Refrigeration system including thermoelectric module

Information

  • Patent Grant
  • 7310953
  • Patent Number
    7,310,953
  • Date Filed
    Wednesday, November 9, 2005
    19 years ago
  • Date Issued
    Tuesday, December 25, 2007
    17 years ago
Abstract
A refrigeration system for multi-temperature and single-temperature applications combines a refrigeration circuit and a single-phase fluid heat-transfer circuit in heat-conducting contact through a thermoelectric device. A vapor compression cycle provides a first stage of cooling and the thermoelectric device in conjunction with the heat-transfer circuit provides the second stage of cooling. Polarity of the thermoelectric device can be reversed to provide a defrost function for the refrigeration system.
Description
FIELD

The present teachings relate to refrigeration systems and, more particularly, to refrigeration systems that include a thermoelectric module.


BACKGROUND

Refrigeration systems incorporating a vapor compression cycle can be utilized for single-temperature applications, such as a freezer or refrigerator having one or more compartments that are to be maintained at a similar temperature, and for multi-temperature applications, such as refrigerators having multiple compartments that are to be kept at differing temperatures, such as a lower temperature (freezer) compartment and a medium or higher temperature (fresh food storage) compartment.


The vapor compression cycle utilizes a compressor to compress a working fluid (e.g., refrigerant) along with a condenser, an evaporator and an expansion device. For multi-temperature applications, the compressor is typically sized to run at the lowest operating temperature for the lower temperature compartment. As such, the compressor is typically sized larger than needed, resulting in reduced efficiency. Additionally, the larger compressor may operate at a higher internal temperature such that an auxiliary cooling system for the lubricant within the compressor may be needed to prevent the compressor from burning out.


To address the above concerns, refrigeration systems may use multiple compressors along with the same or different working fluids. The use of multiple compressors and/or multiple working fluids, however, may increase the cost and/or complexity of the refrigeration system and may not be justified based upon the overall efficiency gains.


Additionally, in some applications, the compressor and/or refrigerant that can be used may be limited based on the temperature that is to be achieved. For example, with an open drive shaft compressor, the seal along the drive shaft is utilized to maintain the working fluid within the compressor. When a working fluid, such as R134A, is utilized with an open drive shaft sealed compressor, the minimum temperature that can be achieved without causing leaks past the drive shaft seal is limited. That is, if too low a temperature were attempted to be achieved, a vacuum may develop such that ambient air may be pulled into the interior of the compressor and contaminate the system. To avoid this, other types of compressors and/or working fluids may be required. These other types of compressors and/or working fluids, however, may be more expensive and/or less efficient.


Additionally, the refrigeration systems may require a defrost cycle to thaw out any ice that has accumulated or formed on the evaporator. Traditional defrost systems utilize an electrically powered radiant heat source that is selectively operated to heat the evaporator and melt the ice that is formed thereon. Radiant heat sources, however, are inefficient and, as a result, increase the cost of operating the refrigeration system and add to the complexity. Hot gas from the compressor may also be used to defrost the evaporator. Such systems, however, require additional plumbing and controllers and, as a result, increase the cost and complexity of the refrigeration system.


SUMMARY

A refrigeration system may be used to meet the temperature/load demands of both multi-temperature and single-temperature applications. The refrigeration system may include a vapor compression (refrigeration) circuit and a liquid heat-transfer circuit in heat-transferring relation with one another through one or more thermoelectric devices. The refrigeration system may stage the cooling with the vapor compression circuit providing a second stage of cooling and the thermoelectric device in conjunction with the heat-transfer circuit providing the first stage of cooling. The staging may reduce the load imparted on a single compressor and, thus, allows a smaller, more efficient compressor to be used. Additionally, the reduced load on the compressor may allow a greater choice in the type of compressor and/or refrigerant utilized. Moreover, the operation of the thermoelectric device may be reversed to provide a defrost function.


First and second sides of a thermoelectric device may be in heat-transferring relation with a compressible working fluid flowing through a refrigeration circuit and a heat-transfer fluid flowing through a heat-transfer circuit, respectively. The thermoelectric device forms a temperature gradient between the compressible working fluid and heat-transfer fluid, which allows heat to be extracted from one of the compressible working fluid and the heat-transfer fluid and transferred to the other through the thermoelectric device.


The refrigeration system may include a thermoelectric device in heat-transferring relation with a heat-transfer circuit and a vapor compression circuit. The heat-transfer circuit may transfer heat between a heat-transfer fluid flowing therethrough and a first refrigerated space. The vapor compression circuit may transfer heat between a refrigerant flowing therethrough and an airflow. The thermoelectric device transfers heat between the heat-transfer fluid and the refrigerant.


Methods of operating refrigeration systems having a vapor compression circuit, a heat-transfer circuit and a thermoelectric device include transferring heat between a heat-transfer fluid flowing through the heat-transfer circuit and a first side of the thermoelectric device and transferring heat between a refrigerant flowing through the vapor compression circuit and a second side of the thermoelectric device.


Further, the refrigeration system may be operated in a cooling mode including transferring heat from the heat-transfer circuit to the thermoelectric device and transferring heat from the thermoelectric device to the refrigeration circuit. Also, the refrigeration system may be operated in a defrost mode including transferring heat through the thermoelectric device to the heat-transfer circuit and defrosting the heat exchanger with a heat-transfer fluid flowing through the heat-transfer circuit. The refrigeration system may be operated by selectively switching between the cooling mode and the defrost mode.


A method of conditioning a space with a refrigeration system includes forming a first heat sink for a first side of a thermoelectric device with a vapor compression cycle and forming a second heat sink for a heat-transfer fluid flow with a second side of the thermoelectric device. Heat may be transferred from the heat-transfer fluid flow to a refrigerant in the vapor compression cycle through the thermoelectric device to thereby condition the space.


Further areas of applicability of the present teachings will become apparent from the detailed description provided hereinafter. It should be understood that the detailed description and specific examples are intended for purposes of illustration only and are not intended to limit the scope of the teachings.





BRIEF DESCRIPTION OF THE DRAWINGS

The present teachings will become more fully understood from the detailed description and the accompanying drawings, wherein:



FIG. 1 is a schematic diagram of a refrigeration system according to the present teachings;



FIG. 2 is a schematic diagram of a refrigeration system according to the present teachings;



FIG. 3 is a schematic diagram of a refrigeration system according to the present teachings;



FIG. 4 is a schematic diagram of the refrigeration system of FIG. 3 operating in a defrost mode; and



FIG. 5 is a schematic diagram of a refrigeration system according to the present teachings.





DETAILED DESCRIPTION

The following description is merely exemplary in nature and is in no way intended to limit the teachings, their application, or uses. In describing the various teachings herein, reference indicia are used. Like reference indicia are used for like elements. For example, if an element is identified as 10 in one of the teachings, a like element in subsequent teachings may be identified as 110, 210, etc. As used herein, the term “heat-transferring relation” refers to a relationship that allows heat to be transferred from one medium to another medium and includes convection, conduction and radiant heat transfer.


Referring now to FIG. 1, a refrigeration system 20 is a multi-temperature system having a first compartment or refrigerated space (hereinafter compartment) 22 designed to be maintained at a first temperature and a second compartment or refrigerated space (hereinafter compartment) 24 designed to be maintained at a lower temperature than the first compartment 22. For example, refrigeration system 20 can be a commercial or residential refrigerator with first compartment 22 being a medium-temperature compartment designed for fresh food storage while second compartment 24 is a low-temperature compartment designed for frozen food storage. Refrigeration system 20 is a hybrid or combination system which uses a vapor compression cycle or circuit (VCC) 26, a thermoelectric module (TEM) 28 and a heat-transfer circuit 29 to cool compartments 22, 24 and maintain a desired temperature therein. TEM 28 and heat-transfer circuit 29 maintain second compartment 24 at the desired temperature while VCC 26 maintains first compartment 22 at the desired temperature and absorbs the waste heat from TEM 28. VCC 26, TEM 28 and heat-transfer circuit 29 are sized to meet the heat loads of first and second compartments 22, 24.


TEM 28 includes one or more thermoelectric elements or devices 30 in conjunction with heat exchangers to remove heat from the heat-transfer fluid flowing through heat-transfer circuit 29 and direct the heat into the refrigerant flowing through VCC 26. The thermoelectric devices 30 are connected to a power supply 32 that selectively applies DC current (power) to each thermoelectric device 30. Thermoelectric devices 30 convert electrical energy from power supply 32 into a temperature gradient, known as the Peltier effect, between opposing sides of each thermoelectric device 30. Thermoelectric devices can be acquired from various suppliers. For example, Kryotherm USA of Carson City, Nev. is a source for thermoelectric devices. Power supply 32 may vary or modulate the current flow to thermoelectric devices 30.


The current flow through the thermoelectric devices 30 results in each thermoelectric device 30 having a relatively lower temperature or cold side 34 and a relatively higher temperature or hot side 36 (hereinafter referred to as cold side and hot side). It should be appreciated that the terms “cold side” and “hot side” may refer to specific sides, surfaces or areas of the thermoelectric devices. Cold side 34 is in heat-transferring relation with heat-transfer circuit 29 while hot side 36 is in heat-transferring relation with VCC 26 to transfer heat from heat-transfer circuit 29 to VCC 26.


Cold side 34 of thermoelectric device 30 is in heat-transferring relation with a heat exchange element 38 and forms part of heat-transfer circuit 29. Heat-transfer circuit 29 includes a fluid pump 42, heat exchanger 44 and TEM 28 (thermoelectric device 30 and heat exchange element 38). A heat-transfer fluid flows through the components of heat-transfer circuit 29 to remove heat from second compartment 24. Heat-transfer circuit 29 may be a single-phase fluid circuit in that the heat-transfer fluid flowing therethrough remains in the same phase throughout the circuit. A variety of single-phase fluids may be used within heat transfer circuit 29. By way of non-limiting example, the single-phase fluid may be potassium formate or other types of secondary heat transfer fluids, such as those available from Environmental Process Systems Limited of Cambridgeshire, UK and sold under the Tyfo® brand, and the like.


Pump 42 pumps the heat-transfer fluid through the components of heat-transfer circuit 29. The heat-transfer fluid flowing through heat exchange element 38 is cooled therein via the thermal contact with cold side 34 of thermoelectric device 30. Heat exchange element 38 functions to facilitate thermal contact between the heat-transfer fluid flowing through heat-transfer circuit 29 and the cold side 34 of thermoelectric device 30. The heat-transfer may be facilitated by increasing the heat-transferring surface area that is in contact with the heat-transfer fluid. One type of heat exchange element 38 that may possibly accomplish this includes micro-channel tubing that is in thermal contact with cold side 34 of each thermoelectric device 30 and having channels through which the heat-transfer fluid flows. The thermal contact with cold side 34 lowers the temperature, by way of non-limiting example to −25° F., of the heat-transfer fluid flowing through heat exchange element 38 by extracting heat therefrom. The heat-transfer fluid exits heat exchange element 38 and flows through pump 42.


From pump 42, the heat transfer fluid flows through heat exchanger 44 at an initial ideal temperature of −25° F., by way of non-limiting example. A fan 48 circulates air within second compartment 24 over evaporator 44. Heat Q1 is extracted from the heat load and transferred to the heat-transfer fluid flowing through heat exchanger 44. The heat-transfer fluid exits heat exchanger 44 and flows through heat exchange element 38 to discharge the heat Q1, extracted from the air flow that flows through second compartment 24, to VCC 26.


Heat flows through thermoelectric devices 30 from cold side 34 to hot side 36. To facilitate the removal of heat from hot side 36 TEM 28 includes another heat exchange element 60 in thermal contact with hot side 36 of each thermoelectric device 30. Heat exchange element 60 forms part of VCC 26 and moves the heat extracted from the air flow that flows through second compartment 24 into the refrigerant flowing therethrough. Heat exchange element 60 can take a variety of forms. Heat exchange element 60 functions to facilitate heat-transfer between hot side 36 of thermoelectric devices 30 and the refrigerant flowing through VCC 26. Increasing the thermally conductive surface area in contact with the refrigerant flowing through heat exchange element 60 facilitates the transfer of heat therebetween. One possible form of heat exchange element 60 that may accomplish this includes a micro-channel tubing that is in thermal contact with hot side 36 of each thermoelectric device 30. The thermal contact increases the temperature of the refrigerant flowing through heat exchange element 60.


Power supply 32 is operated to provide a current through thermoelectric devices 30 in order to maintain a desired temperature gradient, such as by way of non-limiting example ΔT=45° F., across thermoelectric devices 30. The electric current flowing through thermoelectric devices 30 generates heat therein (i.e., Joule heat). Therefore, the total heat Q2 to be transferred by thermoelectric devices 30 into the refrigerant flowing through heat exchange element 60 is the sum of the Joule heat plus the heat being extracted from the heat-transfer fluid through cold side 34 (the heat Q1 extracted from the air flow that flows through second compartment 24).


VCC 26 includes a compressor 62, a condenser 64, an evaporator 66 and first and second expansion devices 68, 70, along with heat exchange element 60. These components of VCC 26 are included in a refrigeration circuit 72. A refrigerant, such as by way of non-limiting example R134A or R404A, flows through refrigeration circuit 72 and the components of VCC 26 to remove heat from first compartment 22 and from TEM 28. The specific type of compressor 62 and refrigerant used may vary based on the application and the demands thereof.


Compressor 62 compresses the refrigerant supplied to condenser 64, which is disposed outside of first compartment 22. A fan 74 blows ambient air across condenser 64 to extract heat Q4 from the refrigerant flowing through condenser 64, whereby the refrigerant exiting condenser 64 has a lower temperature than the refrigerant entering condenser 64. A portion of the refrigerant flows from condenser 64 to evaporator 66 and the remaining refrigerant flows to heat exchange element 60. First expansion device 68 controls the quantity of refrigerant flowing through evaporator 66, while second expansion device 70 controls the quantity of refrigerant flowing through heat exchange element 60. Expansion devices 68, 70 can take a variety of forms. By way of non-limiting example, expansion devices 68, 70 can be thermostatic expansion valves, capillary tubes, micro valves, and the like.


A fan 78 circulates air within first compartment 22 over evaporator 66. Evaporator 66 extracts heat Q3 from the air flow and transfers the heat Q3 to the refrigerant flowing therethrough. The temperature of the refrigerant exiting evaporator 66 may be, by way of non-limiting example, 20° F.


The refrigerant flowing through heat exchange element 60 extracts the heat Q2 from thermoelectric devices 30 and facilitates maintaining of hot side 36 of thermoelectric devices 30 at a desired temperature, such as by way of non-limiting example 20° F. The refrigerant flowing through heat exchange element 60 ideally exits at the same temperature as hot side 36.


Refrigerant exiting evaporator 66 and heat exchange element 60 flow back into compressor 62. The refrigerant then flows through compressor 62 and begins the cycle again. Evaporator 66 and heat exchange element 60 may be configured, arranged and controlled to operate at approximately the same temperature, such as by way of non-limiting example 20° F. That is, the refrigerant flowing therethrough would exit the evaporator 66 and heat exchange element 60 at approximately the same temperature. As such, expansion devices 68, 70 adjust the flow of refrigerant therethrough to correspond to the demands placed upon evaporator 66 and heat exchange element 60. Thus, such an arrangement provides simple control of the refrigerant flowing through VCC 26.


First and second expansion devices 68, 70 may also be replaced with a single expansion device which is located within circuit 72 upstream of where the refrigerant flow is separated to provide refrigerant flow to evaporator 66 and heat exchange element 60. Additionally, expansion devices 68, 70 may be controlled in unison or separately, as desired, to provide desired refrigerant flows through evaporator 66 and heat exchange element 60.


Referring now to FIG. 2, a refrigeration system 120 is shown similar to refrigeration system 20, but including an evaporator 166 designed to be operated at a higher-temperature, such as by way of non-limiting example 45° F., and does not operate at a temperature generally similar to heat exchange element 160. A pressure regulating device 184 may be disposed downstream of evaporator 166 at a location prior to the refrigerant flowing therethrough joining with the refrigerant flowing through heat exchange element 160. Pressure regulating device 184 controls the refrigerant pressure immediately downstream of evaporator 166. Pressure regulating device 184 may be operated to create a pressure differential across the coils of evaporator 166, thereby allowing evaporator 166 to be operated at a temperature different than that of heat exchange element 60. By way of non-limiting example, heat exchange element 60 may be operated at 20° F. while evaporator 166 is operated at 45° F. Pressure regulating device 184 also provides a downstream pressure generally similar to that of the refrigerant exiting heat exchange element 60, and compressor 162 still receives refrigerant at a generally similar temperature and pressure.


In sum, VCC 126 includes an evaporator 166 and heat exchange element 160 that are operated in parallel and at different temperatures. Thus, in refrigeration system 120, a single compressor serves multiple temperature loads (heat exchange element 160 and evaporator 166).


The use of both a vapor compression cycle along with a thermoelectric device or module and heat-transfer circuit 29 capitalizes on the strengths and benefits of each while reducing the weaknesses associated with systems that are either entirely vapor compression cycle systems or entirely thermoelectric module systems. That is, by using a thermoelectric module with heat-transfer circuit 29 to provide the temperature for a particular compartment, a more efficient refrigeration system can be obtained with thermoelectric modules that have a lower level of efficiency (ZT). For example, in a multi-temperature application system that relies entirely upon thermoelectric modules, a higher ZT value is required than when used in a system in conjunction with a vapor compression cycle. With the use of a vapor compression cycle, a thermoelectric module with a lower ZT can be utilized while providing an overall system that has a desired efficiency. Additionally, such systems may be more cost effective than the use of thermoelectric modules only.


Thus, the use of a system incorporating both a vapor compression cycle, thermoelectric modules and a heat-transfer circuit to provide a refrigeration system for multi-temperature applications may be advantageously employed over existing systems. Additionally, the use of a thermoelectric module is advantageous in that they are compact, solid state, have an extremely long life span, a very quick response time, do not require lubrication and have a reduced noise output over a vapor compression cycle. Moreover, the use of thermoelectric modules for portions of the refrigeration system also eliminates some of the vacuum issues associated with the use of particular types of compressors for low temperature refrigeration. Accordingly, the refrigeration system utilizing a vapor compression cycle, thermoelectric modules and a heat-transfer circuit may be employed to meet the demands of a multi-temperature application.


Referring now to FIG. 3, a refrigeration system 220 is used for a single-temperature application. Refrigeration system 220 utilizes a vapor compression cycle 226 in conjunction with a thermoelectric module 228 and heat-transfer circuit 229 to maintain a compartment or refrigerated space (hereinafter compartment) 286 at a desired temperature. By way of non-limiting example, compartment 286 can be a low-temperature compartment that operates at −25° F. or can be a cryogenic compartment that operates at −60° F.


Refrigeration system 220 stages the heat removal from compartment 286. A first stage of heat removal is performed by heat-transfer circuit 229 and TEM 228. The second stage of heat removal is performed by VCC 226 in conjunction with TEM 228. Heat-transfer circuit 229 utilizes a heat-transfer fluid that flows through heat exchange element 238, which is in heat conductive contact with cold side 234 of thermoelectric devices 230. Fluid pump 242 causes the heat-transfer fluid to flow through heat-transfer circuit 229.


Heat-transfer fluid leaving heat exchange element 238 is cooled (has heat removed) by the heat-transferring relation with cold side 234 of thermoelectric devices 230. The cooled heat-transfer fluid flows through pump 242 and into heat exchanger 244. Fan 248 causes air within compartment 286 to flow across heat exchanger 244. Heat exchanger 244 extracts heat Q201 from the air flow and transfers it to the heat-transfer fluid flowing therethrough. The heat-transfer fluid then flows back into heat exchange element 238 wherein the heat Q201 is extracted from the heat-transfer fluid by TEM 228.


DC current is selectively supplied to TEM 228 by power supply 232. The current flow causes thermoelectric devices 230 within TEM 228 to produce a temperature gradient between cold side 234 and hot side 236. The temperature gradient facilitates the transferring of heat from the heat-transfer fluid flowing through heat-transfer circuit 229 into the refrigerant flowing through VCC 226. Heat Q202 flows from heat exchange element 260 into the refrigerant flowing therethrough. Heat Q202 includes the heat extracted from the heat-transfer fluid flowing through heat exchange element 238 along with the Joule heat produced within thermoelectric devices 230.


The refrigerant exiting heat exchange element 260 flows through compressor 262 and on to condenser 264. Fan 274 provides a flow of ambient air across condenser 264 to facilitate the removal of heat Q204 from the refrigerant flowing therethrough. The refrigerant exiting condenser 264 flows through an expansion device 270 and then back into heat exchange element 260. VCC 226 thereby extracts heat Q202 from TEM 228 and expels heat Q204 to the ambient environment.


Compressor 262 and expansion device 270 are sized to meet the heat removal needs of TEM 228. The power supplied to thermoelectric devices 230 by power supply 232 is modulated to maintain a desired temperature gradient between hot and cold sides 236, 234. Pump 242 can vary the flow rate of the heat-transfer fluid flowing therethrough to provide the desired heat removal from compartment 286.


With this configuration, refrigeration system 220 allows compressor 262 to be smaller than that required in a single-stage refrigeration system. Additionally, by staging the heat removal, compressor 262 and the refrigerant flowing therethrough can be operated at a higher temperature than that required with a single stage operation, which enables the use of a greater variety of compressors and/or different refrigerants. Additionally, the higher temperature enables a more efficient vapor compression cycle to be utilized while still achieving the desired low temperature within compartment 286 through the use of TEM 228 and heat-transfer circuit 229. The enhanced efficiency is even more pronounced in cryogenic applications, such as when compartment 286 is maintained at a cryogenic temperature, such as −60° F.


Staging also avoids some of the overheating issues associated with using a single-stage refrigeration system and a compressor sized to meet that cooling load. For example, to meet the cooling load with a single-stage vapor compression cycle, the compressor may need to be run at a relatively high temperature that might otherwise cook the compressor or cause the lubricant therein to break down. The use of TEM 228 and heat-transfer circuit 229 avoids these potential problems by allowing compressor 262 to be sized to maintain a relatively high temperature and then meeting a relatively low-temperature cooling load through the use of TEM 228 and heat-transfer circuit 229. The use of a smaller compressor 262 may also increase the efficiency of the compressor and, thus, of VCC 226.


Referring now to FIG. 4, refrigeration system 220 is shown operating in a defrost mode, which allows defrosting of heat exchanger 244 without the use of a radiant electrical heating element or a hot gas defrost. Additionally, the system facilitates the defrosting by allowing the elevated temperature of heat exchanger 244 to be achieved quickly and efficiently.


To defrost heat exchanger 244, VCC 226 is operated so that heat exchange element 260 is operated at a relatively higher temperature, such as 30° F. The polarity of the current being supplied to thermoelectric devices 230 is reversed so that the hot and cold sides 234, 236 are reversed from that shown during the normal (cooling) operation (FIG. 3). With the polarity reversed, heat flow Q205 will travel from heat exchange element 260 toward heat exchange element 238 and enter into the heat transfer fluid flowing through heat exchange element 238. The power supplied to thermoelectric devices 30 can be modulated to minimize the temperature gradient across thermoelectric devices 230. For example, the power supply can be modulated to provide a 10° F. temperature gradient between cold side 234 and hot side 236.


The heated heat transfer fluid exiting heat exchange element 238 flows through fluid pump 242 and into heat exchanger 244. Fan 248 is turned off during the defrost cycle. The relatively warm heat transfer fluid flowing through heat exchanger 244 warms heat exchanger 244 and melts or defrosts any ice buildup on heat exchanger 244. By not operating fan 248, the impact of the defrost cycle on the temperature of the food or products being stored within compartment 286 is minimized. The heat transfer fluid exits heat exchanger 244 and flows back into heat exchange element 238 to again be warmed up and further defrost heat exchanger 244.


Thus, refrigeration system 220 may be operated in a normal mode to maintain compartment 286 at a desired temperature and operated in a defrost mode to defrost the heat exchanger associated with compartment 286. The system advantageously uses a combination of a vapor compression cycle along with a thermoelectric module and heat-transfer circuit to perform both operating modes without the need for radiant electrical heat or other heat sources to perform a defrosting operation.


Referring now to FIG. 5, a refrigeration system 320 is shown similar to refrigeration system 20. In refrigeration system 320, there is no heat transfer circuit to cool second compartment 324. Rather, heat exchange element 338 is in the form of fins and fan 348 circulates air within second compartment 324 across the fins of heat exchange element 338. Heat Q301 is extracted from the air flow and transferred to thermoelectric device 330. VCC 326 includes a single mid-temperature evaporator 390 that is in heat-transferring relation with hot side 336 of thermoelectric devices 330. In other words, evaporator 390 functions as the hot side heat exchange element of TEM 328.


Power supply 332 is operated to provide a current through thermoelectric devices 330 in order to maintain a desired temperature gradient, such as by way of non-limiting example ΔT=45° F., across thermoelectric devices 330. Electric current flowing through thermoelectric devices 330 generates heat therein (i.e., Joule heat). Therefore, the total heat Q302 transferred by thermoelectric devices 330 into the refrigerant flowing through evaporator 390 is the sum of the Joule heat plus the heat Q301 being extracted from the air flow flowing across heat exchange element 338. The heat-transferring relation between thermoelectric devices 330 and evaporator 390 allows heat Q302 to be transferred to the working fluid flowing through evaporator 390. Evaporator 390 is also in heat-transferring relation with an air flow circulated thereacross and through first compartment 322 by fan 378. Heat Q306 is transferred from the air flow to the working fluid flowing through evaporator 390 to condition first compartment 322.


Heat Q304 is transferred from the working fluid flowing through VCC 326 to the air flow circulated by fan 374 across condenser 364. Thus, in refrigeration system 320, TEM 328 directly extracts heat Q301 from the air circulating through second compartment 324 and transfers that heat to the working fluid flowing through evaporator 390 which is in heat-transferring relation with hot side 336. Evaporator 390 also serves to extract heat from the air circulating through first compartment 322.


While the present teachings have been described with reference to the drawings and examples, changes may be made without deviating from the spirit and scope of the present teachings. For example, a liquid suction heat exchanger (not shown) can be employed between the refrigerant flowing into the compressor and the refrigerant exiting the condenser to exchange heat between the liquid cooling side and the vapor superheating side. Moreover, it should be appreciated that the compressors utilized in the refrigeration system shown can be of a variety of types. For example, the compressors can be either internally or externally driven compressors and may include rotary compressors, screw compressors, centrifugal compressors, orbital scroll compressors and the like. Furthermore, while the condensers and evaporators are described as being coil units, it should be appreciated that other types of evaporators and condensers can be employed. Additionally, while the present teachings have been described with reference to specific temperatures, it should be appreciated these temperatures are provided as non-limiting examples of the capabilities of the refrigeration systems. Accordingly, the temperatures of the various components within the various refrigeration systems can vary from those shown.


Furthermore, it should be appreciated that the refrigeration systems shown may be used in both stationary and mobile applications. Moreover, the compartments that are conditioned by the refrigeration systems can be open or closed compartments or spaces. Additionally, the refrigeration systems shown may also be used in applications having more than two compartments or spaces that are desired to be maintained at the same or different temperatures. Moreover, it should be appreciated that the cascading of the vapor compression cycle, the thermoelectric module and the heat-transfer circuit can be reversed from that shown. That is, a vapor compression cycle can be used to extract heat from the lower temperature compartment while the thermoelectric module and a heat-transfer circuit can be used to expel heat from the higher temperature compartment although all of the advantages of the present teachings may not be realized. Additionally, it should be appreciated that the heat exchange devices utilized on the hot and cold sides of the thermoelectric devices may be the same or differ from one another. Moreover, with a single-phase fluid flowing through one of the heat exchange devices and a refrigerant flowing through the other heat exchange device, such configurations may be optimized for the specific fluid flowing therethrough. Moreover, it should be appreciated that the various teachings disclosed herein may be combined in combinations other than those shown. For example, the TEMs used in FIGS. 1-4 may incorporate fins on the cold side thereof with the fan blowing the air directly over the fins to transfer heat therefrom in lieu of the use of a heat-transfer circuit. Moreover, the TEMs may be placed in heat-transferring relation with a single evaporator that is in heat-transferring relation with both the TEM and the air flow flowing through the first compartment. Thus, the heat exchange devices on opposite sides of the thermoelectric devices can be the same or different from one another. Accordingly, the description is merely exemplary in nature and variations are not to be regarded as a departure from the spirit and scope of the teachings.

Claims
  • 1. A refrigeration system comprising: a thermoelectric device that forms a temperature gradient between first and second sides;a compressible working fluid flowing through a refrigeration circuit in heat-transferring relation to said first side of said thermoelectric device;a heat transfer fluid flowing through a heat-transfer circuit in heat-transferring relation to said second side of said thermoelectric device;wherein heat is extracted from one of said compressible working fluid and heat transfer fluid and transferred to the other of said compressible working fluid and heat transfer fluid through said thermoelectric device.
  • 2. The refrigeration system of claim 1, further comprising a compressor in said refrigeration circuit and wherein said compressible working fluid is compressed by said compressor.
  • 3. The refrigeration system of claim 2, further comprising a condenser and an expansion device in said refrigeration circuit, said condenser operable to extract heat from said compressible working fluid.
  • 4. The refrigeration system of claim 3, further comprising an evaporator in said refrigeration circuit in heat-transferring relation with a first air flow, wherein a first portion of said compressible working fluid flows in heat-transferring relation with said evaporator and a second portion of said compressible working fluid flows in heat-transferring relation with said first side of said thermoelectric device, such that said first and second portions flow in parallel in said refrigeration circuit.
  • 5. The refrigeration system of claim 4, wherein said expansion device is a first expansion device and further comprising a second expansion device in said refrigeration circuit, said first and second expansion devices regulating the respective flow of said first and second portions of said compressible working fluid.
  • 6. The refrigeration system of claim 4, further comprising a heat exchanger in said heat-transfer circuit in heat-transferring relation with a second air flow such that said heat-transfer fluid is in heat-transferring relation with both said second air flow and said second side of said thermoelectric device.
  • 7. The refrigeration system of claim 6, further comprising: a first space maintained at a first temperature and through which said first air flow travels;a second space maintained at a second temperature different than said first space and through which said second air flow travels;wherein said heat exchanger extracts heat from said second air flow and transfers said second air flow extracted heat to said heat-transfer fluid, said thermoelectric device transfers said second air flow extracted heat from said heat-transfer fluid to said second portion of said compressible working fluid, and said evaporator extracts heat from said first air flow and transfers said first air flow extracted heat to said first portion of said compressible working fluid.
  • 8. The refrigeration system of claim 3, further comprising a heat exchanger in said heat-transfer circuit in heat-transferring relation with said heat-transfer fluid, said heat exchanger operable to transfer heat between said heat-transfer fluid and an air flow, wherein said expansion device regulates flow of said compressible working fluid.
  • 9. The refrigeration system of claim 8, further comprising a space maintained at a predetermined temperature and through which said air flow travels, and wherein said heat exchanger extracts heat from said air flow and transfers said heat to said heat-transfer fluid, said thermoelectric device transfers said heat from said heat transfer fluid to said compressible working fluid, and said condenser transfers said heat to the ambient environment thereby maintaining said space at said predetermined temperature.
  • 10. The refrigeration system of claim 1, wherein said heat-transfer fluid is a single-phase fluid in said heat-transfer circuit.
  • 11. A refrigeration system comprising: a heat-transfer circuit operable to transfer heat between a heat-transfer fluid flowing therethrough and a first refrigerated space;a vapor compression circuit operable to transfer heat between a refrigerant flowing therethrough and an air flow;a thermoelectric device in heat-transferring relation with said heat-transfer circuit and said vapor compression circuit, said thermoelectric device operable to transfer heat between said heat-transfer fluid and said refrigerant.
  • 12. The refrigeration system of claim 11, wherein said heat-transfer circuit maintains said first refrigerated space at a first predetermined temperature and said heat-transfer circuit includes: a fluid pump pumping said heat-transfer fluid through said heat-transfer circuit; anda heat exchanger transferring heat between said heat-transfer fluid and said first refrigerated space.
  • 13. The refrigeration system of claim 12, wherein said vapor compression circuit includes: a compressor compressing said refrigerant;a condenser transferring heat between said refrigerant and said air flow; andan expansion device regulating flow of said refrigerant.
  • 14. The refrigeration system of claim 13, wherein said vapor compression circuit maintains a second refrigerated space at a second predetermined temperature and said vapor compression circuit includes an evaporator transferring heat between said refrigerant and said second refrigerated space.
  • 15. The refrigeration system of claim 14, wherein different portions of said refrigerant flow through said evaporator and in heat-transferring relation with said thermoelectric device and rejoin prior to flowing through said compressor.
  • 16. The refrigeration system of claim 15, wherein said vapor compression circuit includes a pressure regulating device downstream of said evaporator and creating a pressure differential across said evaporator.
  • 17. The refrigeration system of claim 11, further comprising a power supply operable to selective supply an electric current flow to said thermoelectric device.
  • 18. The refrigeration system of claim 11, wherein said heat-transferring fluid is a single-phase fluid in said heat-transfer circuit.
  • 19. A refrigeration system comprising: a thermoelectric device including a temperature gradient between first and second sides;a first air flow flowing through a first space in heat-transferring relation with said first side;a compressible working fluid flowing through a refrigeration circuit in heat-transferring relation with said second side;wherein heat is extracted from one of said first air flow and said working fluid and transferred to the other of said first air flow and said working fluid through said thermoelectric device.
  • 20. The refrigeration system of claim 19, further comprising a compressor in said refrigeration circuit and wherein said working fluid is compressed by said compressor.
  • 21. The refrigeration system of claim 20, further comprising an evaporator in said refrigeration circuit in heat-transferring relation with a second air flow flowing through a second space, said evaporator extracting heat from said second air flow thereby cooling said second space.
  • 22. The refrigeration system of claim 21, wherein said second side of said thermoelectric device is in heat-transferring relation with said working fluid flowing through said evaporator.
  • 23. The refrigeration system of claim 19, wherein heat is extracted from said first air flow and transferred to said working fluid through said thermoelectric device.
  • 24. A method comprising: transferring heat between a fluid flowing through a heat-transfer circuit and a first side of a thermoelectric device;transferring heat between a refrigerant flowing through a vapor compression circuit and a second side of said thermoelectric device.
  • 25. The method of claim 24, further comprising: removing heat from a first refrigerated space with the heat-transfer circuit;transferring said removed heat to a cold side of said thermoelectric device;transferring said removed heat to said ref rifrigerant through a hot side of said thermoelectric device.
  • 26. The method of claim 25, further comprising transferring said removed heat from said refrigerant to the ambient environment with a condenser.
  • 27. The method of claim 25, further comprising: removing heat from a second refrigerated space with said refrigerant;transferring said heat removed from said first and second refrigerated spaces from said refrigerant to the ambient environment with a condenser in the vapor compression circuit.
  • 28. The method of claim 27, further comprising: transferring said heat removed from said first refrigerated space to a first portion of said refrigerant in heat transferring relation with said hot side of said thermoelectric device;transferring heat from an air flow through said second refrigerated space to a second portion of said refrigerant in heat transferring relation with an evaporator;joining said first and second portions of said refrigerant together prior to said refrigerant flowing through a compressor.
  • 29. The method of claim 28, further comprising operating said hot side of said thermoelectric device and said evaporator at approximately a same temperature.
  • 30. The method of claim 28, further comprising operating said hot side of said thermoelectric device and said evaporator at different temperatures.
  • 31. The method of claim 25, wherein removing heat from said first refrigerated space includes: transferring heat from said first refrigerated space to said heat-transfer fluid within said heat exchanger; andtransferring heat from said heat-transfer fluid to said cold side of said thermoelectric device.
  • 32. The method of claim 24, further comprising: supplying an electric current flow to the thermoelectric device thereby creating a temperature gradient between said first and second sides of said thermoelectric device;cooling a first refrigerated space by transferring heat from said heat-transfer fluid to said refrigerant flow through said thermoelectric device;defrosting heat exchanger in said heat-transfer circuit by transferring heat to said heat-transfer fluid through said thermoelectric device.
  • 33. The method of claim 24, further comprising maintaining said heat-transfer fluid in a single-phase throughout the heat-transfer circuit.
  • 34. The method of claim 24, further comprising: removing heat from a first refrigerated space by circulating an air flow through said first refrigerated space and in heat-transferring relation with a cold side of said thermoelectric device;transferring said removed heat to said refrigerant through a hot side of said thermoelectric device.
  • 35. A method comprising: transferring heat between a fluid and a first side of a thermoelectric device;transferring heat between a refrigerant flowing through a vapor compression circuit and a second side of said thermoelectric device;removing heat from a first refrigerated space by circulating an air flow through said first refrigerated space and in heat-transferring relation with a cold side of said thermoelectric device;transferring said removed heat to said refrigerant through a hot side of said thermoelectric device;removing heat from a second refrigerated space with said refrigerant;transferring said heat removed from said first and second refrigerated spaces from said refrigerant to the ambient environment with a condenser in the vapor compression circuit.
  • 36. The method of claim 24, further comprising creating a temperature gradient between said first and second sides of said thermoelectric device by supplying an electric current flow to said thermoelectric device.
  • 37. The method of claim 35, further comprising creating a temperature gradient between said first and second sides of said thermoelectric device by supplying an electric current flow to said thermoelectric device.
  • 38. The method of claim 37, wherein said first side has a first temperature, said second side has a second temperature, and said first temperature is lower than said second temperature.
  • 39. The method of claim 35, wherein circulating an air flow through said first refrigerated space and in heat-transferring relation with a cold side of said thermoelectric device includes circulating said air flow in direct contact with at least one heat transfer fin which is in heat-transfer relation with said cold side of said thermoelectric device.
  • 40. The method of claim 35, wherein transferring said removed heat to said refrigerant include transferring said removed heat from said hot side of said thermoelectric device to said refrigerant in an evaporator and removing heat from said second refrigerated space includes transferring said heat from said second refrigerated space to said refrigerant in said evaporator.
US Referenced Citations (306)
Number Name Date Kind
2997514 Roeder, Jr. Aug 1961 A
3073126 Staebler Jan 1963 A
3111813 Blumentritt Nov 1963 A
3205667 Frantti Sep 1965 A
3212274 Eidus Oct 1965 A
3237415 Newton Mar 1966 A
3295667 Kittle Jan 1967 A
3481393 Chu Dec 1969 A
3559437 Withers, Jr. Feb 1971 A
4001588 Elsner Jan 1977 A
4109707 Wilson et al. Aug 1978 A
RE30652 Germano et al. Jun 1981 E
4281516 Berthet et al. Aug 1981 A
4362023 Falco Dec 1982 A
4383414 Beitner May 1983 A
4400948 Moorehead Aug 1983 A
4402185 Perchak Sep 1983 A
4499329 Benicourt et al. Feb 1985 A
4545967 Reynolds et al. Oct 1985 A
4611089 Elsner et al. Sep 1986 A
4622822 Beitner Nov 1986 A
4639542 Bass et al. Jan 1987 A
4644753 Burke Feb 1987 A
4730459 Schlicklin et al. Mar 1988 A
4734139 Shakun et al. Mar 1988 A
4744220 Kerner et al. May 1988 A
4764193 Clawson Aug 1988 A
4829771 Koslow et al. May 1989 A
4833888 Kerner et al. May 1989 A
4855810 Gelb et al. Aug 1989 A
4947648 Harwell et al. Aug 1990 A
5006505 Skertic Apr 1991 A
5022928 Buist Jun 1991 A
5029446 Suzuki Jul 1991 A
5057490 Skertic Oct 1991 A
5092129 Bayes et al. Mar 1992 A
5103286 Ohta et al. Apr 1992 A
5154661 Higgins Oct 1992 A
5156004 Wu et al. Oct 1992 A
5168339 Yokotani et al. Dec 1992 A
5222216 Parish et al. Jun 1993 A
5232516 Hed Aug 1993 A
5247798 Collard, Jr. Sep 1993 A
5248639 Elsner et al. Sep 1993 A
5292376 Suse et al. Mar 1994 A
5304846 Azar et al. Apr 1994 A
5314586 Chen May 1994 A
5319937 Fritsch et al. Jun 1994 A
5367879 Doke et al. Nov 1994 A
5398510 Gilley et al. Mar 1995 A
5409547 Watanabe et al. Apr 1995 A
5431021 Gwilliam et al. Jul 1995 A
5434744 Fritz et al. Jul 1995 A
5436467 Elsner et al. Jul 1995 A
5441576 Bierschenk et al. Aug 1995 A
5448109 Cauchy Sep 1995 A
5448449 Bright et al. Sep 1995 A
5449288 Bass Sep 1995 A
5456081 Chrysler et al. Oct 1995 A
5456164 Bang Oct 1995 A
5465581 Haertl et al. Nov 1995 A
5470395 Yater et al. Nov 1995 A
5471850 Cowans Dec 1995 A
5501076 Sharp, III et al. Mar 1996 A
5505046 Nelson et al. Apr 1996 A
5515238 Fritz et al. May 1996 A
5524440 Nishioka et al. Jun 1996 A
5544487 Attey et al. Aug 1996 A
5550387 Elsner et al. Aug 1996 A
5584183 Wright et al. Dec 1996 A
5588300 Larsson et al. Dec 1996 A
RE35441 Yokotani et al. Feb 1997 E
5605047 Park et al. Feb 1997 A
5623119 Yater et al. Apr 1997 A
5623292 Shrivastava et al. Apr 1997 A
5636520 Spauschus et al. Jun 1997 A
5644185 Miller Jul 1997 A
5653111 Attey et al. Aug 1997 A
5705434 Imanishi et al. Jan 1998 A
5705770 Ogasawara et al. Jan 1998 A
5713208 Chen et al. Feb 1998 A
5715684 Watanabe et al. Feb 1998 A
5722158 Fritz et al. Mar 1998 A
5722249 Miller, Jr. Mar 1998 A
5724818 Iwata et al. Mar 1998 A
5737923 Gilley et al. Apr 1998 A
5753574 Donaldson et al. May 1998 A
5765316 Kavarsky Jun 1998 A
5782094 Freeman Jul 1998 A
5784890 Polkinghorne Jul 1998 A
5802856 Schaper et al. Sep 1998 A
5809785 Polkinghorne Sep 1998 A
5813233 Okuda et al. Sep 1998 A
5817188 Yahatz et al. Oct 1998 A
5822993 Attey Oct 1998 A
5823005 Alexander et al. Oct 1998 A
5841064 Maekawa et al. Nov 1998 A
5845497 Watanabe et al. Dec 1998 A
5856210 Leavitt et al. Jan 1999 A
5886291 Imanishi et al. Mar 1999 A
5887441 Spauschus et al. Mar 1999 A
5892656 Bass Apr 1999 A
5921087 Bhatia et al. Jul 1999 A
5924289 Bishop, II Jul 1999 A
5927078 Watanabe et al. Jul 1999 A
5950067 Maegawa et al. Sep 1999 A
5969290 Kagawa et al. Oct 1999 A
5981863 Yamashita et al. Nov 1999 A
5987891 Kim et al. Nov 1999 A
5994637 Imanishi et al. Nov 1999 A
6003319 Gilley et al. Dec 1999 A
6005182 Imanishi et al. Dec 1999 A
6019098 Bass et al. Feb 2000 A
6020671 Pento et al. Feb 2000 A
6031751 Janko Feb 2000 A
6034317 Watanabe et al. Mar 2000 A
6043423 Satomura et al. Mar 2000 A
6053163 Bass Apr 2000 A
6067802 Alonso May 2000 A
6076357 Holdren et al. Jun 2000 A
6094919 Bhatia Aug 2000 A
6096964 Ghamaty et al. Aug 2000 A
6096965 Ghamaty et al. Aug 2000 A
6096966 Nishimoto et al. Aug 2000 A
6097088 Sakuragi Aug 2000 A
6103967 Cauchy et al. Aug 2000 A
6127619 Xi et al. Oct 2000 A
6161388 Uttam Dec 2000 A
6164076 Chu et al. Dec 2000 A
6207887 Bass et al. Mar 2001 B1
6222113 Ghoshal Apr 2001 B1
6226178 Broder et al. May 2001 B1
6233944 Yamada et al. May 2001 B1
6252154 Kamada et al. Jun 2001 B1
6253556 Schendel Jul 2001 B1
6258215 Samsonov et al. Jul 2001 B1
6264446 Rajendran et al. Jul 2001 B1
6266962 Ghoshal Jul 2001 B1
6272873 Bass Aug 2001 B1
6274802 Fukuda et al. Aug 2001 B1
6274803 Yoshioka et al. Aug 2001 B1
6279337 Davidson et al. Aug 2001 B1
6279470 Simeray et al. Aug 2001 B2
6282907 Ghoshal Sep 2001 B1
6293107 Kitagawa et al. Sep 2001 B1
6295819 Mathiprakasam et al. Oct 2001 B1
6307142 Allen et al. Oct 2001 B1
6308519 Bielinski Oct 2001 B1
6313636 Pohl et al. Nov 2001 B1
6319437 Elsner et al. Nov 2001 B1
6324860 Maeda et al. Dec 2001 B1
6338251 Ghoshal Jan 2002 B1
6345506 Kontani et al. Feb 2002 B1
6345507 Gillen Feb 2002 B1
6351950 Duncan Mar 2002 B1
6354002 Wright et al. Mar 2002 B1
6359440 Pohl et al. Mar 2002 B2
6362959 Tracy Mar 2002 B2
6370882 Adamski et al. Apr 2002 B1
6370884 Kelada Apr 2002 B1
6393842 Kim et al. May 2002 B2
6400013 Tsuzaki et al. Jun 2002 B1
6401461 Harrison et al. Jun 2002 B1
6401462 Bielinski Jun 2002 B1
6410971 Otey Jun 2002 B1
6412287 Hughes et al. Jul 2002 B1
6418729 Dominguez-Alonso et al. Jul 2002 B1
6438964 Giblin Aug 2002 B1
6439867 Clendenin Aug 2002 B1
6444893 Onoue et al. Sep 2002 B1
6446442 Batchelor et al. Sep 2002 B1
6463743 Laliberte Oct 2002 B1
6466002 Elsner et al. Oct 2002 B1
6489551 Chu et al. Dec 2002 B2
6490869 Uetsuji et al. Dec 2002 B1
6490874 Chu et al. Dec 2002 B2
6519947 Bass et al. Feb 2003 B1
6521991 Yamada et al. Feb 2003 B1
6527548 Kushch et al. Mar 2003 B1
6530231 Nagy et al. Mar 2003 B1
6532749 Rudick et al. Mar 2003 B2
6548750 Picone Apr 2003 B1
6548894 Chu et al. Apr 2003 B2
6560968 Ko May 2003 B2
RE38128 Gallup et al. Jun 2003 E
6574967 Park et al. Jun 2003 B1
6580025 Guy Jun 2003 B2
6588215 Ghoshal Jul 2003 B1
6595004 Ghoshal Jul 2003 B1
6598403 Ghoshal Jul 2003 B1
6612116 Fu et al. Sep 2003 B2
6619044 Batchelor et al. Sep 2003 B2
6620994 Rossi Sep 2003 B2
6624349 Bass Sep 2003 B1
6655172 Perevozchikov et al. Dec 2003 B2
6662570 Venkatasubramanian Dec 2003 B2
6662571 Nagy et al. Dec 2003 B1
6679683 Seibel et al. Jan 2004 B2
6700053 Hara et al. Mar 2004 B2
6705089 Chu et al. Mar 2004 B2
6715298 Guo et al. Apr 2004 B2
6722139 Moon et al. Apr 2004 B2
6727423 Tauchi et al. Apr 2004 B2
6735959 Najewicz May 2004 B1
6739138 Saunders et al. May 2004 B2
6759586 Shutoh et al. Jul 2004 B2
6767766 Chu et al. Jul 2004 B2
6770808 Itakura et al. Aug 2004 B2
6807811 Lee Oct 2004 B2
6815814 Chu et al. Nov 2004 B2
6821092 Gehret et al. Nov 2004 B1
6828579 Ghamaty et al. Dec 2004 B2
6845622 Sauciuc et al. Jan 2005 B2
6855880 Feher Feb 2005 B2
6857276 Finn et al. Feb 2005 B2
6893902 Cordes et al. May 2005 B2
6894215 Akiba May 2005 B2
6895762 Lin May 2005 B1
6941761 Gatecliff et al. Sep 2005 B2
6951113 Adamski Oct 2005 B1
7000407 Miozza et al. Feb 2006 B2
7007501 Hu Mar 2006 B2
7022553 Ahn et al. Apr 2006 B2
7026712 Hayashi et al. Apr 2006 B2
7032389 Cauchy Apr 2006 B2
20010005990 Kim et al. Jul 2001 A1
20010013224 Ohkubo et al. Aug 2001 A1
20010052234 Venkatasubramanian Dec 2001 A1
20010052357 Kajihara et al. Dec 2001 A1
20020024154 Hara et al. Feb 2002 A1
20020038550 Gillen Apr 2002 A1
20020046762 Rossi Apr 2002 A1
20020059951 Tauchi et al. May 2002 A1
20020062853 Kajihara et al. May 2002 A1
20020062855 Chu et al. May 2002 A1
20020063327 Chu et al. May 2002 A1
20020083716 Ko Jul 2002 A1
20020100499 Hayashi et al. Aug 2002 A1
20020121095 Adamski et al. Sep 2002 A1
20020121096 Harrison et al. Sep 2002 A1
20020149896 Tauchi et al. Oct 2002 A1
20020162339 Harrison et al. Nov 2002 A1
20020170296 Guo et al. Nov 2002 A1
20020179135 Shutoh et al. Dec 2002 A1
20020184894 Batchelor et al. Dec 2002 A1
20030024565 Guy Feb 2003 A1
20030029173 Bell et al. Feb 2003 A1
20030029175 Lee Feb 2003 A1
20030056819 Imai et al. Mar 2003 A1
20030057560 Tatoh et al. Mar 2003 A1
20030066554 Feher Apr 2003 A1
20030097845 Saunders et al. May 2003 A1
20030102554 Chu et al. Jun 2003 A1
20030115892 Fu et al. Jun 2003 A1
20030121540 Onoue Jul 2003 A1
20030122245 Chu et al. Jul 2003 A1
20030126865 Venkatasubramanian Jul 2003 A1
20030131609 Venkatasubramanian Jul 2003 A1
20030140957 Akiba Jul 2003 A1
20030145605 Moon et al. Aug 2003 A1
20030154726 Finn et al. Aug 2003 A1
20030183839 Yamashita et al. Oct 2003 A1
20030188538 Chu et al. Oct 2003 A1
20030193087 Hayashi et al. Oct 2003 A1
20030214031 Onoue Nov 2003 A1
20030230332 Venkatasubramanian et al. Dec 2003 A1
20030234037 Tanaka Dec 2003 A1
20040042181 Nagasaki Mar 2004 A1
20040128041 Hiller et al. Jul 2004 A1
20040177876 Hightower Sep 2004 A1
20040177877 Hightower Sep 2004 A1
20040187501 Sauciuc et al. Sep 2004 A1
20040207037 Kucherov et al. Oct 2004 A1
20040231339 Miozza et al. Nov 2004 A1
20040238022 Hiller et al. Dec 2004 A1
20050000559 Horio et al. Jan 2005 A1
20050028858 Rossi Feb 2005 A1
20050029637 Hu et al. Feb 2005 A1
20050039465 Welch Feb 2005 A1
20050056310 Shikata et al. Mar 2005 A1
20050094381 Imamura et al. May 2005 A1
20050121065 Otey Jun 2005 A1
20050126184 Cauchy Jun 2005 A1
20050126185 Joshi Jun 2005 A1
20050139249 Ueki et al. Jun 2005 A1
20050139251 Shutoh et al. Jun 2005 A1
20050146060 Suzuki Jul 2005 A1
20050146850 Meir Jul 2005 A1
20050172991 Arai et al. Aug 2005 A1
20050204748 Yamanaka et al. Sep 2005 A1
20050241690 Tajima et al. Nov 2005 A1
20050247337 Chen et al. Nov 2005 A1
20050279104 Leija et al. Dec 2005 A1
20050279105 Pastorino Dec 2005 A1
20060000221 Culp et al. Jan 2006 A1
20060000500 Sauciuc et al. Jan 2006 A1
20060005873 Kambe et al. Jan 2006 A1
20060033206 Adar et al. Feb 2006 A1
20060048807 Lee et al. Mar 2006 A1
20060053805 Flinner et al. Mar 2006 A1
20060075761 Kitchens et al. Apr 2006 A1
20060086118 Venkatasubramanian et al. Apr 2006 A1
20060090787 Onvural May 2006 A1
20060096300 Reinstein et al. May 2006 A1
20060117761 Bormann Jun 2006 A1
20060118160 Funahashi et al. Jun 2006 A1
Foreign Referenced Citations (11)
Number Date Country
0 949 461 Oct 1999 EP
0 566 646 Jun 2000 EP
0 759 141 Apr 2003 EP
62-169981 Jul 1987 JP
62-182562 Aug 1987 JP
2000-304396 Nov 2000 JP
10-2000-0010150 Feb 2000 KR
WO 9213243 Aug 1992 WO
WO 9531688 Nov 1995 WO
WO 9926996 Jun 1999 WO
WO 0125711 Apr 2001 WO
Related Publications (1)
Number Date Country
20070101748 A1 May 2007 US