Wada et al. Dec 2004 B2
6915647 Tsuchikawa et al. Jul 2005 B2
6935121 Fang et al. Aug 2005 B2
6946941 Chell Sep 2005 B2
6971245 Kuroyanagi Dec 2005 B2
7148777 Chell et al. Dec 2006 B2
7297270 Bernard et al. Nov 2007 B2
7313926 Gurin Jan 2008 B2
7481064 Kitanovski et al. Jan 2009 B2
7552592 Iwasaki et al. Jun 2009 B2
7644588 Shin et al. Jan 2010 B2
7863789 Zepp et al. Jan 2011 B2
7897898 Muller et al. Mar 2011 B2
7938632 Smith May 2011 B2
8061147 Dinesen et al. Nov 2011 B2
8069662 Albert Dec 2011 B1
8099964 Saito et al. Jan 2012 B2
8174245 Carver May 2012 B2
8191375 Sari et al. Jun 2012 B2
8209988 Zhang Jul 2012 B2
8216396 Dooley et al. Jul 2012 B2
8310325 Zhang et al. Nov 2012 B2
8375727 Sohn Feb 2013 B2
8378769 Heitzler et al. Feb 2013 B2
8448453 Bahl et al. May 2013 B2
8551210 Reppel et al. Oct 2013 B2
8596084 Herrera et al. Dec 2013 B2
8616009 Dinesen et al. Dec 2013 B2
8656725 Muller et al. Feb 2014 B2
8695354 Heitzler et al. Apr 2014 B2
8729718 Kuo et al. May 2014 B2
8763407 Carroll et al. Jul 2014 B2
8769966 Heitzler et al. Jul 2014 B2
8869541 Heitzler et al. Oct 2014 B2
8904806 Cramet et al. Dec 2014 B2
8935927 Kobayashi et al. Jan 2015 B2
8978391 Muller et al. Mar 2015 B2
9175885 Katter Nov 2015 B2
9245673 Carroll et al. Jan 2016 B2
9377221 Benedict Jun 2016 B2
9400126 Takahashi et al. Jul 2016 B2
9523519 Muller Dec 2016 B2
9534817 Benedict et al. Jan 2017 B2
9548151 Muller Jan 2017 B2
9599374 Takahashi et al. Mar 2017 B2
9631843 Benedict Apr 2017 B2
9702594 Vetrovec Jul 2017 B2
9739510 Hassen Aug 2017 B2
9797630 Benedict et al. Oct 2017 B2
9810454 Tasaki et al. Nov 2017 B2
9857105 Schroeder et al. Jan 2018 B1
9857106 Schroeder et al. Jan 2018 B1
9927155 Boeder et al. Mar 2018 B2
9978487 Katter et al. May 2018 B2
10006675 Benedict et al. Jun 2018 B2
10018385 Radermacher et al. Jul 2018 B2
20020040583 Barclay et al. Apr 2002 A1
20020066368 Zornes Jun 2002 A1
20030010054 Esch et al. Jan 2003 A1
20030051774 Saito Mar 2003 A1
20040093877 Wada May 2004 A1
20040182086 Chiang et al. Sep 2004 A1
20040187510 Jung Sep 2004 A1
20040187803 Regev Sep 2004 A1
20040250550 Bruck Dec 2004 A1
20050109490 Harmon et al. May 2005 A1
20050274676 Kumar et al. Dec 2005 A1
20060130518 Kang Jun 2006 A1
20060231163 Hirosawa et al. Oct 2006 A1
20070130960 Muller et al. Jun 2007 A1
20070220901 Kobayashi Sep 2007 A1
20080236171 Saito et al. Oct 2008 A1
20080236175 Chaparro Monferrer et al. Oct 2008 A1
20080303375 Carver Dec 2008 A1
20090091411 Zhang et al. Apr 2009 A1
20090158749 Sandeman Jun 2009 A1
20090217674 Kaji et al. Sep 2009 A1
20090236930 Nashiki Sep 2009 A1
20090266083 Shin et al. Oct 2009 A1
20090308080 Han et al. Dec 2009 A1
20100000228 Wiest et al. Jan 2010 A1
20100058775 Kaji et al. Mar 2010 A1
20100071383 Zhang et al. Mar 2010 A1
20100116471 Reppel May 2010 A1
20100122488 Fukai May 2010 A1
20100162747 Hamel et al. Jul 2010 A1
20100209084 Nelson et al. Aug 2010 A1
20100236258 Heitzler et al. Sep 2010 A1
20100276627 Mazet Nov 2010 A1
20100303917 Watson et al. Dec 2010 A1
20110000206 Aprad Jan 2011 A1
20110042608 Reesink Feb 2011 A1
20110048031 Barve Mar 2011 A1
20110048690 Reppel et al. Mar 2011 A1
20110058795 Kleman et al. Mar 2011 A1
20110061398 Shih et al. Mar 2011 A1
20110062821 Chang et al. Mar 2011 A1
20110082026 Sakatani et al. Apr 2011 A1
20110162388 Barve et al. Jul 2011 A1
20110168363 Reppel et al. Jul 2011 A9
20110173993 Muller et al. Jul 2011 A1
20110182086 Mienko et al. Jul 2011 A1
20110192836 Muller et al. Aug 2011 A1
20110218921 Addala et al. Sep 2011 A1
20110239662 Bahl et al. Oct 2011 A1
20110284196 Zanadi Nov 2011 A1
20110302931 Sohn Dec 2011 A1
20110308258 Smith et al. Dec 2011 A1
20110314836 Heitzler et al. Dec 2011 A1
20120031108 Kobayashi et al. Feb 2012 A1
20120033002 Seeler et al. Feb 2012 A1
20120036868 Heitzler et al. Feb 2012 A1
20120045698 Shima Feb 2012 A1
20120060526 May et al. Mar 2012 A1
20120079834 Dinesen Apr 2012 A1
20120222427 Hassen Sep 2012 A1
20120222428 Celik et al. Sep 2012 A1
20120266591 Morimoto et al. Oct 2012 A1
20120266607 Morimoto et al. Oct 2012 A1
20120267090 Kruglick Oct 2012 A1
20120272665 Watanabe et al. Nov 2012 A1
20120272666 Watanabe Nov 2012 A1
20120285179 Morimoto Nov 2012 A1
20120291453 Watanabe et al. Nov 2012 A1
20130019610 Zimm et al. Jan 2013 A1
20130020529 Chang et al. Jan 2013 A1
20130104568 Kuo et al. May 2013 A1
20130106116 Kuo et al. May 2013 A1
20130145573 Bizhanzadeh Jun 2013 A1
20130180263 Choi et al. Jul 2013 A1
20130186107 Shih et al. Jul 2013 A1
20130187077 Katter Jul 2013 A1
20130192269 Wang Aug 2013 A1
20130199460 Duplessis et al. Aug 2013 A1
20130227965 Yagi et al. Sep 2013 A1
20130232993 Saito et al. Sep 2013 A1
20130255279 Tomimatsu et al. Oct 2013 A1
20130269367 Meillan Oct 2013 A1
20130298571 Morimoto et al. Nov 2013 A1
20130300243 Gieras et al. Nov 2013 A1
20130319012 Kuo et al. Dec 2013 A1
20130327062 Watanabe et al. Dec 2013 A1
20140020881 Reppel et al. Jan 2014 A1
20140075958 Takahashi et al. Mar 2014 A1
20140116538 Tanaka et al. May 2014 A1
20140165594 Benedict Jun 2014 A1
20140165595 Zimm et al. Jun 2014 A1
20140190182 Benedict Jul 2014 A1
20140216057 Oezcan Aug 2014 A1
20140260373 Gerber et al. Sep 2014 A1
20140290273 Benedict et al. Oct 2014 A1
20140290275 Muller Oct 2014 A1
20140291570 Klausner et al. Oct 2014 A1
20140305137 Benedict Oct 2014 A1
20140305139 Takahashi et al. Oct 2014 A1
20140325996 Muller Nov 2014 A1
20140366557 Mun et al. Dec 2014 A1
20150007582 Kim et al. Jan 2015 A1
20150027133 Benedict Jan 2015 A1
20150030483 Ryu Jan 2015 A1
20150033762 Cheng et al. Feb 2015 A1
20150033763 Saito et al. Feb 2015 A1
20150047371 Hu et al. Feb 2015 A1
20150068219 Komorowski et al. Mar 2015 A1
20150089960 Takahashi et al. Apr 2015 A1
20150114007 Neilson et al. Apr 2015 A1
20150168030 Leonard et al. Jun 2015 A1
20150211440 Joffroy Jul 2015 A1
20150260433 Choi et al. Sep 2015 A1
20150267943 Kim et al. Sep 2015 A1
20150362225 Schwartz Dec 2015 A1
20150369524 Ikegami et al. Dec 2015 A1
20160000999 Focht et al. Jan 2016 A1
20160084544 Radermacher et al. Mar 2016 A1
20160091227 Leonard et al. Mar 2016 A1
20160216012 Benedict et al. Jul 2016 A1
20160238287 Benedict Aug 2016 A1
20160273811 Smith et al. Sep 2016 A1
20160282021 Zhao et al. Sep 2016 A1
20160355898 Vieyra Villegas et al. Dec 2016 A1
20160356529 Humburg Dec 2016 A1
20160367982 Pennie Dec 2016 A1
20170059213 Barclay et al. Mar 2017 A1
20170071234 Garg Mar 2017 A1
20170138648 Cui et al. May 2017 A1
20170176083 Sul Jun 2017 A1
20170328603 Barclay et al. Nov 2017 A1
20170328649 Brandmeier Nov 2017 A1
20170370624 Zimm et al. Dec 2017 A1
20180005735 Scharf et al. Jan 2018 A1
20180023852 Schroeder et al. Jan 2018 A1
20180195775 Schroeder et al. Jul 2018 A1
20180283740 Holladay et al. Oct 2018 A1
Foreign Referenced Citations (50)
Number Date Country
2893874 Jun 2014 CA
2919117 Jan 2015 CA
101979937 Feb 2011 CN
201772566 Mar 2011 CN
101788207 Sep 2011 CN
202432596 Sep 2012 CN
103090583 May 2013 CN
103712401 Apr 2014 CN
102077303 Apr 2015 CN
106481842 Mar 2017 CN
102013223959 May 2015 DE
202015106851 Mar 2016 DE
0187078 Jul 1986 EP
2071255 Jun 2009 EP
2108904 Oct 2009 EP
2215955 Aug 2010 EP
2322072 May 2011 EP
3306082 Apr 2018 EP
2935468 Mar 2010 FR
59232922 Dec 1984 JP
H08166182 Jun 1996 JP
3205196 Sep 2001 JP
2002315243 Oct 2002 JP
2007147136 Jun 2007 JP
2007291437 Nov 2007 JP
2008051412 Mar 2008 JP
2010112606 May 2010 JP
2010525291 Jul 2010 JP
6212955 Dec 2014 JP
2014228216 Dec 2014 JP
5907023 Apr 2016 JP
6079498 Feb 2017 JP
6191539 Sep 2017 JP
2017207222 Nov 2017 JP
101100301 Dec 2011 KR
1238234 Mar 2013 KR
WO 0212800 Feb 2002 WO
WO 03016794 Feb 2003 WO
WO 2004068512 Aug 2004 WO
WO 2007036729 Apr 2007 WO
WO 2009024412 Feb 2009 WO
WO2010119591 Oct 2010 WO
WO 2011034594 Mar 2011 WO
WO 2014099199 Jun 2014 WO
WO 2014170447 Oct 2014 WO
WO 2014173787 Oct 2014 WO
WO 2015017230 Feb 2015 WO
WO2016035267 Mar 2016 WO
WO 2017042266 Mar 2017 WO
WO2017097989 Jun 2017 WO
Non-Patent Literature Citations (13)
Entry
C Aprea, et al., An innovative rotary permanent magnet magnetic refrigerator based on AMR cycle, Thermal Energy Systems: Production, Storage, Utilization and the Environment, dated May 2015, Napoli, Italy, pp. 1-5.
International Search Report issued in connection with PCT Application No. PCT/US2014/042485 dated Oct. 23, 2014.
International Search Report issued in connection with PCT Application No. PCT/US2014/017431 dated May 9, 2014.
International search report issued in connection with PCT/US2013/070518, dated Jan. 22, 2014.
Tetsuji Okamura, Performance of a room-temperature rotary magnet refrigerator, dated Nov. 28, 2005, Elsevier.
Journal of Alloys and Compounds, copyright 2008 Elsevier B.. V.
Evaluation of Ni—Mn—In—Si Alloys for Magnetic Refrigerant Application, Rahul Das, A. Perumal and A. Srinivasan, Dept of Physics, Indian Institute of Technology, Oct. 10, 2011.
Effects of annealing on the magnetic entropy change and exchange bias behavior in melt-spun Ni—Mn—In ribbons, X.Z. Zhao, C.C. Hsieh, et al Science Direct, Scripta Materialia 63 (2010).
PCT International Search Report and Written Opinion issued in connection with PCT Application No. PCT/US2013/070023 dated Feb. 27, 2014.
Barbara Pulko, Epoxy-bonded La—Fe—Co—Si magnetocaloric plates, Journal of Magnetism and Magnetic Materials, 375 (2015) 65-73.
International Search Report of PCT/US2014/047925 dated Nov. 10, 2014.
Andrej Kitanovski, Present and future caloric refrigeration and heat-pump technologies, International Journal of Refrigeration, vol. 57 Sep. 2015, pp. 288-298.
Stefano Dall'Olio, et al., Numerical Simulation of a Tapered Bed AMR, Technical University of Denmark, 2015, 2 pages.
Related Publications (1)
Number Date Country
20180340715 A1 Nov 2018 US