WO2011148567A1

WO2011148567A1 - Refrigeration device and cooling and heating device

Info

Publication number: WO2011148567A1
Application number: PCT/JP2011/002369
Authority: WO
Inventors: 一彦丸本; 藤高　章; 川邉　義和; 横山　昭一
Original assignee: パナソニック株式会社
Priority date: 2010-05-27
Filing date: 2011-04-22
Publication date: 2011-12-01
Also published as: JP2011247482A; BR112012029878A2; KR20130088020A; CN102918338A; EP2578966A1; EP2578966A4; EP2578966B1

Abstract

When an in-door heat exchanger acts as an evaporator, each of parts is composed of an inlet part, an intermediate part and an outlet part when observed along the flow of a cooling medium, wherein the in-tube mass flow rates per unit performance of the cooling medium that flows through the above-mentioned parts are not less than 0.44 g/mm²hW and less than 0.50 g/mm²hW, not less than 0.14 g/mm²hW and less than 0.16 g/mm²hW, and not less than 0.13 g/mm²hW and less than 0.15 g/mm²hW, respectively.

Description

Refrigeration equipment and air conditioning equipment

The present invention relates to a refrigeration apparatus and a cooling / heating apparatus using a refrigerant.

As the refrigerant used in the refrigeration apparatus, HCFC is used as an alternative refrigerant after ozone layer destruction due to the use of Freon has become a problem, and HFC (R410A) is currently widely used as shown in FIG. For example, see Patent Document 1.)

JP 2000-81223 A

However, the global warming potential (GWP) of the R410A refrigerant is as large as 2088, which is a problem from the viewpoint of preventing global warming.

From the viewpoint of preventing global warming, for example, HWP1234yf of GWP4 has been proposed as a refrigerant with a small GWP, but this refrigerant has a small refrigerating capacity per unit volume as compared with the R410A refrigerant.

Therefore, if this refrigerant is applied as it is in the conventional apparatus to obtain the same capacity as the R410A refrigerant, it is necessary to increase the volume circulation amount of the refrigerant by increasing the rotation speed of the compressor.

Especially, when the cylinder volume of the compressor is increased so as to increase the refrigerant circulation amount so as to have the same capacity as the R410A refrigerant during the cooling operation, the pressure loss in the heat exchanger increases, and the predetermined cooling capacity cannot be secured.

The present invention has been made in view of such problems of the prior art, and reduces the pressure loss of the heat exchanger even when a refrigerant having a small refrigeration capacity per unit volume compared to the R410A refrigerant is used. It is an object of the present invention to provide a highly efficient refrigeration apparatus and air conditioning apparatus while ensuring cooling capacity.

In order to achieve the above object, the present invention comprises at least a compressor, an outdoor heat exchanger, a throttle device, and an indoor heat exchanger in order to form an annular refrigerant circuit, and as a refrigerant sealed in the refrigerant circuit, In the refrigeration apparatus using a refrigerant having a larger specific volume than the R410A refrigerant, the indoor heat exchanger includes a plurality of fins arranged at predetermined intervals, and the refrigerant passes through the fins at a substantially right angle so that the refrigerant passes inside. A heat transfer tube that circulates is provided, and the mass flow rate of the refrigerant that flows inside the heat transfer tube includes three or more different portions.

This makes it possible to reduce the pressure loss of the heat exchanger even when a refrigerant having a smaller refrigeration capacity per unit volume than that of the R410A refrigerant is used.

According to the present invention, the pressure loss of the heat exchanger can be reduced even when a refrigerant having a small refrigeration capacity per unit volume compared to the R410A refrigerant can be used, so that the cooling capacity of the refrigeration apparatus can be ensured and high efficiency can be achieved. Can be.

1 is a configuration diagram of an air conditioning apparatus according to Embodiment 1 of the present invention. FIG. 2 is a diagram of refrigeration capacity per unit volume of R410A refrigerant and HFO1234yf refrigerant. FIG. 3 is an indoor heat exchanger piping diagram for the R410A refrigerant. FIG. 4 is a diagram of mass flow rate, dryness, saturation temperature difference, and cooling capacity when an indoor heat exchanger for R410A refrigerant is used. FIG. 5 is a PH diagram when an indoor heat exchanger for R410A refrigerant is used. FIG. 6 is an indoor heat exchanger piping diagram according to Embodiment 1 of the present invention. FIG. 7 is a diagram of mass flow rate, dryness, saturation temperature difference, and cooling capacity when the indoor heat exchanger of FIG. 6 is used. FIG. 8 is a PH diagram when the indoor heat exchanger piping of FIG. 6 is used. 9 (a) and 9 (b) are partial arrangement diagrams of the indoor heat exchanger in FIG. FIG. 10 is a diagram showing a calculation result when the mass flow rate per unit capacity is changed. FIG. 11 is a block diagram of a conventional air conditioning unit

In the refrigeration apparatus according to the first aspect of the present invention, a refrigerant having a smaller refrigeration capacity per unit volume than the R410A refrigerant is used as the refrigerant sealed in the refrigerant circuit, and the indoor heat exchangers are arranged at predetermined intervals. Provided with a plurality of fins and a heat transfer tube that passes through the fin substantially perpendicularly and through which the refrigerant flows, and has three or more different parts where the mass flow rate of the refrigerant flowing inside the heat transfer tube is optimized. It is a thing. According to this aspect, it is possible to optimize the mass flow rate during cooling operation, suppress pressure loss, and obtain an appropriate temperature difference between air and refrigerant.

According to a second aspect of the present invention, in the refrigeration apparatus according to the first aspect, when the indoor heat exchanger functions as an evaporator, the portion is configured as an inlet portion, an intermediate portion, and an outlet portion along the refrigerant flow. The mass flow rate in the pipe of the refrigerant per unit capacity flowing to the inlet part, the intermediate part, and the outlet part is 0.44 g / mm ² hW or more and less than 0.50 g / mm ² hW, 0.14 g / mm ² hW more than 0.16 g / ^mm 2 less than hW, those having the structure such that a 0.15 g / ^mm 2 less than hW at 0.13 g / ^mm 2 hW more. According to this aspect, it is possible to optimize the mass flow rate during cooling operation, suppress pressure loss, and obtain an appropriate temperature difference between air and refrigerant.

According to a third aspect of the present invention, in the refrigeration apparatus according to the first or second aspect, the dryness of the refrigerant flowing through the inlet portion, the intermediate portion, and the outlet portion is 0.215 or more at the standard cooling capacity. And below 0.437, above 0.437 and below 0.8, and above 0.8 and below 1.0. According to this aspect, it is possible to optimize the mass flow rate during cooling operation, suppress pressure loss, and obtain an appropriate temperature difference between air and refrigerant.

According to a fourth aspect of the present invention, in the refrigeration apparatus according to any one of the first to third aspects, the refrigerant flowing through the inlet portion, the intermediate portion, and the outlet portion when the indoor heat exchanger has an intermediate cooling capacity. The dryness was 0.23 or more and less than 0.408, 0.408 or more and less than 0.645, and 0.645 or more and 1.0 or less. According to this aspect, it is possible to optimize the mass flow rate during cooling operation, suppress pressure loss, and obtain an appropriate temperature difference between air and refrigerant.

According to a fifth aspect of the present invention, in the refrigeration apparatus according to any one of the first to fourth aspects, the part includes the outlet part, the intermediate part, and the inlet when the indoor heat exchanger functions as a condenser. pipe mass flow rate of refrigerant per unit capacity flowing through the site, each 0.121 g / ^mm 2 less than hW at 0.120 g / ^mm 2 hW above, 0.127 g / ^mm 2 hW least 0.129 g / ^mm 2 hW below, was constructed such that a 0.451 g / ^mm 2 less than hW at 0.446 g / ^mm 2 hW more. According to this aspect, it is possible to suppress the performance degradation even during the heating operation, and to obtain an optimal annual efficiency that is well balanced with the cooling performance.

According to a sixth aspect of the present invention, in the refrigeration apparatus according to any one of the first to fifth aspects, when the indoor heat exchanger has a standard heating capacity, the refrigerant flowing through the outlet part, the intermediate part, and the inlet part The dryness was 0.408 or more and less than 1.00, 0 or more and less than 0.408 and 0.00. According to this aspect, it is possible to suppress the performance degradation even during the heating operation, and to obtain an optimal annual efficiency that is well balanced with the cooling performance.

According to a seventh aspect of the present invention, in the refrigeration apparatus according to any one of the first to sixth aspects, the refrigerant flowing through the outlet portion, the intermediate portion, and the inlet portion when the indoor heat exchanger has an intermediate heating capacity. The dryness was 0.681 or more and less than 1.00, 0.163 or more and less than 0.681, and 0.00 or more and 0.681 or less.

According to an eighth aspect of the present invention, there is provided a four-way valve in the refrigeration apparatus according to any one of the first to seventh aspects to change the direction of the refrigerant flowing through the outdoor heat exchanger and the indoor heat exchanger. Made possible. According to this aspect, it is possible to switch between the cooling operation and the heating operation.

According to a ninth aspect of the present invention, in the refrigeration apparatus or the air conditioning apparatus according to any one of the first to eighth aspects, an indoor air supply mechanism that supplies the indoor heat exchanger is provided, and the indoor heat exchanger is a condenser. When functioning, the downstream of the flow direction of the refrigerant in the indoor heat exchanger is the upstream of the air flow formed by the indoor blowing mechanism. According to this aspect, the efficiency at the time of heating operation can be improved.

According to a tenth aspect of the present invention, in the refrigerating apparatus or the air conditioning apparatus according to any one of the first to ninth aspects, the refrigerant is a refrigerant having a base component of hydrofluoroolefin having a double bond between carbon and carbon. A single refrigerant or a mixed refrigerant containing the refrigerant is filled. According to this aspect, by using a refrigerant with a small global warming coefficient, even if a refrigerant that is not recovered is released into the atmosphere, the influence on global warming can be kept to a minimum.

Hereinafter, the present invention will be described taking the case of an air conditioning apparatus as an example. Note that the present invention is not limited to the embodiments.

(Embodiment 1)
FIG. 1 is a configuration diagram of an air conditioning apparatus according to the present embodiment.

The air conditioning apparatus according to Embodiment 1 includes a compressor 1 that compresses refrigerant, a four-way valve 2 that switches a refrigerant circuit during cooling and heating operation, an outdoor heat exchanger 3 that exchanges heat between the refrigerant and outside air, and a throttle that depressurizes the refrigerant. The apparatus 4 includes an indoor heat exchanger 5 that exchanges heat between refrigerant and room air. The compressor 1, the four-way valve 2, the outdoor heat exchanger 3, the expansion device 4, and the indoor heat exchanger 5 are connected in a ring shape with a connecting pipe. The outdoor unit 10 includes a compressor 1, a four-way valve 2, an outdoor heat exchanger 3, and an expansion device 4, and the indoor unit 11 includes an indoor heat exchanger 5. The outdoor unit 10 and the indoor unit 11 are connected by a connection pipe A12 and a connection pipe B13.

During the cooling operation, the refrigerant compressed by the compressor 1 becomes a high-temperature and high-pressure refrigerant and is sent to the outdoor heat exchanger 3 through the four-way valve 2. Then, heat is exchanged with the outside air to dissipate the heat, and the high-pressure liquid refrigerant is sent to the expansion device 4. In the expansion device 4, the refrigerant is decompressed to become a low-temperature and low-pressure two-phase refrigerant, passes through the connecting pipe B 13, enters the indoor heat exchanger 5, exchanges heat with the indoor air, absorbs heat, evaporates and becomes a low-temperature gas refrigerant. At this time, the room air is cooled to cool the room. Further, the refrigerant is returned to the compressor 1 through the connection pipe A12 and the four-way valve 2.

During the heating operation, the refrigerant compressed by the compressor 1 becomes a high-temperature and high-pressure refrigerant and is sent to the connection pipe A12 through the four-way valve 2. Then, it enters the indoor heat exchanger 5 to exchange heat with room air to dissipate heat, and is cooled to become a high-pressure liquid refrigerant. At this time, the room air is heated to heat the room. Thereafter, the refrigerant is sent to the expansion device 4 through the connection pipe B13, and is reduced in pressure by the expansion device 4 to become a low-temperature and low-pressure two-phase refrigerant, and is sent to the outdoor heat exchanger 3 to exchange heat with the outside air to evaporate. And returned to the compressor 1 via the four-way valve 2. In this way, the air conditioning operation is performed.

The refrigerant circuit constituting the cooling / heating apparatus according to the present embodiment encloses a refrigerant having a smaller refrigeration capacity per unit volume than the R410A refrigerant. This refrigerant is a refrigerant based on tetrafluoropropene in a hydrofluoroolefin having a double bond between carbon and carbon. In this embodiment, HFO1234yf will be described as an example.

Next, the case where the indoor heat exchanger 5 is an evaporator will be described in detail.

FIG. 2 shows a comparison of the refrigeration capacity per unit volume between the R410A refrigerant and the HFO1234yf refrigerant.

FIG. 2 shows saturated gas density, latent heat of vaporization, and refrigerating capacity per unit volume of the evaporator (saturated gas density x latent heat of vaporization) for R410A refrigerant and HFO1234yf refrigerant when the evaporation temperature of the evaporator is 5 ° C and 10 ° C. Yes.

As shown in FIG. 2, the refrigerating capacity per unit volume at the time of cooling operation, when the evaporation temperature 5 ° C., a 3310.5kJ / ^{m 3} In 7715.1kJ ^/ m 3, HFO1234yf at R410A, also the evaporation temperature 10 At 410 ° C., R410A has 8742.6 kJ / m ³ , HFO1234yf has 3791.7 kJ / m ³ , and HFO1234yf is about 1 / 2.3 times R410A. Therefore, in order to make the refrigeration capacity of HFO1234yf comparable to R410A, the volume flow rate of refrigerant per unit time (hereinafter referred to as refrigerant circulation amount) needs to be about 2.3 times that of R410A.

FIG. 3 shows an example of the indoor heat exchanger 5 for the R410A refrigerant.

The indoor heat exchanger 5 includes a plurality of fins 19 arranged at predetermined intervals, and heat transfer tubes that penetrate the fins 19 at substantially right angles and through which the refrigerant flows. Further, air and the refrigerant exchange heat with the blower 18. Furthermore, it comprises an inlet part 80, an intermediate part 81, and an outlet part 82 along the flow of the refrigerant, and has different mass flow rates for each part.

The flow of the refrigerant is sent from the expansion device 4, flows in from the heat transfer tube 50, enters the heat transfer tube 52 through the heat transfer tube 51, and reaches the heat transfer tube 53. After four branches from the heat transfer tube 53 to the

heat transfer tubes

60, 61, 62 and 63, the refrigerant reaches the heat transfer tubes 60 ', 61', 62 'and 63', respectively. The refrigerant of the heat transfer tubes 60 ′, 61 ′, 62 ′, and 63 ′ branches, for example, through a header (not shown) into the

heat transfer tubes

70 and 71 at a substantially equal flow rate to reach the heat transfer tubes 70 ′ and 71 ′. The refrigerant is returned to the compressor 1 through the connection pipe B13 and the four-way valve 2.

FIG. 4 shows the mass flow rate, the dryness, the saturation temperature difference, and the cooling capacity of each part of each refrigerant when the indoor heat exchanger 5 for R410A refrigerant in FIG. 3 is used and R410A and HFO1234yf are used as refrigerants. Yes.

The saturation temperature difference was used as an index of pressure loss. The saturation temperature difference was determined by obtaining the saturation temperature for each refrigerant from the refrigerant pressure at the inlet and outlet of the indoor heat exchanger 5. Since the relationship between pressure and temperature differs depending on the refrigerant, the pressure loss related to performance cannot be simply compared as a pressure difference. When comparing the pressure loss of different refrigerants, it is customary to match the saturation temperature difference, and it can be determined that the greater the saturation temperature difference, the greater the pressure loss.

FIG. 4 also shows data under conditions where the cooling capacity is maximized by increasing the refrigerant circulation rate when HFO1234yf is used. As can be seen from FIG. 4, the capacity of HFO1234yf is about 74% of R410A (= 2890 ÷ 3903 × 100). This is due to the large pressure loss of HFO1234yf as can be seen from the saturation temperature difference. Furthermore, it demonstrates using FIG.

FIG. 5 shows a PH diagram under the conditions of FIG. 4 using the indoor heat exchanger 5 for R410A refrigerant in FIG. 3 and using HFO1234yf refrigerant.

Point A indicates the compressor inlet, point B indicates the compressor discharge, point C indicates the condenser inlet, point D indicates the condenser outlet, point E indicates the evaporator inlet, and point F indicates the evaporator outlet. ing.

FIG. 5 shows that the slope of the line from the point E to the point F at the entrance / exit of the evaporator is large, and the pressure loss is large because the refrigerant circulation amount is increased. Further, since the temperature of the refrigerant increases from the point F toward the point E, the temperature difference between the refrigerant and the air that is the heat exchange fluid gradually decreases, and the temperature difference at the point E that is the inlet of the indoor heat exchanger 5. Is negligible. Thus, since the heat exchange amount is reduced by reducing the difference between the refrigerant and the air temperature, a predetermined cooling capacity cannot be ensured.

That is, since the refrigerant circulation amount is increased, the pressure loss increases and the temperature difference between the refrigerant and the air becomes small, so it can be said that the capacity cannot be secured.

FIG. 6 is an example of the indoor heat exchanger 5 of the present invention.

The indoor heat exchanger 5 includes a plurality of fins 19 arranged at predetermined intervals, and heat transfer tubes that penetrate the fins 19 at substantially right angles and through which the refrigerant flows. Further, air and the refrigerant exchange heat with the blower 18. At this time, the refrigerant flow and the air flow direction are the same. Furthermore, it is comprised of the inlet part 15, the intermediate part 16, and the outlet part 17 along the flow of the refrigerant, and the mass flow rate per unit capacity is different for each part.

The flow of the refrigerant is sent from the expansion device 4, branches into the

heat transfer tubes

20 and 21, and flows into the heat transfer tubes 20 'and 21', respectively. The refrigerant of the heat transfer tubes 20 ′ and 21 ′ passes, for example, through a header (not shown), and is approximately equally branched into the

heat transfer tubes

30, 31, 32, 33, 34, 35, and 36, and the heat transfer tubes 30 ′, 31 ′, and 32, respectively. ', 33', 34 ', 35', 36 ', and further, for example, through a header (not shown), through the

heat transfer tubes

40, 41, 42, 43, 44, 45, respectively, to the heat transfer tubes 40', 41 ', The refrigerant reaches 42 ', 43', 44 ', 45', and is returned to the compressor 1 via the four-way valve 2 through the connecting pipe B13 via a header (not shown), for example.

Furthermore, as an example of the pipe diameter, φ6.35 mm may be used at the inlet portion 15 and the intermediate portion 16, and φ7 mm may be used at the outlet portion 17. Further, the entrance portion 15 may have 2 passes, the intermediate portion 16 may have 7 passes, and the exit portion 17 may have 6 passes.

FIG. 7 shows the mass flow rate, the dryness, and the saturation temperature difference of each part of each refrigerant calculated by simulation with the standard cooling capacity when the indoor heat exchanger 5 of the present invention in FIG. 6 is used and HFO1234yf is used as the refrigerant. And the cooling capacity.

From FIG. 7, the mass flow rate in the pipe of the refrigerant per unit capacity flowing through the inlet portion 15, the intermediate portion 16, and the outlet portion 17 is 0.44 g / mm ² hW or more and less than 0.50 g / mm ² hW and 0.14 g, respectively. / ^mm 2 hW more than 0.16 g / ^mm 2 less than hW, becomes less than 0.15 g / ^mm 2 hW at 0.13 g / ^mm 2 hW above, the dryness in the cooling standard capacity, respectively 0.215 or 0 Less than .437, 0.437 or more and less than 0.8, 0.8 or more and 1.0 or less.

Moreover, the dryness at the time of cooling intermediate period capacity is 0.23 or more and less than 0.408, 0.408 or more and less than 0.645, and 0.645 or more and 1.0 or less.

The saturation temperature difference is about 9.5 K, and the cooling capacity is 3912 W, which is almost the same as when the R410A refrigerant shown in FIG. 4 is used, and the cooling capacity can be secured.

FIG. 8 shows a PH diagram under the conditions of FIG. 7 using the indoor heat exchanger 5 of the present invention in FIG. 6 and using HFO1234yf refrigerant.

A point is the compressor inlet, B is the compressor discharge, C is the condenser inlet, D is the condenser outlet, E 'is the evaporator inlet, and F is the evaporator outlet. Show. In addition, point E indicates the indoor heat exchanger inlet when the indoor heat exchanger 5 for R410A is used.

FIG. 8 shows that when the indoor heat exchanger 5 for R410A is used, the pressure loss is large and the slope of the line from the F point to the E point is large, whereas the indoor heat exchanger 5 of the present invention is When used, it can be seen that the slope from the point F to the point E ′ is gentle. Therefore, an appropriate refrigerant and air temperature can be secured, that is, a heat exchange amount can be secured, and a predetermined cooling capacity can be secured.

Meanwhile, the case where the indoor heat exchanger 5 is a condenser will be described.

The case where the indoor heat exchanger 5 of the present invention in FIG. 6 is used will be described. During the heating operation, the refrigerant flow is reversed from that during the cooling operation.

That is, the gas refrigerant that has passed through the connection pipe B13 reaches the heat transfer pipes 40 ′, 41 ′, 42 ′, 43 ′, 44 ′, and 45 ′, and further passes through the

heat transfer pipes

40, 41, 42, 43, 44, and 45. For example, the heat transfer tubes 30 ′, 31 ′, 32 ′, 33 ′, 34 ′, 35 ′, and 36 ′ are branched substantially evenly through a header (not shown). Further, the

heat transfer tubes

30, 31, 32, 33, 34, 35, and 36 pass through, for example, a header (not shown), branch substantially evenly, flow into the heat transfer tubes 20 ′ and 21 ′, and enter the

heat transfer tubes

20 and 21. To the connecting pipe A13. At this time, the refrigerant is composed of the outlet part 17, the intermediate part 16, and the inlet part 15 along the flow, and has a mass flow rate per unit capacity that is different for each part. Mass flow rate per unit capacity of each site was calculated by simulation, 0.120g / ^mm 2 hW more than 0.121 g / ^mm 2 less than hW, 0.127g / ^mm 2 hW more than 0.129 g / ^mm 2 hW below, the 0.451 g / ^mm 2 less than hW at 0.446 g / ^mm 2 hW more.

Also, the dryness of each of the simulations is 0.408 or more and less than 1.00 at the heating standard capacity, 0 or more and less than 0.408 or 0.00 at the heating standard capacity, and 0.681 or more and less than 1.00 at the heating intermediate capacity. 0.163 or more and less than 0.681, and 0.00 or more and 0.681 or less.

Furthermore, at this time, the air and the refrigerant exchange heat with the blower 18. At this time, the refrigerant flow and the air flow direction are the same. The downstream of the flow direction of the refrigerant in the indoor heat exchanger 5 is the upstream of the air flow formed by the blower 18, that is, the flow direction of the air sent by the blower 18 is opposite to the flow direction of the refrigerant. Therefore, since the average temperature difference is larger than that flowing in the same direction, the efficiency is improved.

Fig. 9 shows the layout of the parts. When the indoor heat exchanger 5 is configured, an example in which the inlet portion 15, the intermediate portion 16, and the outlet portion 17 are configured in FIG. 9 is shown. As shown in FIG. 9 (a), each part may be divided and arranged, or as shown in FIG. 9 (b), the three parts may overlap, and the arrangement of each part is not limited to this figure. Absent.

Further, FIG. 10 shows the calculation results when the indoor heat exchanger 5 of the present invention is used and when the mass flow rate per unit capacity is changed in each of the inlet part 15, the intermediate part 16, and the outlet part 17. In FIG. 10, the case where the indoor heat exchanger 5 of the present invention is used is shown in bold in the center of the table, the cooling standard, the cooling middle, the heating standard and the heating middle capacity are set to 100%, and the period efficiency is set to 100%. it's shown.

As can be seen from FIG. 10, it can be seen that there is nothing exceeding the period efficiency of 100% when the indoor heat exchanger 5 of the present invention is used.

However, in particular, it can be seen that the heating capacity is higher at the mass flow rate per unit capacity of 0.117 g / mm ² hW at (3) the exit part in FIG. 10, but the heating performance is somewhat lowered as a characteristic of this refrigerant. However, it can be seen that the point is to improve the cooling performance.

In addition, since the pipe diameter is determined as a standard, any pipe diameter cannot be selected. Therefore, the pipe diameter and the number of passes are appropriately selected so as to be as close as possible to the mass speed and the dryness of the refrigerant shown in the embodiment.

In the above embodiment, HFO1234yf has been described as an example. However, a refrigerant using a hydrofluoroolefin having a double bond between carbon and a carbon as a base component may be used. For example, HFO1234ze may be used, and such a refrigerant may be used alone or as a mixed refrigerant containing the refrigerant, for example, a refrigerant mixed with hydrofluorocarbon having no double bond as the working refrigerant.

Specifically, a mixed refrigerant in which the hydrofluoroolefin is tetrafluoropropene (HFO1234yf or HFO1234ze) and the hydrofluorocarbon is difluoromethane (HFC32) may be used as the working refrigerant.

Also, a mixed refrigerant in which the hydrofluoroolefin is tetrafluoropropene (HFO1234yf) and the hydrofluorocarbon is pentafluoroethane (HFC125) may be used as the working refrigerant.

Also, a three-component mixed refrigerant in which the hydrofluoroolefin is tetrafluoropropene (HFO1234yf) and the hydrofluorocarbon is pentafluoroethane (HFC125) and difluoromethane (HFC32) may be used as the working refrigerant.

Moreover, although it demonstrated as an air conditioning apparatus in the said embodiment, it is applicable also as refrigeration apparatuses only for heating which does not have a four-way valve, for example, a water heater, etc., for cooling only, for example, a cooler, a freezer, etc. A heat exchanger and an outdoor heat exchanger are a condenser and an evaporator.

According to the present invention, it is possible to use a refrigerant having a small GWP, such as HFO1234yf of GWP4.

DESCRIPTION OF SYMBOLS 1 Compressor 2 Four-way valve 3 Outdoor heat exchanger 4 Throttle device 5 Indoor heat exchanger 6 Refrigerant with small refrigerating capacity per unit volume 15 Inlet part 16 Intermediate part 17 Outlet part 18 Blower 19

Fin

20, 21, 20 ′, 21 ', 30, 31, 32, 33, 34, 35, 36,
30 ', 31', 32 ', 33', 34 ', 35', 36 ', 40, 41, 42, 43, 44, 45, 40', 41 ', 42', 43 ', 44', 45 ' Heat transfer tube

Claims

At least the compressor, the outdoor heat exchanger, the expansion device, and the indoor heat exchanger are connected in order by a connecting pipe to form an annular refrigerant circuit, and the refrigerant enclosed in the refrigerant circuit is per unit volume as compared with the R410A refrigerant. Refrigeration equipment using a small refrigerant,
The indoor heat exchanger includes a plurality of fins arranged at predetermined intervals, and a heat transfer tube that passes through the fins at a substantially right angle and through which the refrigerant flows, and the mass flow rate of the refrigerant flowing through the heat transfer tube is three. A refrigeration apparatus having two or more different parts.
2. The refrigeration apparatus according to claim 1, wherein, when the indoor heat exchanger functions as an evaporator, the part is configured as an inlet part, an intermediate part, and an outlet part along a refrigerant flow, and the inlet part and the intermediate part The mass flow rate in the pipe of the refrigerant per unit capacity flowing to the outlet site is 0.44 g / mm 2 hW or more and less than 0.50 g / mm 2 hW, 0.14 g / mm 2 hW or more and 0.16 g / mm, respectively. A refrigeration apparatus configured to be less than mm 2 hW, 0.13 g / mm 2 hW or more and less than 0.15 g / mm 2 hW.
3. The indoor heat exchanger according to claim 1, wherein the dryness of the refrigerant flowing through the inlet portion, the intermediate portion, and the outlet portion is 0.215 or more and less than 0.437, respectively, at a standard capacity of cooling. A refrigeration apparatus configured to be 0.437 or more and less than 0.8 and 0.8 or more and 1.0 or less.
The refrigeration apparatus according to any one of claims 1 to 3, wherein when the indoor heat exchanger has an intermediate capacity of cooling, the dryness of the refrigerant flowing through the inlet part, the intermediate part, and the outlet part is 0.23 or more, respectively. A refrigeration apparatus configured to be less than 0.408, 0.408 or more and less than 0.645, or 0.645 or more and 1.0 or less.
The refrigeration apparatus according to any one of claims 1 to 4, wherein when the indoor heat exchanger functions as a condenser, the part is a refrigerant per unit capacity flowing through the outlet part, the intermediate part, and the inlet part. a mass flow rate piping, respectively 0.120 g / mm 2 hW more than 0.121 g / mm 2 less than hW, 0.129 g / mm 2 less than hW at 0.127 g / mm 2 hW above, 0.446 g / mm 2 hW The refrigeration apparatus according to claim 1, wherein the refrigeration apparatus is configured to be less than 0.451 g / mm 2 hW.
6. The refrigeration apparatus according to claim 1, wherein when the indoor heat exchanger has a standard heating capacity, the dryness of the refrigerant flowing through the outlet part, the intermediate part, and the inlet part is 0.408 or more, respectively. The refrigeration apparatus is configured to be less than 1.00, 0 or more and less than 0.408 and 0.00.
The refrigeration apparatus according to any one of claims 1 to 6, wherein when the indoor heat exchanger has an intermediate heating capacity, the dryness of the refrigerant flowing through the outlet part, the intermediate part, and the inlet part is 0.681 or more, respectively. The refrigeration apparatus is configured to be less than 1.00, 0.163 or more and less than 0.681, and 0.00 or more and 0.681 or less.
8. A cooling / heating device provided with a four-way valve in the refrigeration apparatus according to claim 1 to enable cooling / heating by changing the direction of refrigerant flowing in the outdoor heat exchanger and the indoor heat exchanger.
The refrigeration apparatus or cooling / heating apparatus according to any one of claims 1 to 8, further comprising a blower that supplies the indoor heat exchanger, wherein the indoor heat exchanger functions as a condenser. The refrigerant | coolant flow direction downstream is the upstream of the air flow which the said air blower forms, The refrigeration apparatus or the air conditioning apparatus characterized by the above-mentioned.
2. The refrigerant according to claim 1, wherein the refrigerant is filled with a single refrigerant composed of a refrigerant composed of carbon and a hydrofluoroolefin having a double bond between carbons or a mixed refrigerant containing the refrigerant. 10. The refrigeration apparatus or air conditioning apparatus according to any one of 9.