Abstract:
A module, such as a module configured to be used in a refrigeration system, includes a gas-liquid separator which is configured to receive a first refrigerant, to separate the first refrigerant into a gas portion of the first refrigerant and a liquid portion of the first refrigerant, and to transmit the gas portion of the first refrigerant. The module also includes a heat exchanger which is configured to receive a second refrigerant and to exchange heat between the second refrigerant and the gas portion of the first refrigerant and/or the liquid portion of the first refrigerant. Moreover, the heat exchanger is disposed within the gas-liquid separator.

Description:
BACKGROUND OF THE INVENTION 
       [0001]    1. Field of the Invention 
         [0002]    The present invention relates generally to vapor compression refrigerating systems and modules which are used in such vapor compression refrigerating system. In particular, the present invention is directed towards vapor compression refrigerating systems and modules in which the module comprises a gas-liquid separator and a heat exchanger disposed within, e.g., surrounded by, the gas-liquid separator. 
         [0003]    2. Description of Related Art 
         [0004]    An exemplary, known vapor compression refrigerating system, such as the vapor compression refrigerating system described in Japanese Patent Publication No. JP-A-11-193967, uses a natural refrigerant, such as carbon dioxide, as a refrigerant. The known vapor compression refrigerating system includes an inside heat exchanger for exchanging heat between refrigerant at an exit side of a radiator and refrigerant at a suction side of a compressor, which increases an efficiency of the vapor compression refrigerating system. 
         [0005]    One exemplary, known vapor compression refrigerating system is depicted in  FIG. 11 . The high-temperature and high-pressure refrigerant compressed by a compressor  201  is introduced into a radiator  202 , and heat is exchanged between the refrigerant and an outside fluid. The refrigerant flows from radiator  202  to an inside heat exchanger  203 , and then from inside heat exchanger  203  to a pressure-reducing mechanism  204  which reduces the pressure of the refrigerant. The pressure reduced refrigerant flows from pressure-reducing mechanism  204  to an evaporator  205 , and then from evaporator  205  to a gas-liquid separator  206 . The gas-liquid separator  206  then separates a gas portion of the refrigerant from a liquid portion of the refrigerant, stores the liquid portion of the refrigerant, and the gas portion of the refrigerant flows from gas-liquid separator  206  to inside heat exchanger  203 . Heat then is exchanged between the refrigerant which flows from radiator  202  to inside heat exchanger  203  and the gas portion of the refrigerant which flows from gas-liquid separator  206  to inside heat exchanger  203 . The gas portion of the refrigerant then flows from inside heat exchanger  203  to compressor  201 . 
         [0006]    In a vapor compression refrigerating system including such an inside heat exchanger, a pressure in the high-pressure side of the system may be elevated by decreasing a specific enthalpy of refrigerant at the exit side of the radiator, as compared with a refrigerating system which does not include an inside heat exchanger. Consequently, it may be possible to improve a coefficient of performance of the system, and to prevent a liquid compression of the compressor by providing a certain degree of superheating to the refrigerant which is sucked into the compressor. 
         [0007]    When carbon dioxide is used as the refrigerant, although the refrigerant discharged from the compressor is cooled by the radiator, because the refrigerant at the outlet of the radiator may reach a supercritical condition without being liquefied when a temperature of an outside fluid, e.g., air, to be exchanged in heat with the refrigerant in the radiator exceeds a certain temperature, e.g., a temperature greater than the critical temperature of carbon dioxide, if the pressure of the refrigerant is reduced and the refrigerant is evaporated by an evaporator, the refrigeration ability of the refrigeration system may substantially decrease. Therefore, exchanging heat between the refrigerant at the exit side of the radiator and the refrigerant at the suction side of the compressor via the inside heat exchanger may increase or maintain the refrigeration ability of the refrigerating system, and also may reduce the pressure of the high-pressure side and improve the coefficient of performance of the refrigerating system. 
         [0008]    Another known vapor compression refrigerating system is described in Japanese Patent Publication No. JP-A-2004-100974. In this known vapor compression refrigerating system, the number of refrigerant tubes and coupling portions thereof are reduced by integrally forming the inside heat exchanger around a refrigerant storing space of the gas-liquid separator, thereby reducing the number of parts used in the refrigerating system and the amount of space occupied by the refrigerating system. 
         [0009]    Nevertheless, when the inside heat exchanger is provided as a single, separated piece of equipment, because refrigerant tubes and coupling portions therefor are required for the inside heat exchanger, it may be difficult to reduce the cost of the system. Further, when the inside heat exchanger is integrated with the gas-liquid separator around the gas-liquid separator, although the number of the refrigerant tubes and the coupling portions therefor is reduced, the configuration of the integrated equipment may become complicated, and it may be difficult to practically manufacture the integrated equipment. Moreover, oil in the gas-liquid separator may remain inside the inside heat exchanger integrated with the gas-liquid separator. 
       SUMMARY OF THE INVENTION 
       [0010]    Therefore, a need has arisen for a vapor compression refrigerating systems which overcome these and other shortcomings of the related art. A technical advantage of the present invention is that a vapor compression refrigerating system may include a module which includes a gas-liquid separator and a heat exchanger disposed within, e.g., surround by, the gas-liquid separator. This may reduce the number of parts included in the refrigerating system, the costs associated with maintaining the refrigerating system, and the weight of the weight of the refrigerating system, relative to known refrigerating systems. 
         [0011]    According to an embodiment of the present invention, a vapor compression refrigerating system comprises a compressor configured to compress a refrigerant, and a radiator in fluid communication with the compressor. The radiator is configured to receive the refrigerant from the compressor and to reduce a temperature of the refrigerant. The system also comprises a module in fluid communication with each of the radiator and the compressor, and the module is configured to receive the refrigerant from the radiator. The system further comprises a first pressure-reducing mechanism in fluid communication with the module, and the first pressure-reducing mechanism is configured to receive the refrigerant from the first pressure-reducing module and to reduce a pressure of the refrigerant. Moreover, the system comprises an evaporator in fluid communication with each of the first pressure-reducing mechanism and the module, and the evaporator is configured to receive the refrigerant from the first pressure-reducing mechanism and to evaporate the refrigerant, and the module is further configured to receive the refrigerant from the evaporator. Specifically, the module comprises a gas-liquid separator which is configured to receive the refrigerant from the evaporator, to separate the refrigerant into a gas portion of the refrigerant and a liquid portion of the refrigerant, and to transmit the gas portion of the refrigerant to the compressor. The module also comprises a heat exchanger which is configured to receive the refrigerant from the radiator and to exchange heat between the refrigerant received from the radiator and at least one of the gas portion of the refrigerant and the liquid portion of the refrigerant. For example, heat may be exchanged between the refrigerant received from the radiator and both the gas portion of the refrigerant and the liquid portion of the refrigerant. Moreover, the heat exchanger is disposed within, e.g., surrounded by, the gas-liquid separator. 
         [0012]    According to another embodiment of the present invention, a module comprises a gas-liquid separator which is configured to receive a first refrigerant, to separate the first refrigerant into a gas portion of the first refrigerant and a liquid portion of the first refrigerant, and to transmit the gas portion of the first refrigerant. The module also comprises a heat exchanger which is configured to receive a second refrigerant and to exchange heat between the second refrigerant and at least one of the gas portion of the first refrigerant and the liquid portion of the first refrigerant. Moreover, the heat exchanger is disposed within, e.g., surrounded by, the gas-liquid separator. 
         [0013]    Other objects, features, and advantage will be apparent to persons of ordinary skill in the art from the following detailed description of the invention and the accompanying drawings. 
     
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         [0014]    For a more complete understanding of the present invention, needs satisfied thereby, and the objects, features, and advantages thereof, reference now is made to the following description taken in connection with the accompanying drawings. 
           [0015]      FIG. 1  is a circuit diagram of a refrigerating system, according to an embodiment of the present invention. 
           [0016]      FIG. 2  is a schematic, circuit diagram of the refrigerating system of  FIG. 1 . 
           [0017]      FIG. 3  is a vertical, sectional view of a module of the refrigerating system of  FIG. 1 , according to an embodiment of the present invention. 
           [0018]      FIG. 4  is a vertical, sectional view of a module of a refrigerating system, according to another embodiment of the present invention. 
           [0019]      FIG. 5  is a perspective view of an exemplary flat tube with a plurality of holes therein disposed in parallel to each other, according to an embodiment of the present invention. 
           [0020]      FIG. 6  is a perspective view of an exemplary low-fin tube, according to an embodiment of the present invention. 
           [0021]      FIG. 7  is a circuit diagram of refrigerating system, according to another embodiment of the present invention. 
           [0022]      FIG. 8  is a schematic, circuit diagram of the refrigerating system of  FIG. 7 . 
           [0023]      FIG. 9  is a vertical, sectional view of a module of the refrigerating system of  FIG. 7 , according to an embodiment of the present invention. 
           [0024]      FIG. 10  is a Mollier chart of the refrigerating system of  FIG. 7 , according to an embodiment of the present invention. 
           [0025]      FIG. 11  is a circuit diagram of a known refrigerating system. 
       
    
    
     DETAILED DESCRIPTION OF EMBODIMENTS 
       [0026]    Embodiments of the present invention, and their features and advantages, may be understood by referring to  FIGS. 1-10 , like numerals being used for like corresponding parts in the various drawings. 
         [0027]      FIG. 1  depicts a circuit diagram of a vapor compression refrigerating system, according to an embodiment of the present invention. The vapor compression refrigerating system may comprise a compressor  1 , a radiator  2  in fluid communication with compressor  1 , a heat exchanger  3  in fluid communication with each of radiator  2  and compressor  1 , and a pressure-reducing mechanism  4  in fluid communication with heat exchanger  3 . The vapor compression refrigerating system also may comprise an evaporator  5  in fluid communication with pressure-reducing mechanism  4 , and a gas-liquid separator  6  in fluid communication with each of evaporator  5  and heat exchanger  3 . 
         [0028]    In operation, a refrigerant, such as a natural refrigerant, e.g., carbon dioxide, may be compressed by compressor  1 , which contracts the refrigerant and increases the temperature of the refrigerant. The refrigerant then may flow from compressor  1  to radiator  2 , and heat may be exchanged between the refrigerant and an outside fluid, e.g., air. The refrigerant then may flow from radiator  2  to heat exchanger  3 , and the refrigerant may be cooled by an exchange of heat with refrigerant flowing in a circuit of a suction side of compressor  1 . The refrigerant then may flow from heat exchanger  3  to pressure-reducing mechanism  4  which may reduce the pressure of the refrigerant. The refrigerant then may flow from pressure reducing mechanism  4  to evaporator  5 , and heat may be exchanged between the refrigerant and the outside fluid. The refrigerant then may flow from evaporator  5  to gas-liquid separator  6 . Gas-liquid separator  6  may separate a gas portion of the refrigerant from a liquid portion of the refrigerant, store the liquid portion of the refrigerant, and supply the gas portion of the refrigerant to a refrigerant circuit in fluid communication with compressor  1 . 
         [0029]    For example, referring to  FIG. 2 , heat exchanger  3  may be formed integral with gas-liquid separator  6 , such that heat exchanger  3  and gas-liquid separator  6  comprise a module  7 . The liquid portion of the refrigerant may be stored in the bottom portion in module  7 , and the gas portion of the refrigerant may be discharged from module  7  and transmitted to compressor  1 . In module  7 , the refrigerant which flows from radiator  2  passes through a refrigerant storing space in module  7 , the refrigerant is cooled by a low-pressure refrigerant of the liquid portion of the refrigerant and the gas portion of the refrigerant present in module  7 , and the refrigerant flows out from module  7  to pressure-reducing mechanism  4 . 
         [0030]      FIG. 3  depicts module  7 , according to an embodiment of the present invention. Module  7  may comprise a refrigerant storing vessel  100  which separates the refrigerant into a gas portion of the refrigerant and a liquid portion of the refrigerant, and stores an excessive liquid refrigerant portion of the refrigerant. Refrigerant flows from evaporator  5  flows to a low-pressure refrigerant inlet  106 , the and refrigerant is separated into a gas portion of the refrigerant and a liquid portion of the refrigerant  111 , and the liquid portion of the refrigerant  111  is stored therein. The refrigerant which flows from evaporator  5  may include a lubricant, such as oil, and oil  112  may be separated from the refrigerant which flows from evaporator  5  and may be stored in the bottom portion in module  7 . The gas portion of the refrigerant is discharged from a low-pressure refrigerant discharge tube  101  to compressor  1 . Moreover, at least a portion of oil  112  stored in the bottom portion in module  7  is sucked through an oil returning hole  102  provided at a lower portion of low-pressure refrigerant discharge tube  101 , and the sucked portion of the oil is sent to compressor  1  with the gas portion of the refrigerant through a low-pressure refrigerant outlet  109 . A diffuser  105  prevents the gas-liquid mixed refrigerant which flows from low-pressure refrigerant inlet  106  into module  7  from directly flowing into low-pressure refrigerant discharge tube  101 . The oil and the liquid portion of the refrigerant may not be completely separated as depicted in the  FIG. 3 , and in practice, a small amount of liquid refrigerant generally is contained in the oil. 
         [0031]    Referring to  FIGS. 3 and 4 , the high-temperature and high-pressure refrigerant which flows from radiator  2  flows into module  7  through a high-pressure refrigerant inlet  108 , passes through a high-pressure refrigerant tube  103 , e.g., a substantially W-shaped tube or a substantially U-shaped tube, and flows out to pressure-reducing mechanism  4  through a high-pressure refrigerant outlet  107 . A portion of high-pressure refrigerant tube  103  may contact the liquid portion of the refrigerant  111 , as depicted in  FIG. 3 , and the high-temperature and high-pressure refrigerant may be cooled by an exchange of heat between the high-temperature and high-pressure refrigerant flowing in the tube  103  and the liquid portion of the refrigerant  111 . Moreover, because heat also may be exchanged between high-pressure refrigerant tube  103  and the gas portion of the refrigerant in refrigerant storing space  110 , the high-temperature and high-pressure refrigerant flowing in tube  103  may be cooled by both the gas portion of the refrigerant and the liquid portion of the refrigerant  111  present in refrigerant storing space  110 . Moreover, fins  104  may provided on the surface of high-pressure refrigerant tube  103 , which may further accelerate the exchange of heat between the high-temperature and high-pressure refrigerant and the refrigerant present in refrigerant storing space  110 . High-pressure refrigerant tube  103  may be structured by forming a flat tube with a plurality of holes therein disposed in parallel to each other as a W-shaped configuration or a U-shaped configuration, and providing fins between the tube portions of the tube. 
         [0032]      FIG. 5  depicts an example of a flat tube with a plurality of holes therein disposed in parallel to each other for forming high-pressure refrigerant tube  103 . The plurality of parallel holes form a plurality of parallel refrigerant passages  103   a . Further, as depicted in  FIG. 6 , a low-fin tube formed with a refrigerant passage  103   c  and provided with low fins  103   b  on the surface may be used as high-pressure refrigerant tube  103 . Such a low-fin tube may be manufacture by rolling. 
         [0033]    In this embodiment of the present invention, inlet  106 , inlet  108 , outlet  107 , and outlet  109  each may be provided on the same surface, e.g., the upper surface, of module  7 , such that module  7  may be compact, and even when module  7  is mounted to a vehicle, the tubes readily may be coupled. 
         [0034]      FIG. 7  depicts a vapor compression refrigerating system, according to another embodiment of the present invention. The vapor compression refrigerating system of this embodiment of the present invention is substantially similar to the vapor compression refrigerating system of the above-described embodiments of the present invention. Therefore, only those differences between this embodiment of the present invention and the above-described embodiments of the present invention are discussed with respect to this embodiment of the present invention. In this embodiment of the present invention, a pressure-reducing mechanism  8  is added to the vapor compression refrigerating system. Specifically, pressure-reducing mechanism  8  is in fluid communication with radiator  2  and heat exchanger  3 , such that heat exchanger  3  is in fluid communication with radiator  2  via pressure-reducing mechanism  8 . Specifically, the refrigerant flows from radiator  2  to pressure-reducing mechanism  8  which reduces the pressure of the refrigerant, and the pressure-reduced refrigerant then flows to heat exchanger  3  which cools the refrigerant by the refrigerant of the suction side of compressor  1 . The cooled refrigerant then flows to first pressure-reducing mechanism  4  which reduces the pressure of the cooled refrigerant. The remaining operation of the vapor compression refrigerating system in this embodiment of the present invention is substantially the same as in the above-described embodiments of the present invention. 
         [0035]    Referring to  FIG. 8 , in an embodiment of the present invention, second pressure-reducing mechanism  8 , heat exchanger  3 , and gas-liquid separator  6  are integrally formed as a module  9 . With respect to this embodiment of the present invention as compared to the above-described embodiments of the present invention, because second pressure-reducing mechanism  8  in module  9  reduces the pressure of the refrigerant passing through the refrigerant storing space of module  9 , it is possible to decrease the thickness of the material of the tube passing through the space to be less than the thickness of the high-pressure refrigerant tube used in the first embodiment. 
         [0036]    Referring to  FIG. 9 , with respect to module  9 , the high-temperature and high-pressure refrigerant which flows from radiator  2  flows into an orifice  113  and reduced in pressure by orifice  113 . For example, orifice  113  may correspond to second pressure-reducing mechanism  8 . The remaining components of module  9  operate in substantially the same manner as their corresponding components in module  7 . Therefore, module  9  is not discussed in further detail. 
         [0037]    In this embodiment, because the pressure inside high-pressure refrigerant tube  103  may be less than in the above-described embodiments, the thickness of high-pressure refrigerant tube  103  in this embodiment may be less than the thickness of high-pressure refrigerant tube  103  in the above-described embodiments, such that the exchange of heat between the refrigerant which flows from radiator  2  and the liquid portion of the refrigerant  111  and the gas portion of the refrigerant may occur more quickly in this embodiment relative the above-described embodiments.  FIG. 10  shows a Mollier chart in the operation of the refrigerating system according to this second embodiment. 
         [0038]    The module according to the present invention is suitable for a vapor compression refrigerating system, in particular, for a vapor compression refrigerating system using carbon dioxide as its refrigerant, especially, a vapor compression refrigerating system used in an air conditioning system for a vehicle. 
         [0039]    While the invention has been described in connection with embodiments of the invention, it will be understood by those skilled in the art that variations and modifications of the embodiments described above may be made without departing from the scope of the invention. Other embodiments will be apparent to those skilled in the art from a consideration of the specification or from a practice of the invention disclosed herein. It is intended that the specification and the described examples are consider exemplary only, with the true scope of the invention indicated by the following claims.