The present disclosure concerns refrigeration systems, and more particularly to mechanical subcooling of transcritical R-744 refrigeration systems with heat pump heat reclaim and floating head pressure.
R-744 transcritical refrigeration systems are used in supermarkets to refrigerate or to maintain in frozen state perishable products, such as foodstuff.
However, a problem with conventional R-744 transcritical refrigeration systems consists mainly of their very low energy efficiency ratio (refrigeration capacity divided by consumed power).
For example, a R-744 transcritical refrigeration system operating at 21.2° F. evaporating temperature and gas leaving the gas cooler at 98.6° F. (ambient air temperature at 90° F.) will have an energy efficiency ratio of 6.09 while a R-507 refrigeration system operating under the same conditions will have an energy efficiency ratio of 10 which is almost 50% more efficient.
Accordingly, there is a need for a system and method for improving the energy efficiency ratio of transcritical R-744 refrigeration systems.
It is an object of the present disclosure to provide an improved transcritical R-744 refrigeration system with a higher energy efficiency ratio.
It is a further object of the present disclosure to provide a transcritical R-744 refrigeration system with an energy efficiency ratio (EER) of a level comparable to that of refrigeration systems using R-717, R-507, R-404a and other common refrigerants by mechanically subcooling of the R-744 refrigerant.
Accordingly, the present disclosure provides a mechanical subcooling system for use with a transcritical R-744 refrigeration system having at least one compressor for compressing R-744 vapors directed to a cooler operatively connected to a first throttling device, for reducing the pressure and temperature of the R-744 vapors to a level required for the normal operation of the R-744 refrigeration system, through a first heat exchanger, the first heat exchanger being operatively connected to the at least one compressor to provide the R-744 vapors to the at least one first compressor and to receive compressed R-744 vapors from the at least one first compressor, a by-pass valve for maintaining a required flow of R-744 vapors through the first heat exchanger, and a first receiver for receiving the R-744 vapors from the first throttling device, the first receiver being operatively connected to at least one defrost compressor, the mechanical subcooling system comprising:
The present disclosure further provides a transcritical R-744 refrigeration system including the above-described mechanical subcooling system.
The present disclosure also provides a method for improving the energy efficiency ratio of a transcritical R-744 refrigeration system having at least one compressor for compressing R-744 vapors directed to a cooler operatively connected to a first throttling device, for reducing the pressure and temperature of the R-744 vapors to a level required for the normal operation of the R-744 refrigeration system, through a first heat exchanger, the first heat exchanger being operatively connected to the at least one compressor to provide the R-744 vapors to the at least one first compressor and to receive compressed R-744 vapors from the at least one first compressor, a by-pass valve for maintaining a required flow of R-744 vapors through the first heat exchanger, and a first receiver for receiving the R-744 vapors from the first throttling device, the first receiver being operatively connected to at least one defrost compressor, the method comprising mechanically subcooling of the R-744 vapors leaving the cooler.
Embodiments of the disclosure will be described by way of examples only with reference to the accompanying drawing, in which:
Similar references used in different Figures denote similar components.
Generally stated, the non-limitative illustrative embodiment of the present disclosure provides a transcritical R-744 refrigeration system with an energy efficiency ratio (EER) of a level comparable to that of refrigeration systems using R-717, R-507, R-404a and other common refrigerants by mechanically subcooling of the R-744 refrigerant. Mechanical subcooling increases the refrigeration capacity without increasing the power consumption of the refrigeration system's compressors. The compressors used to provide the refrigeration capacity for the subcooling process operate at much more favorable conditions, therefore have a very high energy efficiency ratio. The result is higher refrigeration capacity and lower power consumption.
Referring to
In order to increase the energy efficiency ratio (EER) of typical transcritical R-744 refrigeration systems, such as the transcritical R-744 refrigeration systems 50 in
R-744 Transcritical Refrigeration System with Mechanical Subcooling
Referring now to
The compressors 2 are used for mechanical subcooling of the R-744 refrigerant leaving the cooler 11 through heat exchanger 3 or for heat reclaim through heat exchanger 4. Additional subcooling is provided for R-744 refrigerant leaving the receiver 14 by means of heat exchanger 43. The suction ports of compressors 2 are connected through motorized valves 9 and 44, and through conduits 26 and 48 to heat exchangers 3 and 43 or through motorized valve 10 and conduit 27 to heat exchanger 4.
When subcooling is required, valves 9 and 44 are open, and valve 10 is closed. Liquid R-744 is fed through conduits 23, 46 and 24 to expansion valves 8 and 45. The evaporation of the liquid R-744 in heat exchangers 3 and 43 absorbs heat from the R-744 refrigerant flowing through the other side of heat exchangers 3 and 43 (vapors in heat exchanger 3 and liquid in heat exchanger 43), thus reducing its temperature. The liquid R-744 is then fed through conduit 30 to throttling device 16 where its pressure and temperature are reduced to a level required for normal operation of the transcritical R-744 system 60 both at low and medium temperatures, and then is fed to receiver 17, which is operatively connected to the defrost compressors 18.
The evaporated R-744 refrigerant from heat exchangers 3 and 43 is fed through conduits 26 and 48, and through motorized valves 9 and 44 to the suction ports of compressors 2. The compressed R-744 vapors from compressors 2 are fed through heat exchanger 5 and conduit 39 to throttling device 6. From the throttling device 6 the R-744 vapors are fed through conduits 40 and 20 to cooler 11. The heat from the compressed R-744 vapors from compressors 2 is transferred in heat exchanger 5 to, for example, a glycol circulation system through conduits 41 and 42, and is used during the warm periods of the year for dehumidification purposes or water heating.
During colder periods of the year, where subcooling is not required, valves 8, 9, 44 and 45 are closed. Valves 7 and 10 are opened. Liquid R-744 is fed through conduits 23 and 47 to the expansion valve 7 and then to heat exchanger 4 where it evaporates and absorbs heat from the compressed R-744 vapors from compressors 1, which are fed through conduit 34, oil separator 31 and conduit 19 to heat exchanger 4.
The heat is then, by means of compressors 2, transferred in heat exchanger 5 to, for example, a glycol circulation system through conduits 41 and 42, and is used for comfort heating of the premises.
By using mechanical subcooling as disclosed above with a transcritical R-744 refrigeration system 60, the EER may go up to, for example, about 9.27 compared to the EER of a typical transcritical R-744 refrigeration system 50, which is about 6.09. The compressors 2 used for the mechanical subcooling have an energy efficiency ratio of about 14.00 due to their favorable operating conditions.
It is clear that the mechanical subcooling of R-744 transcritical refrigeration systems eliminates their major disadvantage of having low energy efficiency.
During the cold periods of the year, a transcritical R-744 refrigeration system with mechanical subcooling 60 can operate as a subcritical R-744 refrigeration system 50 and its energy efficiency then becomes similar to the energy efficiency of a Freon refrigeration system when the ambient air temperature is lower than about 12° C. (53.6° F.). No mechanical subcooling should be required during these periods. What is important, however, is that there is need of heat recuperation for comfort heating of the premises. The R-744 will provide heat but at a low temperature level of around 70° F., which is not appropriate for space heating.
During these periods the compressors 2 used for subcooling operate as a heat pump extracting heat from the refrigeration compressors 1 and elevate this heat to usable temperatures for space heating.
The mechanical subcooling is provided by the mechanical subcooling system 62, which can be incorporated into existing R-744 refrigeration systems, and consists of compressors 2, heat exchangers 3, 4 and 43, valves 6, 7, 8, 9, 10, 13, 37, 44 and 45, and receiver 14.
Although the present disclosure has been described with a certain degree of particularity and by way of an illustrative embodiments and examples thereof, it is to be understood that the present disclosure is not limited to the features of the embodiments described and illustrated herein, but includes all variations and modifications within the scope and spirit of the disclosure as hereinafter claimed.
This application claims the benefits of U.S. provisional patent application No. 61/602,276 filed on Feb. 23, 2012, which is herein incorporated by reference.
Number | Date | Country | |
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61602276 | Feb 2012 | US |