US20230408166A1 - Hot gas defrost system using hot gas from low temperature compressor - Google Patents
Hot gas defrost system using hot gas from low temperature compressor Download PDFInfo
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- US20230408166A1 US20230408166A1 US17/844,654 US202217844654A US2023408166A1 US 20230408166 A1 US20230408166 A1 US 20230408166A1 US 202217844654 A US202217844654 A US 202217844654A US 2023408166 A1 US2023408166 A1 US 2023408166A1
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- 239000003507 refrigerant Substances 0.000 claims abstract 38
- 238000005057 refrigeration Methods 0.000 claims abstract 31
- 230000008878 coupling Effects 0.000 claims 12
- 238000010168 coupling process Methods 0.000 claims 12
- 238000005859 coupling reaction Methods 0.000 claims 12
- 238000000034 method Methods 0.000 claims 9
- 238000011144 upstream manufacturing Methods 0.000 claims 6
- 239000007788 liquid Substances 0.000 claims 3
- 238000001816 cooling Methods 0.000 claims 1
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25D—REFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
- F25D21/00—Defrosting; Preventing frosting; Removing condensed or defrost water
- F25D21/06—Removing frost
- F25D21/12—Removing frost by hot-fluid circulating system separate from the refrigerant system
- F25D21/125—Removing frost by hot-fluid circulating system separate from the refrigerant system the hot fluid being ambient air
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B47/00—Arrangements for preventing or removing deposits or corrosion, not provided for in another subclass
- F25B47/02—Defrosting cycles
- F25B47/022—Defrosting cycles hot gas defrosting
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B1/00—Compression machines, plants or systems with non-reversible cycle
- F25B1/10—Compression machines, plants or systems with non-reversible cycle with multi-stage compression
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B41/00—Fluid-circulation arrangements
- F25B41/20—Disposition of valves, e.g. of on-off valves or flow control valves
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B5/00—Compression machines, plants or systems, with several evaporator circuits, e.g. for varying refrigerating capacity
- F25B5/02—Compression machines, plants or systems, with several evaporator circuits, e.g. for varying refrigerating capacity arranged in parallel
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2347/00—Details for preventing or removing deposits or corrosion
- F25B2347/02—Details of defrosting cycles
- F25B2347/021—Alternate defrosting
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/07—Details of compressors or related parts
- F25B2400/075—Details of compressors or related parts with parallel compressors
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/13—Economisers
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/23—Separators
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2600/00—Control issues
- F25B2600/25—Control of valves
- F25B2600/2519—On-off valves
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2700/00—Sensing or detecting of parameters; Sensors therefor
- F25B2700/19—Pressures
- F25B2700/197—Pressures of the evaporator
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2700/00—Sensing or detecting of parameters; Sensors therefor
- F25B2700/21—Temperatures
- F25B2700/2117—Temperatures of an evaporator
- F25B2700/21175—Temperatures of an evaporator of the refrigerant at the outlet of the evaporator
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B41/00—Fluid-circulation arrangements
- F25B41/30—Expansion means; Dispositions thereof
- F25B41/39—Dispositions with two or more expansion means arranged in series, i.e. multi-stage expansion, on a refrigerant line leading to the same evaporator
Definitions
- This disclosure relates generally to refrigeration systems. More particularly, in certain embodiments, this disclosure relates to hot gas defrost system using hot gas from low temperature compressor.
- Refrigeration systems are used to regulate environmental conditions within an enclosed space. Refrigeration systems are used for a variety of applications, such as in supermarkets and warehouses, to cool stored items. For example, refrigeration systems may provide cooling operations for refrigerators and freezers.
- a refrigeration system that facilitates improved evaporator defrost using discharge gas from one or more low-temperature (LT) compressors located downstream of a low temperature portion of the refrigeration system. While one or a portion of the evaporators of the refrigeration system are operating in a normal refrigeration mode, other evaporator(s) can be operated in a defrost mode using hot gas produced by the refrigeration process.
- a check valve is positioned in refrigerant conduit connecting an outlet of the LT compressor(s) to a flash tank and is configured to open if a pressure of refrigerant from the LT compressor(s) exceeds a threshold value.
- a refrigeration system includes a plurality of evaporators that include at least one low-temperature evaporator and at least one medium-temperature evaporator.
- the refrigeration system includes one or more low-temperature compressors configured to compress refrigerant received from the at least one low-temperature evaporator.
- the refrigeration system includes one or more medium-temperature compressors configured to compress refrigerant received from the at least one medium-temperature evaporator.
- the refrigeration system includes a controllable valve positioned downstream from the one or more low-temperature compressors.
- FIG. 1 is a diagram of an example refrigeration system of this disclosure configured to operate evaporators in a refrigeration mode
- FIG. 2 is a diagram of the example refrigeration system of FIG. 1 configured to operate an evaporator in a defrost mode
- FIG. 3 is a flowchart of an example method of operating the refrigeration system of FIGS. 1 and 2 to provide improved evaporator defrost.
- the refrigeration system of this disclosure provides improvements in defrost performance and energy efficiency.
- the refrigeration system of this disclosure may be a CO 2 refrigeration system.
- CO 2 refrigeration systems may differ from conventional refrigeration systems in that these systems circulate refrigerant that may become a supercritical fluid (i.e., where distinct liquid and gas phases are not present) above the critical point.
- the critical point for carbon dioxide (CO 2 ) is 31° C. and 73.8 MPa, and above this point, CO 2 becomes a homogenous mixture of vapor and liquid that is called a supercritical fluid.
- This unique characteristic of transcritical refrigerants is associated with certain operational differences between transcritical and conventional refrigeration systems.
- transcritical refrigerants are typically associated with discharge temperatures that are higher than their critical temperatures and discharge pressures that are higher than their critical pressures.
- the refrigerant may become a “supercritical fluid”—a homogenous mixture of gas and liquid.
- Supercritical fluid does not undergo phase change process (vapor to liquid) in a gas cooler as occurs in a condenser of a conventional refrigeration system circulating traditional refrigerant. Rather, supercritical fluid cools down to a lower temperature in the gas cooler.
- the gas cooler in a CO 2 transcritical refrigeration system may receive and cool supercritical fluid, and the transcritical refrigerant undergoes a partial state change from gas to liquid as it is discharged from an expansion valve.
- FIGS. 1 and 2 illustrate an example refrigeration system 100 configured for improved defrost operation.
- the refrigeration system 100 shown in FIG. 1 is configured to operate evaporators 116 , 128 in a refrigeration mode, such that the evaporators 116 , 128 provide cooling to a corresponding space, such as a freezer and deep freeze, respectively (not shown for clarity and conciseness).
- FIG. 2 illustrates the example refrigeration system 100 when configured for operation of evaporator 128 in a defrost mode, such that evaporator 128 is defrosted and evaporator 116 still provides cooling to a space.
- refrigerant from one or more low-temperature (LT) compressors 138 is provided to the evaporators 116 , 128 to facilitate defrosting of the evaporators 116 , 128 .
- the refrigerant removes ice buildup from coils of the evaporator(s) 116 , 128 .
- Refrigeration system 100 includes one or more medium-temperature (MT) compressors 102 , refrigerant conduit subsystem 104 , controllable valve 106 , check valve 118 , gas cooler 108 , flash tank 112 , one or more MT evaporators 116 and corresponding valves 114 , 120 , 122 , 124 , one or more LT evaporators 128 and corresponding valves 126 , 132 , 134 , 136 , one or more LT compressors 138 , a valve 140 , a flash-gas bypass valve 142 , and controller 150 .
- refrigeration system 100 is a transcritical refrigeration system that circulates a transcritical refrigerant such as CO 2 .
- Valve 106 is generally a motorized or otherwise electronically controllable valve, such as a motorized ball valve, solenoid valve, or the like. Valve 106 receives compressed refrigerant from the LT compressor(s) 128 and is adjustable to control flow of refrigerant towards one or more of the MT and/or LT evaporators 116 , 128 to provide defrost.
- the controller 150 is in communication with valve 106 and controls its operation.
- valve 140 may adjust the pressure of refrigerant provided to the flash tank 112 as appropriate to facilitate refrigerant flow as illustrated in FIG. 2 .
- the first valve 114 upstream of the evaporator 116 is open and the second valve 120 downstream of the evaporator 116 is open.
- the third valve 124 and fourth valve 122 are both closed.
- the liquid refrigerant from flash tank 112 flows through expansion valve 114 , where the pressure of the refrigerant is decreased, before it reaches the evaporator 116 .
- Expansion valve 114 may be configured to achieve a refrigerant temperature into the evaporator 116 at a predefined temperature for a given application (e.g., about ⁇ 6° C.).
- Refrigerant from the MT evaporator 116 that is operating in refrigeration mode is provided to the one or more MT compressors 102 .
- valve 106 When the MT evaporator 116 is operated in the defrost mode (not shown for conciseness), valve 106 is adjusted such that at least a portion of compressed refrigerant from the LT compressor(s) 138 is directed towards the MT evaporator 116 .
- the first valve 114 upstream of the evaporator 116 is closed, and the second valve 120 downstream of the evaporator 116 is closed.
- Third valve 124 and fourth valve 122 are opened to allow flow of compressed refrigerant from the valve 106 toward the MT evaporator 116 .
- heated refrigerant from LT compressor(s) 138 flows through the evaporator 116 and defrosts the evaporator 116 .
- Expansion valve 140 expands the refrigerant (i.e., decreases pressure of the refrigerant) before it flows back into the flash tank 112 .
- Expansion valve 140 may be the same as or similar to expansion valve 114 , described above.
- the controller 150 may end defrost mode operation and return to refrigeration mode operation by closing valves 122 and 124 and opening valves 114 and 120 .
- the controller 150 may cause defrost mode to end after a predefined period of time included in the instructions 158 and/or schedule 162 .
- the controller 150 may cause defrost mode operation to end after predefined conditions indicated in the instructions 158 are reached (e.g., after a temperature and/or pressure 160 measured by sensor 144 reaches a threshold 164 ).
- the LT evaporator 128 is generally similar to the MT evaporator 116 but is configured to operate at lower temperatures (e.g., for deep freezing applications near about ⁇ 30° C. or the like). When operated in refrigeration mode (see FIG. 1 ), the LT evaporator 128 receives cooled liquid refrigerant from the flash tank 112 and uses the cooled refrigerant to provide cooling. As an example, the evaporator 128 may be part of a deep freezer for relatively long-term storage of perishable items that must be kept at particular temperatures. For clarity and conciseness, the components of a single LT evaporator 128 are illustrated.
- the refrigeration system 100 may include any appropriate number of LT evaporators 128 with corresponding valves 126 , 132 , 134 , 136 .
- the LT evaporator 128 includes valves 126 , 132 , 134 , 136 to facilitate operation of the LT evaporator 128 in a refrigeration mode (see FIG. 1 ) and a defrost mode (see FIG. 2 ).
- Valve 126 may be an expansion valve that is the same as or similar to valve 114 , described above. Expansion valve 126 may be configured to receive liquid refrigerant from flash tank 112 and reduce the pressure of the received refrigerant. In some embodiments, this reduction in pressure causes some of the refrigerant to vaporize.
- the valve 106 is adjusted such that at least a portion of compressed refrigerant from the LT compressor(s) 138 is directed towards the LT evaporator 128 .
- the first valve 126 upstream of the evaporator 128 is closed, and the second valve 132 downstream of the evaporator 128 is closed.
- Third valve 136 and fourth valve 134 are opened to allow flow of compressed refrigerant from the valve 106 toward the LT evaporator 128 .
- heated refrigerant from LT compressor(s) 138 flows through the evaporator 128 and defrosts the evaporator 128 .
- Refrigerant exiting the evaporator 128 flows through the opened valve 136 and to optional expansion valve 140 , described above.
- the controller 150 may end defrost mode operation and return to refrigeration mode operation by closing valves 134 and 136 and opening valves 126 and 132 , as shown in the example of FIG. 1 .
- the controller 150 may cause defrost mode to end after a predefined period of time included in the instructions 158 and/or schedule 162 .
- the controller 150 may cause defrost mode operation to end after predefined conditions indicated in the instructions 158 are reached (e.g., after a temperature and/or pressure 160 measured by sensor 146 reaches a threshold 164 ).
- instructions 158 stored by the controller 150 may indicate that defrost mode operation is needed on a certain schedule 162 or at a certain time.
- a temperature and/or pressure 160 of the evaporators 116 , 128 may indicate that defrost mode operation is needed (e.g., because the temperature and/or pressure 160 indicates that expected cooling performance or efficiency is not being obtained).
- a check valve 118 is positioned in refrigerant conduit of the conduit subsystem 104 coupling an outlet of the LT compressor(s) 138 to an inlet of the flash tank 112 .
- the check valve 118 is configured to allow flow of refrigerant from the LT compressor(s) 138 to the flash tank 112 when a pressure difference across the check valve exceeds a threshold value (e.g., of about 6 bar to 10 bar).
- a threshold value e.g., of about 6 bar to 10 bar.
- the check valve 118 is a one-way valve and prevents flow from the flash tank 112 to the conduit subsystem 104 connecting to the LT compressor(s) 138 and only allows flow to the flash tank 112 if a threshold pressure is reached. If the pressure difference across the check valve 118 is below the threshold value, flow is prevented to the flash tank 112 .
- Flash gas bypass valve 142 may be located in refrigerant conduit of the conduit subsystem 104 connecting the flash tank 112 to the MT compressor(s) 102 and configured to open and close to permit or restrict the flow of flash gas discharged from flash tank 112 .
- controller 150 controls the opening and closing of flash gas bypass valve 142 . As depicted in FIGS. 1 and 2 , closing flash gas bypass valve 142 may restrict flash gas from flowing to MT compressor(s) 102 , and opening flash gas bypass valve 142 may permit flow of flash gas to MT compressor(s) 102 .
- the processor 152 may be a programmable logic device, a microcontroller, a microprocessor, or any suitable combination of the preceding.
- the processor 152 is communicatively coupled to and in signal communication with the memory 154 .
- the one or more processors are configured to process data and may be implemented in hardware or software.
- the processor 152 may be 8-bit, 16-bit, 32-bit, 64-bit or of any other suitable architecture.
- the I/O interface 156 may provide and/or receive, for example, compressor speed signals, compressor on/off signals, valve open/close signals, temperature signals, pressure signals, temperature setpoints, environmental conditions, and an operating mode status for the refrigeration system 100 and send electrical signals to the components of the refrigeration system 100 .
- the I/O interface 156 may include ports or terminals for establishing signal communications between the controller 150 and other devices.
- the I/O interface 156 may be configured to enable wired and/or wireless communications.
- refrigeration system 100 may include any suitable components.
- refrigeration system 100 may include one or more additional sensors configured to detect temperature and/or pressure information.
- the controller 150 causes the evaporator 116 , 128 determined at operation 304 to be operated in the defrost mode. For instance, if defrost of the LT evaporator 128 is needed, the controller 150 may cause the valve 106 to allow a portion of refrigerant from the LT compressor(s) 138 to flow towards the LT evaporator 128 . First valve 126 and second valve 132 are closed, and third valve 136 and fourth valve 134 are opened. This achieves the defrost mode configuration of evaporator 128 illustrated in FIG. 2 .
- Method 300 may include more, fewer, or other operations. For example, operations may be performed in parallel or in any suitable order. While at times discussed as controller 150 , refrigeration system 100 , or components thereof performing the operations, any suitable refrigeration system or components of the refrigeration system may perform one or more operations of the method 300 .
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Abstract
A refrigeration system includes at least one low-temperature evaporator, at least one medium-temperature evaporator, one or more low-temperature compressors, and one or more medium-temperature compressors. A controllable valve positioned downstream from the one or more low-temperature compressors directs flow of refrigerant from the low-temperature compressor(s) to one or both of (i) the medium-temperature compressor(s) and (ii) one or more evaporators based on an operation mode of evaporators. A controller is communicatively coupled to the controllable valve. A controller determines that operation of a first evaporator in a defrost mode is indicated and causes the first evaporator to operate in the defrost mode by adjusting the controllable valve to direct a portion of the received compressed refrigerant to the first evaporator.
Description
- This disclosure relates generally to refrigeration systems. More particularly, in certain embodiments, this disclosure relates to hot gas defrost system using hot gas from low temperature compressor.
- Refrigeration systems are used to regulate environmental conditions within an enclosed space. Refrigeration systems are used for a variety of applications, such as in supermarkets and warehouses, to cool stored items. For example, refrigeration systems may provide cooling operations for refrigerators and freezers.
- During operation of refrigeration systems, ice may build up on evaporators. These evaporators need to be defrosted to remove ice buildup and prevent loss of performance. Previous evaporator defrost processes are limited in terms of their efficiency and effectiveness. For example, using previous technology, defrost processes may take a relatively long time and consume a relatively large amount of energy. In some cases, previous technology may be incapable of providing adequate defrosting, for instance, in cases where a relatively large number of evaporators need to be defrosted in a multiple-evaporator refrigeration system.
- This disclosure provides technical solutions to the problems of previous technology, including those described above. For example, a refrigeration system is described that facilitates improved evaporator defrost using discharge gas from one or more low-temperature (LT) compressors located downstream of a low temperature portion of the refrigeration system. While one or a portion of the evaporators of the refrigeration system are operating in a normal refrigeration mode, other evaporator(s) can be operated in a defrost mode using hot gas produced by the refrigeration process. A check valve is positioned in refrigerant conduit connecting an outlet of the LT compressor(s) to a flash tank and is configured to open if a pressure of refrigerant from the LT compressor(s) exceeds a threshold value. Embodiments of this disclosure may provide improved defrost operations to evaporators of refrigeration systems, such as CO2 refrigeration systems. In certain embodiments, the refrigeration system does not require specialized high pressure evaporator components because hot gas is provided at a moderate pressure from the LT compressor(s). In certain embodiments, system complexity and cost is decreased, for example, because a pressure-regulating valve is not used at the discharge of the LT compressor(s). 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.
- In an embodiment, a refrigeration system includes a plurality of evaporators that include at least one low-temperature evaporator and at least one medium-temperature evaporator. The refrigeration system includes one or more low-temperature compressors configured to compress refrigerant received from the at least one low-temperature evaporator. The refrigeration system includes one or more medium-temperature compressors configured to compress refrigerant received from the at least one medium-temperature evaporator. The refrigeration system includes a controllable valve positioned downstream from the one or more low-temperature compressors. The controllable valve is configured to receive the compressed refrigerant from the one or more low-temperature compressors and direct flow of the received refrigerant to one or both of (i) the one or more medium-temperature compressors positioned downstream from the controllable valve and (ii) one or more evaporators of the plurality of evaporators based on an operation mode of the plurality of evaporators. A controller is communicatively coupled to the controllable valve. The controller determines that operation of a first evaporator of the plurality of evaporators in a defrost mode is indicated and, after determining that operation of the first evaporator in the defrost mode is indicated, causes the first evaporator to operate in the defrost mode by adjusting the controllable valve to direct a portion of the received compressed refrigerant to the first evaporator.
- 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:
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FIG. 1 is a diagram of an example refrigeration system of this disclosure configured to operate evaporators in a refrigeration mode; -
FIG. 2 is a diagram of the example refrigeration system ofFIG. 1 configured to operate an evaporator in a defrost mode; and -
FIG. 3 is a flowchart of an example method of operating the refrigeration system ofFIGS. 1 and 2 to provide improved evaporator defrost. - Embodiments of the present disclosure and its advantages are best understood by referring to
FIGS. 1-3 of the drawings, like numerals being used for like and corresponding parts of the various drawings. - As described above, prior to this disclosure, defrost operations of refrigeration systems suffered from certain inefficiencies and drawbacks. The refrigeration system of this disclosure provides improvements in defrost performance and energy efficiency. The refrigeration system of this disclosure may be a CO2 refrigeration system. CO2 refrigeration systems may differ from conventional refrigeration systems in that these systems circulate refrigerant that may become a supercritical fluid (i.e., where distinct liquid and gas phases are not present) above the critical point. As an example, the critical point for carbon dioxide (CO2) is 31° C. and 73.8 MPa, and above this point, CO2 becomes a homogenous mixture of vapor and liquid that is called a supercritical fluid. This unique characteristic of transcritical refrigerants is associated with certain operational differences between transcritical and conventional refrigeration systems. For example, transcritical refrigerants are typically associated with discharge temperatures that are higher than their critical temperatures and discharge pressures that are higher than their critical pressures. When a transcritical refrigerant is at or above its critical temperature and/or pressure, the refrigerant may become a “supercritical fluid”—a homogenous mixture of gas and liquid. Supercritical fluid does not undergo phase change process (vapor to liquid) in a gas cooler as occurs in a condenser of a conventional refrigeration system circulating traditional refrigerant. Rather, supercritical fluid cools down to a lower temperature in the gas cooler. Stated differently, the gas cooler in a CO2 transcritical refrigeration system may receive and cool supercritical fluid, and the transcritical refrigerant undergoes a partial state change from gas to liquid as it is discharged from an expansion valve.
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FIGS. 1 and 2 illustrate anexample refrigeration system 100 configured for improved defrost operation. Therefrigeration system 100 shown inFIG. 1 is configured to operateevaporators evaporators FIG. 2 illustrates theexample refrigeration system 100 when configured for operation ofevaporator 128 in a defrost mode, such thatevaporator 128 is defrosted andevaporator 116 still provides cooling to a space. When at least one of theevaporators compressors 138 is provided to theevaporators evaporators -
Refrigeration system 100 includes one or more medium-temperature (MT)compressors 102,refrigerant conduit subsystem 104,controllable valve 106,check valve 118,gas cooler 108,flash tank 112, one ormore MT evaporators 116 andcorresponding valves more LT evaporators 128 andcorresponding valves more LT compressors 138, avalve 140, a flash-gas bypass valve 142, andcontroller 150. In some embodiments,refrigeration system 100 is a transcritical refrigeration system that circulates a transcritical refrigerant such as CO2. - The MT compressor(s) 102 are configured to compress refrigerant discharged from the MT evaporator(s) 116 that are operating in refrigeration mode (as shown in
FIGS. 1 and 2 ) and provide supplemental compression to refrigerant discharged from any of theLT evaporators 128 that are operating in refrigeration mode (as shown inFIG. 1 ).Refrigeration system 100 may include any suitable number ofMT compressors 102. MT compressor(s) 102 may vary by design and/or by capacity. For example, some compressor designs may be more energy efficient than other compressor designs, and someMT compressors 102 may have modular capacity (e.g., a capability to vary capacity). Thecontroller 150 is in communication with theMT compressors 102 and controls their operation. -
Refrigerant conduit subsystem 104 facilitates the movement of refrigerant (e.g., CO2) through a refrigeration cycle such that the refrigerant flows in the refrigeration mode as illustrated by the arrows inFIG. 1 . Therefrigerant conduit subsystem 104 includes conduit, tubing, and the like that facilitates the movement of refrigerant between components of therefrigeration system 100. - Valve 106 is generally a motorized or otherwise electronically controllable valve, such as a motorized ball valve, solenoid valve, or the like. Valve 106 receives compressed refrigerant from the LT compressor(s) 128 and is adjustable to control flow of refrigerant towards one or more of the MT and/or
LT evaporators controller 150 is in communication withvalve 106 and controls its operation. -
Gas cooler 108 is generally operable to receive refrigerant (e.g., from MT compressor(s) 102) and apply a cooling stage to the received refrigerant. In some embodiments,gas cooler 108 is a heat exchanger comprising cooler tubes configured to circulate the received refrigerant and coils through which ambient air is forced. Insidegas cooler 108, the coils may absorb heat from the refrigerant, thereby cooling the refrigerant. -
Flash tank 112 is configured to receive mixed-state refrigerant and separate the received refrigerant into flash gas and liquid refrigerant.Flash tank 112 may include one or more tanks operable to hold refrigerant at least temporarily. Typically, the flash gas collects near the top offlash tank 112, and the liquid refrigerant is collected in the bottom offlash tank 112. Avalve 110 may be disposed at or near an inlet of theflash tank 112 to reduce pressure of refrigerant received by theflash tank 112. When bothevaporators FIG. 1 ), the liquid refrigerant flows fromflash tank 112 and provides cooling to theMT evaporator 116 andLT evaporator 128. When evaporator 128 is operated in defrost mode (seeFIG. 2 ), hot gas refrigerant provided to defrostevaporator 128 is provided toflash tank 112.Valve 140 may adjust the pressure of refrigerant provided to theflash tank 112 as appropriate to facilitate refrigerant flow as illustrated inFIG. 2 . - When operated in refrigeration mode (see
FIG. 1 ), theMT evaporator 116 receives cooled liquid refrigerant from theflash tank 112 and uses the cooled refrigerant to provide cooling. As an example, theevaporator 116 may be part of a refrigerated case and/or cooler for storing items that must be kept at particular temperatures. Therefrigeration system 100 may include any appropriate number ofMT evaporators 116 with the same or a similar configuration to that shown for theexample MT evaporator 116 shown inFIGS. 1 and 2 . - Each of the one or
more MT evaporators 116 has correspondingvalves MT evaporator 116 in a refrigeration mode and a defrost mode.Valve 114 may be an expansion valve.Expansion valve 114 may be configured to receive liquid refrigerant fromflash tank 112 and reduce the pressure of the received refrigerant. In some embodiments, this reduction in pressure causes some of the refrigerant to vaporize.Valves controller 150 is in communication withvalves - When the
MT evaporator 116 is operated in the refrigeration mode illustrated inFIGS. 1 and 2 , thefirst valve 114 upstream of theevaporator 116 is open and thesecond valve 120 downstream of theevaporator 116 is open. Thethird valve 124 andfourth valve 122 are both closed. In this configuration, the liquid refrigerant fromflash tank 112 flows throughexpansion valve 114, where the pressure of the refrigerant is decreased, before it reaches theevaporator 116.Expansion valve 114 may be configured to achieve a refrigerant temperature into theevaporator 116 at a predefined temperature for a given application (e.g., about −6° C.). Refrigerant from the MT evaporator 116 that is operating in refrigeration mode is provided to the one ormore MT compressors 102. - When the
MT evaporator 116 is operated in the defrost mode (not shown for conciseness),valve 106 is adjusted such that at least a portion of compressed refrigerant from the LT compressor(s) 138 is directed towards theMT evaporator 116. Thefirst valve 114 upstream of theevaporator 116 is closed, and thesecond valve 120 downstream of theevaporator 116 is closed.Third valve 124 andfourth valve 122 are opened to allow flow of compressed refrigerant from thevalve 106 toward theMT evaporator 116. In this configuration, heated refrigerant from LT compressor(s) 138 flows through theevaporator 116 and defrosts theevaporator 116. Refrigerant exiting theevaporator 116 flows through the openedvalve 124 and tooptional expansion valve 140.Expansion valve 140, if present, expands the refrigerant (i.e., decreases pressure of the refrigerant) before it flows back into theflash tank 112.Expansion valve 140 may be the same as or similar toexpansion valve 114, described above. - Once defrost mode operation is complete, the
controller 150 may end defrost mode operation and return to refrigeration mode operation by closingvalves valves controller 150 may cause defrost mode to end after a predefined period of time included in theinstructions 158 and/orschedule 162. In some embodiments, thecontroller 150 may cause defrost mode operation to end after predefined conditions indicated in theinstructions 158 are reached (e.g., after a temperature and/orpressure 160 measured bysensor 144 reaches a threshold 164). - The
LT evaporator 128 is generally similar to theMT evaporator 116 but is configured to operate at lower temperatures (e.g., for deep freezing applications near about −30° C. or the like). When operated in refrigeration mode (seeFIG. 1 ), theLT evaporator 128 receives cooled liquid refrigerant from theflash tank 112 and uses the cooled refrigerant to provide cooling. As an example, theevaporator 128 may be part of a deep freezer for relatively long-term storage of perishable items that must be kept at particular temperatures. For clarity and conciseness, the components of asingle LT evaporator 128 are illustrated. Therefrigeration system 100 may include any appropriate number ofLT evaporators 128 withcorresponding valves - The
LT evaporator 128 includesvalves LT evaporator 128 in a refrigeration mode (seeFIG. 1 ) and a defrost mode (seeFIG. 2 ).Valve 126 may be an expansion valve that is the same as or similar tovalve 114, described above.Expansion valve 126 may be configured to receive liquid refrigerant fromflash tank 112 and reduce the pressure of the received refrigerant. In some embodiments, this reduction in pressure causes some of the refrigerant to vaporize.Valves valve controller 150 is in communication withvalves - When the
LT evaporator 128 is operated in the refrigeration mode illustrated inFIG. 1 , thefirst valve 126 upstream of theevaporator 128 is open and thesecond valve 132 downstream of theevaporator 128 is open. Thethird valve 136 andfourth valve 134 are both closed. In this configuration, the liquid refrigerant fromflash tank 112 flows throughexpansion valve 126, where the pressure of the refrigerant is decreased, before it reaches theevaporator 128.Expansion valve 126 may be configured to achieve a refrigerant temperature into theevaporator 128 at a predefined temperature for a given application (e.g., about −30° C.). Refrigerant from theLT evaporator 128 that is operating in refrigeration mode is provided to the one ormore LT compressors 138. - When the
LT evaporator 128 is operated in the defrost mode ofFIG. 2 , thevalve 106 is adjusted such that at least a portion of compressed refrigerant from the LT compressor(s) 138 is directed towards theLT evaporator 128. Thefirst valve 126 upstream of theevaporator 128 is closed, and thesecond valve 132 downstream of theevaporator 128 is closed.Third valve 136 andfourth valve 134 are opened to allow flow of compressed refrigerant from thevalve 106 toward theLT evaporator 128. In this configuration, heated refrigerant from LT compressor(s) 138 flows through theevaporator 128 and defrosts theevaporator 128. Refrigerant exiting theevaporator 128 flows through the openedvalve 136 and tooptional expansion valve 140, described above. - Once defrost mode operation is complete, the
controller 150 may end defrost mode operation and return to refrigeration mode operation by closingvalves valves FIG. 1 . In some embodiments, thecontroller 150 may cause defrost mode to end after a predefined period of time included in theinstructions 158 and/orschedule 162. In some embodiments, thecontroller 150 may cause defrost mode operation to end after predefined conditions indicated in theinstructions 158 are reached (e.g., after a temperature and/orpressure 160 measured bysensor 146 reaches a threshold 164). - The temperature and/or
pressure sensors evaporators evaporators sensors pressure 160 measured bysensors MT evaporator 116 and/orLT evaporator 128, defrost mode operation may be indicated. In some cases, defrost mode operation is determined to be indicated based on a schedule 162 (e.g., defrost mode operation may be performed at certain predefined time intervals or at certain times). -
Valves MT evaporator 116 andvalves LT evaporator 128 may be in communication withcontroller 150, and thecontroller 150 may provide instructions for adjusting thesevalves instructions 158 implemented by theprocessor 152 of thecontroller 150 may determine that operation of theMT evaporator 116 and/or theLT evaporator 128 in a defrost mode is indicated. For example,instructions 158 stored by thecontroller 150 may indicate that defrost mode operation is needed on acertain schedule 162 or at a certain time. As another example, a temperature and/orpressure 160 of theevaporators pressure 160 indicates that expected cooling performance or efficiency is not being obtained). - A
check valve 118 is positioned in refrigerant conduit of theconduit subsystem 104 coupling an outlet of the LT compressor(s) 138 to an inlet of theflash tank 112. Thecheck valve 118 is configured to allow flow of refrigerant from the LT compressor(s) 138 to theflash tank 112 when a pressure difference across the check valve exceeds a threshold value (e.g., of about 6 bar to 10 bar). In other words, thecheck valve 118 is a one-way valve and prevents flow from theflash tank 112 to theconduit subsystem 104 connecting to the LT compressor(s) 138 and only allows flow to theflash tank 112 if a threshold pressure is reached. If the pressure difference across thecheck valve 118 is below the threshold value, flow is prevented to theflash tank 112. - Flash
gas bypass valve 142 may be located in refrigerant conduit of theconduit subsystem 104 connecting theflash tank 112 to the MT compressor(s) 102 and configured to open and close to permit or restrict the flow of flash gas discharged fromflash tank 112. In some embodiments,controller 150 controls the opening and closing of flashgas bypass valve 142. As depicted inFIGS. 1 and 2 , closing flashgas bypass valve 142 may restrict flash gas from flowing to MT compressor(s) 102, and opening flashgas bypass valve 142 may permit flow of flash gas to MT compressor(s) 102. - As described above,
controller 150 is in communication with at leastvalve 106;valves MT evaporator 116;valves LT evaporator 128; andcompressors controller 150 adjusts operation of components of therefrigeration system 100 to operate theevaporators controller 150 includes aprocessor 152,memory 154, and input/output (I/O)interface 156. Theprocessor 152 includes one or more processors operably coupled to thememory 154. Theprocessor 152 is any electronic circuitry including, but not limited to, state machines, one or more central processing unit (CPU) chips, logic units, cores (e.g., a multi-core processor), field-programmable gate array (FPGAs), application specific integrated circuits (ASICs), or digital signal processors (DSPs) that communicatively couples tomemory 154 and controls the operation ofrefrigeration system 100. - The
processor 152 may be a programmable logic device, a microcontroller, a microprocessor, or any suitable combination of the preceding. Theprocessor 152 is communicatively coupled to and in signal communication with thememory 154. The one or more processors are configured to process data and may be implemented in hardware or software. For example, theprocessor 152 may be 8-bit, 16-bit, 32-bit, 64-bit or of any other suitable architecture. Theprocessor 152 may include an arithmetic logic unit (ALU) for performing arithmetic and logic operations, processor registers that supply operands to the ALU and store the results of ALU operations, and a control unit that fetches instructions frommemory 154 and executes them by directing the coordinated operations of the ALU, registers, and other components. Theprocessor 152 may include other hardware and software that operates to process information, control therefrigeration system 100, and perform any of the functions described herein (e.g., with respect toFIGS. 1-3 ). Theprocessor 152 is not limited to a single processing device and may encompass multiple processing devices. Similarly, thecontroller 150 is not limited to a single controller but may encompass multiple controllers. - The
memory 154 includes one or more disks, tape drives, or solid-state drives, and may be used as an over-flow data storage device, to store programs when such programs are selected for execution, and to storeinstructions 158 and data that are read during program execution. Thememory 154 may be volatile or non-volatile and may include ROM, RAM, ternary content-addressable memory (TCAM), dynamic random-access memory (DRAM), and static random-access memory (SRAM). Thememory 154 is operable (or configured) to store information used by thecontroller 150 and/or any other logic and/or instructions for performing the function described in this disclosure. - The I/
O interface 156 is configured to communicate data and signals with other devices. For example, the I/O interface 156 may be configured to communicate electrical signals with components of therefrigeration system 100 includingvalves sensors compressors O interface 156 may be configured to communicate with other devices and systems. The I/O interface 156 may provide and/or receive, for example, compressor speed signals, compressor on/off signals, valve open/close signals, temperature signals, pressure signals, temperature setpoints, environmental conditions, and an operating mode status for therefrigeration system 100 and send electrical signals to the components of therefrigeration system 100. The I/O interface 156 may include ports or terminals for establishing signal communications between thecontroller 150 and other devices. The I/O interface 156 may be configured to enable wired and/or wireless communications. - Although this disclosure describes and depicts
refrigeration system 100 including certain components, this disclosure recognizes thatrefrigeration system 100 may include any suitable components. As an example,refrigeration system 100 may include one or more additional sensors configured to detect temperature and/or pressure information. - In an example operation of the
refrigeration system 100, therefrigeration system 100 is initially operating with bothevaporators FIG. 1 . In this mode,first valve 126 andsecond valve 132 ofLT evaporator 128 are open, andthird valve 136 andfourth valve 134 are closed. At some point during operation of therefrigeration system 100, thecontroller 150 determines that defrost mode operation is needed for theLT evaporator 128. For example, theLT evaporator 128 may be scheduled for defrost at the time that has just been reached. After determining that the defrost mode operation is indicated, thecontroller 150 causes the LT evaporator 128 to be configured according toFIG. 2 . In other words, thecontroller 150 causes thevalve 106 to allow a portion of refrigerant from the LT compressor(s) 138 to flow towards the LT evaporator 128 (e.g., by partially closing valve 106).First valve 126 andsecond valve 132 are closed, andthird valve 136 andfourth valve 134 are opened. - Once defrost of the
LT evaporator 128 is complete (e.g., because defrost mode operation has been performed for a predefined period of time and/or a threshold pressure and/ortemperature 160 of theLT evaporator 128 has been reached), thecontroller 150 causes the LT evaporator 128 to operate in the refrigeration mode, as illustrated inFIG. 1 and described above. -
FIG. 3 illustrates anexample method 300 of operating therefrigeration system 100 described above with respect toFIGS. 1 and 2 . Themethod 300 may be implemented using theprocessor 152,memory 154, and I/O interface 156 of thecontroller 150 ofFIGS. 1 and 2 . Themethod 300 may begin atoperation 302 where thecontroller 150 initially operates theevaporator operation 304, thecontroller 150 determines whether defrost mode is indicated for any of theevaporators controller 150 may determine whether theinstructions 158 and/orschedule 162 indicate that a defrost cycle is needed for one of theevaporators controller 150 may determine whether a temperature and/orpressure 160 measured at anevaporator threshold value 164 of temperature and/orpressure 160 is not being reached). This behavior may indicate that a defrost mode operation is indicated. If defrost mode is not indicated, thecontroller 150 returns tooperation 302 and continues to operate theevaporators controller 150 proceeds tooperation 306. - At
operation 306, thecontroller 150 causes theevaporator operation 304 to be operated in the defrost mode. For instance, if defrost of theLT evaporator 128 is needed, thecontroller 150 may cause thevalve 106 to allow a portion of refrigerant from the LT compressor(s) 138 to flow towards theLT evaporator 128.First valve 126 andsecond valve 132 are closed, andthird valve 136 andfourth valve 134 are opened. This achieves the defrost mode configuration ofevaporator 128 illustrated inFIG. 2 . - At
operation 308, thecontroller 150 determines whether defrost mode operation of theevaporator 128 is complete. For example, thecontroller 150 may determine whether defrost mode operation has been performed for a predefined period of time indicated byschedule 162 and/or if athreshold value 164 is reached for a pressure and/ortemperature 160 of theLT evaporator 128. If defrost mode operation is not complete, the controller continues to operate in the defrost mode atoperation 306. Once defrost mode operation is complete, thecontroller 150 returns tooperation 302 and operates theevaporator 128 in the refrigeration mode. - Modifications, additions, or omissions may be made to
method 300 depicted inFIG. 3 .Method 300 may include more, fewer, or other operations. For example, operations may be performed in parallel or in any suitable order. While at times discussed ascontroller 150,refrigeration system 100, or components thereof performing the operations, any suitable refrigeration system or components of the refrigeration system may perform one or more operations of themethod 300. - While several embodiments have been provided in the present disclosure, it should be understood that the disclosed systems and methods might be embodied in many other specific forms without departing from the spirit or scope of the present disclosure. The present examples are to be considered as illustrative and not restrictive, and the intention is not to be limited to the details given herein. For example, the various elements or components may be combined or integrated in another system or certain features may be omitted, or not implemented.
- In addition, techniques, systems, subsystems, and methods described and illustrated in the various embodiments as discrete or separate may be combined or integrated with other systems, modules, techniques, or methods without departing from the scope of the present disclosure. Other items shown or discussed as coupled or directly coupled or communicating with each other may be indirectly coupled or communicating through some interface, device, or intermediate component whether electrically, mechanically, or otherwise. Other examples of changes, substitutions, and alterations are ascertainable by one skilled in the art and could be made without departing from the spirit and scope disclosed herein.
- To aid the Patent Office, and any readers of any patent issued on this application in interpreting the claims appended hereto, applicants note that they do not intend any of the appended claims to invoke 35 U.S.C. § 112(f) as it exists on the date of filing hereof unless the words “means for” or “step for” are explicitly used in the particular claim.
Claims (20)
1. A refrigeration system, comprising:
a plurality of evaporators comprising at least one low-temperature evaporator and at least one medium-temperature evaporator;
one or more low-temperature compressors configured to compress refrigerant received from the at least one low-temperature evaporator;
one or more medium-temperature compressors configured to compress refrigerant received from the at least one medium-temperature evaporator;
a controllable valve positioned downstream from the one or more low-temperature compressors, the controllable valve configured to receive the compressed refrigerant from the one or more low-temperature compressors and direct flow of the received refrigerant to one or both of (i) the one or more medium-temperature compressors positioned downstream from the controllable valve and (ii) one or more evaporators of the plurality of evaporators based on an operation mode of the plurality of evaporators;
and a controller communicatively coupled to the controllable valve, wherein the controller is configured to:
determine that operation of a first evaporator of the plurality of evaporators in a defrost mode is indicated; and
after determining that operation of the first evaporator in the defrost mode is indicated, cause the first evaporator to operate in the defrost mode by adjusting the controllable valve to direct a portion of the received compressed refrigerant to the first evaporator.
2. The refrigeration system of claim 1 , wherein the controller is further configured to cause the first evaporator to operate in the defrost mode by at least partially closing the controllable valve.
3. The refrigeration system of claim 1 , further comprising:
a gas cooler configured to receive refrigerant from the one or more medium-temperature compressors and facilitate heat transfer from the received refrigerant; and
a flash tank located downstream from the gas cooler and configured to receive the refrigerant and store at least a portion of the received refrigerant.
4. The refrigeration system of claim 3 , further comprising:
a first valve located upstream from the first evaporator in refrigerant conduit coupling a liquid outlet of the flash tank to the first evaporator, wherein, when the first evaporator is operating in a refrigeration mode, the first valve is open; and
a second valve located downstream from the first evaporator in refrigerant conduit allowing flow of refrigerant towards the one or more medium-temperature compressors, wherein, when the first evaporator is operating in the refrigeration mode, the second valve is open;
wherein the controller is further configured to cause the first evaporator to operate in the defrost mode by causing the first valve to close and causing the second valve to close.
5. The refrigeration system of claim 4 , further comprising:
a third valve located upstream from the first evaporator in refrigerant conduit coupling an inlet of the flash tank to the first evaporator, wherein, when the first evaporator is operating in a refrigeration mode, the third valve is closed; and
a fourth valve located downstream from the first evaporator in refrigerant conduit coupling the first evaporator to the controllable valve, wherein, when the first evaporator is operating in the refrigeration mode, the fourth valve is closed;
wherein the controller is further configured to cause the first evaporator to operate in the defrost mode by causing the third valve to open and causing the fourth valve to open.
6. The refrigeration system of claim 3 , further comprising a check valve positioned in refrigerant conduit coupling an outlet of the one or more low-temperature compressors to an inlet of the flash tank, wherein the check valve is configured to allow flow of refrigerant from the one or more low-temperature compressors to the flash tank when a pressure difference across the check valve exceeds a threshold value.
7. The refrigeration system of claim 1 , wherein the controller is further configured to:
determine that defrost mode operation of the first evaporator is complete; and
after determining that defrost mode operation of the first evaporator is complete, cause the first evaporator to operate in a refrigeration mode.
8. The refrigeration system of claim 1 , wherein, while the first evaporator is caused to operate in the defrost mode, a second evaporator of the plurality of evaporators is caused to operate in a refrigeration mode.
9. A method of operating a refrigeration system, the method comprising:
operating a first evaporator of a plurality of evaporators in a refrigeration mode;
determining that operation of the first evaporator in a defrost mode is indicated; and
after determining that operation of the first evaporator in the defrost mode is indicated, causing the first evaporator to operate in the defrost mode by:
adjusting a controllable valve positioned in refrigerant conduit coupling one or more low-temperature compressors of the refrigeration system to one or more medium-temperature compressors of the refrigeration system; and
directing at least a portion of refrigerant compressed by the one or more low-temperature compressors to the first evaporator.
10. The method of claim 9 , further comprising causing the first evaporator to operate in the defrost mode by at least partially closing the controllable valve.
11. The method claim 9 , further comprising:
receiving, by a gas cooler of the refrigeration system, refrigerant from the one or more compressors and cooling the refrigerant; and
receiving and storing, by a flash tank, the cooled refrigerant.
12. The method of claim 11 , further comprising causing the first evaporator to operate in the defrost mode by:
closing a first valve located upstream from the first evaporator in refrigerant conduit coupling a liquid outlet of the flash tank to the first evaporator; and
closing a second valve located downstream from the first evaporator in refrigerant conduit allowing flow of refrigerant towards the one or more medium-temperature compressors.
13. The method of claim 12 , further comprising:
opening a third valve located upstream from the first evaporator in refrigerant conduit coupling an inlet of the flash tank to the first evaporator, wherein, when the first evaporator is operating in a refrigeration mode, the third valve is closed; and
opening a fourth valve located downstream from the first evaporator in refrigerant conduit coupling the first evaporator to the controllable valve, wherein, when the first evaporator is operating in the refrigeration mode, the fourth valve is closed.
14. The method of claim 11 , further comprising, by a check valve positioned in refrigerant conduit coupling an outlet of the one or more low-temperature compressors to an inlet of the flash tank, allowing flow of refrigerant from the one or more low-temperature compressors to the flash tank when a pressure difference across the check valve exceeds a threshold value.
15. The method of claim 9 , further comprising:
determining that defrost mode operation of the first evaporator is complete; and
after determining that defrost mode operation of the first evaporator is complete, causing the first evaporator to operate in the refrigeration mode.
16. The method of claim 9 , wherein, while causing the first evaporator to operate in the defrost mode, causing a second evaporator of the plurality of evaporators to operate in a refrigeration mode.
17. A controller of a refrigeration system, the controller comprising:
an input/output interface communicatively coupled to a controllable valve positioned downstream from one or more low-temperature compressors of the refrigeration system, wherein the controllable valve is configured to receive the compressed refrigerant from the one or more low-temperature compressors and direct flow of the received refrigerant to one or both of (i) one or more medium-temperature compressors positioned downstream from the controllable valve and (ii) one or more evaporators of the plurality of evaporators based on an operation mode of the plurality of evaporators; and
a processor configured to:
determine that operation of a first evaporator of a plurality of evaporators of the refrigeration system in a defrost mode is indicated; and
after determining that operation of the first evaporator in the defrost mode is indicated, cause the first evaporator to operate in the defrost mode by adjusting the controllable valve to direct a portion of the received compressed refrigerant to the first evaporator.
18. The controller of claim 17 , wherein the processor is further configured to cause the first evaporator to operate in the defrost mode by at least partially closing the controllable valve.
19. The controller of claim 17 , wherein:
the input/output interface communicatively coupled to:
a first valve located upstream from the first evaporator in refrigerant conduit coupling a liquid outlet of the flash tank to the first evaporator, wherein, when the first evaporator is operating in a refrigeration mode, the first valve is open; and
a second valve located downstream from the first evaporator in refrigerant conduit allowing flow of refrigerant towards the one or more medium-temperature compressors, wherein, when the first evaporator is operating in the refrigeration mode, the second valve is open; and
the processor is further configured to cause the first evaporator to operate in the defrost mode by causing the first valve to close and causing the second valve to close.
20. The controller of claim 19 , wherein:
the input/output interface is further communicatively coupled to:
a third valve located upstream from the first evaporator in refrigerant conduit coupling an inlet of the flash tank to the first evaporator, wherein, when the first evaporator is operating in a refrigeration mode, the third valve is closed; and
a fourth valve located downstream from the first evaporator in refrigerant conduit coupling the first evaporator to the controllable valve, wherein, when the first evaporator is operating in the refrigeration mode, the fourth valve is closed; and
the processor is further configured to cause the first evaporator to operate in the defrost mode by causing the third valve to open and causing the fourth valve to open.
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US17/844,654 US20230408166A1 (en) | 2022-06-20 | 2022-06-20 | Hot gas defrost system using hot gas from low temperature compressor |
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US17/844,654 US20230408166A1 (en) | 2022-06-20 | 2022-06-20 | Hot gas defrost system using hot gas from low temperature compressor |
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US4012921A (en) * | 1976-01-07 | 1977-03-22 | Emhart Industries, Inc. | Refrigeration and hot gas defrost system |
US4831835A (en) * | 1988-04-21 | 1989-05-23 | Tyler Refrigeration Corporation | Refrigeration system |
US7610766B2 (en) * | 2002-07-08 | 2009-11-03 | Dube Serge | High-speed defrost refrigeration system |
US9261299B2 (en) * | 2006-09-22 | 2016-02-16 | Siemens Industry, Inc. | Distributed microsystems-based control method and apparatus for commercial refrigeration |
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