This invention relates generally to transport refrigeration units and, more specifically, to facilitating the pull down of the temperature of product when loaded into a transport container provided with a refrigeration unit.
Refrigerated freight containers require a refrigeration unit for maintaining a desired temperature environment within the interior volume of the container. The refrigeration unit must have sufficient refrigeration capacity to maintain the product stored within the container at the desired temperature over a wide range of outdoor ambient temperatures and load conditions. Refrigerated freight containers are used to transport a wide variety of products, ranging for example from freshly picked produce to deep frozen seafood. Product may be loaded into the container unit directly from the field, such as freshly picked fruits and vegetables, or from a warehouse.
Conventional transport refrigeration units used in connection with cooling refrigerated freight containers include a refrigerant compressor, a condenser coil, a thermostatic expansion valve (TXV), and an evaporator coil connected via appropriate refrigerant lines in a closed refrigerant flow circuit. The refrigeration unit is generally contained in a housing mountable to the container such that the air or gas/air mixture or other gas within the interior volume of the container may be circulated over the evaporator coil by means of an evaporator fan associated with the evaporator coil. The refrigerant unit may also be equipped with an economizer incorporated into the refrigerant circuit, if desired.
Generally, products loaded into a container from a warehouse have already been cooled to the desired product storage temperature within a refrigeration facility at the warehouse. Thus, the chilled products may be transferred into a container, without increasing the refrigeration load on the refrigeration unit. In conventional practice, the refrigeration unit is typically designed with a refrigeration capacity sized to provide stable temperature at a low box temperature desired for deep frozen product, which as noted before when loaded into the container has already been pre-cooled to the desired product storage temperature for transport. The TXV, which is located in the refrigerant circuit at the inlet to the evaporator coil, is a mechanical device using a thermal expansion bulb measuring refrigerant temperature leaving the evaporator to meter the refrigerant entering the evaporator, thereby adjusting and controlling the amount of refrigerant flow through the refrigerant circuit. The TXV is sized to be the largest possible yet most stable valve at the deep frozen condition.
However, when product which has not been pre-cooled, such as for example fresh fruits and vegetables direct from the field, is loaded into the container “hot”, that is at a temperature above the desired product storage temperature, such as for example directly from the field at ambient outdoor temperature, a substantial refrigeration load is imposed upon the transport refrigeration unit in pulling the temperature of the product down from ambient outdoor temperature to the desired product storage temperature. The TXV valve, being sized as noted above for the stable low box temperature condition, typically is undersized when the product is loaded into the container at a temperature above desired product storage temperature, typically referred to as the set point temperature.
Products applied hot require the refrigeration unit to pull the product temperature down to set point temperature, typically about 2° C. (about 36° F.) from product temperatures ranging as high as 38° C. (100° F.) or above. During pull down, the refrigerant unit requires high refrigerant mass flow to cool the product down as rapidly as possible. However, the refrigerant mass flow through the refrigerant circuit is limited by the TXV size required for low temperature stability. When product is loaded in the refrigerated container at temperatures higher than the desired product storage temperature, the TXV typically will respond by opening up to maintain a desired superheat. In the event the TXV reaches its maximum capacity the valve is no longer able to provide a stable or adequate superheat. As a result, the refrigeration capacity of the refrigeration unit will decrease and the evaporator superheat will rise above the level require for adequate cooling. Consequently, the time required to pull the product down to the set point temperature will increase. Sizing the TXV for pull down adversely affects the ability of refrigeration unit to provide stable temperature control at low set point temperatures because the TXV is too large for the required system mass flow rates. The orifice size being too large causes flooding of evaporator coil which negatively impacts product temperature control and stability.
The operating temperature range requirements associated with refrigerated freight containers have increased to the point where the TXV is limiting the performance of the cooling circuit. An electronic expansion valve (EXV) can achieve a larger range of temperature control than a TXV but is more costly and may become a reliability problem by itself and with the system because an EXV is not fail safe in the event power was inadvertently shut off while in operation.
Accordingly, it would be desirable to provide for increased refrigerant mass flow during product temperature pull down to increase refrigeration capacity without resorting to replacement of the TXV with an EXV and while maintaining reliability and keeping the system simple.
To increase the ability of the TXV to control the range from low temperature transport volumes to pull down conditions, a transport refrigerant unit is provided with a dual-path, parallel flow expansion circuit. The expansion circuit is inserted in the refrigerant circuit to increase the refrigerant mass flow during pull down. The expansion circuit includes a primary expansion device disposed in a primary refrigerant flow path and an auxiliary expansion device disposed in a secondary refrigerant flow path. The main refrigerant line from the condenser coil outlet to the evaporator coil forms the primary refrigerant flow path of the expansion circuit and the primary expansion device is the evaporator TXV disposed in this refrigerant line. The secondary refrigerant flow path of the expansion circuit comprises a bypass refrigerant line which connects at its inlet end to the refrigerant circuit upstream with respect to refrigerant flow of the evaporator TXV and at its outlet end to the refrigerant circuit downstream with respect to refrigerant flow of the evaporator TXV. The auxiliary expansion device and a bypass valve are disposed in the bypass line. The bypass line is shut off during low box temperature operation. The auxiliary expansion device may be a fixed orifice or an additional TXV. A controller opens the bypass valve when it is desired to allow refrigerant flow through the bypass line and closes the bypass valve when it is desired to pass refrigerant flow only through the TXV. In an embodiment, the fixed orifice is located within the bypass valve itself.
For a further understanding of these and objects of the invention, reference will be made to the following detailed description of the invention which is to be read in connection with the accompanying drawing, where:
Referring now to
As in conventional practice, refrigerant line 2 connects the discharge outlet of the compressor 20 in refrigerant flow communication with the inlet to the condenser heat exchanger coil 32, refrigerant line 4 connects the outlet of the condenser heat exchanger coil 32 in refrigerant flow communication with the inlet to the evaporator heat exchanger coil 42, and refrigerant line 6 connects the outlet of the evaporator heat exchanger coil 42 in refrigerant flow communication with the suction inlet of the compressor 20, thereby completing the refrigerant flow circuit. As depicted in the exemplary embodiments illustrated in
The refrigeration unit also includes an electronic controller 55 such as, for example an MicroLink™ controller available from Carrier Corporation of Syracuse, N.Y., USA. The electronic controller 55 is configured to operate the refrigeration unit 10 to maintain a predetermined thermal environment within the enclosed volume, termed a box, wherein the product is stored. The electronic controller 55 maintains the predetermined environment by selectively controlling the operation of the compressor 20, the condenser fan(s) 34 associated with the condenser heat exchanger coil 32, the evaporator fan(s) 44 associated with the evaporator heat exchanger coil 42, and the suction modulation valve 12. For example, when cooling of the environment within the box is required, the electronic controller 55 provides electrical power to activate the compressor 20, the condenser fan and the evaporator fan. Additionally, the electronic controller 55 adjusts the position of the suction modulation valve 12 to increase or decrease the flow of refrigerant supplied to the compressor 20 as appropriate to control and stabilize the temperature within the box at the set point temperature, which corresponds to the desired product storage temperature for the particular product stored within the box.
In the exemplary embodiment depicted in
In each of the embodiments depicted in
Referring now also to
In the embodiment depicted schematically in
In the embodiment depicted schematically in
When the refrigeration unit 10 is operating under normal load, that is operating to maintain a stable box temperature at a temperature set point equal to a desired product storage temperature for the particular product within the box with which the refrigeration unit is associated, the controller 55 maintains the bypass valve 74 in its normal closed position. Referring now to
However, when the temperature of the product within the box is above a predetermined temperature, for example when the product has been loaded into the box in a “hot” condition, the load will be considered to be in a pull down condition. When the refrigeration unit 10 is required to pull-down the temperature of, the controller 55 will energize the solenoid valve 74 to position the solenoid valve 74 in its open position, thereby permitting refrigerant to flow from section 4A of refrigerant line 4 through refrigerant line 8 into section 4B of refrigerant line 4 to pass through the evaporator heat exchanger coil 42 while bypass the TXV 50. Referring now to
The controller 55 may be configured to open and close the bypass solenoid valve 74 in response to evaporator or compressor suction superheat in addition to a fixed return air temperature range. A fixed temperature range can be used knowing the existing limitations of the current valve and system. At temperatures below this transition point, the controller 55 will de-energize the solenoid valve 74 thereby causing the solenoid valve 74 to move to its closed position, thereby closing refrigerant line 8. With the solenoid valve 74 closed, the mechanical evaporator TXV 50 will assume control of the amount of refrigerant flowing through the evaporator heat exchanger coil 42 as in conventional practice.
While the present invention has been particularly shown and described with reference to the preferred mode as illustrated in the drawing, it will be understood by one skilled in the art that various changes in detail may be effected therein without departing from the spirit and scope of the invention as defined by the claims.
Reference is made to and this application claims priority from and the benefit of U.S. Provisional Application Ser. No. 60/787,244, filed Mar. 30, 2006, and entitled TRANSPORT REFRIGERATION UNIT, which application is incorporated herein in its entirety by reference.
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/US07/05220 | 2/28/2007 | WO | 00 | 9/12/2008 |