EP1795833A1 - Kühlvorrichtung - Google Patents

Kühlvorrichtung Download PDF

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Publication number
EP1795833A1
EP1795833A1 EP05782353A EP05782353A EP1795833A1 EP 1795833 A1 EP1795833 A1 EP 1795833A1 EP 05782353 A EP05782353 A EP 05782353A EP 05782353 A EP05782353 A EP 05782353A EP 1795833 A1 EP1795833 A1 EP 1795833A1
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EP
European Patent Office
Prior art keywords
refrigerant
compressor
drawn
wet state
expander
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.)
Withdrawn
Application number
EP05782353A
Other languages
English (en)
French (fr)
Other versions
EP1795833A4 (de
Inventor
Katsumi Kanaoka Factory Sakai Plant SAKITANI
Michio Kanaoka Factory Sakai Plant MORIWAKI
Yume Kanaoka Factory Sakai Plant INOKUCHI
Tetsuya Kanaoka Factory Sakai Plant OKAMOTO
Yoshinari Kanaoka Factory Sakai Plant SASAKI
Eiji Kanaoka Factory Sakai Plant KUMAKURA
Masakazu Kanaoka Factory Sakai Plant OKAMOTO
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.)
Daikin Industries Ltd
Original Assignee
Daikin Industries Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Daikin Industries Ltd filed Critical Daikin Industries Ltd
Publication of EP1795833A1 publication Critical patent/EP1795833A1/de
Publication of EP1795833A4 publication Critical patent/EP1795833A4/de
Withdrawn legal-status Critical Current

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Classifications

    • 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
    • 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
    • F25B13/00—Compression machines, plants or systems, with reversible cycle
    • 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
    • F25B11/00—Compression machines, plants or systems, using turbines, e.g. gas turbines
    • F25B11/02—Compression machines, plants or systems, using turbines, e.g. gas turbines as expanders
    • 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
    • F25B43/00—Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
    • 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
    • F25B9/00—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
    • F25B9/002—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant
    • F25B9/008—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant the refrigerant being carbon dioxide
    • 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
    • F25B9/00—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
    • F25B9/06—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point using expanders
    • 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
    • F25B1/04—Compression machines, plants or systems with non-reversible cycle with compressor of rotary type
    • 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
    • F25B2309/00—Gas cycle refrigeration machines
    • F25B2309/06—Compression machines, plants or systems characterised by the refrigerant being carbon dioxide
    • F25B2309/061—Compression machines, plants or systems characterised by the refrigerant being carbon dioxide with cycle highest pressure above the supercritical pressure
    • 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
    • F25B2313/00—Compression machines, plants or systems with reversible cycle not otherwise provided for
    • F25B2313/027—Compression machines, plants or systems with reversible cycle not otherwise provided for characterised by the reversing means
    • F25B2313/0272—Compression machines, plants or systems with reversible cycle not otherwise provided for characterised by the reversing means using bridge circuits of one-way valves
    • 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
    • F25B2600/17—Control issues by controlling the pressure of the condenser
    • 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
    • F25B2600/2513—Expansion valves

Definitions

  • the present invention generally relates to the field of refrigeration apparatuses. This invention is concerned in particular with a refrigeration apparatus capable of performing operation with an optimum COP (coefficient of performance).
  • Refrigeration apparatuses having a refrigerant circuit configured to circulate refrigerant to perform a vapor compression refrigeration cycle as disclosed in JP-A-2003-106609 , have heretofore been known in the conventional technology.
  • Some of these refrigeration apparatuses are provided with a refrigerant circuit in which a compressor, condenser, expansion valve and evaporator are connected. The opening of the expansion valve is controlled such that gas refrigerant having a predetermined degree of superheat is drawn into the compressor. This prevents the compressor from getting damaged by wet compression.
  • a primary object of the invention is to enable drawing of refrigerant in a proper wet state into a compressor, which wet state provides the maximum or substantially maximum coefficient of performance, so that energy saving operation is realized.
  • the present invention provides the following aspects.
  • the present invention provides, as a first aspect, a refrigeration apparatus comprising a refrigerant circuit (20) for performing a refrigeration cycle which circuit includes a compressor (31).
  • This apparatus is configured such that refrigerant in a wet state, which provides an optimum coefficient of performance (COP) for a present operating state, is drawn into the compressor (31).
  • COP coefficient of performance
  • the refrigerant circulates to perform a vapor compression refrigeration cycle in the refrigerant circuit (20).
  • the high pressure and low pressure of the refrigeration cycle, the compression efficiency of the compressor (31) and others, for instance, are set as operating conditions for every operating state and the dryness fraction (wet state) of the refrigerant which provides the optimum coefficient of performance (COP) for each operating state is set. Since the refrigerant having the set dryness fraction is drawn into the compressor (31), the refrigeration apparatus will perform operation with the best coefficient of performance without fail.
  • the present invention provides, as a second aspect, a refrigeration apparatus comprising the refrigerant circuit (20) for performing a refrigeration cycle which circuit includes the compressor (31).
  • This apparatus is configured such that the refrigerant in a superheated state is drawn into the compressor (31) during a cooling operation mode and the refrigerant in a wet state is drawn into the compressor (31) during a heating operation mode.
  • the refrigerant circulates to perform a vapor compression refrigeration cycle in the refrigerant circuit (20).
  • the refrigerant in a wet state i.e., having a dryness fraction of less than 1.00 is constantly drawn into the compressor (31). Therefore, the coefficient of performance (COP) remarkably increases compared to the case where superheated refrigerant having a dryness fraction of 1.00 or more is drawn, as seen from the result of simulation shown in Figs. 3, 4.
  • the refrigeration apparatus can perform energy saving operation. Further energy saving can be achieved by drawing the refrigerant into the compressor (31), the refrigerant having the optimum dryness fraction that is varied according to operating states so as to provide the maximum coefficient of performance.
  • the invention provides, as a third aspect, a refrigeration apparatus comprising the refrigerant circuit (20) for performing a refrigeration cycle which circuit includes the compressor (31).
  • the above apparatus is configured such that a target discharge temperature for the compressor (31) is set so as to obtain the optimum coefficient of performance (COP) for a present operating state and the refrigerant in a wet state, which makes the discharge temperature of the compressor (31) equal to the target discharge temperature, is drawn into the compressor (31).
  • COP coefficient of performance
  • the refrigerant circulates to perform a vapor compression refrigeration cycle in the refrigerant circuit (20).
  • a target discharge temperature for the compressor (31) that provides the optimum coefficient of performance is set according to a given set of operating conditions which include the high pressure and low pressure of the refrigeration cycle, the compression efficiency of the compressor (31), etc. More specifically, since the discharge temperature of the compressor (31) drops with decreases in the dryness fraction of the refrigerant and rises with increases in the dryness fraction of the refrigerant, the discharge temperature of the compressor (31) is determined in accordance with the dryness fraction of the refrigerant under each set of operating conditions. It is understood from this that as shown in Figs.
  • the dryness fraction (wet state) of the refrigerant that provides the optimum coefficient of performance is determined for each set of operating conditions and the target discharge temperature for the compressor (31) that corresponds to this dryness fraction of the refrigerant is set. Therefore, operation can be performed with the optimum coefficient of performance without fail by drawing, into the compressor (31), the refrigerant having a dryness fraction that makes the discharge temperature of the compressor (31) equal to a target discharge temperature.
  • the discharge temperature of the compressor (31) since the refrigerant in a wet state is drawn into the compressor (31), the discharge temperature of the compressor (31) more significantly drops, compared to the case where refrigerant in a superheated state is drawn. Therefore, abnormal heating of the motor of the compressor (31) can be avoided and deterioration of the refrigerating machine fluid due to high temperature can be restrained. This leads to an increase in the reliability of the compressor (31).
  • the invention provides, as a fourth aspect, the refrigeration apparatus according to any one of the first to third aspects, wherein the refrigerant circuit (20) is provided with an expansion valve (23).
  • This apparatus is configured such that the wet state of a suction refrigerant of the compressor (31) is controlled by adjusting the opening of the expansion valve (23).
  • the opening of the expansion valve (23) is increased thereby increasing the amount of refrigerant to be supplied to the evaporator. This increases the amount of refrigerant which cannot be evaporated by the evaporator so that refrigerant in a wetter state is drawn into the compressor (31).
  • the opening of the expansion valve (23) is reduced thereby reducing the amount of refrigerant to be supplied to the evaporator.
  • the dryness fraction of the refrigerant which provides the maximum coefficient of performance is set according to operating conditions and the opening of the expansion valve (23) is adjusted according to the set dryness fraction, whereby energy saving operation which provides the maximum coefficient of performance corresponding to each set of operating conditions can be performed.
  • the invention provides, as a fifth aspect, the refrigeration apparatus according to any one of the first to third aspects, wherein the refrigerant circuit (20) has a gas-liquid separator (25) disposed between evaporators (22, 24) and the suction side of the compressor (31).
  • the gas-liquid separator (25) includes a liquid injection pipe (26) having a flow rate control valve (27), for guiding liquid refrigerant from the gas-liquid separator (25) to the suction side of the compressor (31).
  • This apparatus is further configured such that the wet state of the suction refrigerant of the compressor (31) is controlled by adjusting the flow rate control valve (27).
  • the opening of the flow rate control valve (27) when increasing the wetness fraction of the suction refrigerant of the compressor (31) for instance, that is, when reducing the dryness fraction of the suction refrigerant, the opening of the flow rate control valve (27) is increased thereby increasing the flow rate of the liquid refrigerant to be drawn into the compressor (31).
  • the opening of the flow rate control valve (27) when reducing the wetness fraction of the suction refrigerant of the compressor (31), that is, when increasing the dryness fraction of the suction refrigerant, the opening of the flow rate control valve (27) is reduced thereby reducing the flow rate of the liquid refrigerant to be drawn into the compressor (31).
  • the dryness fraction of the refrigerant which provides the maximum coefficient of performance is set according to operating conditions and the opening of the flow rate control valve (27) is adjusted according to the set dryness fraction, whereby energy saving operation which provides the maximum coefficient of performance corresponding to each set of operating conditions can be performed.
  • the invention provides, as a sixth aspect, the refrigeration apparatus according to any one of the first to third aspects, wherein the refrigerant circuit (20) has an expander (33) mechanically connected to the compressor (31) through a motor (32) of the compressor (31).
  • the refrigerant circuit (20) includes a bypass pipe (44) through which a part of the refrigerant flowing to the expander (33) flows, bypassing the expander (33), and a flow rate control valve (45) provided in the bypass pipe (44).
  • This apparatus is configured such that the wet state of the suction refrigerant of the compressor (31) is controlled by adjusting the flow rate control valve (45).
  • the opening of the flow rate control valve (45) is increased, that is, the amount of refrigerant that flows, bypassing the expander (33) is increased, thereby increasing the amount of refrigerant supplied to the evaporator.
  • the amount of refrigerant that cannot be evaporated by the evaporator increases so that refrigerant in a wetter state is drawn into the compressor (31).
  • the opening of the flow rate control valve (45) is reduced, that is, the amount of refrigerant that flows, bypassing the expander (33) is reduced, thereby reducing the amount of refrigerant supplied to the evaporator.
  • the amount of refrigerant that cannot be evaporated by the evaporator decreases so that refrigerant in a less wet state is drawn into the compressor (31).
  • the dryness fraction of the refrigerant which provides the maximum coefficient of performance is set according to operating conditions and the opening of the flow rate control valve (45) is adjusted according to the set dryness fraction, whereby energy saving operation which provides the maximum coefficient of performance corresponding to each set of operating conditions can be performed.
  • the energy generated when the refrigerant is expanded by the expander (33) is converted into a rotating force which is in turn recovered as the power of the compressor (31) through the motor (32).
  • the compressor (31) and the expander (33) used herein are of the positive displacement type and therefore the balance between the compressor (31) and the expander (33) in terms of the flow rate of the refrigerant flowing therein is lost owing to variations in the operating conditions.
  • the flow rates of the refrigerant flowing in the compressor (31) and in the expander (33) can be rebalanced by the above-described technique in which the amount of refrigerant sent to the expander (33) is controlled by adjusting the opening of the flow rate control valve (27) provided that the dryness fraction of the refrigerant drawn into the compressor (31) is optimum. This enables higher-efficiency operation.
  • the invention provides, as a seventh aspect, the refrigeration apparatus according to any one of the first to third aspects, wherein the refrigerant circuit (20) is configured such that the high pressure of the refrigeration cycle is higher than the critical pressure of the refrigerant.
  • the compressor (31) compresses the refrigerant to a specified level of pressure higher than the critical pressure of the refrigerant. This means that the discharge refrigerant of the compressor (31) is in a supercritical state. Thereby, even if the refrigerant in a wet state is drawn into the compressor (31), no liquid refrigerant exists at least in the discharge section so that the so-called liquid compression can be avoided without fail.
  • the invention provides, as an eighth aspect, the refrigeration apparatus according to the seventh aspect, wherein the refrigerant is carbon dioxide.
  • the apparatus constructed according to the eighth aspect is earth-conscious, because the refrigerant is carbon dioxide (CO 2 ).
  • the coefficient of performance (COP) can be improved, compared to the case where refrigerant in a superheated state is drawn. Further, the maximum energy saving can be attained in the operation by bringing the suction refrigerant of the compressor (31) into a wet state that provides the maximum coefficient of performance.
  • refrigerant in a wet state is drawn into the compressor (31)
  • not only the discharge temperature of the compressor (31) can be lowered but also degradation of the refrigerating machine fluid in the compressor (31) due to high temperature can be restrained, compared to the case where refrigerant in a superheated state is drawn. In consequence, the reliability of the apparatus can be improved.
  • the refrigeration apparatus since refrigerant in a wet state is drawn into the compressor (31) during the heating operation mode, at least heating operation can be performed with the optimum coefficient of performance.
  • the refrigeration apparatus since refrigerant in a wet state is drawn into the compressor (31) such that the discharge temperature of the compressor (31) becomes equal to a predetermined temperature that provides the optimum coefficient of performance, the refrigeration apparatus can perform operation with the optimum coefficient of performance without fail. Further, since the wet state of the refrigerant may be controlled according to the discharge temperature of the compressor (31), the coefficient of performance of the refrigeration cycle can be easily controlled.
  • the refrigeration apparatus can perform operation with the maximum coefficient of performance over a wide range of operating conditions without fail by setting a dryness fraction of the refrigerant that provides the optimum coefficient of performance according to operating conditions.
  • the amount of refrigerant supplied to the expander (33) can be controlled by adjusting the opening of the flow rate control valve (45) provided that the suction refrigerant of the compressor (31) has an optimum dryness fraction, so that the amounts of refrigerant in the expander (33) and in the compressor (31) can be rebalanced. This leads to a further improvement in the efficiency.
  • the refrigerant circuit (20) is configured to perform a supercritical cycle in which the high pressure of the refrigeration cycle is higher than the critical pressure of the refrigerant, the discharge refrigerant of the compressor (31) comes into a superheated state without fail. Accordingly, when refrigerant in a wet state is drawn into the compressor (31), the refrigerant in the discharging section of the compressor (31) is already in a superheated state and therefore, liquid compression can be prevented from occurring in the compressor (31) without fail. In consequence, a highly-reliable apparatus can be achieved.
  • An air conditioner (10) constitutes the refrigeration apparatus of the invention.
  • the air conditioner (10) is of the so-called separate type and includes an outdoor unit (11) and an indoor unit (12).
  • Housed in the outdoor unit (11) are a compressor (31), a four way switch valve (21), an outdoor heat exchanger (24), an expansion valve (23) and a gas-liquid separator (25).
  • Housed in the indoor unit (12) is an indoor heat exchanger (22).
  • the outdoor unit (11) is installed outdoors whereas the indoor unit (12) is installed indoors.
  • the outdoor unit (11) is connected to the indoor unit (12) with a pair of interunit pipelines (13, 14).
  • the air conditioner (10) includes a refrigerant circuit (20).
  • the refrigerant circuit (20) is constructed in the form of a closed circuit to which a compressor (31), the indoor heat exchanger (22) and others are connected.
  • the refrigerant circuit (20) is filled with carbon dioxide (CO 2 ) serving as refrigerant and configured to circulate the refrigerant, thereby performing a vapor compression refrigeration cycle.
  • CO 2 carbon dioxide
  • the compressor (31) is driven by a motor (32) mechanically connected thereto and constituted, for instance, by a scroll compressor of the hermetic, high pressure dome type.
  • This compressor (31) is designed to compress the refrigerant to a pressure level higher than the critical pressure of the refrigerant.
  • the high pressure of the vapor compression refrigeration cycle becomes higher than the critical pressure of carbon dioxide.
  • the outdoor heat exchanger (24) and the indoor heat exchanger (22) are both constituted by a fin and tube heat exchanger of the cross fin type.
  • the outdoor heat exchanger (24) the heat of the refrigerant circulating in the refrigerant circuit (20) is exchanged with the heat of outdoor air.
  • the indoor heat exchanger (22) the heat of the refrigerant circulating in the refrigerant circuit (20) is exchanged with the heat of indoor air.
  • the four way switch valve (21) has four ports.
  • the first port is connected to a discharge pipe (3a) of the compressor (31);
  • the second port is to a suction pipe (3b) of the compressor (31) through the gas-liquid separator (25);
  • the third port is to one end of the outdoor heat exchanger (24);
  • the fourth port is to one end of the indoor heat exchanger (22) through the interunit pipeline (13).
  • the other end of the indoor heat exchanger (22) is connected to the other end of the outdoor heat exchanger (24) through the interunit pipeline (14) and the expansion valve (23).
  • the four way switch valve (21) is switchable between a first state that allows fluid communication between the first port and the third port and fluid communication between the second port and the fourth port (the sate as indicated by broken line in Fig. 1) and a second state that allows fluid communication between the first port and the fourth port and fluid communication between the second port and the third port (the sate as indicated by solid line in Fig. 1).
  • the refrigerant circuit (20) is switchable between a cooling operation mode and a heating operation mode by switching effectuated by the four way switch valve (21). Specifically, when the four way switch valve (21) has been switched to the state indicated by broken line in Fig. 1, the refrigerant circuit (20) circulates the refrigerant so as to perform cooling operation in which the refrigerant dissipates heat in the outdoor heat exchanger (24) and evaporates in the indoor heat exchanger (22). When the four way switch valve (21) has been switched to the state indicated by solid line in Fig. 1, the refrigerant circuit (20) circulates the refrigerant so as to perform heating operation in which the refrigerant dissipates heat in the indoor heat exchanger (22) and evaporates in the outdoor heat exchanger (24).
  • the indoor heat exchanger (22) serves as an evaporator whereas the outdoor heat exchanger (24) as a heat dissipater.
  • the outdoor heat exchanger (24) serves as an evaporator the indoor heat exchanger (22) as a heat dissipater.
  • the gas-liquid separator (25) is provided with a liquid injection pipe (26). More concretely, the liquid injection pipe (26) is connected at one end to a liquid reservoir section of the gas-liquid separator (25) and connected at the other end to the suction pipe (3b) of the compressor (31). The liquid injection pipe (26) is configured to guide the liquid refrigerant stored in the gas-liquid separator (25) to the suction side of the compressor (31).
  • the liquid injection pipe (26) is provided with a flow rate control valve (27) constituted by a motor-operated valve for controlling the flow rate of the liquid refrigerant flowing in the liquid injection pipe (26).
  • the air conditioner (10) is configured such that, during the normal cooling operation mode, gas refrigerant in a specified superheated state is drawn into the compressor (31) and, during the normal heating operation mode, refrigerant having a specified level of dryness fraction (wet state) is drawn into the compressor (31). That is, the present invention is intended for use in normal operation mode applications and is not intended for use in special operations (e.g., defrost operation) nor conditions such as when the high pressure of a refrigeration cycle becomes abnormally high or the discharge temperature of the compressor (31) becomes abnormally high.
  • special operations e.g., defrost operation
  • the opening of the expansion valve (23) is set such that the refrigerant evaporates into a gas refrigerant in a specified superheated state (e.g., a degree of superheat of 0 ⁇ to 5 ⁇ ) in the indoor heat exchanger (22).
  • a specified superheated state e.g., a degree of superheat of 0 ⁇ to 5 ⁇
  • the opening of the expansion valve (23) is set such that the refrigerant evaporates in the outdoor heat exchanger (24) so as to have a predetermined level of dryness fraction (e.g., 0.83 to 0.89).
  • This predetermined level of dryness fraction has been found by simulation and set to a value that makes the coefficient of performance of the air conditioner (10) in the heating operation mode be optimum.
  • the dryness fraction of the refrigerant drawn into the compressor (31) peaks at 0.83 to 0.89. It is seen from Figs. 3, 4 that as the dryness fraction decreases or increases from the peak region, the coefficient of performance decreases and that as the dryness fraction increases after exceeding 1.00, the coefficient of performance further decreases. It is understood from the above fact that the coefficient of performance can be made closer to its optimum value by drawing the refrigerant in a wet state, i.e., having a dryness fraction of at least less than 1.00 into the compressor (31).
  • the air conditioner (10) is configured such that the dryness fraction of the refrigerant is controlled by controlling the evaporative power of the outdoor heat exchanger (24) by mainly adjusting the opening of the expansion valve (23). Concretely, for increasing the dryness fraction of the refrigerant, the opening of the expansion valve (23) is reduced, and for decreasing the dryness fraction of the refrigerant, the opening of the expansion valve (23) is increased.
  • the dryness fraction of the refrigerant may be controlled through an adjustment of the opening of the flow rate control valve (27) of the liquid injection pipe (26). Specifically, the flow rate of the liquid refrigerant introduced from the gas-liquid separator (25) into the compressor (31) is controlled through an adjustment of the opening of the flow rate control valve (27), thereby controlling the wet state of the refrigerant.
  • the dryness fraction of the refrigerant drawn into the compressor (31) is determined based on the discharge temperature of the compressor (31).
  • the air conditioner (10) is configured such that the dryness fraction of the refrigerant is controlled by adjusting the opening of the expansion valve (23) or the flow rate control valve (27) so as to make the discharge temperature of the compressor (31) equal to a target discharge temperature.
  • the target discharge temperature has been set to a value that allows the coefficient of performance to be optimum.
  • the discharge temperature of the compressor (31) drops as the dryness fraction of the refrigerant drawn into the compressor (31) decreases and rises as the dryness fraction of the refrigerant increases, and therefore, the discharge temperature of the compressor (31) corresponding to the dryness fraction of the refrigerant is determined for every set of operating conditions.
  • the dryness fraction of the refrigerant that makes the coefficient of performance optimum is set for every set of operating conditions and the discharge temperature of the compressor (31) which corresponds to this dryness fraction of the refrigerant is set as a target discharge temperature.
  • the four way switch valve (21) is switched to the state indicated by broken line in Fig. 1. If the motor (32) is activated in this condition, the refrigerant circulates in the direction indicated by dashed arrow in Fig. 1 in the refrigerant circuit (20), thereby performing a vapor compression refrigeration cycle. It should be noted that the flow rate control valve (27) of the liquid injection pipe (26) is in a fully closed state.
  • the refrigerant which has been compressed by the compressor (31), is discharged through the discharge pipe (3a).
  • the pressure of the refrigerant is higher than the critical pressure of the refrigerant.
  • the discharged refrigerant flows to the outdoor heat exchanger (24) through the four way switch valve (21), exchanging heat with the heat of outdoor air for heat dissipation.
  • the refrigerant which has dissipated heat in the outdoor heat exchanger (24) is decompressed down to a predetermined level of pressure by the expansion valve (23) and then exchanges heat with the heat of indoor air in the indoor heat exchanger (22) so that it becomes a gas refrigerant in a superheated state.
  • indoor air is cooled.
  • the gas refrigerant in the superheated state is drawn into the compressor (31) by the suction pipe (3b) after passing through the four way switch valve (21) and then compressed again to be discharged.
  • the four way switch valve (21) is switched to the state indicated by solid line in Fig. 1. If the motor (32) is activated in this condition, the refrigerant circulates in the direction indicated by solid arrow in Fig. 1 in the refrigerant circuit (20), thereby performing a vapor compression refrigeration cycle. In this circulation, the state of the refrigerant changes in the cycle of A1 ⁇ B1 ⁇ C ⁇ D, as indicated by dashed line in Fig. 2.
  • the flow rate control valve (27) of the liquid injection pipe (26) is in a fully closed state. It should be noted that the cycle of A ⁇ B ⁇ C ⁇ D in Fig.
  • FIG. 2 is the conventional refrigeration cycle made when the degree of superheat of the suction refrigerant of the compressor (31) is zero.
  • the refrigerant in the state of point B which has been discharged from the compressor, dissipates heat in the heat dissipater so that it comes into the state of point C.
  • the refrigerant is decompressed in the expansion mechanism so that it comes into the state of point C.
  • the refrigerant evaporates, in the evaporator, into a gas refrigerant having a degree of superheat of zero (point A) which is in turn drawn into the compressor.
  • the refrigerant decompressed by the compressor (31) is discharged from the discharge pipe (3a) (point B in Fig. 2).
  • the pressure of the refrigerant is higher than the critical pressure of the refrigerant.
  • the discharge refrigerant flows to the indoor heat exchanger (22) by way of the four way switch valve (21) and then dissipates heat, exchanging heat with the heat of indoor air (point C in Fig. 2) . At that time, the indoor air is heated.
  • the refrigerant which has dissipated heat in the indoor heat exchanger (22) is decompressed down to a predetermined level of pressure (point D) by the expansion valve (23), it evaporates, exchanging heat with the heat of outdoor air in the outdoor heat exchanger (24) (point A1 in Fig. 2).
  • the refrigerant which has evaporated has the predetermined level of dryness fraction (wet state) that makes the coefficient of performance optimum.
  • the refrigerant in the wet state is drawn into the compressor (31) by the suction pipe (3b) after passing through the four way switch valve (21). This refrigerant is decompressed again, coming into the superheated state and then discharged. In this way, the heating operation is performed with the optimum coefficient of performance so that energy saving is achieved.
  • the values of the high pressure, low pressure etc. of the refrigeration cycle are altered to provide a new set of operating conditions and a target discharge temperature for the compressor (31) is set according to the new set of operating conditions. Thereafter, the opening of the expansion valve (23) is adjusted or alternatively, the opening of the flow rate control valve (27) of the liquid injection pipe (26) is adjusted, such that the discharge temperature of the compressor (31) becomes equal to the target discharge temperature. Thereby, the dryness fraction of the refrigerant drawn into the compressor (31) becomes optimum, whereby operation can be performed with the optimum coefficient of performance corresponding to the given set of operating conditions.
  • the discharge temperature of the compressor (31) significantly drops compared to the case where the refrigerant in a superheated state is drawn like the prior art. Thanks to this, the temperature of the motor (32) is prevented from abnormally rising and the refrigerating machine fluid within the compressor (31) is prevented from being heated to high temperature and deteriorating. This results in an improvement in the reliability of the refrigeration apparatus.
  • the refrigerating machine fluid discharged from the compressor (31) together with the refrigerant generally flows to the evaporator and tends to stay in the evaporator because the refrigerant flowing out from the evaporator is in a perfect gaseous state.
  • the refrigerant flowing out from the outdoor heat exchanger (24) that serves as an evaporator is in a wet state, that is, a gas-liquid two-phase state, and therefore it more easily carries the refrigerating machine fluid out of the heat exchanger than a refrigerant in a gaseous state does. Since a large amount of refrigerating machine fluid is thus allowed to flow back to the compressor (31), defective lubrication of the compressor (31) can be restrained.
  • the first embodiment can optimize the coefficient of performance in normal operation, unlike the conventional liquid injection that is employed in applications such as defrost operation or when the discharge temperature of the compressor (31) becomes abnormally high.
  • the refrigeration apparatus can perform operation with the optimum coefficient of efficiency without fail.
  • the refrigeration apparatus can easily perform operation with the optimum coefficient of performance without fail.
  • the air conditioner (10) of the second embodiment is configured such that an expander (33) mechanically connected to the compressor (31) through the motor (32) is employed in place of the expansion valve (23) used as an expansion mechanism for the refrigeration cycle in the first embodiment.
  • the compressor (31), the motor (32) and the expander (33) are housed in a casing as one unit.
  • the compressor (31) is implemented, for example, by a positive displacement type compressor such as rotary compressor, scroll compressor etc.
  • the expander (33) is implemented, for example, by a positive displacement type expander such as rotary expander, scroll expander etc.
  • the expander (33) is implemented by the so-called two-stage expander provided with two cylinders, which is expanded by a first-stage cylinder and then further expanded by a second-stage cylinder.
  • the expander (33) is designed to recover power. Specifically, the expander (33) recovers power in such a way that the energy generated in the expansion of the refrigerant in the expander (33) is utilized as a rotating power for driving the compressor (31).
  • the casing for housing the compressor (31) and the expander (33) has, in addition to the discharge pipe (3a) and suction pipe (3b) for the compressor (31), an inflow port (3c) through which the refrigerant flows into the first-stage cylinder of the expander (33) and an outflow port (3d) through which the refrigerant after expansion goes out from the second-stage cylinder to the outside of the casing.
  • the refrigerant circuit (20) includes a bridge circuit (41) disposed between the interunit pipeline (14) and the outdoor heat exchanger (24) which are provided in the outdoor unit (11).
  • the bridge circuit (41) comprises a bridge connection of four check valves (CV1, CV2, CV3, CV4).
  • the bridge circuit (41) is configured such that the inflow sides of the first check valve (CV1) and the fourth check valve (CV4) are connected to the outflow port (3d) of the expander (33); the outflow sides of the second check valve (CV2) and the third check valve (CV3) are connected to the inflow port (3c) of the expander (33); the outflow side of the first check valve (CV1) and the inflow side of the second check valve (CV2) are connected to the other end of the indoor heat exchanger (22) through the interunit pipeline (14); and the inflow side of the third check valve (CV3) and the outflow side of the fourth check valve (CV4) are connected to the other end of the outdoor heat exchanger (24).
  • the refrigerant circuit (20) has an injection pipe (42).
  • the injection pipe (42) is connected, at one end, between the bridge circuit (41) and the inflow port (3c) of the expander (33) and connected, at the other end, to an intermediate port (not shown) of the first-stage and second-stage cylinders of the expander (33).
  • the injection pipe (42) is provided with an injection valve (43).
  • This injection valve (43) is a motor-operated valve for controlling the flow rate of the refrigerant in the injection pipe (42) and constitutes a flow rate control valve.
  • the refrigerant circuit (20) is provided with a bypass pipe (44).
  • the bypass pipe (44) is connected, at one end, between the bridge circuit (41) and the inflow port (3c) of the expander (33) and connected, at the other end, between the inflow port (3c) of the expander (33) and the bridge circuit (41).
  • the bypass pipe (44) is provided with a bypass valve (45).
  • This bypass valve (45) is a motor-operated valve for controlling the flow rate of the refrigerant in the bypass pipe (44) and constitutes a flow rate control valve.
  • the bypass pipe (44) is configured such that a part of the refrigerant flowing from the bridge circuit (41) to the expander (33) flows so as to bypass the expander (33) when the bypass valve (45) is in its open state.
  • the air conditioner (10) of the second embodiment is configured such that, like the first embodiment, gas refrigerant in a specified superheated state is drawn into the compressor (31) during the cooling operation mode and refrigerant in a specified wet state is drawn into the compressor (31) during the heating operation mode. More concretely, in the cooling operation, the opening of the injection valve (43) is set so as to make the refrigerant evaporate into a gas refrigerant in a specified superheated state (e.g., having a degree of superheat of 0 ⁇ to 5 ⁇ ) in the indoor heat exchanger (22).
  • a specified superheated state e.g., having a degree of superheat of 0 ⁇ to 5 ⁇
  • the opening of the injection valve (43) is set so as to make the refrigerant evaporate and have a predetermined dryness fraction (e.g., 0.71 to 0.77) in the outdoor heat exchanger (24).
  • the predetermined dryness fraction is set to a value that makes the coefficient of performance optimum, as shown in the lower table of Fig. 3 and indicated by line E in the graph of Fig. 4.
  • This simulation was done with the following operating conditions: the high pressure and low pressure of the refrigeration cycle were set to 10 MPa and 3.5 MPa respectively, the outlet temperature of the indoor heat exchanger (22) was set to 25 ⁇ , and the compression efficiency of the compressor (31) was set to 70%.
  • the dryness fraction of the refrigerant is controlled by mainly adjusting the openings of the injection valve (43) and the bypass valve (45). Concretely, only the opening of the injection valve (43) is adjusted while the bypass valve (45) being in its fully closed state. For increasing the dryness fraction of the refrigerant for instance, the opening of the injection valve (43) is reduced. For decreasing the dryness fraction of the refrigerant, the opening of the injection valve (43) is increased. If the injection valve (43) has been fully opened and therefore the flow rate of the refrigerant in the injection pipe (42) cannot be increased any more, the opening of the bypass valve (45) will be adjusted with the injection valve (43) being in its fully open state.
  • the dryness fraction of the refrigerant may be controlled by adjusting the opening of the flow rate control valve (27) of the liquid injection pipe (26) similarly to the first embodiment.
  • the four way switch valve (21) is switched to the state indicated by broken line in Fig. 5.
  • the motor (32) is activated, the refrigerant circulates in the direction indicated by dashed arrow in Fig. 5 in the refrigerant circuit (20), thereby performing a vapor compression refrigeration cycle.
  • the bypass valve (45) and the flow rate control valve (27) are placed in a fully closed state.
  • the refrigerant which has dissipated heat in the outdoor heat exchanger (24), passes through the third check valve (CV3) of the bridge circuit (41). Then, a part of it flows into the first-stage cylinder of the expander (33) through the inflow port (3c) whereas the remaining part flows into the intermediate port of the expander (33) through the injection pipe (42).
  • the expander (33) the refrigerant expands and its internal energy is converted into the rotating force of the motor (32) which is in turn recovered as the power of the compressor (31).
  • the refrigerant after expansion flows out from the outflow port (3d) and flows into the indoor heat exchanger (22) after passing through the first check valve (CV1) of the bridge circuit (41).
  • the indoor heat exchanger (22) the refrigerant evaporates, exchanging heat with the heat of indoor air so that it becomes a gas refrigerant in a superheated state.
  • the four way switch valve (21) is switched to the state indicated by solid line in Fig. 5. If the motor (32) is activated in this condition, the refrigerant circulates in the direction indicated by solid arrow in Fig. 5 in the refrigerant circuit (20), thereby performing a vapor compression refrigeration cycle. In this circulation, the state of the refrigerant changes in the cycle of A2 ⁇ B2 ⁇ C ⁇ D2, as indicated by solid line in Fig. 2. It should be noted that the bypass valve (45) and the flow rate control valve (27) are placed in a fully closed state.
  • the discharge refrigerant (indicated by point B2 in Fig. 2) of the compressor (31) dissipates heat in the indoor heat exchanger (22) (at point C in Fig. 2).
  • this refrigerant has passed through the second check valve (CV2) of the bridge circuit (41)
  • a part of it flows into the first-stage cylinder of the expander (33) through the inflow port (3c) whereas the remaining part flows into the intermediate port of the expander (33) through the injection pipe (42).
  • the refrigerant expands and its internal energy is converted into the rotating force of the motor (32) which is in turn recovered as the power of the compressor (31) (at point D2 in Fig. 2).
  • the refrigerant After expansion, the refrigerant goes out from the outflow port (3d) and then flows into the outdoor heat exchanger (24) by way of the fourth check valve (CV4) of the bridge circuit (41).
  • the refrigerant evaporates, exchanging heat with the heat of outdoor air (at point A2 in Fig. 2).
  • the evaporated refrigerant has a predetermined dryness fraction (wet state) that makes the coefficient of performance optimum.
  • the high pressure and low pressure of the refrigeration cycle are altered to set a new set of operating conditions according to which a target discharge temperature is set for the compressor (31). Then, the opening of the injection valve (43) is adjusted such that the discharge temperature of the compressor (31) becomes equal to the target discharge temperature. When the injection valve (43) is fully opened, the opening of the bypass valve (45) is then adjusted. Alternatively, the opening of the flow rate control valve (27) of the liquid injection pipe (26) is properly adjusted. Thereby, the dryness fraction of the refrigerant drawn into the compressor (31) becomes optimum so that the refrigeration apparatus can perform with the optimum coefficient of performance in accordance with the given set of operating conditions.
  • the air conditioner (10) of the second embodiment even if the balance between the amount of refrigerant flowing in the expander (33) and the amount of refrigerant flowing in the compressor (31) is lost because of variations in the operating conditions, the amounts of refrigerant flowing in the expander (33) and in the compressor (31) can be rebalanced by introducing a part of the refrigerant from the injection pipe (42) and making the part of the refrigerant bypass the expander (33) by means of the bypass pipe (44), provided that the suction refrigerant of the compressor (31) has an optimum dryness fraction. This leads to an improvement in the rate of power recovery and, in consequence, further energy saving can be achieved. Other arrangements, functions and effects of the second embodiment do not differ from those of the first embodiment.
  • the dryness fraction of the refrigerant may be controlled by adjusting only the opening of the flow rate control valve (27) of the liquid injection pipe (26) provided in the gas-liquid separator (25).
  • the liquid injection pipe (26) of the gas-liquid separator (25) may be omitted. More specifically, the first and second embodiments may be modified such that the dryness fraction of the refrigerant is controlled by adjusting only the openings of the expansion valve (23) and the injection valve (43).
  • bypass pipe (44) and the injection pipe (42) are both provided in the second embodiment, it is possible to provide either one of them and control the dryness fraction of the refrigerant with the flow rate control valve provided for it.
  • the present invention finds useful applications in the field of refrigeration apparatuses having a refrigerant circuit for performing a vapor compression refrigeration cycle.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Analytical Chemistry (AREA)
  • Power Engineering (AREA)
  • Air Conditioning Control Device (AREA)
  • Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
EP05782353.6A 2004-09-09 2005-09-09 Kühlvorrichtung Withdrawn EP1795833A4 (de)

Applications Claiming Priority (2)

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JP2004262176A JP2006078087A (ja) 2004-09-09 2004-09-09 冷凍装置
PCT/JP2005/016643 WO2006028218A1 (ja) 2004-09-09 2005-09-09 冷凍装置

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EP1795833A1 true EP1795833A1 (de) 2007-06-13
EP1795833A4 EP1795833A4 (de) 2014-12-24

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EP (1) EP1795833A4 (de)
JP (1) JP2006078087A (de)
KR (1) KR20070067121A (de)
CN (1) CN100501270C (de)
AU (1) AU2005280900B2 (de)
WO (1) WO2006028218A1 (de)

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JP4258553B2 (ja) 2007-01-31 2009-04-30 ダイキン工業株式会社 熱源ユニット及び冷凍装置
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JP5887902B2 (ja) * 2011-12-14 2016-03-16 パナソニック株式会社 冷凍サイクル装置
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JP2014181869A (ja) * 2013-03-21 2014-09-29 Fujitsu General Ltd 空気調和機
JP6266942B2 (ja) * 2013-10-10 2018-01-24 日立ジョンソンコントロールズ空調株式会社 空気調和機
EP3062045B1 (de) 2013-10-24 2020-12-16 Mitsubishi Electric Corporation Klimaanlage
CN107208937A (zh) * 2015-01-23 2017-09-26 三菱电机株式会社 空气调节装置
CN105115062B (zh) * 2015-08-21 2018-03-30 Tcl空调器(中山)有限公司 空调室外机和空调器
CN105783136B (zh) * 2016-04-14 2019-04-02 海信（山东）空调有限公司 一种室外空调机及空调系统
CN107576096A (zh) * 2017-09-12 2018-01-12 海信（山东）空调有限公司 压缩机单元及空调系统
CN108444128B (zh) * 2018-05-14 2019-05-24 西安交通大学 一种跨临界co2湿压缩热泵系统及其操作方法
JP7275876B2 (ja) * 2019-06-07 2023-05-18 株式会社デンソー 冷凍サイクル装置
CN111059683B (zh) * 2019-12-03 2021-04-02 珠海格力电器股份有限公司 防止压缩机吸气带液发生液击的控制方法、空调器
JP7309045B2 (ja) * 2020-04-07 2023-07-14 三菱電機株式会社 冷凍サイクル装置
EP4134603A4 (de) * 2020-04-07 2023-05-24 Mitsubishi Electric Corporation Kältekreislaufvorrichtung
CN112432341A (zh) * 2020-12-08 2021-03-02 合肥美的暖通设备有限公司 空调系统的控制方法、空调系统和可读存储介质
IT202100007316A1 (it) * 2021-03-25 2022-09-25 Ariston S P A Metodo di gestione di una pompa di calore operante con un fluido operativo a basso impatto ambientale
JP2022157187A (ja) * 2021-03-31 2022-10-14 ダイキン工業株式会社 ヒートポンプ装置
CN114608181B (zh) * 2022-03-21 2023-12-26 青岛海尔空调电子有限公司 电子膨胀阀的控制方法、装置、介质及空气源热泵机组

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AU2005280900B2 (en) 2009-03-05
CN101014813A (zh) 2007-08-08
WO2006028218A1 (ja) 2006-03-16
EP1795833A4 (de) 2014-12-24
AU2005280900A1 (en) 2006-03-16
JP2006078087A (ja) 2006-03-23
CN100501270C (zh) 2009-06-17
US20090113907A1 (en) 2009-05-07
KR20070067121A (ko) 2007-06-27

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