EP2339269B1 - Air conditioner - Google Patents
Air conditioner Download PDFInfo
- Publication number
- EP2339269B1 EP2339269B1 EP10252001.2A EP10252001A EP2339269B1 EP 2339269 B1 EP2339269 B1 EP 2339269B1 EP 10252001 A EP10252001 A EP 10252001A EP 2339269 B1 EP2339269 B1 EP 2339269B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- heat exchanger
- refrigerant
- pipe
- expansion valve
- pressure
- 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
Links
Images
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
- 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
- F25B40/00—Subcoolers, desuperheaters or superheaters
- F25B40/02—Subcoolers
-
- 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
- F25B2313/02741—Compression machines, plants or systems with reversible cycle not otherwise provided for characterised by the reversing means using one four-way valve
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/13—Economisers
-
- 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
- F25B2600/2509—Economiser valves
Definitions
- the present invention relates to an air conditioner having a reversible refrigerating cycle. More particularly, it relates to an air conditioner having a double-pipe heat exchanger in a liquid-side refrigerant pipe connecting an outdoor heat exchanger and an indoor heat exchanger to each other.
- a refrigerating cycle having a double-pipe heat exchanger to increase the degree of supercooling As one of refrigerating cycles applied to an air conditioner, a refrigerating cycle having a double-pipe heat exchanger to increase the degree of supercooling has been known.
- some of a high-pressure liquid refrigerant condensed by a condenser is split and decompressed, and is heat-exchanged with a mainstream high-pressure liquid refrigerant.
- FIG. 3 One example thereof is explained with reference to FIG. 3 .
- Document US 2006/196225 A1 discloses an improvement system of energy efficiency for a refrigeration cycle is comprised of an auxiliary heat exchanger unit for heat-exchanging between refrigerant liquid having high pressure and refrigerant vapor having low pressure and a cabinet which houses a pressure support value placed at an inlet of an inner pipe of the auxiliary heat exchanger unit. A pressure of the refrigerant liquid having high pressure condensed at the outdoor heat exchanger is decreased by the pressure support value, and a condensed pressure of the outdoor heat exchanger is maintained.
- a refrigerating cycle 1B of this conventional example includes, as a basic configuration, a compressor 10, a four-way valve 20, an outdoor heat exchanger 30, and an indoor heat exchanger 40, and the discharge side of the compressor 10 is connected to either one of the outdoor heat exchanger 30 and the indoor heat exchanger 40 via the four-way valve 20.
- the discharge side of the compressor 10 is connected to the outdoor heat exchanger 30, the outdoor heat exchanger 30 functions as a condenser, and the indoor heat exchanger 40 functions as an evaporator.
- the discharge side of the compressor 10 is connected to the indoor heat exchanger 40, the indoor heat exchanger 40 functions as a condenser, and the outdoor heat exchanger 30 functions as an evaporator.
- a condensed liquid refrigerant is mainly caused to flow. Therefore, the refrigerant pipe connecting the outdoor heat exchanger 30 and the indoor heat exchanger 40 to each other is usually called a liquid-side refrigerant pipe 50.
- the liquid-side refrigerant pipe 50 is provided with a double-pipe heat exchanger 60. Also, between the double-pipe heat exchanger 60 and the outdoor heat exchanger 30, a heating expansion valve 51 is provided, and between the double-pipe heat exchanger 60 and the indoor heat exchanger 40, a cooling expansion valve 52 is provided.
- the double-pipe heat exchanger 60 consists, for example, of an inner pipe and an outer pipe arranged coaxially, and a high-pressure liquid refrigerant is caused to flow in the inner pipe.
- a bypass pipe 61 branched from the liquid-side refrigerant pipe 50 is connected, and the bypass pipe 61 is provided with a bypass expansion valve 62.
- a two-way valve 53 and a three-way valve 54 provided on both sides of the indoor heat exchanger 40 are connection pipes for connecting the indoor heat exchanger 40 to the refrigerating cycle when the air conditioner is installed.
- the heating expansion valve 51 is fully opened, and the cooling expansion valve 52 is throttled to a predetermined degree of opening, so that the refrigerant flows as indicated by the solid-line arrow marks in FIG. 3 .
- the cooling expansion valve 52 is fully opened, and the heating expansion valve 51 is throttled to a predetermined degree of opening, so that the refrigerant flows as indicated by the broken-line arrow marks in FIG. 3 .
- the high-pressure liquid refrigerant (mainstream) condensed by the outdoor heat exchanger 30 or the indoor heat exchanger 40 is caused to flow.
- a low-pressure two-phase refrigerant that is split from the mainstream high-pressure liquid refrigerant and decompressed by the bypass expansion valve 62 is caused to flow.
- the low-pressure two-phase refrigerant is heat-exchanged with the mainstream high-pressure liquid refrigerant and is evaporated, and the mainstream high-pressure liquid refrigerant is cooled.
- the degree of opening of the bypass expansion valve 62 is controlled so that the degree of supercooling of the high-pressure liquid refrigerant becomes a target degree of supercooling.
- the low-pressure two-phase refrigerant is evaporated by the heat exchange with the high-pressure liquid refrigerant, and is returned to a suction pipe 11 of the compressor 10 as a low-pressure gas refrigerant (for example, refer to Japanese Patent Application Publication No. 2006-23073 ).
- the solid line indicates the mainstream of the high-pressure liquid refrigerant flowing in the liquid-side refrigerant pipe 50
- the dash-and-dot line indicates a bypass stream flowing in the bypass pipe 61.
- FIG. 4A shows a refrigerating cycle in which the refrigerant circulates in the optimum state. Even if the refrigerant reaches the indoor heat exchanger 40 in the optimum state with the degree of supercooling being A and the mainstream and the bypass stream are mixed with each other, a state of gas phase is established.
- the low-pressure two-phase refrigerant that is split from the mainstream and decompressed by the bypass expansion valve 62 evaporates in the double-pipe heat exchanger 60, and becomes in an overheated state of (c1).
- the mainstream evaporates in the indoor heat exchanger 40 and returns to the compressor 10 in the state of (a1), and on the suction side of the compressor 10, (a1) and (c1) are mixed with each other, and the state of (b1) is formed.
- the temperature of the bypass stream at the outlet of the double-pipe heat exchanger 60 is monitored to suppress the flow rate of bypass stream.
- the circulation amount of refrigerant in the evaporator (for example, the indoor heat exchanger 40) is only the amount of the mainstream, so that the heat exchange amount sometimes comes short.
- an object of the present invention is to provide an air conditioner having a double-pipe heat exchanger in a refrigerating cycle, wherein the degree of opening of a bypass expansion valve can be controlled easily without liquid return to a compressor and without considering the state of a low-pressure two-phase refrigerant in the double-pipe heat exchanger.
- the present invention provides an air conditioner including a refrigerating cycle in which a double-pipe heat exchanger is provided in a liquid-side refrigerant pipe between an outdoor heat exchanger and an indoor heat exchanger which are selectively connected to the discharge side of a compressor via a four-way valve; a heating expansion valve is provided between the outdoor heat exchanger and the double-pipe heat exchanger; a cooling expansion valve is provided between the indoor heat exchanger and the double-pipe heat exchanger; and in the double-pipe heat exchanger, a high-pressure liquid refrigerant flowing in the liquid-side refrigerant pipe is heat-exchanged with a gas-liquid low-pressure two-phase refrigerant which is formed by decompressing some of the high-pressure liquid refrigerant by a bypass expansion valve, wherein a low-pressure refrigerant outflow portion of the double-pipe heat exchanger is branched in a fork form; one branch is connected to the refrigerant pipe between the outdoor heat exchanger and the heating expansion valve
- the heating expansion valve is fully opened and the cooling expansion valve is throttled to a predetermined degree of opening; and the low-pressure refrigerant heat-exchanged by the double-pipe heat exchanger is supplied to the indoor heat exchanger on the evaporator side via the second valve means together with the refrigerant decompressed by the cooling expansion valve.
- the cooling expansion valve is fully opened and the heating expansion valve is throttled to a predetermined degree of opening; and the low-pressure refrigerant heat-exchanged by the double-pipe heat exchanger is supplied to the outdoor heat exchanger on the evaporator side via the first valve means together with the refrigerant decompressed by the heating expansion valve.
- check valves which are opened with the low-pressure refrigerant outflow portion being on the high pressure side or solenoid valves which are opened and closed by an external signal may be used.
- the refrigerant going out of the double-pipe heat exchanger is caused to flow to the evaporator side, the refrigerant is evaporated by the evaporator and is returned to the compressor even if not being evaporated completely by the double-pipe heat exchanger. Therefore, liquid return to the compressor can be eliminated.
- the state of the low-pressure refrigerant in the double-pipe heat exchanger need not be considered, and the control has only to be carried out so that the degree of supercooling of the high-pressure liquid refrigerant becomes a target degree of supercooling. Therefore, the bypass expansion valve can be controlled easily.
- the degree of supercooling of the high-pressure liquid refrigerant can be made high, so that the improvement in performance of the refrigerating cycle can be expected accordingly.
- FIGS. 1 and 2 An embodiment of the present invention will now be described with reference to FIGS. 1 and 2 .
- the present invention is not limited to this embodiment.
- the same reference numerals are applied to elements that are essentially the same as the elements in the conventional example explained with reference to FIG. 3 .
- a refrigerating cycle 1A in accordance with this embodiment includes, as a basic configuration, a compressor 10, a four-way valve 20, an outdoor heat exchanger 30, and an indoor heat exchanger 40.
- the compressor 10 may be either a rotary compressor or a scroll compressor.
- the discharge side of the compressor 10 is connected to either one of the outdoor heat exchanger 30 and the indoor heat exchanger 40 via the four-way valve 20, and in a liquid-side refrigerant pipe 50 that connects the outdoor heat exchanger 30 and the indoor heat exchanger 40 to each other, a double-pipe heat exchanger 60 is interposed.
- a heating expansion valve 51 is provided between the outdoor heat exchanger 30 and the double-pipe heat exchanger 60, and between the indoor heat exchanger 40 and the double-pipe heat exchanger 60, a cooling expansion valve 52 is provided.
- the double-pipe heat exchanger 60 consists, for example, of an inner pipe and an outer pipe arranged coaxially, and a high-pressure liquid refrigerant condensed by the outdoor heat exchanger 30 or the indoor heat exchanger 40 is caused to flow in the inner pipe.
- This high-pressure liquid refrigerant caused to flow in the inner pipe is a mainstream.
- a bypass pipe 61 branched from the liquid-side refrigerant pipe 50 is connected, and the bypass pipe 61 is provided with a bypass expansion valve 62.
- Some of the high-pressure liquid refrigerant split from the bypass pipe 61 is decompressed, and flows in the outer pipe as a low-pressure two-phase refrigerant.
- the high-pressure liquid refrigerant may be caused to flow on the outer pipe side, and the low-pressure two-phase refrigerant may be caused to flow on the inner pipe side.
- a low-pressure refrigerant outflow portion 60a of the double-pipe heat exchanger 60 is connected to a refrigerant pipe portion 50a between the outdoor heat exchanger 30 and the heating expansion valve 51 via a first check valve 71, and is also connected to a refrigerant pipe portion 50b between the indoor heat exchanger 40 and the cooling expansion valve 52 via a second check valve 72.
- the forward direction of flow is a direction directed from the low-pressure refrigerant outflow portion 60a to the refrigerant pipe portions 50a and 50b.
- a solenoid valve that is opened and closed by an external signal may be used.
- the four-way valve 20 is changed over to the state indicated by the solid line in FIG. 1 .
- the heating expansion valve 51 is fully opened, the cooling expansion valve 52 is throttled to a predetermined degree of opening, and the refrigerant circulates as indicated by the solid-line arrow marks in FIG. 1 .
- a high-pressure gas refrigerant discharged from the compressor 10 reaches the outdoor heat exchanger 30 through the four-way valve 20, being condensed into the high-pressure liquid refrigerant by the outdoor heat exchanger 30, and is further cooled by the double-pipe heat exchanger 60.
- the high-pressure liquid refrigerant from which the degree of supercooling is removed by the double-pipe heat exchanger 60 is split in a portion of the bypass pipe 61.
- One stream (the mainstream) is sent to the cooling expansion valve 52, and the other stream (a bypass stream) is sent to the bypass expansion valve 62.
- bypass stream is decompressed into the gas-liquid low-pressure two-phase refrigerant by the bypass expansion valve 62, and is heat-exchanged with the high-pressure liquid refrigerant by the double-pipe heat exchanger 60 and is evaporated.
- the refrigerant in the refrigerant pipe portion 50a on the outdoor heat exchanger 30 side has a pressure higher than the pressure of refrigerant at the low-pressure refrigerant outflow portion 60a
- the refrigerant in the refrigerant pipe portion 50b on the indoor heat exchanger 40 side has a pressure lower than the pressure of refrigerant at the low-pressure refrigerant outflow portion 60a.
- the evaporated gas refrigerant reaches the refrigerant pipe portion 50b via the second check valve 72, joining with the mainstream-side refrigerant decompressed by the cooling expansion valve 52, and is sent to the indoor heat exchanger 40 on the evaporator side.
- the indoor heat exchanger 40 the refrigerant is heat-exchanged with indoor air and is evaporated, and the gas refrigerant is returned to the compressor 10 through a suction pipe 11 and an accumulator 12.
- the flow rate of refrigerant in the refrigerating cycle is regulated by the cooling expansion valve 52, and the degree of opening of the bypass expansion valve 62 is controlled so that the degree of supercooling of the high-pressure liquid refrigerant becomes a target degree of supercooling.
- the four-way valve 20 is changed over to the state indicated by the broken line in FIG. 1 .
- the cooling expansion valve 52 is fully opened, the heating expansion valve 51 is throttled to a predetermined degree of opening, and the refrigerant circulates as indicated by the broken-line arrow marks in FIG. 1 .
- the high-pressure gas refrigerant discharged from the compressor 10 reaches the indoor heat exchanger 40 through the four-way valve 20, and is condensed into the high-pressure liquid refrigerant by the indoor heat exchanger 40.
- the high-pressure liquid refrigerant is split in the portion of the bypass pipe 61 in front of the double-pipe heat exchanger 60.
- One stream (the mainstream) flows in the inner pipe of the double-pipe heat exchanger 60 and reaches the heating expansion valve 51, and the other stream (the bypass stream) is sent to the bypass expansion valve 62.
- the bypass stream is decompressed into the gas-liquid low-pressure two-phase refrigerant by the bypass expansion valve 62, and is heat-exchanged with the high-pressure liquid refrigerant on the mainstream side by the double-pipe heat exchanger 60 and is evaporated.
- the refrigerant in the refrigerant pipe portion 50b on the indoor heat exchanger 40 side has a pressure higher than the pressure of refrigerant at the low-pressure refrigerant outflow portion 60a
- the refrigerant in the refrigerant pipe portion 50a on the outdoor heat exchanger 30 side has a pressure lower than the pressure of refrigerant at the low-pressure refrigerant outflow portion 60a.
- the evaporated gas refrigerant reaches the refrigerant pipe portion 50a via the first check valve 71, joining with the mainstream-side refrigerant decompressed by the heating expansion valve 51, and is sent to the outdoor heat exchanger 30 on the evaporator side.
- the refrigerant is heat-exchanged with the outside air and is evaporated, and the gas refrigerant is returned to the compressor 10 through the suction pipe 11 and the accumulator 12.
- the flow rate of refrigerant in the refrigerating cycle is regulated by the heating expansion valve 51, and the degree of opening of the bypass expansion valve 62 is controlled so that the degree of supercooling of the high-pressure liquid refrigerant becomes the target degree of supercooling.
- the gas-liquid low-pressure two-phase refrigerant need not be evaporated completely in the double-pipe heat exchanger 60. Therefore, a large amount of low-pressure two-phase refrigerant can be caused to flow in the double-pipe heat exchanger 60 by increasing the target degree of supercooling of the high-pressure liquid refrigerant.
- the refrigerating cycle of the present invention (the case of cooling operation) is explained.
- the solid line indicates the mainstream of the high-pressure liquid refrigerant flowing in the liquid-side refrigerant pipe 50
- the dash-and-dot line indicates the bypass stream flowing in the bypass pipe 61.
- the refrigerant is sucked into the compressor 10, and the compressed refrigerant becomes at high temperature and pressure (point x) and is condensed by the outdoor heat exchanger 30 (point a).
- the refrigerant is heat-exchanged with the later-described bypass stream (g-f) by the double-pipe heat exchanger 60 and becomes in a supercooled state (point b), and is decompressed by the cooling expansion valve 52 (point d).
- the bypass circuit some of the mainstream heat-exchanged by the double-pipe heat exchanger 60 is split in the bypass pipe 61, and is decompressed by the bypass expansion valve 62 (point g). Thereafter, the refrigerant is heat-exchanged with the mainstream (a-b) (point f). The mainstream and the bypass stream are joined with each other (point e) and flow into the indoor heat exchanger 30. The refrigerant is evaporated by the indoor heat exchanger 30, and is sucked into the compressor 10 (point D).
- the bypass stream used in the double-pipe heat exchanger 60 does not return directly to the suction side of the compressor 10, and is heat-exchanged by the indoor heat exchanger 30, so that no wasteful refrigerant is generated. Therefore, the performance (COP) is improved. Also, since there is no fear of liquid back, supercooling can be performed until the refrigerant can be supplied to the indoor heat exchanger 30 in the optimum state.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
Description
- The present invention relates to an air conditioner having a reversible refrigerating cycle. More particularly, it relates to an air conditioner having a double-pipe heat exchanger in a liquid-side refrigerant pipe connecting an outdoor heat exchanger and an indoor heat exchanger to each other.
- As one of refrigerating cycles applied to an air conditioner, a refrigerating cycle having a double-pipe heat exchanger to increase the degree of supercooling has been known. In the refrigerating cycle of this type, some of a high-pressure liquid refrigerant condensed by a condenser is split and decompressed, and is heat-exchanged with a mainstream high-pressure liquid refrigerant. One example thereof is explained with reference to
FIG. 3 . DocumentUS 2006/196225 A1 discloses an improvement system of energy efficiency for a refrigeration cycle is comprised of an auxiliary heat exchanger unit for heat-exchanging between refrigerant liquid having high pressure and refrigerant vapor having low pressure and a cabinet which houses a pressure support value placed at an inlet of an inner pipe of the auxiliary heat exchanger unit. A pressure of the refrigerant liquid having high pressure condensed at the outdoor heat exchanger is decreased by the pressure support value, and a condensed pressure of the outdoor heat exchanger is maintained.. - A refrigerating
cycle 1B of this conventional example includes, as a basic configuration, acompressor 10, a four-way valve 20, anoutdoor heat exchanger 30, and anindoor heat exchanger 40, and the discharge side of thecompressor 10 is connected to either one of theoutdoor heat exchanger 30 and theindoor heat exchanger 40 via the four-way valve 20. - That is, at the time of cooling operation, the discharge side of the
compressor 10 is connected to theoutdoor heat exchanger 30, theoutdoor heat exchanger 30 functions as a condenser, and theindoor heat exchanger 40 functions as an evaporator. At the time of heating operation, contrarily, the discharge side of thecompressor 10 is connected to theindoor heat exchanger 40, theindoor heat exchanger 40 functions as a condenser, and theoutdoor heat exchanger 30 functions as an evaporator. - In both the cases, in a pipe leading from the four-
way valve 20 to theoutdoor heat exchanger 30 and theindoor heat exchanger 40, a gas refrigerant is caused to flow, and in arefrigerant pipe 11 leading from the four-way valve 20 to
anaccumulator 12 as well, the gas refrigerant is caused to flow. Therefore, these pipes are called gas-side refrigerant pipes. - In contrast, in a refrigerant pipe connecting the
outdoor heat exchanger 30 and theindoor heat exchanger 40 to each other, a condensed liquid refrigerant is mainly caused to flow. Therefore, the refrigerant pipe connecting theoutdoor heat exchanger 30 and theindoor heat exchanger 40 to each other is usually called a liquid-side refrigerant pipe 50. - The liquid-
side refrigerant pipe 50 is provided with a double-pipe heat exchanger 60. Also, between the double-pipe heat exchanger 60 and theoutdoor heat exchanger 30, aheating expansion valve 51 is provided, and between the double-pipe heat exchanger 60 and theindoor heat exchanger 40, acooling expansion valve 52 is provided. - The double-
pipe heat exchanger 60 consists, for example, of an inner pipe and an outer pipe arranged coaxially, and a high-pressure liquid refrigerant is caused to flow in the inner pipe. To the outer pipe, abypass pipe 61 branched from the liquid-side refrigerant pipe 50 is connected, and thebypass pipe 61 is provided with abypass expansion valve 62. - A two-
way valve 53 and a three-way valve 54 provided on both sides of theindoor heat exchanger 40 are connection pipes for connecting theindoor heat exchanger 40 to the refrigerating cycle when the air conditioner is installed. - At the time of cooling operation, the
heating expansion valve 51 is fully opened, and thecooling expansion valve 52 is throttled to a predetermined degree of opening, so that the refrigerant flows as indicated by the solid-line arrow marks inFIG. 3 . At the time of heating operation, thecooling expansion valve 52 is fully opened, and theheating expansion valve 51 is throttled to a predetermined degree of opening, so that the refrigerant flows as indicated by the broken-line arrow marks inFIG. 3 . - In both the operations, in the inner pipe of the double-
pipe heat exchanger 60, the high-pressure liquid refrigerant (mainstream) condensed by theoutdoor heat exchanger 30 or theindoor heat exchanger 40 is caused to flow. In the outer pipe thereof, a low-pressure two-phase refrigerant that is split from the mainstream high-pressure liquid refrigerant and decompressed by thebypass expansion valve 62 is caused to flow. The low-pressure two-phase refrigerant is heat-exchanged with the mainstream high-pressure liquid refrigerant and is evaporated, and the mainstream high-pressure liquid refrigerant is cooled. In this case, the degree of opening of thebypass expansion valve 62 is controlled so that the degree of supercooling of the high-pressure liquid refrigerant becomes a target degree of supercooling. - As described above, the low-pressure two-phase refrigerant is evaporated by the heat exchange with the high-pressure liquid refrigerant, and is returned to a
suction pipe 11 of thecompressor 10 as a low-pressure gas refrigerant (for example, refer to Japanese Patent Application Publication No.2006-23073 - Unfortunately, in the above-described conventional example, since the gas refrigerant evaporated by the heat exchange with the high-pressure liquid refrigerant in the double-
pipe heat exchanger 60 is returned to thesuction pipe 11 side of thecompressor 10, there arise problems described below in controlling thebypass expansion valve 62 so that the degree of supercooling of high-pressure liquid refrigerant becomes the target degree of supercooling. - With reference to the Mollier chart of
FIG. 4 , the case of cooling operation is explained. InFIG. 4 , the solid line indicates the mainstream of the high-pressure liquid refrigerant flowing in the liquid-side refrigerant pipe 50, and the dash-and-dot line indicates a bypass stream flowing in thebypass pipe 61. - In particular, in the case where a pipe for connecting an outdoor unit and an indoor unit to each other must be lengthened on account of the circumstances of the place at which the air conditioner is installed, in order to optimize the state in which the refrigerant reaches the indoor heat exchanger 40 (to demonstrate the capacity of indoor unit to a maximum), supercooling as shown in
FIG. 4A is needed. -
FIG. 4A shows a refrigerating cycle in which the refrigerant circulates in the optimum state. Even if the refrigerant reaches theindoor heat exchanger 40 in the optimum state with the degree of supercooling being A and the mainstream and the bypass stream are mixed with each other, a state of gas phase is established. - That is, the low-pressure two-phase refrigerant that is split from the mainstream and decompressed by the
bypass expansion valve 62 evaporates in the double-pipe heat exchanger 60, and becomes in an overheated state of (c1). The mainstream evaporates in theindoor heat exchanger 40 and returns to thecompressor 10 in the state of (a1), and on the suction side of thecompressor 10, (a1) and (c1) are mixed with each other, and the state of (b1) is formed. - On the other hand, as shown in
FIG. 4B , in the case where the bypass amount to the double-pipe heat exchanger 60 is increased to change the degree of supercooling deep from A to A' (in the left direction inFIG. 4B ) because the refrigerant reaching the indoor unit is not optimal, the mainstream is heat-exchanged sufficiently by theindoor heat exchanger 40, and a gas phase (a2) is formed. - However, if all of the bypass refrigerant becomes impossible to evaporate, the refrigerant is returned in the two-phase state of (c2) in which the degree of overheating is zero. Therefore, the refrigerant mixed on the suction side of the
compressor 10 becomes in the two-phase state (b2) containing the liquid refrigerant, and liquid back occurs. - Accordingly, in order to make (b2) in a gas-phase state to avoid liquid back, the degree of supercooling must be made shallow (from A' to A, in the right direction in
FIG. 4B ). In this case, the refrigerant does not reach theindoor heat exchanger 40 in the optimum state, and the performance (COP) deteriorates. - Thus, in the above-described example, since there is a fear of liquid return to the
compressor 10, the temperature of the bypass stream at the outlet of the double-pipe heat exchanger 60 is monitored to suppress the flow rate of bypass stream. As a result, there occurs the case where the target degree of supercooling is not reached. Also, the circulation amount of refrigerant in the evaporator (for example, the indoor heat exchanger 40) is only the amount of the mainstream, so
that the heat exchange amount sometimes comes short. - As one method for making the bypass stream a gas refrigerant by evaporating all of the bypass stream, a method is available in which the double-
pipe heat exchanger 60 is increased in size. However, this method is unfavorable because the piping system becomes large in size. - Accordingly, an object of the present invention is to provide an air conditioner having a double-pipe heat exchanger in a refrigerating cycle, wherein the degree of opening of a bypass expansion valve can be controlled easily without liquid return to a compressor and without considering the state of a low-pressure two-phase refrigerant in the double-pipe heat exchanger.
- To achieve the above object, the present invention provides an air conditioner including a refrigerating cycle in which a double-pipe heat exchanger is provided in a liquid-side refrigerant pipe between an outdoor heat exchanger and an indoor heat exchanger which are selectively connected to the discharge side of a compressor via a four-way valve; a heating expansion valve is provided between the outdoor heat exchanger and the double-pipe heat exchanger; a cooling expansion valve is provided between the indoor heat exchanger and the double-pipe heat exchanger; and in the double-pipe heat exchanger, a high-pressure liquid refrigerant flowing in the liquid-side refrigerant pipe is heat-exchanged with a gas-liquid low-pressure two-phase refrigerant which is formed by decompressing some of the high-pressure liquid refrigerant by a bypass expansion valve, wherein a low-pressure refrigerant outflow portion of the double-pipe heat exchanger is branched in a fork form; one branch is connected to the refrigerant pipe between the outdoor heat exchanger and the heating expansion valve via first valve means; and the other branch is connected to the refrigerant pipe between the indoor heat exchanger and the cooling expansion valve via second valve means.
- In the present invention, at the time of cooling operation of the refrigerating cycle, the heating expansion valve is fully opened and the cooling expansion valve is throttled to a predetermined degree of opening; and the low-pressure refrigerant heat-exchanged by the double-pipe heat exchanger is supplied to the indoor heat exchanger on the evaporator side via the second valve means together with the refrigerant decompressed by the cooling expansion valve.
- Also, at the time of heating operation of the refrigerating cycle, the cooling expansion valve is fully opened and the heating expansion valve is throttled to a predetermined degree of opening; and the low-pressure refrigerant heat-exchanged by the double-pipe heat exchanger is supplied to the outdoor heat exchanger on the evaporator side via the first valve means together with the refrigerant decompressed by the heating expansion valve.
- In the present invention, as the first and second valve means, check valves which are opened with the low-pressure refrigerant outflow portion being on the high pressure side or solenoid valves which are opened and closed by an external signal may be used.
- According to the present invention, since the low-pressure refrigerant going out of the double-pipe heat exchanger is caused to flow to the evaporator side, the refrigerant is evaporated by the evaporator and is returned to the compressor even if not being evaporated completely by the double-pipe heat exchanger. Therefore, liquid return to the compressor can be eliminated.
- Also, in controlling the bypass expansion valve, the state of the low-pressure refrigerant in the double-pipe heat exchanger need not be considered, and the control has only to be carried out so that the degree of supercooling of the high-pressure liquid refrigerant becomes a target degree of supercooling.
Therefore, the bypass expansion valve can be controlled easily. - Also, since a large amount of low-pressure refrigerant can be caused to flow in the double-pipe heat exchanger, the degree of supercooling of the high-pressure liquid refrigerant can be made high, so that the improvement in performance of the refrigerating cycle can be expected accordingly.
-
-
FIG. 1 is a refrigerant circuit diagram showing an embodiment of a refrigerating cycle applied to an air conditioner of the present invention; -
FIG. 2 is a Mollier chart of the refrigerating cycle shown inFIG. 1 ; -
FIG. 3 is a refrigerant circuit diagram showing a conventional refrigerating cycle; -
FIG. 4A is a Mollier chart in the case where the degree of overheating is established in a double-pipe heat exchanger of the conventional refrigerating cycle shown inFIG. 3 ; and -
FIG. 4B is a Mollier chart in the case where the degree of overheating is not established in a double-pipe heat exchanger of the conventional refrigerating cycle shown inFIG. 3 . - An embodiment of the present invention will now be described with reference to
FIGS. 1 and 2 . The present invention is not limited to this embodiment. In the explanation of this embodiment, the same reference numerals are applied to elements that are essentially the same as the elements in the conventional example explained with reference toFIG. 3 . - As shown in
FIG. 1 , a refrigeratingcycle 1A in accordance with this embodiment includes, as a basic configuration, acompressor 10, a four-way valve 20, anoutdoor heat exchanger 30, and anindoor heat exchanger 40. Thecompressor 10 may be either a rotary compressor or a scroll compressor. - The discharge side of the
compressor 10 is connected to either one of theoutdoor heat exchanger 30 and theindoor heat exchanger 40 via the four-way valve 20, and in a liquid-side refrigerant pipe 50 that connects theoutdoor heat exchanger 30 and theindoor heat exchanger 40 to each other, a double-pipe heat exchanger 60 is interposed. - Also, between the
outdoor heat exchanger 30 and the double-pipe heat exchanger 60, aheating expansion valve 51 is provided, and between theindoor heat exchanger 40 and the double-pipe heat exchanger 60, a coolingexpansion valve 52 is provided. - The double-
pipe heat exchanger 60 consists, for example, of an inner pipe and an outer pipe arranged coaxially, and a high-pressure liquid refrigerant condensed by theoutdoor heat exchanger 30 or theindoor heat exchanger 40 is caused to flow in the inner pipe. This high-pressure liquid refrigerant caused to flow in the inner pipe is a mainstream. - To the outer pipe of the double-
pipe heat exchanger 60, abypass pipe 61 branched from the liquid-side refrigerant pipe 50 is connected, and thebypass pipe 61 is provided with abypass expansion valve 62. Some of the high-pressure liquid refrigerant split from thebypass pipe 61 is decompressed, and flows in the outer pipe as a low-pressure two-phase refrigerant. The high-pressure liquid refrigerant may be caused to flow on the outer pipe side, and the low-pressure two-phase refrigerant may be caused to flow on the inner pipe side. - According to the present invention, a low-pressure
refrigerant outflow portion 60a of the double-pipe heat exchanger 60 is connected to arefrigerant pipe portion 50a between theoutdoor heat exchanger 30 and theheating expansion valve 51 via afirst check valve 71, and is also connected to arefrigerant pipe portion 50b between theindoor heat exchanger 40 and thecooling expansion valve 52 via asecond check valve 72. - In both the
check valves refrigerant outflow portion 60a to therefrigerant pipe portions - At the time of cooling operation, the four-
way valve 20 is changed over to the state indicated by the solid line inFIG. 1 . In this state, theheating expansion valve 51 is fully opened, the coolingexpansion valve 52 is throttled to a predetermined degree of opening, and the refrigerant circulates as indicated by the solid-line arrow marks inFIG. 1 . - That is, a high-pressure gas refrigerant discharged from the
compressor 10 reaches theoutdoor heat exchanger 30 through the four-way valve 20, being condensed into the high-pressure liquid refrigerant by theoutdoor heat exchanger 30, and is further cooled by the double-pipe heat exchanger 60. - The high-pressure liquid refrigerant from which the degree of supercooling is removed by the double-
pipe heat exchanger 60 is split in a portion of thebypass pipe 61. One stream (the mainstream) is sent to thecooling expansion valve 52, and the other stream (a bypass stream) is sent to thebypass expansion valve 62. - The bypass stream is decompressed into the gas-liquid low-pressure two-phase refrigerant by the
bypass expansion valve 62, and is heat-exchanged with the high-pressure liquid refrigerant by the double-pipe heat exchanger 60 and is evaporated. - At the time of cooling operation, the refrigerant in the
refrigerant pipe portion 50a on theoutdoor heat exchanger 30 side has a pressure higher than the pressure of refrigerant at the low-pressurerefrigerant outflow portion 60a, and the refrigerant in therefrigerant pipe portion 50b on theindoor heat exchanger 40 side has a pressure lower than the pressure of refrigerant at the low-pressurerefrigerant outflow portion 60a. - Therefore, the evaporated gas refrigerant reaches the
refrigerant pipe portion 50b via thesecond check valve 72, joining with the mainstream-side refrigerant decompressed by the coolingexpansion valve 52, and is sent to theindoor heat exchanger 40 on the evaporator side. In theindoor heat exchanger 40, the refrigerant is heat-exchanged with indoor air and is evaporated, and the gas refrigerant is returned to thecompressor 10 through asuction pipe 11 and anaccumulator 12. - At the time of cooling operation, the flow rate of refrigerant in the refrigerating cycle is regulated by the cooling
expansion valve 52, and the degree of opening of thebypass expansion valve 62 is controlled so that the degree of supercooling of the high-pressure liquid refrigerant becomes a target degree of supercooling. - At the time of heating operation, the four-
way valve 20 is changed over to the state indicated by the broken line inFIG. 1 . In this state, the coolingexpansion valve 52 is fully opened, theheating expansion valve 51 is throttled to a predetermined degree of opening, and the refrigerant circulates as indicated by the broken-line arrow marks inFIG. 1 . - That is, the high-pressure gas refrigerant discharged from the
compressor 10 reaches theindoor heat exchanger 40 through the four-way valve 20, and is condensed into the high-pressure liquid refrigerant by theindoor heat exchanger 40. - Thereafter, the high-pressure liquid refrigerant is split in the portion of the
bypass pipe 61 in front of the double-pipe heat exchanger 60. One stream (the mainstream) flows in the inner pipe of the double-pipe heat exchanger 60 and reaches theheating expansion valve 51, and the other stream (the bypass stream) is sent to thebypass expansion valve 62. - The bypass stream is decompressed into the gas-liquid low-pressure two-phase refrigerant by the
bypass expansion valve 62, and is heat-exchanged with the high-pressure liquid refrigerant on the mainstream side by the double-pipe heat exchanger 60 and is evaporated. - At the time of heating operation, the refrigerant in the
refrigerant pipe portion 50b on theindoor heat exchanger 40 side has a pressure higher than the pressure of refrigerant at the low-pressurerefrigerant outflow portion 60a, and the refrigerant in therefrigerant pipe portion 50a on theoutdoor heat exchanger 30 side has a pressure lower than the pressure of refrigerant at the low-pressurerefrigerant outflow portion 60a. - Therefore, the evaporated gas refrigerant reaches the
refrigerant pipe portion 50a via thefirst check valve 71, joining with the mainstream-side refrigerant decompressed by theheating expansion valve 51, and is sent to theoutdoor heat exchanger 30 on the evaporator side. In theoutdoor heat exchanger 30, the refrigerant is heat-exchanged with the outside air and is evaporated, and the gas refrigerant is returned to thecompressor 10 through thesuction pipe 11 and theaccumulator 12. - At the time of heating operation as well, the flow rate of refrigerant in the refrigerating cycle is regulated by the
heating expansion valve 51, and the degree of opening of thebypass expansion valve 62 is controlled so that the degree of supercooling of the high-pressure liquid refrigerant becomes the target degree of supercooling. - As described above, according to the present invention, at both of the cooling operation time and the heating operation time, since the low-pressure refrigerant going out of the double-
pipe heat exchanger 60 is caused to flow from the downstream side of the coolingexpansion valve 52 or theheating expansion valve 51 toward the evaporator, the gas-liquid low-pressure two-phase refrigerant need not be evaporated completely in the double-pipe heat exchanger 60. Therefore, a large amount of low-pressure two-phase refrigerant can be caused to flow in the double-pipe heat exchanger 60 by increasing the target degree of supercooling of the high-pressure liquid refrigerant. - With reference to the Mollier chart of
FIG. 2 , the refrigerating cycle of the present invention (the case of cooling operation) is explained. InFIG. 2 , the solid line indicates the mainstream of the high-pressure liquid refrigerant flowing in the liquid-side refrigerant pipe 50, and the dash-and-dot line indicates the bypass stream flowing in thebypass pipe 61. - At point D, the refrigerant is sucked into the
compressor 10, and the compressed refrigerant becomes at high temperature and pressure (point x) and is condensed by the outdoor heat exchanger 30 (point a). The refrigerant is heat-exchanged with the later-described bypass stream (g-f) by the double-pipe heat exchanger 60 and becomes in a supercooled state (point b), and is decompressed by the cooling expansion valve 52 (point d). - On the other hand, in the bypass circuit, some of the mainstream heat-exchanged by the double-
pipe heat exchanger 60 is split in thebypass pipe 61, and is decompressed by the bypass expansion valve 62 (point g). Thereafter, the refrigerant is heat-exchanged with the mainstream (a-b) (point f). The mainstream and the bypass stream are joined with each other (point e) and flow into theindoor heat exchanger 30. The refrigerant is evaporated by theindoor heat exchanger 30, and is sucked into the compressor 10 (point D). - In the present invention, as described above, the bypass stream used in the double-
pipe heat exchanger 60 does not return directly to the suction side of thecompressor 10, and is heat-exchanged by theindoor heat exchanger 30, so that no wasteful refrigerant is generated. Therefore, the performance (COP) is improved. Also, since there is no fear of liquid back, supercooling can be performed until the refrigerant can be supplied to theindoor heat exchanger 30 in the optimum state. - Also, conventionally, both of the electronic expansion valve for double-pipe heat exchanger and the electronic expansion valves of the whole of refrigerating cycle have been needed to be controlled exactly. According to the present invention, however, since liquid back does not occur, the control program for these electronic expansion valves can be simplified significantly.
Claims (5)
- An air conditioner including a refrigerating cycle in which a double-pipe heat exchanger (60) is provided in a liquid-side refrigerant pipe (50) between an outdoor heat exchanger (30) and an indoor heat exchanger (40) which are selectively connected to the discharge side of a compressor (10) via a four-way valve (20); a heating expansion valve (51) is provided between the outdoor heat exchanger (30) and the double-pipe heat exchanger (60); a cooling expansion valve (52) is provided between the indoor heat exchanger (40) and the double-pipe heat exchanger (60); and in the double-pipe heat exchanger (60), a high-pressure liquid refrigerant flowing in the liquid-side refrigerant pipe (50) is heat-exchanged with a gas-liquid low-pressure two-phase refrigerant which is formed by decompressing some of the high-pressure liquid refrigerant by a bypass expansion valve (62), wherein
a low-pressure refrigerant outflow portion (60a) of the double-pipe heat exchanger (60) is branched in a fork form;
characterized in that one branch is connected to the refrigerant pipe (50) between the outdoor heat exchanger (30) and the heating expansion valve (51) via first valve means (71); and the other branch is connected to the refrigerant pipe (50) between the indoor heat exchanger (40) and the cooling expansion valve (52) via second valve means (72). - The air conditioner according to claim 1, wherein at the time of cooling operation of the refrigerating cycle, the heating expansion valve (51) is fully opened and the cooling expansion valve (52) is throttled to a predetermined degree of opening; and the low-pressure refrigerant heat-exchanged by the double-pipe heat exchanger (60) is supplied to the indoor heat exchanger (40) on the evaporator side via the second valve means (72) together with the refrigerant decompressed by the cooling expansion valve (52).
- The air conditioner according to claim 1, wherein at the time of heating operation of the refrigerating cycle, the cooling expansion valve (52) is fully opened and the heating expansion valve (51) is throttled to a predetermined degree of opening; and the low-pressure refrigerant heat-exchanged by the double-pipe heat exchanger (60) is supplied to the outdoor heat exchanger (30) on the evaporator side via the first valve means (71) together with the refrigerant decompressed by the heating expansion valve (51).
- The air conditioner according to claim 1, wherein the first (71) and second valve means (72) consist of check valves which are opened with the low-pressure refrigerant outflow portion (60a) being on the high pressure side.
- The air conditioner according to claim 1, wherein the first (71) and second valve means (72) consist of solenoid valves which are opened and closed by an external signal.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2009293650A JP2011133177A (en) | 2009-12-25 | 2009-12-25 | Air conditioner |
Publications (3)
Publication Number | Publication Date |
---|---|
EP2339269A2 EP2339269A2 (en) | 2011-06-29 |
EP2339269A3 EP2339269A3 (en) | 2011-07-13 |
EP2339269B1 true EP2339269B1 (en) | 2019-01-23 |
Family
ID=43873806
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP10252001.2A Not-in-force EP2339269B1 (en) | 2009-12-25 | 2010-11-25 | Air conditioner |
Country Status (6)
Country | Link |
---|---|
US (1) | US20110154847A1 (en) |
EP (1) | EP2339269B1 (en) |
JP (1) | JP2011133177A (en) |
CN (1) | CN102109202B (en) |
AU (1) | AU2010246508A1 (en) |
ES (1) | ES2715928T3 (en) |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104736949B (en) * | 2012-10-18 | 2016-06-15 | 大金工业株式会社 | Air-conditioning device |
KR101474356B1 (en) * | 2013-07-18 | 2014-12-19 | 한국에너지기술연구원 | Heat pump system capable of adjusting refrigerant amount of liquid receiver |
CN103900222B (en) * | 2014-03-07 | 2017-05-24 | 广东美的暖通设备有限公司 | Method for cooling air conditioner electronic control frequency conversion module and air conditioner |
CN104266416B (en) * | 2014-09-29 | 2017-03-15 | 特灵空调系统(中国)有限公司 | Multi-connected machine throttling and supercooling controlling organization |
CN104534725A (en) * | 2015-01-23 | 2015-04-22 | 珠海格力电器股份有限公司 | Air conditioner |
CN106032950A (en) * | 2015-03-18 | 2016-10-19 | 青岛海尔空调电子有限公司 | Air-conditioning system |
CN104848579B (en) * | 2015-05-05 | 2017-12-01 | 广东美的制冷设备有限公司 | Air conditioner and its heat-exchange system |
JP6350577B2 (en) * | 2016-03-31 | 2018-07-04 | ダイキン工業株式会社 | Air conditioner |
JP6341321B2 (en) * | 2016-06-30 | 2018-06-13 | ダイキン工業株式会社 | Air conditioner |
CN111051793B (en) * | 2017-09-07 | 2022-03-29 | 三菱电机株式会社 | Air conditioning apparatus |
JP6863395B2 (en) * | 2019-02-18 | 2021-04-21 | ダイキン工業株式会社 | Air conditioner |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20060196225A1 (en) * | 2003-03-31 | 2006-09-07 | Myung-Bum Han | System of energy efficiency for refrigeration cycle |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS59116777U (en) * | 1983-01-26 | 1984-08-07 | 三菱電機株式会社 | Refrigeration equipment |
US5253482A (en) * | 1992-06-26 | 1993-10-19 | Edi Murway | Heat pump control system |
JPH09152195A (en) * | 1995-11-28 | 1997-06-10 | Sanyo Electric Co Ltd | Refrigerating apparatus |
JPH1054616A (en) * | 1996-08-14 | 1998-02-24 | Daikin Ind Ltd | Air conditioner |
JP2006023073A (en) | 2004-06-11 | 2006-01-26 | Daikin Ind Ltd | Air conditioner |
EP1938022A4 (en) * | 2005-10-18 | 2010-08-25 | Carrier Corp | Economized refrigerant vapor compression system for water heating |
JP2008057807A (en) * | 2006-08-29 | 2008-03-13 | Samsung Electronics Co Ltd | Refrigerating cycle, and air conditioner and refrigerator using the same |
-
2009
- 2009-12-25 JP JP2009293650A patent/JP2011133177A/en active Pending
-
2010
- 2010-11-25 ES ES10252001T patent/ES2715928T3/en active Active
- 2010-11-25 EP EP10252001.2A patent/EP2339269B1/en not_active Not-in-force
- 2010-11-29 AU AU2010246508A patent/AU2010246508A1/en not_active Abandoned
- 2010-12-07 US US12/926,724 patent/US20110154847A1/en not_active Abandoned
- 2010-12-17 CN CN201010622998.0A patent/CN102109202B/en not_active Expired - Fee Related
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20060196225A1 (en) * | 2003-03-31 | 2006-09-07 | Myung-Bum Han | System of energy efficiency for refrigeration cycle |
Also Published As
Publication number | Publication date |
---|---|
JP2011133177A (en) | 2011-07-07 |
CN102109202B (en) | 2014-09-03 |
EP2339269A2 (en) | 2011-06-29 |
US20110154847A1 (en) | 2011-06-30 |
CN102109202A (en) | 2011-06-29 |
ES2715928T3 (en) | 2019-06-07 |
EP2339269A3 (en) | 2011-07-13 |
AU2010246508A1 (en) | 2011-07-14 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP2339269B1 (en) | Air conditioner | |
US9068766B2 (en) | Air-conditioning and hot water supply combination system | |
JP5992089B2 (en) | Air conditioner | |
EP3521732B1 (en) | Air conditioner | |
JP5901107B2 (en) | Multi-type air conditioning system | |
JP5593618B2 (en) | Refrigeration equipment | |
JP5992088B2 (en) | Air conditioner | |
US11022354B2 (en) | Air conditioner | |
EP3736513B1 (en) | Circulation system for air conditioner and air conditioner | |
WO2013179334A1 (en) | Air conditioning device | |
JP2007064510A (en) | Air conditioner | |
JP2006284035A (en) | Air conditioner and its control method | |
JP2009264605A (en) | Refrigerating device | |
WO2017138108A1 (en) | Air conditioning device | |
JP2008170063A (en) | Multiple type air conditioner | |
JP6379769B2 (en) | Air conditioner | |
JP2009145032A (en) | Refrigeration cycle apparatus and air conditioner equipped with the same | |
JP5186398B2 (en) | Air conditioner | |
JP2008267653A (en) | Refrigerating device | |
JP6400223B2 (en) | Air conditioner and control method of air conditioner | |
JP4767340B2 (en) | Heat pump control device | |
JP6021943B2 (en) | Air conditioner | |
KR20040054282A (en) | Air-conditioner | |
JP4023386B2 (en) | Refrigeration equipment | |
JP2006125762A (en) | Indoor unit, air conditioning device comprising the same, and its operating method |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
PUAL | Search report despatched |
Free format text: ORIGINAL CODE: 0009013 |
|
AK | Designated contracting states |
Kind code of ref document: A2 Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR |
|
AX | Request for extension of the european patent |
Extension state: BA ME |
|
AK | Designated contracting states |
Kind code of ref document: A3 Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR |
|
AX | Request for extension of the european patent |
Extension state: BA ME |
|
17P | Request for examination filed |
Effective date: 20120112 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: EXAMINATION IS IN PROGRESS |
|
17Q | First examination report despatched |
Effective date: 20170310 |
|
GRAP | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOSNIGR1 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: GRANT OF PATENT IS INTENDED |
|
INTG | Intention to grant announced |
Effective date: 20180717 |
|
GRAS | Grant fee paid |
Free format text: ORIGINAL CODE: EPIDOSNIGR3 |
|
GRAJ | Information related to disapproval of communication of intention to grant by the applicant or resumption of examination proceedings by the epo deleted |
Free format text: ORIGINAL CODE: EPIDOSDIGR1 |
|
GRAL | Information related to payment of fee for publishing/printing deleted |
Free format text: ORIGINAL CODE: EPIDOSDIGR3 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: EXAMINATION IS IN PROGRESS |
|
GRAR | Information related to intention to grant a patent recorded |
Free format text: ORIGINAL CODE: EPIDOSNIGR71 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: GRANT OF PATENT IS INTENDED |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE PATENT HAS BEEN GRANTED |
|
INTC | Intention to grant announced (deleted) | ||
INTG | Intention to grant announced |
Effective date: 20181213 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: FG4D |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: EP |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R096 Ref document number: 602010056702 Country of ref document: DE |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: REF Ref document number: 1091756 Country of ref document: AT Kind code of ref document: T Effective date: 20190215 |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: FG4D |
|
REG | Reference to a national code |
Ref country code: NL Ref legal event code: MP Effective date: 20190123 |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FG2A Ref document number: 2715928 Country of ref document: ES Kind code of ref document: T3 Effective date: 20190607 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190123 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190123 Ref country code: NO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190423 Ref country code: PT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190523 Ref country code: SE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190123 Ref country code: PL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190123 Ref country code: LT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190123 |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: MK05 Ref document number: 1091756 Country of ref document: AT Kind code of ref document: T Effective date: 20190123 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: RS Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190123 Ref country code: GR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190424 Ref country code: HR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190123 Ref country code: BG Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190423 Ref country code: LV Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190123 Ref country code: IS Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190523 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R097 Ref document number: 602010056702 Country of ref document: DE |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190123 Ref country code: RO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190123 Ref country code: DK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190123 Ref country code: EE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190123 Ref country code: AL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190123 Ref country code: CZ Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190123 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SM Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190123 |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: AT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190123 |
|
26N | No opposition filed |
Effective date: 20191024 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20191112 Year of fee payment: 10 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190123 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 20191029 Year of fee payment: 10 Ref country code: IT Payment date: 20191108 Year of fee payment: 10 Ref country code: ES Payment date: 20191202 Year of fee payment: 10 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: TR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190123 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MC Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190123 Ref country code: LI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20191130 Ref country code: CH Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20191130 Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20191125 |
|
REG | Reference to a national code |
Ref country code: BE Ref legal event code: MM Effective date: 20191130 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 20191125 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20191125 Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20191125 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20191130 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: CY Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190123 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R119 Ref document number: 602010056702 Country of ref document: DE |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190123 Ref country code: HU Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT; INVALID AB INITIO Effective date: 20101125 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20201130 Ref country code: IT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20201125 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20210601 |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FD2A Effective date: 20220203 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: ES Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20201126 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190123 |