This disclosure relates generally to a cooling system, such as a refrigeration system.
Cooling systems are used to cool spaces, such as residential dwellings, commercial buildings, and/or refrigeration units. These systems cycle a refrigerant (also referred to as charge) that is used to cool the spaces.
This disclosure contemplates an unconventional cooling system that uses an auxiliary cooling system to remove heat from a refrigerant during a power outage. The system directs refrigerant from a flash tank to an auxiliary cooling system during a power outage. The auxiliary cooling system removes heat from the refrigerant and directs the refrigerant back to the flash tank. In this manner, refrigerant in the cooling system is kept cool during a power outage, which reduces the amount of refrigerant lost from the system during the power outage in some embodiments. As a result, less maintenance needs to be performed on the system after the power outage. Certain embodiments of the system will be described below.
According to an embodiment, an apparatus includes a high side heat exchanger, a flash tank, a first load, a first compressor, an auxiliary cooling system, and a first check valve. The high side heat exchanger removes heat from a refrigerant. The flash tank stores the refrigerant from the high side heat exchanger. The first load uses the refrigerant to remove heat from a space proximate the first load. The first compressor compresses the refrigerant from the first load. The auxiliary cooling system removes heat from the refrigerant stored in the flash tank during a power outage. The first check valve directs the refrigerant between the first load and the first compressor back to the flash tank when the pressure of the refrigerant between the first load and the first compressor exceeds a threshold during the power outage.
According to another embodiment, a method includes removing, by a high side heat exchanger, heat from a refrigerant and storing, by a flash tank, the refrigerant from the high side heat exchanger. The method also includes using, by a first load, the refrigerant to remove heat from a space proximate the first load and compressing, by a first compressor, the refrigerant from the first load. The method further includes removing, by an auxiliary cooling system, heat from the refrigerant stored in the flash tank during a power outage and directing, by a first check valve, refrigerant between the first load and the first compressor back to the flash tank when the pressure of the refrigerant between the first load and the first compressor exceeds a threshold during the power outage.
According to yet another embodiment, a system includes a high side heat exchanger, a flash tank, a first load, a first compressor, an auxiliary heat exchanger, an auxiliary compressor, an auxiliary high side heat exchanger, an auxiliary generator, and a first check valve. The high side heat exchanger removes heat from a first refrigerant. The flash tank stores the first refrigerant from the high side heat exchanger. The first load uses the first refrigerant to remove heat from a space proximate the first load. The first compressor compresses the first refrigerant from the first load. The auxiliary heat exchanger transfers heat from the first refrigerant stored in the flash tank to a second refrigerant during a power outage. The auxiliary compressor compresses the second refrigerant. The auxiliary high side heat exchanger removes heat from the second refrigerant. The auxiliary generator powers the auxiliary compressor during the power outage. The first check valve directs the first refrigerant between the first load and the first compressor back to the flash tank when the pressure of the first refrigerant between the first load and the first compressor exceeds a threshold during the power outage.
Certain embodiments provide one or more technical advantages. For example, an embodiment reduces the amount of refrigerant lost from a cooling system during a power outage. As another example, an embodiment reduces the amount of maintenance needed on a cooling system after a power outage. Certain embodiments may include none, some, or all of the above technical advantages. One or more other technical advantages may be readily apparent to one skilled in the art from the figures, descriptions, and claims included herein.
For a more complete understanding of the present disclosure, reference is now made to the following description, taken in conjunction with the accompanying drawings, in which:
Embodiments of the present disclosure and its advantages are best understood by referring to
Cooling systems are used to cool spaces, such as residential dwellings, commercial buildings, and/or refrigeration units. These systems cycle a refrigerant (e.g., a carbon dioxide refrigerant) that is used to cool the spaces. In existing refrigeration systems, such as ones in grocery stores, refrigerant is cycled through various cooling cases to keep food cold. Generally, these refrigeration systems use two types of loads known as medium temperature loads and low temperature loads. The medium temperature loads may be produce shelves that keep a space cooled above freezing temperatures (e.g., above 32 degrees Fahrenheit), and the low temperature loads may be freezer cases that keep a space cooled below freezing temperatures (e.g., at or below 32 degrees Fahrenheit).
During a power outage, the refrigerant in the cooling system stops flowing and begins to absorb heat from the environment. Because the cooling system stops removing the heat from the refrigerant, the refrigerant becomes warmer and its pressure increases until the pressure trips a release valve, which causes the refrigerant to be released from the system. In some instances, enough refrigerant is lost from the system during the power outage that maintenance needs to be performed after the power outage to replenish the refrigerant in the system before the system can function normally.
This disclosure contemplates an unconventional cooling system that uses an auxiliary cooling system to remove heat from a refrigerant during a power outage. The system directs refrigerant from a flash tank to an auxiliary cooling system during a power outage. The auxiliary cooling system removes heat from the refrigerant and directs the refrigerant back to the flash tank. In this manner, refrigerant in the cooling system is kept cool during a power outage, which reduces the amount of refrigerant lost from the system during the power outage in some embodiments. As a result, less maintenance needs to be performed on the system after the power outage. The cooling system will be described in more detail using
High side heat exchanger 105 removes heat from a refrigerant. When heat is removed from the refrigerant, the refrigerant is cooled. This disclosure contemplates high side heat exchanger 105 being operated as a condenser and/or a gas cooler. When operating as a condenser, high side heat exchanger 105 cools the refrigerant such that the state of the refrigerant changes from a gas to a liquid. When operating as a gas cooler, high side heat exchanger 105 cools gaseous and/or supercritical refrigerant and the refrigerant remains a gas and/or a supercritical fluid. In certain configurations, high side heat exchanger 105 is positioned such that heat removed from the refrigerant may be discharged into the air. For example, high side heat exchanger 105 may be positioned on a rooftop so that heat removed from the refrigerant may be discharged into the air. As another example, high side heat exchanger 105 may be positioned external to a building and/or on the side of a building.
Flash tank 110 stores refrigerant received from high side heat exchanger 105. This disclosure contemplates flash tank 110 storing refrigerant in any state such as, for example, a liquid state and/or a gaseous state. Refrigerant leaving flash tank 110 is fed to low temperature load 120 and medium temperature load 115. In some embodiments, a flash gas and/or a gaseous refrigerant is released from flash tank 110. By releasing flash gas, the pressure within flash tank 110 may be reduced.
System 100 may include a low temperature portion and a medium temperature portion. The low temperature portion typically operates at a lower temperature than the medium temperature portion. In some refrigeration systems, the low temperature portion may be a freezer system and the medium temperature system may be a regular refrigeration system. In a grocery store setting, the low temperature portion may include freezers used to hold frozen foods, and the medium temperature portion may include refrigerated shelves used to hold produce. As seen in
Refrigerant flows from flash tank 110 to both the low temperature and medium temperature portions of the refrigeration system. For example, the refrigerant may flow to low temperature load 120 and medium temperature load 115. When the refrigerant reaches low temperature load 120 or medium temperature load 115, the refrigerant removes heat from the air around low temperature load 120 or medium temperature load 115. As a result, the air is cooled. The cooled air may then be circulated such as, for example, by a fan to cool a space such as, for example, a freezer and/or a refrigerated shelf. As refrigerant passes through low temperature load 120 and medium temperature load 115, the refrigerant may change from a liquid state to a gaseous state as it absorbs heat.
Refrigerant flows from low temperature load 120 and medium temperature load 115 to compressors 125 and 135. This disclosure contemplates system 100 including any number of low temperature compressors 125 and medium temperature compressors 135. The low temperature compressor 125 and medium temperature compressor 135 may be configured to increase the pressure of the refrigerant. As a result, the heat in the refrigerant may become concentrated and the refrigerant may become a high-pressure gas. Low temperature compressor 125 compresses refrigerant from low temperature load 120 and sends the compressed refrigerant to medium temperature compressor 135 or to desuperheater 130. Medium temperature compressor 135 compresses refrigerant from low temperature compressor 125, desuperheater 130, and/or medium temperature load 115. The refrigerant from low temperature compressor 125 mixes with and is cooled by the refrigerant from medium temperature load 115 before entering medium temperature compressor 135. Medium temperature compressor 135 may then send the compressed refrigerant to high side heat exchanger 105 or oil separator 140.
Desuperheater 130 is an optional component within system 100. Desuperheater 130 removes heat from the refrigerant compressed by low temperature compressor 125 before that refrigerant reaches medium temperature compressor 135. By removing heat from that refrigerant, desuperheater 130 allows medium temperature compressor 135 to operate more efficiently and effectively. In embodiments where desuperheater 130 is not present, the compressed refrigerant from low temperature compressor 125 is sent directly to medium temperature compressor 135.
Accumulator 130 is an optional component within system 100. Accumulator 130 can accumulate and separate liquid refrigerant from vapor refrigerant coming from medium temperature load 115 and only allow vapor refrigerant to reach medium temperature compressor 135. In this manner, liquid refrigerant may be prevented from entering medium temperature compressor 135, which improves the operation of and maintains the condition of medium temperature compressor 135. In embodiments where accumulator 130 is not present, refrigerant from medium temperature load 115 is sent directly to medium temperature compressor 135.
Oil separator 140 is another component within system 100. Oil separator 140 removes any dissolved oils from the refrigerant leaving medium temperature compressor 135 before that refrigerant is received at high side heat exchanger 105. By removing the oil from the refrigerant, that oil is prevented from clogging other components of system 100 as the refrigerant flows through system 100, which maintains the efficiency and operation of system 100. The removed oil can be collected and put back into one or more of compressors 125 and 135.
Bypass valve 145 controls the flow of gaseous refrigerant (e.g., a flash gas) from flash tank 110 to medium temperature compressor 135. By opening valve 145, the gaseous refrigerant is allowed to leave flash tank 110 and flow to medium temperature compressor 135. Closing valve 145 prevents the gaseous refrigerant from flowing from flash tank 110 to medium temperature compressor 135. By allowing gaseous refrigerant to leave flash tank 110, the pressure within flash tank 110 and the pressure at medium temperature compressor 135 can be regulated.
During a power outage one or more components of system 100 cease to operate. For example, low temperature compressor 125 and medium temperature compressor 135 may stop compressing the refrigerant in system 100. As a result, the refrigerant in system 100 stops flowing and heat in the refrigerant is not removed. Additionally, during the power outage the refrigerant in the system continues absorbing heat from the environment around cooling system 100 and the refrigerant grows warmer. As the refrigerant grows warmer, its pressure increases. Because the heat in the refrigerant is not removed during the power outage, the pressure of the refrigerant will increase until a pressure release valve is tripped. When the pressure release valve is tripped, the refrigerant in system 100 is released into the environment and lost from system 100. In some instances, enough refrigerant is lost during the power outage that maintenance needs to be performed after the power outage to replenish the refrigerant in system 100.
This disclosure contemplates auxiliary cooling system 150 removing the heat from the refrigerant in system 100 during a power outage. For example, auxiliary cooling system 150 may transfer heat from the refrigerant in system 100 to a second refrigerant in auxiliary cooling system 150. Auxiliary cooling system 150 then removes the heat from the second refrigerant. In some embodiments, auxiliary cooling system 150 is powered by an auxiliary generator during the power outage. In this manner, heat from the refrigerant in system 100 is removed during the power outage which maintains and/or reduces the pressures of the refrigerant such that the pressure release valve does not trip in some embodiments. As a result, less refrigerant is lost during the power outage and less maintenance may be required after the power outage. In some installations, auxiliary cooling system 150 can cycle through the refrigerant in system 100 in about half an hour and pull down the temperature of the refrigerant in flash tank 110. Auxiliary cooling system 150 will be described in more detail using
Check valve 155 directs refrigerant between medium temperature load 115 and medium temperature compressor 135 back to flash tank 110 when the pressure of that refrigerant exceeds a threshold during a power outage. Check valve 160 directs refrigerant between low temperature load 120 and low temperature compressor 125 back to flash tank 110 when the pressure of that refrigerant exceeds a threshold during the power outage. Each of check valves 155 and 160 can be configured to open when the pressure of the refrigerant between the loads 115 and 120 and compressors 125 and 135 exceeds certain thresholds. In some embodiments, these thresholds are set below the pressure at which the pressure release valve trips. As a result, the refrigerant is directed back to flash tank 110 so that it can be cooled by auxiliary cooling system 150 before the refrigerant pressure trips the pressure release valve. As a result, the amount of refrigerant in system 100 is maintained during the power outage.
Auxiliary high side heat exchanger 205 removes heat from the second refrigerant circulated in auxiliary cooling system 150. When heat is removed from the second refrigerant, the second refrigerant is cooled. This disclosure contemplates auxiliary high side heat exchanger 125 being operated as a condenser and/or a gas cooler. When operating as a condenser, high side heat exchanger 205 cools the refrigerant such that the state of the refrigerant changes from a gas to a liquid. When operating as a gas cooler, high side heat exchanger 205 cools gaseous and/or supercritical refrigerant and the refrigerant remains a gas and/or a supercritical fluid. In certain configurations, high side heat exchanger 205 is positioned such that heat removed from the refrigerant may be discharged into the air. For example, high side heat exchanger 205 may be positioned on a rooftop so that heat removed from the refrigerant may be discharged into the air. As another example, high side heat exchanger 205 may be positioned external to a building and/or on the side of a building.
Heat exchanger 210 transfers heat from the refrigerant from flash tank 110 to the second refrigerant circulated in auxiliary cooling system 150. In certain embodiments, heat exchanger 210 is a plate heat exchanger. Refrigerant from flash tank 110 enters heat exchanger 210 during a power outage. Heat exchanger 210 transfers heat from the refrigerant from flash tank 110 into the second refrigerant circulated in auxiliary cooling system 150. As a result, the refrigerant from flash tank 110 cools. As that refrigerant cools, its pressure decreases. In some embodiments, heat exchanger 210 lowers the pressure of the refrigerant from flash tank 110 such that a pressure release valve in system 100 does not trip during a power outage.
Auxiliary compressor 215 compresses the second refrigerant circulated in auxiliary cooling system 150. Compressor 215 may be configured to increase the pressure of the second refrigerant. As a result, the heat in the second refrigerant may become concentrated and the second refrigerant may become a high-pressure gas. Compressor 215 may then send the compressed refrigerant to high side heat exchanger 205.
Auxiliary generator 220 powers auxiliary compressor 215 during a power outage. Generator 220 may be any suitable generator such as, for example, a gas or solar generator. By providing power to auxiliary compressor 215, the second refrigerant is allowed to circulate in auxiliary cooling system 150 during a power outage. In this manner, the second refrigerant is capable of removing heat from the refrigerant from flash tank 110. That heat is then dispelled by auxiliary high side heat exchanger 205.
In certain embodiments, by removing heat from the refrigerant from flash tank 110, auxiliary cooling system 150 lowers the pressure of the refrigerant in system 100 during a power outage. As a result, the refrigerant is not lost through a pressure release valve. Additionally, less maintenance is required after the power outage to replenish the refrigerant in system 100.
A high side heat exchanger may begin method 300 by removing heat from a refrigerant in step 305. In step 310, a flash tank stores the refrigerant. A load then uses the refrigerant to remove heat from the space in step 315. In step 320, a compressor compresses the refrigerant.
After a power outage occurs, the refrigerant in the system may begin absorbing heat from the environment and its pressure may increase. In step 325, an auxiliary cooling system removes heat from the refrigerant stored in the flash tank during the power outage. The auxiliary cooling system may include a second refrigerant that absorbs the heat from the refrigerant in the cooling system. The heat in the second refrigerant is then removed from the second refrigerant. The auxiliary cooling system may be powered by a generator. In step 330, a check valve directs refrigerant back to the flash tank when the pressure of the refrigerant exceeds a threshold during the power outage. The check valve may be located between the load and the compressor. The threshold may be set such that it is below the pressure threshold of a pressure release valve. In this manner, the check valve directs the refrigerant back to the flash tank for auxiliary cooling before the pressure of the refrigerant trips the pressure release valve and the refrigerant is lost.
Modifications, additions, or omissions may be made to method 300 depicted in
Modifications, additions, or omissions may be made to the systems and apparatuses described herein without departing from the scope of the disclosure. The components of the systems and apparatuses may be integrated or separated. Moreover, the operations of the systems and apparatuses may be performed by more, fewer, or other components. Additionally, operations of the systems and apparatuses may be performed using any suitable logic comprising software, hardware, and/or other logic. As used in this document, “each” refers to each member of a set or each member of a subset of a set.
Although the present disclosure includes several embodiments, a myriad of changes, variations, alterations, transformations, and modifications may be suggested to one skilled in the art, and it is intended that the present disclosure encompass such changes, variations, alterations, transformations, and modifications as fall within the scope of the appended claims.
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