The present disclosure relates to transport refrigeration units and, more particularly, to all-electric transport refrigeration units.
Traditional refrigerated cargo trucks or refrigerated tractor trailers, such as those utilized to transport cargo via sea, rail, or road, is a truck, trailer or cargo container, generally defining a cargo compartment, and modified to include a refrigeration system located at one end of the truck, trailer, or cargo container. Refrigeration systems typically include a compressor, a condenser, an expansion valve, and an evaporator serially connected by refrigerant lines in a closed refrigerant circuit in accord with known refrigerant vapor compression cycles. A power unit, such as a combustion engine, drives the compressor of the refrigeration unit, and may be diesel powered, natural gas powered, or other type of engine. In many tractor trailer transport refrigeration systems, the compressor is driven by the engine shaft either through a belt drive or by a mechanical shaft-to-shaft link. In other systems, the engine of the refrigeration unit drives a generator that generates electrical power, which in-turn drives the compressor.
With current environmental trends, improvements in transport refrigeration units are desirable particularly toward aspects of environmental impact. With environmentally friendly refrigeration units, improvements in reliability, cost, and weight reduction are also desirable.
A transport refrigeration unit according to one, non-limiting, embodiment of the present disclosure includes a compressor constructed and arranged to compress a refrigerant; an electric compressor motor configured to drive the compressor; a generator configured to provide electric power to the compressor motor during standard set point conditions; and an energy storage device configured to supplement the electric power to the compressor motor during temperature pulldown conditions.
Additionally to the foregoing embodiment, the transport refrigeration unit includes at least one heat exchanger operatively coupled to the compressor; at least one fan configured to provide air flow over the at least one heat exchanger; and at least one electric fan motor configured to drive the at least one fan, and wherein the generator is configured to provide electric power to the at least one fan motor during standard set point conditions.
In the alternative or additionally thereto, in the foregoing embodiment, the transport refrigeration unit includes at least one heat exchanger operatively coupled to the compressor; at least one fan configured to provide air flow over the at least one heat exchanger; and at least one electric fan motor configured to drive the at least one fan, and wherein the energy storage device is configured to provide electric power to the at least one fan motor during standard set point conditions.
In the alternative or additionally thereto, in the foregoing embodiment, the energy storage device is configured to supplement the electric power to the at least one fan motor during temperature pulldown conditions.
In the alternative or additionally thereto, in the foregoing embodiment, the at least one heat exchanger includes an evaporator heat exchanger, the at least one fan includes an evaporator fan, and the at least one electric fan motor includes an evaporator fan motor.
In the alternative or additionally thereto, in the foregoing embodiment, the at least one heat exchanger includes a condenser heat exchanger, the at least one fan includes a condenser fan, and the at least one electric fan motor includes a condenser fan motor.
In the alternative or additionally thereto, in the foregoing embodiment, the refrigerant is a natural refrigerant.
In the alternative or additionally thereto, in the foregoing embodiment, the refrigerant is a natural refrigerant.
In the alternative or additionally thereto, in the foregoing embodiment, the energy storage device is a battery.
In the alternative or additionally thereto, in the foregoing embodiment, the battery has a voltage potential with a range of about 48V to 250V.
A method of operating a transport refrigeration unit according to another, non-limiting, embodiment includes utilizing one of an electric generator and an energy storage device to provide electric power generally during steady state conditions; and providing supplemental power from the other of the electric generator and the energy storage device during a temperature pull down state.
Additionally to the foregoing embodiment, the energy storage device is a battery.
In the alternative or additionally thereto, in the foregoing embodiment, the supplemental power is provided to a compressor motor.
In the alternative or additionally thereto, in the foregoing embodiment, the compressor motor is an alternating current motor and the supplemental power is delivered through an inverter.
In the alternative or additionally thereto, in the foregoing embodiment, the electric generator has a maximum power output that is less than a system power load during the temperature pull down state.
In the alternative or additionally thereto, in the foregoing embodiment, the method includes charging the energy storage device by the electric generator during part load operating conditions.
In the alternative or additionally thereto, in the foregoing embodiment, the method includes driving the electric generator by a combustion engine.
In the alternative or additionally thereto, in the foregoing embodiment, an evaporator fan motor and a condenser fan motor of the transport refrigeration unit are direct current motors.
In the alternative or additionally thereto, in the foregoing embodiment, the electric generator provides the power to a compressor motor, an evaporator fan motor and a condenser fan motor during steady state conditions.
In the alternative or additionally thereto, in the foregoing embodiment, the energy storage device provides the power to a compressor motor, an evaporator fan motor and a condenser fan motor during steady state conditions.
The foregoing features and elements may be combined in various combinations without exclusivity, unless expressly indicated otherwise. These features and elements as well as the operation thereof will become more apparent in light of the following description and the accompanying drawings. However, it should be understood that the following description and drawings are intended to be exemplary in nature and non-limiting.
Various features will become apparent to those skilled in the art from the following detailed description of the disclosed non-limiting embodiments. The drawings that accompany the detailed description can be briefly described as follows:
Referring to
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The transport refrigeration unit 26 may be an all-electric transport refrigeration unit 26, and may include a compressor 58, an electric compressor motor 60, a condenser heat exchanger 64 that may be air cooled, a condenser fan assembly 66, a receiver 68, a filter dryer 70, a heat exchanger 72, a thermostatic expansion valve 74, an evaporator heat exchanger 76, an evaporator fan assembly 78, a suction modulation valve 80, and a controller 82 that may include a computer-based processor (e.g., microprocessor). Operation of the transport refrigeration unit 26 may best be understood by starting at the compressor 58, where the suction gas (i.e., natural refrigerant) enters the compressor at a suction port 84 and is compressed to a higher temperature and pressure. The refrigerant gas is emitted from the compressor 58 at an outlet port 85 and may then flow into tube(s) 86 of the condenser heat exchanger 64.
Air flowing across a plurality of condenser coil fins (not shown) and the tubes 86, cools the gas to its saturation temperature. The air flow across the condenser heat exchanger 64 may be facilitated by one or more fans 88 of the condenser fan assembly 66. The condenser fans 88 may be driven by respective condenser fan motors 90 of the fan assembly 66 that may be electric.
By removing latent heat, the gas within the tubes 86 condenses to a high pressure and high temperature liquid and flows to the receiver 68 that provides storage for excess liquid refrigerant during low temperature operation. From the receiver 68, the liquid refrigerant may pass through a subcooler heat exchanger 92 of the condenser heat exchanger 64, through the filter-dryer 70 that keeps the refrigerant clean and dry, then to the heat exchanger 72 that increases the refrigerant subcooling, and finally to the thermostatic expansion valve 74.
As the liquid refrigerant passes through the orifices of the expansion valve 74, some of the liquid vaporizes into a gas (i.e., flash gas). Return air from the refrigerated space (i.e., cargo compartment 40) flows over the heat transfer surface of the evaporator heat exchanger 76. As the refrigerant flows through a plurality of tubes 94 of the evaporator heat exchanger 76, the remaining liquid refrigerant absorbs heat from the return air, and in so doing, is vaporized.
The evaporator fan assembly 78 includes one or more evaporator fans 96 that may be driven by respective fan motors 98 that may be electric. The air flow across the evaporator heat exchanger 76 is facilitated by the evaporator fans 96. From the evaporator heat exchanger 76, the refrigerant, in vapor form, may then flow through the suction modulation valve 80, and back to the compressor 58. A thermostatic expansion valve bulb sensor 100 may be located proximate to an outlet of the evaporator tube 94. The bulb sensor 100 is intended to control the thermostatic expansion valve 74, thereby controlling refrigerant superheat at an outlet of the evaporator tube 94. It is further contemplated and understood that the above generally describes a single stage vapor compression system that may be used for natural refrigerants such as propane and ammonia. Other refrigerant systems may also be applied that use carbon dioxide (CO2) refrigerant, and that may be a two-stage vapor compression system.
A bypass valve (not shown) may facilitate the flash gas of the refrigerant to bypass the evaporator heat exchanger 76. This will allow the evaporator coil to be filled with liquid and completely ‘wetted’ to improve heat transfer efficiency. With CO2 refrigerant, this bypass flash gas may be re-introduced into a mid-stage of a two-stage compressor.
The compressor 58 and the compressor motor 60 may be linked via an interconnecting drive shaft 102. The compressor 58, the compressor motor 60 and the drive shaft 102 may all be sealed within a common housing 104. In some embodiments, the compressor motor 60 may be positioned outside of the compressor housing 104, and therefore the interconnecting drive shaft 102 may pass through a shaft seal located in the compressor housing. The compressor 58 may be a single compressor. The single compressor may be a two-stage compressor, a scroll-type compressor or other compressors adapted to compress natural refrigerants. The natural refrigerant may be CO2, propane, ammonia, or any other natural refrigerant that may include a global-warming potential (GWP) of about one (1).
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In one example, the generator 54 and the battery or battery bank 52 may be electrically arranged in series. The electric power may be generally distributed through the bus 106, and may be direct current (DC). A converter (not shown) may be arranged at the outlet of the generator 54. The fan motors 90, 98 may be DC motors, and the compressor motor 60 may be an alternating current (AC) motor with an inverter (not shown) at the power input to the motor 60. In one example, the generator 54 may have a maximum power output of about 15 kW, the battery bank 52 may output electric power at about 10 kW, the steady state compressor motor 60 load may be about 10 kW, and the evaporator fan motor 98 and condenser fan motor 90 load may be about 2 kW. It is further contemplated and understood that various power conditioning devices may be configured throughout the transport refrigeration unit 26 depending upon the current type and voltage demands of any particular component.
In one embodiment, the generator 54 may be configured or downsized to provide substantially all of the electric power demands of the transport refrigeration unit 26 including the motors 60, 90, 98 during standard set point conditions (i.e., steady state conditions). However, when the transport refrigeration unit 26 is operating in a temperature pulldown state, the batteries 52 are available as a ‘battery boost’ to increase or supplement the DC power through the bus 106 thereby satisfying the temporary increase in power demand of, for example, the compressor motor 60. In this embodiment, the voltage potential of the batteries 52 may be about 5 kW to 7 kW.
In another embodiment, the batteries 52 may be configured to provide substantially all of the electric power demands of the transport refrigeration unit 26 including the motors 60, 90, 98 during standard set point conditions (i.e., steady state conditions). However, when the transport refrigeration unit 26 is operating in a temperature pulldown state, the generator 54 is available as a ‘battery boost’ to increase or supplement the DC power through the bus 106 thereby satisfying the temporary increase or surge in power demand of, for example, the compressor motor 60. In this embodiment, the voltage potential of the batteries 52 may be about 15 kW.
The transport refrigeration unit 26 may further include a battery charger 108 that may be powered by the generator 54 during part-load operating conditions of the transport refrigeration unit 26 (i.e., partial compressor load conditions), and controlled by the controller 82. The battery charger 108 may be controlled by the controller 82 and is configured to charge the batteries 52 when needed and during ideal operating conditions. By charging the batteries 52 during reduced compressor load conditions, the size and weight of the generator 54 and driving engine 56 may be minimized.
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Benefits of the present disclosure when compared to more traditional transport refrigeration units include lower fuel consumption, and a refrigeration unit that may emit less noise and may be lighter in weight. Yet further, the present disclosure includes an energy storage device that is conveniently and efficiently recharged to meet the power demands of the refrigeration unit while meeting combustion engine power and emission requirements that may be enforced by regulatory/government agencies.
While the present disclosure is described with reference to the figures, it will be understood by those skilled in the art that various changes may be made and equivalents may be substituted without departing from the spirit and scope of the present disclosure. In addition, various modifications may be applied to adapt the teachings of the present disclosure to particular situations, applications, and/or materials, without departing from the essential scope thereof. The present disclosure is thus not limited to the particular examples disclosed herein, but includes all embodiments falling within the scope of the appended claims.
Filing Document | Filing Date | Country | Kind |
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PCT/US2017/025911 | 4/4/2017 | WO | 00 |
Number | Date | Country | |
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62318602 | Apr 2016 | US |