EP3086057B1 - Refrigeration circuit with heat recovery module - Google Patents

Refrigeration circuit with heat recovery module Download PDF

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Publication number
EP3086057B1
EP3086057B1 EP16165542.8A EP16165542A EP3086057B1 EP 3086057 B1 EP3086057 B1 EP 3086057B1 EP 16165542 A EP16165542 A EP 16165542A EP 3086057 B1 EP3086057 B1 EP 3086057B1
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EP
European Patent Office
Prior art keywords
refrigerant
gas
liquid
refrigeration circuit
receiver
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Not-in-force
Application number
EP16165542.8A
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German (de)
French (fr)
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EP3086057A1 (en
Inventor
Sascha HELLMANN
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Carrier Corp
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Carrier Corp
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Publication date
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Priority to EP16165542.8A priority Critical patent/EP3086057B1/en
Priority to DK16165542.8T priority patent/DK3086057T3/en
Publication of EP3086057A1 publication Critical patent/EP3086057A1/en
Application granted granted Critical
Publication of EP3086057B1 publication Critical patent/EP3086057B1/en
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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B43/00Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B41/00Fluid-circulation arrangements
    • F25B41/30Expansion means; Dispositions thereof
    • F25B41/39Dispositions with two or more expansion means arranged in series, i.e. multi-stage expansion, on a refrigerant line leading to the same evaporator
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B49/00Arrangement or mounting of control or safety devices
    • F25B49/02Arrangement or mounting of control or safety devices for compression type machines, plants or systems
    • F25B49/027Condenser control arrangements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2339/00Details of evaporators; Details of condensers
    • F25B2339/04Details of condensers
    • F25B2339/047Water-cooled condensers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00General 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
    • F25B2400/06Several compression cycles arranged in parallel
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00General 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
    • F25B2400/13Economisers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00General 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
    • F25B2400/16Receivers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00General 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
    • F25B2400/23Separators
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2600/00Control issues
    • F25B2600/05Refrigerant levels
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2600/00Control issues
    • F25B2600/25Control of valves
    • F25B2600/2519On-off valves
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2700/00Sensing or detecting of parameters; Sensors therefor
    • F25B2700/04Refrigerant level

Definitions

  • Refrigeration circuits comprising in the direction of flow of a circulating refrigerant a compressor, a gas cooler/condenser, an expansion device and an evaporator are known in the state of the art. It is also known to provide a heat recovery module in the refrigeration circuit in order to recover at least some of the energy used for compressing and heating the refrigerant.
  • Document WO 2013/004298 A1 discloses a refrigeration circuit according to the preamble of claim 1 and a method for operating a refrigeration circuit according to the preamble of claim 10. From a thermodynamic point of view such heat recovery modules are applied in a very wide range (high temp heating, low temp heating,...) at maximum performance.
  • a method and a refrigeration circuit according to exemplary embodiments of the invention allow to use a single BPHE, instead of two or even more as in the common wide-range modules, in combination with a constant speed pump for flowing the external heat recovery fluid circuit through the BPHE, in order to account for the need of a cheaper version of the heat recovery module.
  • the gas/liquid separation according to the invention reliably avoids problems related to partial condensation of the refrigerant within or downstream of the heat recovery heat exchanger as according to exemplary embodiments of the invention the liquid component of the refrigerant is separated from the gaseous component and delivered directly to the receiver bypassing the gas cooler/condenser. This in particular avoids that condensed refrigerant is delivered into the gas cooler/condenser where it would deteriorate the gas cooler's/condenser's performance. It further avoids the need of lifting the liquid refrigerant to the level of the condenser/gas cooler, which may be provided at a level significantly above the level of the compressor(s) and the heat recovery module.
  • FIG. 1 shows a schematic view of an exemplary embodiment of a cooling system with a refrigeration circuit 1 comprising in the direction of the flow of a refrigerant, which is circulating within the refrigeration circuit 1 as indicated by the arrows A, a set 2 of compressors 2a, 2b, 2c, 2d connected in parallel to each other, a heat recovery heat exchanger 4, a gas/liquid separator 8, a gas cooler or condenser 10, a high pressure expansion device 12, which is configured to expand the refrigerant from high pressure to a lower medium pressure, a receiver (refrigerant collector) 14, an optional flash gas heat exchanger 16, an evaporator associated expansion device 18, which is configured to expand the refrigerant from medium pressure to low pressure, and an evaporator 20.
  • the outlet side of the evaporator 20 is fluidly connected to the suction (inlet) side of the compressors 2a, 2b, 2c, 2d completing the refrigerant cycle.
  • the exemplary embodiment of a refrigeration circuit 1 shown in figure 1 employs a one-stage compression by means of the compressors 2a, 2b, 2c, 2d connected in parallel and a two-stage expansion by successive expansions by means of the high pressure expansion device 12 and the subsequent evaporator associated expansion device 18.
  • Such a two-stage expansion is in particular employed when CO 2 is used as the refrigerant.
  • the invention may also applied to a refrigeration circuit 1 which employs a single-stage expansion by means of only an evaporator associated expansion device 18 arranged upstream of the evaporator 20 and in which the high pressure expansion device 12 is omitted.
  • a flash gas tapping line 21 fluidly connects an upper portion 14a of the receiver 14 to the inlet side of the compressors 2a, 2b, 2c, 2d allowing flash gas collecting in the upper portion 14a of the receiver 14 to bypass the evaporator 20.
  • a flash gas expansion device 22 is arranged in the flash gas tapping line 21 in order to expand the flash gas delivered from the receiver 14. Downstream of said flash gas expansion device 22 an optional flash gas heat exchanger 16 is provided in order to cool the expanded flash gas by means of heat exchange with the refrigerant supplied from the receiver 14 to the evaporator associated expansion device 18.
  • FIG. 1 comprises only a single gas cooler/condenser 10, a single medium pressure valve 18 and a single evaporator 20, respectively, it is self evident to the skilled person that a plurality of each of said components 10, 18, 20 respectively connected in parallel to each other may by provided in order to provide enhanced condensing and/or cooling capacities.
  • additional switchable valves may be provided in order to allow to selectively activate and deactivate one or more of the plurality of said components in order to adjust the condensing and/or cooling capacity to the actual needs.
  • a single compressor may be provided instead of the set 2 of a plurality of compressors 2a, 2b, 2c, 2d as it is shown in figure 1 .
  • Said single compressor or at least one of the plurality of compressors 2a, 2b, 2c, 2d may be a variable speed compressor allowing to control the cooling capacity provided by the refrigeration circuit 1 by controlling the speed of said compressor.
  • the compressed refrigerant leaving the set 2 of compressors 2a, 2b, 2c, 2d passes a refrigerant circuit side 4a of the heat recovery heat exchanger 4 for transferring heat from the refrigerant to an external heat recovery fluid circulating within a heat recovery fluid circuit 6 and flowing through a heat recovery fluid circuit side 4b of the heat recovery heat exchanger 4.
  • the heated external heat recovery fluid may be used e.g. for heating the building and/or providing heated water.
  • At least a portion of the refrigerant may condensate within or downstream of the heat recovery heat exchanger 4.
  • a refrigerant liquid gas mixture is present in the outlet line 7 of the refrigerant circuit side 4b of the heat recovery heat exchanger 4.
  • Liquid refrigerant entering the gas cooler/condenser 10 will deteriorate the gas cooler's/condenser's 10 performance and when the gas cooler/condenser 10 is installed at a significant higher level, i.e. at a vertical distance d of up to 20m with respect to the other components of the refrigeration circuit 1, the liquid component of the refrigerant may not be able to be transferred completely to the outlet side of the gas cooler/condenser 10, which will deteriorate the performance and efficiency of the refrigeration circuit 1 even further.
  • gas/liquid separator 8 is provided downstream of the refrigerant circuit side 4b of the heat recovery heat exchanger 4 in order to separate the liquid portion of the refrigerant leaving the heat recovery heat exchanger 4 from its gaseous component.
  • the gas/liquid separator 8 may be formed by a vessel or pipe having a significant larger cross-section/diameter than the outlet line 7 of the heat recovery heat exchanger 4, which also forms the inlet line 7 of the gas/liquid separator 8, in order to considerably reduce the velocity of the refrigerant allowing the liquid component of the refrigerant to separate from the refrigerant's gaseous component and to collect at the bottom 8a of the gas/liquid separator 8.
  • the cross-section or diameter of the gas/liquid separator 8 is four to five times larger than the diameter of the outlet line 7 and the velocity of the refrigerant is reduced from approx. 9 m/s at the outlet of the compressors 2a, 2b, 2c, 2d to approx. 0,3 m/s within the vessel or pipe of the gas/liquid separator 8.
  • the gaseous component of the refrigerant leaves the gas/liquid separator 8 via the gas/liquid separator's 8 gaseous phase outlet line 9 fluidly connecting the top 8b of the gas/liquid separator 8 to the inlet side of the gas cooler/condenser 10.
  • the gaseous component of the refrigerant is gas cooled and/or condensed within the gas cooler/condenser 10, expanded by the high-pressure expansion device 12 fluidly connected to the outlet side of the gas cooler/condenser 10 and delivered into the receiver 14, which is fluidly connected to the outlet side of the high-pressure expansion device 12.
  • a liquid phase outlet line 13 of the gas/liquid separator 8 is fluidly connected to the bottom 8a of the gas/liquid separator 8 allowing to transfer liquid refrigerant, which has collected at the bottom 8a of the gas/liquid separator 8, into the receiver 14.
  • At least one switchable valve 24 is arranged in the liquid phase outlet line 13 allowing to selectively open and close the fluid connection between the gas/liquid separator 8 and the receiver 14.
  • the gas/liquid separator 8 is further provided with a liquid level sensor 26, which is configured for sensing the level of liquid refrigerant collected at the bottom 8a of the gas/liquid separator 8.
  • the liquid level sensor 26 is functionally connected to a control unit 28, which is configured for opening the at least one switchable valve 24 when the level of liquid refrigerant collected in the gas/liquid separator 8 exceeds a first predetermined level and for closing the at least one switchable valve 24 when the level of liquid refrigerant collected in the gas/liquid separator 8 falls below a second predetermined level, which is equal or lower than the first predetermined level.
  • Closing the at least one switchable valve 24 avoids that gaseous refrigerant may bypass the gas cooler/condenser 10 via the liquid phase outlet line 13 in case the level of liquid refrigerant collected at the bottom 8a of the gas/liquid separator 8 is so low that it allows gaseous refrigerant to enter the liquid phase outlet line 13 .
  • the liquid level sensor 26 may be a mechanical or electromechanical flush type fluid indicator or an electronic level sensor.
  • the switchable valve 24 may be a simple on/off-valve, having only a closed state and a single open state.
  • the switchable valve 24 may have two or more different open states providing at least two different open cross-sections allowing to regulate the flow of liquid refrigerant form the gas/liquid separator 8 to the receiver even more accurately.
  • the open cross-section of the switchable valve 24 may be controlled continuously for allowing an even finer control of the flow of liquid refrigerant out of the gas/liquid separator 8.
  • At least one additional switchable valve 25 is connected in parallel to the switchable valve 24. Providing two or more switchable valves 24, 25 connected in parallel allows to control the amount of liquid refrigerant flowing out of the gas/liquid separator 8 by selectively opening one or more of said switchable valves 24, 25.
  • the switchable valves 24, 25 may have the same or different open cross-sections (Kv-values).
  • the refrigeration circuit comprises at least one switchable valve configured for selectively opening and closing the liquid-outlet of the gas/liquid separator.
  • the refrigeration circuit further comprises a liquid level sensor, which is configured for detecting the amount of liquid refrigerant present in the gas/liquid separator, and a control unit, which is configured for operating the at least one switchable valve based on the amount of liquid refrigerant detected by the liquid level sensor.
  • the control unit may be integrated with the liquid level sensor or the switchable valve or may be provided as a separate unit.
  • Controlling the at least one switchable valve based on the level of liquid refrigerant collected within the gas/liquid separator allows liquid refrigerant to flow from the gas/liquid separator into the receiver, but avoids gaseous refrigerant from flowing from the gas/liquid separator into the receiver bypassing the gas cooler/condenser.
  • the switchable valve is switchable between a closed state and at least two different open states. Providing a switchable valve having at least two different open states allows to control the flow of liquid refrigerant from the gas/liquid separator into the receiver more accurately. In one embodiment the switchable valve may by controlled continuously which allows an even finer control of the flow of liquid refrigerant from the gas/liquid separator into the receiver.
  • the refrigeration circuit comprises at least two switchable valves, which are connected in parallel. Selectively opening and closing one or more of the at least two switchable valves allows to control the flow of liquid refrigerant from the gas/liquid separator into the receiver more accurately.
  • the switchable valves may have the same or different open cross-sections/Kv-values. Providing switchable valves having different open cross-sections/Kv-values provides additional options for regulating the flow of refrigerant.
  • the at least one gas cooler/condenser is arranged at a level above the level of the heat recovery heat-exchanger in order to improve a flow of air flowing through the gas cooler/condenser, which will enhance the gas cooler's/condenser's gas cooling capabilities.
  • the gas cooler/condenser may in particular be arranged up to approximately 20 meter above the level of the heat recovery heat-exchanger, e.g. on top of the building housing the refrigeration circuit.
  • the refrigeration circuit comprises at least one additional (high-pressure) expansion device fluidly connected between the gas cooler/ condenser and the receiver in order to provide, in combination with the evaporator associated expansion device arranged upstream of the evaporator, a two-stage expansion enhancing the performance and efficiency of the refrigeration circuit.
  • the refrigeration circuit comprises a flash gas tapping line fluidly connecting an upper portion of the receiver to the inlet side of the at least one compressor.
  • a flash gas expansion device may be arranged within the flash gas tapping line.
  • the bypass-line may further comprise a flash gas heat-exchanger arranged downstream of the flash gas expansion device which is configured for heat-exchange of the flash gas with refrigerant flowing from the receiver to the evaporator.
  • Such a flash gas tapping line may help to enhance the performance and efficiency of the refrigeration circuit.
  • At least one compressor is configured as a variable speed compressor allowing to control the cooling capacity provided by the refrigeration circuit by controlling the speed of said compressor.

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  • Mechanical Engineering (AREA)
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Description

  • Refrigeration circuits comprising in the direction of flow of a circulating refrigerant a compressor, a gas cooler/condenser, an expansion device and an evaporator are known in the state of the art. It is also known to provide a heat recovery module in the refrigeration circuit in order to recover at least some of the energy used for compressing and heating the refrigerant. Document WO 2013/004298 A1 discloses a refrigeration circuit according to the preamble of claim 1 and a method for operating a refrigeration circuit according to the preamble of claim 10. From a thermodynamic point of view such heat recovery modules are applied in a very wide range (high temp heating, low temp heating,...) at maximum performance. As such a wide-range applicability requires a lot of different parts, especially differently sized heat exchangers (e.g. brazed plate heat exchangers "BPHE") for the exchange of heat between the circulating refrigerant and an external heat recovery fluid, on stock to be used in the modules, the modules are very expensive, sometimes too expensive for customers.
  • Accordingly, it would be beneficial to provide a cooling system with an inexpensive heat recovery module comprising only a single heat exchanger instead of two or even more heat exchanger allowing to adjust the heat transfer provided by the heat recovery module as in the common wide-range modules, which avoids the problems related to the use of only a single heat exchanger, which may include the problem of partial condensation at the outlet of the heat recovery module. According to the present invention the above objection is solved by a refrigeration circuit having the features of claim 1 and a method according to 10. A method and a refrigeration circuit according to exemplary embodiments of the invention allow to use a single BPHE, instead of two or even more as in the common wide-range modules, in combination with a constant speed pump for flowing the external heat recovery fluid circuit through the BPHE, in order to account for the need of a cheaper version of the heat recovery module.
  • When only a single heat exchanger having a constant heat transfer capacity is used, partial condensation of the refrigerant having passed the heat recovery module may occur. The gas/liquid separation according to the invention, however, reliably avoids problems related to partial condensation of the refrigerant within or downstream of the heat recovery heat exchanger as according to exemplary embodiments of the invention the liquid component of the refrigerant is separated from the gaseous component and delivered directly to the receiver bypassing the gas cooler/condenser. This in particular avoids that condensed refrigerant is delivered into the gas cooler/condenser where it would deteriorate the gas cooler's/condenser's performance. It further avoids the need of lifting the liquid refrigerant to the level of the condenser/gas cooler, which may be provided at a level significantly above the level of the compressor(s) and the heat recovery module.
  • An exemplary embodiment of the invention is described in greater detail below with reference to the figures, wherein:
    • Figure 1 shows a schematic view of a cooling system comprising a refrigeration circuit according to an exemplary embodiment of the invention; and
    • Figure 2 shows an enlarged view of the gas/liquid separator comprised in the cooling system shown in figure 1.
  • Figure 1 shows a schematic view of an exemplary embodiment of a cooling system with a refrigeration circuit 1 comprising in the direction of the flow of a refrigerant, which is circulating within the refrigeration circuit 1 as indicated by the arrows A, a set 2 of compressors 2a, 2b, 2c, 2d connected in parallel to each other, a heat recovery heat exchanger 4, a gas/liquid separator 8, a gas cooler or condenser 10, a high pressure expansion device 12, which is configured to expand the refrigerant from high pressure to a lower medium pressure, a receiver (refrigerant collector) 14, an optional flash gas heat exchanger 16, an evaporator associated expansion device 18, which is configured to expand the refrigerant from medium pressure to low pressure, and an evaporator 20. The outlet side of the evaporator 20 is fluidly connected to the suction (inlet) side of the compressors 2a, 2b, 2c, 2d completing the refrigerant cycle.
  • Thus, the exemplary embodiment of a refrigeration circuit 1 shown in figure 1 employs a one-stage compression by means of the compressors 2a, 2b, 2c, 2d connected in parallel and a two-stage expansion by successive expansions by means of the high pressure expansion device 12 and the subsequent evaporator associated expansion device 18. Such a two-stage expansion is in particular employed when CO2 is used as the refrigerant. The skilled person, however, will easily understand that the invention may also applied to a refrigeration circuit 1 which employs a single-stage expansion by means of only an evaporator associated expansion device 18 arranged upstream of the evaporator 20 and in which the high pressure expansion device 12 is omitted.
  • A flash gas tapping line 21 fluidly connects an upper portion 14a of the receiver 14 to the inlet side of the compressors 2a, 2b, 2c, 2d allowing flash gas collecting in the upper portion 14a of the receiver 14 to bypass the evaporator 20. A flash gas expansion device 22 is arranged in the flash gas tapping line 21 in order to expand the flash gas delivered from the receiver 14. Downstream of said flash gas expansion device 22 an optional flash gas heat exchanger 16 is provided in order to cool the expanded flash gas by means of heat exchange with the refrigerant supplied from the receiver 14 to the evaporator associated expansion device 18.
  • Although the exemplary embodiment shown in figure 1 comprises only a single gas cooler/condenser 10, a single medium pressure valve 18 and a single evaporator 20, respectively, it is self evident to the skilled person that a plurality of each of said components 10, 18, 20 respectively connected in parallel to each other may by provided in order to provide enhanced condensing and/or cooling capacities. In this case additional switchable valves may be provided in order to allow to selectively activate and deactivate one or more of the plurality of said components in order to adjust the condensing and/or cooling capacity to the actual needs.
  • Similarly, only a single compressor may be provided instead of the set 2 of a plurality of compressors 2a, 2b, 2c, 2d as it is shown in figure 1. Said single compressor or at least one of the plurality of compressors 2a, 2b, 2c, 2d may be a variable speed compressor allowing to control the cooling capacity provided by the refrigeration circuit 1 by controlling the speed of said compressor.
  • In operation the compressed refrigerant leaving the set 2 of compressors 2a, 2b, 2c, 2d passes a refrigerant circuit side 4a of the heat recovery heat exchanger 4 for transferring heat from the refrigerant to an external heat recovery fluid circulating within a heat recovery fluid circuit 6 and flowing through a heat recovery fluid circuit side 4b of the heat recovery heat exchanger 4. The heated external heat recovery fluid may be used e.g. for heating the building and/or providing heated water.
  • Depending on the amount of heat transferred from the circulating refrigerant to the external heat recovery fluid at least a portion of the refrigerant may condensate within or downstream of the heat recovery heat exchanger 4. As a result, a refrigerant liquid gas mixture is present in the outlet line 7 of the refrigerant circuit side 4b of the heat recovery heat exchanger 4.
  • Liquid refrigerant entering the gas cooler/condenser 10, however, will deteriorate the gas cooler's/condenser's 10 performance and when the gas cooler/condenser 10 is installed at a significant higher level, i.e. at a vertical distance d of up to 20m with respect to the other components of the refrigeration circuit 1, the liquid component of the refrigerant may not be able to be transferred completely to the outlet side of the gas cooler/condenser 10, which will deteriorate the performance and efficiency of the refrigeration circuit 1 even further.
  • Therefore the gas/liquid separator 8 is provided downstream of the refrigerant circuit side 4b of the heat recovery heat exchanger 4 in order to separate the liquid portion of the refrigerant leaving the heat recovery heat exchanger 4 from its gaseous component.
  • An enlarged view of such a gas/liquid separator 8 is shown in Figure 2.
  • The gas/liquid separator 8 may be formed by a vessel or pipe having a significant larger cross-section/diameter than the outlet line 7 of the heat recovery heat exchanger 4, which also forms the inlet line 7 of the gas/liquid separator 8, in order to considerably reduce the velocity of the refrigerant allowing the liquid component of the refrigerant to separate from the refrigerant's gaseous component and to collect at the bottom 8a of the gas/liquid separator 8. In an exemplary embodiment the cross-section or diameter of the gas/liquid separator 8 is four to five times larger than the diameter of the outlet line 7 and the velocity of the refrigerant is reduced from approx. 9 m/s at the outlet of the compressors 2a, 2b, 2c, 2d to approx. 0,3 m/s within the vessel or pipe of the gas/liquid separator 8.
  • The gaseous component of the refrigerant leaves the gas/liquid separator 8 via the gas/liquid separator's 8 gaseous phase outlet line 9 fluidly connecting the top 8b of the gas/liquid separator 8 to the inlet side of the gas cooler/condenser 10. The gaseous component of the refrigerant is gas cooled and/or condensed within the gas cooler/condenser 10, expanded by the high-pressure expansion device 12 fluidly connected to the outlet side of the gas cooler/condenser 10 and delivered into the receiver 14, which is fluidly connected to the outlet side of the high-pressure expansion device 12.
  • A liquid phase outlet line 13 of the gas/liquid separator 8 is fluidly connected to the bottom 8a of the gas/liquid separator 8 allowing to transfer liquid refrigerant, which has collected at the bottom 8a of the gas/liquid separator 8, into the receiver 14.
  • At least one switchable valve 24 is arranged in the liquid phase outlet line 13 allowing to selectively open and close the fluid connection between the gas/liquid separator 8 and the receiver 14.
  • The gas/liquid separator 8 is further provided with a liquid level sensor 26, which is configured for sensing the level of liquid refrigerant collected at the bottom 8a of the gas/liquid separator 8. The liquid level sensor 26 is functionally connected to a control unit 28, which is configured for opening the at least one switchable valve 24 when the level of liquid refrigerant collected in the gas/liquid separator 8 exceeds a first predetermined level and for closing the at least one switchable valve 24 when the level of liquid refrigerant collected in the gas/liquid separator 8 falls below a second predetermined level, which is equal or lower than the first predetermined level. Closing the at least one switchable valve 24 avoids that gaseous refrigerant may bypass the gas cooler/condenser 10 via the liquid phase outlet line 13 in case the level of liquid refrigerant collected at the bottom 8a of the gas/liquid separator 8 is so low that it allows gaseous refrigerant to enter the liquid phase outlet line 13 .
  • The liquid level sensor 26 may be a mechanical or electromechanical flush type fluid indicator or an electronic level sensor.
  • In a first embodiment the switchable valve 24 may be a simple on/off-valve, having only a closed state and a single open state.
  • In an alternative embodiment the switchable valve 24 may have two or more different open states providing at least two different open cross-sections allowing to regulate the flow of liquid refrigerant form the gas/liquid separator 8 to the receiver even more accurately. In another embodiment the open cross-section of the switchable valve 24 may be controlled continuously for allowing an even finer control of the flow of liquid refrigerant out of the gas/liquid separator 8.
  • In yet another embodiment, at least one additional switchable valve 25 is connected in parallel to the switchable valve 24. Providing two or more switchable valves 24, 25 connected in parallel allows to control the amount of liquid refrigerant flowing out of the gas/liquid separator 8 by selectively opening one or more of said switchable valves 24, 25. The switchable valves 24, 25 may have the same or different open cross-sections (Kv-values).
  • In an embodiment the refrigeration circuit comprises at least one switchable valve configured for selectively opening and closing the liquid-outlet of the gas/liquid separator. The refrigeration circuit further comprises a liquid level sensor, which is configured for detecting the amount of liquid refrigerant present in the gas/liquid separator, and a control unit, which is configured for operating the at least one switchable valve based on the amount of liquid refrigerant detected by the liquid level sensor. The control unit may be integrated with the liquid level sensor or the switchable valve or may be provided as a separate unit.
  • Controlling the at least one switchable valve based on the level of liquid refrigerant collected within the gas/liquid separator allows liquid refrigerant to flow from the gas/liquid separator into the receiver, but avoids gaseous refrigerant from flowing from the gas/liquid separator into the receiver bypassing the gas cooler/condenser.
  • In an embodiment the switchable valve is switchable between a closed state and at least two different open states. Providing a switchable valve having at least two different open states allows to control the flow of liquid refrigerant from the gas/liquid separator into the receiver more accurately. In one embodiment the switchable valve may by controlled continuously which allows an even finer control of the flow of liquid refrigerant from the gas/liquid separator into the receiver.
  • In an embodiment the refrigeration circuit comprises at least two switchable valves, which are connected in parallel. Selectively opening and closing one or more of the at least two switchable valves allows to control the flow of liquid refrigerant from the gas/liquid separator into the receiver more accurately. The switchable valves may have the same or different open cross-sections/Kv-values. Providing switchable valves having different open cross-sections/Kv-values provides additional options for regulating the flow of refrigerant. In an embodiment the at least one gas cooler/condenser is arranged at a level above the level of the heat recovery heat-exchanger in order to improve a flow of air flowing through the gas cooler/condenser, which will enhance the gas cooler's/condenser's gas cooling capabilities. The gas cooler/condenser may in particular be arranged up to approximately 20 meter above the level of the heat recovery heat-exchanger, e.g. on top of the building housing the refrigeration circuit.
  • In an embodiment the refrigeration circuit comprises at least one additional (high-pressure) expansion device fluidly connected between the gas cooler/ condenser and the receiver in order to provide, in combination with the evaporator associated expansion device arranged upstream of the evaporator, a two-stage expansion enhancing the performance and efficiency of the refrigeration circuit. According to the invention the refrigeration circuit comprises a flash gas tapping line fluidly connecting an upper portion of the receiver to the inlet side of the at least one compressor. A flash gas expansion device may be arranged within the flash gas tapping line. The bypass-line may further comprise a flash gas heat-exchanger arranged downstream of the flash gas expansion device which is configured for heat-exchange of the flash gas with refrigerant flowing from the receiver to the evaporator. Such a flash gas tapping line may help to enhance the performance and efficiency of the refrigeration circuit.
  • In an embodiment at least one compressor is configured as a variable speed compressor allowing to control the cooling capacity provided by the refrigeration circuit by controlling the speed of said compressor.
  • While the invention has been described with reference to exemplary embodiments, it will be understood by those skilled in the art that various changes may be made and equivalents may be substituted for elements thereof without departing from the scope of the invention. In addition, many modifications may be made to adapt the particular situation or material to the teachings of the invention without departing from the essential scope thereof. Therefore it is intended that the invention is not limited to the particular embodiments disclosed, but that the invention will include all embodiments falling within the scope of the appended claims.
  • Reference Numerals
  • 1
    refrigeration circuit
    2
    set of compressors
    2a, 2b, 2c, 2d
    compressors
    4
    heat recovery heat exchanger
    4a
    refrigerant circuit side of the heat recovery heat exchanger
    4b
    heat recovery fluid circuit side of the heat recovery heat exchanger
    6
    heat recovery fluid circuit
    7
    inlet line of the gas/liquid separator / outlet line of the heat recovery heat exchanger
    8
    gas/liquid separator
    8a
    bottom of the gas/liquid separator
    8b
    top of the gas/liquid separator
    9
    gaseous phase outlet line of the gas/liquid separator
    10
    gas cooler/condenser
    12
    high-pressure expansion device
    13
    liquid phase outlet line of the gas/liquid separator
    14
    receiver
    14a
    upper portion of the receiver
    16
    flash gas heat exchanger
    18
    evaporator associated expansion device
    20
    evaporator
    21
    flash gas tapping line
    22
    flash gas expansion device
    24
    switchable valve
    25
    additional switchable valve
    26
    liquid level sensor
    28
    control unit

Claims (14)

  1. Refrigeration circuit (1) configured for circulating a refrigerant and comprising in the direction of flow of the refrigerant:
    at least one compressor (2a, 2b, 2c, 2d);
    at least one heat recovery heat exchanger (4);
    a gas/liquid separator (8);
    at least one gas cooler/condenser (10); and
    at least one evaporator (20) with at least one evaporator associated expansion device (18) fluidly connected upstream thereof;
    further comprising a receiver (14);
    wherein the gas/liquid separator (8) comprises
    a refrigerant inlet line (7) fluidly connected to an outlet-side of the at least one heat recovery heat exchanger (4);
    a gaseous phase outlet line (9) fluidly connected to an inlet side of the at least one gas cooler/condenser (10); and
    a liquid phase outlet line (13) fluidly connected to the receiver (14),
    characterized in that
    the receiver (14) is arranged in the direction of flow of the refrigerant between the at least one gas cooler/condenser (10) and the at least one evaporator (20) with the at least one evaporator associated expansion device (18) fluidly connected upstream thereof; and
    a flash gas tapping line (21) is provided fluidly connecting an upper portion of the receiver (14) to an inlet side of the at least one compressor (2a, 2b, 2c, 2d).
  2. Refrigeration circuit (1) of claim 1, further comprising at least one switchable valve (24) configured for selectively opening and closing the liquid phase outlet line (13) of the gas/liquid separator (8).
  3. Refrigeration circuit (1) of claim 2, further comprising a liquid level sensor (26), which is configured for detecting the amount of liquid refrigerant present in the gas/liquid separator (8), and a control unit (28), which is configured for operating the at least one switchable valve (24) based on the amount of liquid refrigerant detected by the liquid level sensor (26).
  4. Refrigeration circuit (1) of claim 2 or 3, wherein the switchable valve (24) is switchable between a closed state and at least two different open states.
  5. Refrigeration circuit (1) of any of claims 2 to 4, comprising at least two switchable valves (24, 25), which are connected in parallel.
  6. Refrigeration circuit (1) of any of the preceding claims, wherein the at least one gas cooler/condenser (10) is arranged at a level above the level of the heat recovery heat exchanger (4).
  7. Refrigeration circuit (1) of any of the preceding claims comprising at least one high-pressure expansion device (12) fluidly connected between the gas cooler/condenser (10) and the receiver (14).
  8. Refrigeration circuit (1) of any of the preceding claims, in which a flash gas expansion device (22) is arranged within the flash gas tapping line (21).
  9. Refrigeration circuit (1) of claim 8, in which the flash gas tapping line (21) comprises a flash gas heat-exchanger (16) which is arranged downstream of the flash gas expansion device (22) and configured for heat-exchange of the flash gas with refrigerant flowing from the receiver (14) to the evaporator (20).
  10. Method of operating a refrigeration circuit (1) comprising the steps of:
    compressing a refrigerant by means of at least one compressor (2a, 2b, 2c, 2d);
    providing heat recovery heat-exchange between the compressed refrigerant and an external heat recovery fluid;
    separating the compressed refrigerant into a gaseous component and a liquid component, wherein
    the gaseous component is cooled and/or condensed and delivered into a receiver (14); and
    the liquid component is delivered directly into the receiver (14);
    expanding and evaporating liquefied refrigerant taken from the receiver (14); and
    tapping gaseous refrigerant from an upper portion of the receiver (14) to an inlet side of the at least one compressor (2a, 2b, 2c, 2d).
  11. Method of operating a refrigeration circuit (1) of claim 10, wherein the step of separating the compressed refrigerant into a gaseous component and a liquid component is performed within a gas/liquid separator (8), the liquid component is collected within the gas/liquid separator (8) and the method further comprises the step of determining the amount of liquid refrigerant collected within the gas/liquid separator (8).
  12. Method of operating a refrigeration circuit (1) of claim 11, wherein the method further comprises the step of transferring liquid refrigerant from the gas/liquid separator (8) to the receiver (14) when the level of liquid refrigerant collected with the gas/liquid separator (8) exceeds a predetermined level.
  13. Method of operating a refrigeration circuit (1) of any of claim 10 to 12 further comprising the steps of
    expanding the tapped gaseous refrigerant; and/or
    providing heat-exchange between the expanded tapped gaseous refrigerant and liquid refrigerant delivered from the receiver (14).
  14. Method of operating a refrigeration circuit (1) of any of claim 10 to 13, wherein the cooled and/or condensed refrigerant is partially expanded before being delivered into the receiver (14).
EP16165542.8A 2013-09-19 2013-09-19 Refrigeration circuit with heat recovery module Not-in-force EP3086057B1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
EP16165542.8A EP3086057B1 (en) 2013-09-19 2013-09-19 Refrigeration circuit with heat recovery module
DK16165542.8T DK3086057T3 (en) 2013-09-19 2013-09-19 COOLING CIRCUIT WITH HEAT RECOVERY MODULE

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
EP16165542.8A EP3086057B1 (en) 2013-09-19 2013-09-19 Refrigeration circuit with heat recovery module
PCT/EP2013/069510 WO2015039688A1 (en) 2013-09-19 2013-09-19 Refrigeration circuit with heat recovery module
EP13763104.0A EP3047218B1 (en) 2013-09-19 2013-09-19 Refrigeration circuit with heat recovery module and a method of operating the same

Related Parent Applications (2)

Application Number Title Priority Date Filing Date
EP13763104.0A Division-Into EP3047218B1 (en) 2013-09-19 2013-09-19 Refrigeration circuit with heat recovery module and a method of operating the same
EP13763104.0A Division EP3047218B1 (en) 2013-09-19 2013-09-19 Refrigeration circuit with heat recovery module and a method of operating the same

Publications (2)

Publication Number Publication Date
EP3086057A1 EP3086057A1 (en) 2016-10-26
EP3086057B1 true EP3086057B1 (en) 2018-06-13

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EP13763104.0A Active EP3047218B1 (en) 2013-09-19 2013-09-19 Refrigeration circuit with heat recovery module and a method of operating the same

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US (1) US20160231040A1 (en)
EP (2) EP3086057B1 (en)
CN (1) CN105556220B (en)
DK (2) DK3086057T3 (en)
RU (1) RU2659679C2 (en)
WO (1) WO2015039688A1 (en)

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6188918B2 (en) * 2014-03-14 2017-08-30 三菱電機株式会社 Refrigeration equipment
CN105899884B (en) * 2014-03-20 2018-12-14 三菱电机株式会社 Heat source side unit and air-conditioning device
EP3023712A1 (en) * 2014-11-19 2016-05-25 Danfoss A/S A method for controlling a vapour compression system with a receiver
DK3256798T3 (en) * 2015-02-09 2023-03-06 Carrier Corp COOLING AND HEATING SYSTEM
CN107850356B (en) * 2015-07-01 2020-12-08 特灵空调系统(中国)有限公司 Heat recovery system with liquid separator application
US11060767B2 (en) * 2015-11-05 2021-07-13 Danfoss A/S Method for switching compressor capacity
CN109073281B (en) * 2016-04-18 2021-05-25 江森自控科技公司 Condenser evaporator system with subcooler for refrigeration system
PL3628942T3 (en) 2018-09-25 2021-10-04 Danfoss A/S A method for controlling a vapour compression system at a reduced suction pressure
EP3628940B1 (en) 2018-09-25 2022-04-20 Danfoss A/S A method for controlling a vapour compression system based on estimated flow
CN111637667B (en) * 2019-03-01 2022-02-11 浙江盾安机电科技有限公司 Economizer and heat transfer system
US11112147B2 (en) 2019-10-24 2021-09-07 M.D, Mechanical Devices Ltd. Cooling system with controlled biphase mixing of refrigerant

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5189885A (en) * 1991-11-08 1993-03-02 H. A. Phillips & Co. Recirculating refrigeration system
JP3257044B2 (en) * 1992-07-15 2002-02-18 株式会社デンソー Injection type refrigeration equipment
US5655379A (en) * 1995-10-27 1997-08-12 General Electric Company Refrigerant level control in a refrigeration system
JP2003106687A (en) * 2001-09-27 2003-04-09 Daikin Ind Ltd Refrigerator
RU2208748C1 (en) * 2002-01-21 2003-07-20 Государственное общеобразовательное учреждение Дальневосточный государственный технический рыбохозяйственный университет Refrigerating plant
US6807813B1 (en) * 2003-04-23 2004-10-26 Gaetan Lesage Refrigeration defrost system
JP2005030586A (en) * 2003-07-07 2005-02-03 Lg Electron Inc Electromagnetic fluid control valve
JP2006038386A (en) * 2004-07-29 2006-02-09 Daikin Ind Ltd Cooling device
WO2006042015A1 (en) * 2004-10-07 2006-04-20 Brooks Automation, Inc. Efficient heat exchanger for refrigeration process
BRPI0519939A2 (en) * 2005-02-02 2009-09-08 Carrier Corp refrigeration system
US20120022706A1 (en) * 2009-03-27 2012-01-26 Carrier Corporation System and method for controlling a refrigeration system
WO2012168544A1 (en) * 2011-06-06 2012-12-13 Huurre Group Oy A multi-evaporator refrigeration circuit
GB2491582B (en) * 2011-06-06 2015-12-02 Excalibur Lpa Ltd Energy recovery system
WO2013004298A1 (en) * 2011-07-05 2013-01-10 Carrier Corporation Refrigeration circuit, gas-liquid separator and heating and cooling system

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
None *

Also Published As

Publication number Publication date
EP3047218A1 (en) 2016-07-27
WO2015039688A1 (en) 2015-03-26
CN105556220B (en) 2019-01-22
RU2659679C2 (en) 2018-07-03
US20160231040A1 (en) 2016-08-11
EP3086057A1 (en) 2016-10-26
DK3086057T3 (en) 2018-09-17
DK3047218T3 (en) 2021-07-05
CN105556220A (en) 2016-05-04
RU2016115092A (en) 2017-10-24
EP3047218B1 (en) 2021-04-28

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