Technical Field
[0001] The present invention relates to an air-conditioning apparatus.
Background Art
[0002] In a typical air-conditioning apparatus, such as a multi-air-conditioning apparatus
for a building, an outdoor unit, functioning as a heat source device, disposed outside
a structure, for example, is connected to an indoor unit disposed in the structure
by pipes to form a refrigerant circuit through which refrigerant is circulated. The
refrigerant is used to transfer heat to or remove heat from air in order to heat or
cool the air, thereby heating or cooling an air-conditioned space.
[0003] In a heating operation of such a multi-air-conditioning apparatus for a building,
a heat exchanger included in the outdoor unit functions as an evaporator and exchanges
heat between low temperature refrigerant and the air. This causes moisture in the
air to condense on fins and heat transfer tubes of the heat exchanger, thus forming
frost on the heat exchanger. The frost on the heat exchanger will block air passages
in the heat exchanger, resulting in a decrease in heat transfer area for heat exchange
with air. This will lead to poor heating capacity.
[0004] Typically, the heating operation is stopped, a refrigerant flow direction is changed
by a refrigerant flow switching device, and the heat exchanger in the outdoor unit
is allowed to function as a condenser, thus achieving a defrosting operation. Performing
such a defrosting operation can prevent a decrease in heating capacity. In the defrosting
operation, however, the heating operation for an indoor space is stopped. Disadvantageously,
an indoor air temperature will fall, thus reducing comfort of an indoor environment.
[0005] To solve the above-described disadvantage, related-art apparatuses are configured
such that an outdoor unit includes a plurality of heat exchangers and gas discharged
from a compressor is allowed to flow into the heat exchangers. Specifically, bypass
pipes for bypassing the heat exchangers through on-off valves are arranged, and each
of the heat exchangers is allowed to function as an evaporator or a condenser such
that the evaporator and the condenser are driven simultaneously, thus achieving the
defrosting operation and the heating operation simultaneously (refer to Patent Literature
1 to 3, for example).
Citation List
Patent Literature
Summary of Invention
Technical Problem
[0007] In an air-conditioning apparatus disclosed in each of Patent Literature 1 and Patent
Literature 2, a plurality of outdoor heat exchangers are used such that an outdoor
heat exchanger is operated as an evaporator for the heating operation and another
outdoor heat exchanger is operated as a condenser for the defrosting operation, and
the heating operation and the defrosting operation are simultaneously performed. While
the defrosting operation is performed such that one outdoor heat exchanger is operated
as a condenser, part of gas refrigerant discharged from a compressor flows into the
condenser and only sensible heat of the gas refrigerant is used to perform the defrosting
operation. The difference in enthalpy between a point prior to the condenser and a
point after the condenser is accordingly insufficient. To achieve sufficient defrosting
capacity, a circulation amount of part of the gas refrigerant discharged from the
compressor has to be increased. This increase causes a decrease in the amount of refrigerant
supplied to the evaporator, resulting in a decrease in indoor heating capacity. This
leads to a reduction in comfort of an indoor environment.
[0008] In an air-conditioning apparatus disclosed in Patent Literature 3, while the defrosting
operation is performed such that an outdoor heat exchanger is operated as a condenser,
an expansion device having a variable opening degree disposed in a passage on a refrigerant
outlet side of the condenser is controlled to accumulate the refrigerant in the condenser.
This enables intermediate pressure defrosting. Consequently, the pressure of the refrigerant
in the condenser is increased to allow a saturation temperature of the refrigerant
to be slightly higher than 0 degrees C (in a range from above approximately 0 to approximately
10 degrees C), such that the saturation temperature is higher than the temperature
of frost. Thus, latent heat of two-phase part of the refrigerant can be used and a
sufficient difference in enthalpy between a point prior to the condenser and a point
after the condenser can be ensured, so that sufficient defrosting capacity can be
achieved with a smaller amount of refrigerant than that in the above-described defrosting
operation.
[0009] The term "intermediate pressure defrosting" as used herein refers to a defrosting
operation performed under conditions where the refrigerant in the condenser, serving
as a defrosting target, has a pressure that is lower than a discharge pressure of
a compressor and is higher than a suction pressure of the compressor (or has a pressure
equivalent to a temperature slightly higher than 0 degrees C in terms of saturation
temperature).
[0010] It is, however, necessary to accumulate the refrigerant in the condenser so that
latent heat of two-phase part of the refrigerant can be used. In other words, accumulating
the refrigerant in the condenser reduces the total amount of refrigerant in a refrigeration
cycle, resulting in a decrease in the amount of refrigerant supplied to an evaporator.
This results in a decrease in indoor heating capacity, leading to a reduction in comfort
of an indoor environment. Additionally, sufficient defrosting capacity is not achieved
until the refrigerant is accumulated in the condenser, because latent heat of two-phase
part of the refrigerant cannot be used. Disadvantageously, the time required for defrosting
is increased, resulting in a decrease in indoor heating capacity. This leads to a
reduction in comfort of the indoor environment.
[0011] The present invention has been made in consideration of the above-described problems
and is intended to provide an air-conditioning apparatus in which, while a heating
operation for an indoor space and a defrosting operation are simultaneously performed
such that an outdoor heat exchanger is operated as a condenser, a decrease in indoor
heating capacity and a decrease in defrosting capacity can be eliminated or reduced.
Solution to Problem
[0012] The present invention provides an air-conditioning apparatus (100, 200) capable of
simultaneously performing a heating operation and a defrosting operation. The apparatus
includes a main circuit including a compressor (10), a load side heat exchanger (21),
a load side expansion device (22), a plurality of heat source side heat exchangers
(12) connected in parallel, and an accumulator (13) that are connected by refrigerant
pipes to form at least a heating circuit, a first gas bypass pipe (5) branching off
from the refrigerant pipe on a discharge side of the compressor (10) and allowing
refrigerant to flow into a defrosting-target heat source side heat exchanger (12)
of the heat source side heat exchangers (12), a second gas bypass pipe (7) branching
off from the refrigerant pipe on the discharge side of the compressor (10) and allowing
the refrigerant to flow into the accumulator (13), a plurality of first opening and
closing devices (30), arranged in the first gas bypass pipe (5), permitting or stopping
the flow of the refrigerant through the first gas bypass pipe (5), and at least one
second opening and closing device (35), disposed in the second gas bypass pipe (7),
permitting or stopping the flow of the refrigerant through the second gas bypass pipe
(7).
Advantageous Effects of Invention
[0013] In the air-conditioning apparatus according to the present invention, while the defrosting
operation in which at least one of the heat source side heat exchangers is operated
as a condenser is performed simultaneously with the heating operation in which the
load side heat exchanger is operated as a condenser and at least one of the other
heat source side heat exchangers is operated as an evaporator, the refrigerant accumulating
in the accumulator can be supplied to the evaporator and the condensers. In the air-conditioning
apparatus according to the present invention, a decrease in the total amount of refrigerant
in a refrigeration cycle can be eliminated or reduced, thus eliminating or reducing
a decrease in heating capacity and defrosting capacity. Consequently, in the air-conditioning
apparatus according to the present invention, the time required for defrosting is
shortened and a decrease in heating capacity is eliminated or reduced, thus achieving
comfort of an indoor environment.
Brief Description of Drawings
[0014]
[Fig. 1] Fig. 1 is a schematic circuit diagram illustrating an example of the circuit
configuration of an air-conditioning apparatus according to Embodiment 1 of the present
invention.
[Fig. 2] Fig. 2 is a schematic diagram illustrating an example of the configuration
of heat source side heat exchangers of the air-conditioning apparatus according to
Embodiment 1 of the present invention.
[Fig. 3] Fig. 3 is a refrigerant circuit diagram illustrating the flow of refrigerant
in a cooling only operation mode of the air-conditioning apparatus according to Embodiment
1 of the present invention.
[Fig. 4] Fig. 4 is a refrigerant circuit diagram illustrating the flow of the refrigerant
in a heating only operation mode of the air-conditioning apparatus according to Embodiment
1 of the present invention.
[Fig. 5] Fig. 5 is a refrigerant circuit diagram illustrating the flow of the refrigerant
in a defrosting operation mode, in which the heat source side heat exchanger is defrosted,
of the air-conditioning apparatus according to Embodiment 1 of the present invention.
[Fig. 6] Fig. 6 is a graph illustrating a change in enthalpy difference, available
for defrosting, caused by a change in saturation temperature in the heat source side
heat exchanger, serving as a defrosting-target heat exchanger, of the air-conditioning
apparatus according to Embodiment 1 of the present invention.
[Fig. 7] Fig. 7 is a graph illustrating the rate of heating capacity in the defrosting
mode with respect to a saturation temperature in the heat source side heat exchanger,
serving as a defrosting-target heat exchanger, of the air-conditioning apparatus according
to Embodiment 1 of the present invention.
[Fig. 8] Fig. 8 is a flowchart illustrating control for operating a second opening
and closing device in the defrosting operation mode of the air-conditioning apparatus
according to Embodiment 1 of the present invention.
[Fig. 9] Fig. 9 is a graph illustrating a change in saturation temperature converted
from a pressure in a load side heat exchanger with respect to a change in flow rate
of high temperature, high pressure gas refrigerant flowing into an accumulator in
the defrosting operation mode of the air-conditioning apparatus according to Embodiment
1 of the present invention.
[Fig. 10] Fig. 10 is a schematic circuit diagram illustrating another example of the
circuit configuration of the air-conditioning apparatus according to Embodiment 1
of the present invention.
[Fig. 11] Fig. 11 is a schematic circuit diagram illustrating an example of the circuit
configuration of an air-conditioning apparatus according to Embodiment 2 of the present
invention.
Description of Embodiments
[0015] Embodiments of the present invention will be described with reference to the drawings.
Note that the dimensional relationship among components in Fig. 1 and subsequent figures
may be different from the actual one. Furthermore, note that components designated
by the same reference numerals in Fig. 1 and the subsequent figures are the same components
or equivalents. The above notes are intended to be common throughout this specification.
Furthermore, note that the forms of components described in the specification are
intended to be illustrative only and are not intended to be limited to the descriptions.
Embodiment 1
[0016] Fig. 1 is a schematic circuit diagram illustrating an example of the circuit configuration
of an air-conditioning apparatus 100 according to Embodiment 1 of the present invention.
[0017] The configuration of the air-conditioning apparatus 100 will now be described in
detail with reference to Fig. 1.
[0018] The air-conditioning apparatus 100 conditions air using a refrigeration cycle through
which refrigerant is circulated. The air-conditioning apparatus 100 permits selection
of any one of a cooling only operation mode in which all of operating indoor units
2 perform cooling, a heating only operation mode in which all of the operating indoor
units 2 perform heating, and a defrosting operation mode in which the indoor units
2 continuously perform a heating operation and heat exchangers (a heat source side
heat exchanger 12a and a heat source side heat exchanger 12b) in an outdoor unit 1
are defrosted.
[0019] As illustrated in Fig. 1, the air-conditioning apparatus 100 includes the outdoor
unit 1 and the indoor unit 2 such that the outdoor unit 1 and the indoor unit 2 are
connected by refrigerant main pipes 4. In the following description, the heat source
side heat exchanger 12a and the heat source side heat exchanger 12b may be collectively
referred to as heat source side heat exchangers 12 or a heat source side heat exchanger
12.
[Outdoor Unit 1]
[0020] The outdoor unit 1 includes a compressor 10, a refrigerant flow switching device
11, such as a four-way valve, the heat source side heat exchanger 12a, the heat source
side heat exchanger 12b, an accumulator 13, a first opening and closing device 30a,
a first opening and closing device 30b, a second opening and closing device 35, a
third opening and closing device 31 a, a third opening and closing device 31 b, a
flow control device 32a, and a flow control device 32b. These components are connected
by refrigerant pipes 3, a first gas bypass pipe 5, and a second gas bypass pipe 7
in the outdoor unit 1.
[0021] The refrigerant pipes 3 connect the compressor 10, the refrigerant flow switching
device 11, the heat source side heat exchanger 12a, the heat source side heat exchanger
12b, the flow control device 32a, the flow control device 32b, and the accumulator
13. The heat source side heat exchanger 12a and the heat source side heat exchanger
12b are connected in parallel by the refrigerant pipes 3.
[0022] The first gas bypass pipe 5 is connected at a first end to the refrigerant pipe 3
between a discharge outlet of the compressor 10 and the refrigerant flow switching
device 11. The first gas bypass pipe 5 branches into two pipes at a second end. At
the second end of the first gas bypass pipe 5, one of the two pipes is connected to
the refrigerant pipe 3 between the heat source side heat exchanger 12a and the third
opening and closing device 31 a, and the other one of the two pipes is connected to
the refrigerant pipe 3 between the heat source side heat exchanger 12b and the third
opening and closing device 31 b.
[0023] The first opening and closing device 30a is disposed in the first gas bypass pipe
5 connected to the heat source side heat exchanger 12a.
[0024] The first opening and closing device 30b is disposed in the first gas bypass pipe
5 connected to the heat source side heat exchanger 12b.
[0025] The second gas bypass pipe 7 is connected at a first end to the refrigerant pipe
3 between the discharge outlet of the compressor 10 and the refrigerant flow switching
device 11. The second gas bypass pipe 7 is connected at a second end to the refrigerant
pipe 3 between the refrigerant flow switching device 11 and the accumulator 13.
[0026] The second opening and closing device 35 is disposed in the second gas bypass pipe
7.
[0027] The third opening and closing device 31 a for stopping the flow of the refrigerant
into the heat source side heat exchanger 12a is disposed in the refrigerant pipe 3
between the heat source side heat exchanger 12a and the refrigerant flow switching
device 11.
[0028] The third opening and closing device 31 b for stopping the flow of the refrigerant
into the heat source side heat exchanger 12b is disposed in the refrigerant pipe 3
between the heat source side heat exchanger 12b and the refrigerant flow switching
device 11.
[0029] Each of the heat source side heat exchangers 12a and 12b is a finned tube heat exchanger
including a plurality of plate-shaped fins (fins 51 in Fig. 2) and heat transfer tubes
(heat transfer tubes 52 in Fig. 2) extending through and orthogonal to the fins. An
example of the configuration of the heat source side heat exchangers 12 will now be
described with reference to Fig. 2. Fig. 2 is a schematic diagram illustrating an
example of the configuration of the heat source side heat exchangers 12 of the air-conditioning
apparatus 100.
[0030] As illustrated in Fig. 2, the heat source side heat exchanger 12 is divided into
a plurality of heat exchangers. A configuration in which the heat source side heat
exchanger 12 is divided into the two heat source side heat exchangers 12a and 12b
will be described as an example. The heat source side heat exchangers 12a and 12b
each include two adjacent sets of fins 51 arranged in a set arrangement direction
(or a left-right direction along the width of the fins aligned so as to face in the
same direction). The heat source side heat exchangers 12a and 12b are arranged at
two levels in a level arrangement direction (or a top-bottom direction along the length
of the fins aligned so as to face in the same direction) in which the heat transfer
tubes 52 are arranged at different levels.
[0031] In other words, the heat source side heat exchanger 12 is divided into the heat source
side heat exchangers 12a and 12b in a housing of the outdoor unit 1 such that the
heat source side heat exchangers 12a and 12b are arranged in the top-bottom direction
along the length of the fins 51 aligned so as to face in the same direction. For example,
as illustrated in Fig. 2, the heat source side heat exchanger 12a is disposed at an
upper level, the heat source side heat exchanger 12b is disposed at a lower level,
and each of the fins 51 extending in the level arrangement direction is a one-piece
member (shared by the heat source side heat exchangers).
[0032] As illustrated in Fig. 2, a refrigerant passage to the heat source side heat exchanger
12a may be divided by a distributer 12a-1 and a header 12a-2. Similarly, a refrigerant
passage to the heat source side heat exchanger 12b may be divided by a distributer
12b-1 and a header 12b-2 as illustrated in Fig. 2.
[0033] In the above-described configuration of Fig. 2, the two adjacent sets of fins are
arranged in the set arrangement direction (or the left-right direction along the width
of the fins aligned so as to face in the same direction). In addition, one set, three
sets, or more sets may be arranged. Another pass pattern different from that in Fig.
2 may be used. As regards the heat source side heat exchangers 12, a plurality of
heat source side heat exchangers may be arranged at three or more levels in the level
arrangement direction (or the top-bottom direction along the length of the fins aligned
so as to face in the same direction) and each of the fins extending in the level arrangement
direction may be a one-piece member (shared by the heat source side heat exchangers).
The number of levels for arrangement of the heat source side heat exchangers is not
limited to that illustrated in Fig. 2. More or less than two levels may be arranged.
[0034] The heat transfer tubes 52, through which the refrigerant passes, are arranged at
multiple levels in the level arrangement direction perpendicular to an air passing
direction such that multiple columns of heat transfer tubes are arranged in the set
arrangement direction identical to the air passing direction.
[0035] The fins 51 are spaced apart such that the air passes through the fins in the air
passing direction.
[0036] Although the heat source side heat exchanger 12 may be divided into two heat exchangers
arranged in the left-right direction, pipe connection would be complicated in such
arrangement, because a refrigerant inlet of the heat source side heat exchanger 12a
and a refrigerant inlet of the heat source side heat exchanger 12b would be arranged
at opposite ends of the outdoor unit 1 in the left-right direction. It is therefore
preferred that the heat source side heat exchanger 12 be divided into two heat exchangers
arranged in the top-bottom direction, as illustrated in Fig. 2.
[0037] As regards the fins 51 of the heat source side heat exchangers 12a and 12b, each
fin 51 may be a one-piece member as illustrated in Fig. 2 or may be divided into two
segments corresponding to the heat exchangers. The number of heat exchangers obtained
by dividing the heat source side heat exchanger 12 is not limited to two. The heat
source side heat exchanger 12 may be divided into any number of heat exchangers.
[0038] Furthermore, outdoor air is sent to the heat source side heat exchangers 12a and
12b by an air-sending device (not illustrated), such as a fan.
[0039] The air-sending devices may be arranged in one-to-one correspondence to the heat
source side heat exchangers 12a and 12b. Alternatively, a single air-sending device
may be shared by the heat source side heat exchangers 12a and 12b.
[0040] The flow control device 32a has a variable opening degree. The flow control device
32a is disposed in the refrigerant pipe 3 extending from the heat source side heat
exchanger 12a toward a load side expansion device 22.
[0041] The flow control device 32b has a variable opening degree. The flow control device
32b is disposed in the refrigerant pipe 3 extending from the heat source side heat
exchanger 12b toward the load side expansion device 22.
[0042] The compressor 10 sucks the refrigerant and compresses the refrigerant into a high
temperature, high pressure state. The compressor 10 is, for example, a capacity-controllable
inverter compressor.
[0043] The refrigerant flow switching device 11 switches a refrigerant flow direction in
the heating only operation mode and a refrigerant flow direction in the cooling only
operation mode.
[0044] The heat source side heat exchangers 12a and 12b function as evaporators in the heating
only operation mode and function as condensers in the cooling only operation mode.
In the defrosting operation, one of the heat source side heat exchangers 12a and 12b
functions as an evaporator and the other one of them functions as a condenser.
[0045] The accumulator 13, which is disposed on a suction side of the compressor 10, stores
an excess of refrigerant caused by the difference between an operation state in the
heating only operation mode and that in the cooling only operation mode or an excess
of refrigerant caused by a transient change in operation.
[0046] The first opening and closing device 30a permits high temperature refrigerant flowing
through the first gas bypass pipe 5 to flow into the heat source side heat exchanger
12a when the heat source side heat exchanger 12a operates as a condenser in the defrosting
operation mode.
[0047] The first opening and closing device 30b permits high temperature refrigerant flowing
through the first gas bypass pipe 5 to flow into the heat source side heat exchanger
12b when the heat source side heat exchanger 12b operates as a condenser in the defrosting
operation mode.
[0048] Each of the first opening and closing devices 30a and 30b may be a component capable
of opening and closing a refrigerant passage, for example, a two-way valve, a solenoid
valve, or an electronic expansion valve.
[0049] In the following description, the first opening and closing devices 30a and 30b may
be collectively referred to as first opening and closing devices 30.
[0050] The third opening and closing device 31 a closes a refrigerant passage to prevent
low temperature two-phase refrigerant, flowing from the indoor unit 2 through the
refrigerant main pipe 4 to the outdoor unit 1, from flowing into the heat source side
heat exchanger 12a when the heat source side heat exchanger 12a operates as a condenser
in the defrosting operation mode.
[0051] The third opening and closing device 31 b closes a refrigerant passage to prevent
low temperature two-phase refrigerant, flowing from the indoor unit 2 through the
refrigerant main pipe 4 to the outdoor unit 1, from flowing into the heat source side
heat exchanger 12b when the heat source side heat exchanger 12b operates as a condenser
in the defrosting operation mode.
[0052] Each of the third opening and closing devices 31 a and 31 b may be a component capable
of opening and closing the refrigerant passage, for example, a two-way valve, a solenoid
valve, or an electronic expansion valve.
[0053] In the following description, the third opening and closing devices 31 a and 31 b
may be collectively referred to as third opening and closing devices 31.
[0054] Each of the flow control devices 32a and 32b is an expansion device whose opening
degree (opening area) is variable to control a pressure in the heat source side heat
exchanger 12 functioning as a condenser.
[0055] Each of the flow control devices 32a and 32b may be, for example, an electronic expansion
valve that is driven by a stepping motor or may include a plurality of small solenoid
valves arranged in parallel such that the opening area is changed by switching the
valves.
[0056] In the following description, the flow control devices 32a and 32b may be collectively
referred to as flow control devices 32.
[0057] The second opening and closing device 35 permits part of high temperature, high pressure
gas refrigerant discharged from the compressor 10 in the defrosting operation mode
to flow into the accumulator 13.
[0058] The second opening and closing device 35 may be a component capable of opening and
closing the refrigerant passage, for example, a two-way valve, a solenoid valve, or
an electronic expansion valve.
[0059] The outdoor unit 1 includes, as pressure detecting units, a first pressure sensor
41 and a second pressure sensor 42.
[0060] The first pressure sensor 41 is disposed in the refrigerant pipe 3 between the compressor
10 and the refrigerant flow switching device 11. The first pressure sensor 41 detects
a pressure of high temperature, high pressure refrigerant discharged from the compressor
10.
[0061] The second pressure sensor 42 is disposed in the refrigerant pipe 3 between the refrigerant
flow switching device 11 and the accumulator 13. The second pressure sensor 42 detects
a pressure of low pressure refrigerant to be sucked into the compressor 10.
[0062] The outdoor unit 1 includes, as temperature detecting units, a first temperature
sensor 43, a second temperature sensor 45, a third temperature sensor 48a, and a third
temperature sensor 48b. Each of the first temperature sensor 43, the second temperature
sensor 45, and the third temperature sensors 48a and 48b may be, for example, a thermistor.
[0063] The first temperature sensor 43 is disposed in the refrigerant pipe 3 between the
compressor 10 and the refrigerant flow switching device 11. The first temperature
sensor 43 measures a temperature of the refrigerant discharged from the compressor
10.
[0064] The second temperature sensor 45 is disposed in an air inlet of either the heat source
side heat exchanger 12a or the heat source side heat exchanger 12b. The second temperature
sensor 45 measures a temperature of ambient air around the outdoor unit 1.
[0065] The third temperature sensor 48a is disposed in the refrigerant pipe 3 between the
heat source side heat exchanger 12a and the refrigerant flow switching device 11.
The third temperature sensor 48a measures a temperature of the refrigerant flowing
into the heat source side heat exchanger 12a operating as an evaporator or a temperature
of the refrigerant flowing out of the heat source side heat exchanger 12a operating
as a condenser.
[0066] The third temperature sensor 48b is disposed in the refrigerant pipe 3 between the
heat source side heat exchanger 12b and the refrigerant flow switching device 11.
The third temperature sensor 48b measures a temperature of the refrigerant flowing
into the heat source side heat exchanger 12b operating as an evaporator or a temperature
of the refrigerant flowing out of the heat source side heat exchanger 12b operating
as a condenser.
[0067] The outdoor unit 1 further includes a controller 50. Information about the pressures
detected by the first pressure sensor 41 and the second pressure sensor 42 and information
about the temperatures detected by the first temperature sensor 43, the second temperature
sensor 45, and the third temperature sensors 48a and 48b are input to the controller
50.
[Indoor Unit 2]
[0068] The indoor unit 2 includes a load side heat exchanger 21 and the load side expansion
device 22 connected in series.
[0069] The load side heat exchanger 21 is connected to the outdoor unit 1 by the refrigerant
main pipes 4 such that the refrigerant flows into and out of the load side heat exchanger
21. The load side heat exchanger 21 exchanges heat between the refrigerant and air
supplied from an air-sending device (not illustrated), such as a fan. The load side
heat exchanger 21 produces heating air or cooling air to be supplied to an indoor
space. A heat medium for heat exchange with the refrigerant in the load side heat
exchanger 21 is not limited to the air. The heat medium may be, for example, water
or brine.
[0070] The load side expansion device 22 functions as a pressure reducing valve or an expansion
valve to depressurize the refrigerant such that the refrigerant is expanded. The load
side expansion device 22 is disposed upstream of the load side heat exchanger 21 in
the refrigerant flow direction in the cooling only operation mode. The load side expansion
device 22 includes a component having a variably controllable opening degree. The
load side expansion device 22 may be, for example, an electronic expansion valve.
[0071] The indoor unit 2 includes, as temperature detecting units, a fourth temperature
sensor 46, a fifth temperature sensor 47, and a sixth temperature sensor 44. Each
of the fourth temperature sensor 46, the fifth temperature sensor 47, and the sixth
temperature sensor 44 may be, for example, a thermistor.
[0072] The fourth temperature sensor 46 is disposed in the refrigerant pipe 3 between the
load side expansion device 22 and the load side heat exchanger 21. The fourth temperature
sensor 46 detects a temperature of the refrigerant flowing into the load side heat
exchanger 21 or a temperature of the refrigerant flowing out of the load side heat
exchanger 21.
[0073] The fifth temperature sensor 47 is disposed in the refrigerant pipe 3 between the
load side heat exchanger 21 and the refrigerant flow switching device 11 of the outdoor
unit 1. The fifth temperature sensor 47 detects a temperature of the refrigerant flowing
into the load side heat exchanger 21 or a temperature of the refrigerant flowing out
of the load side heat exchanger 21.
[0074] The sixth temperature sensor 44 is disposed in an air inlet of the load side heat
exchanger 21. The sixth temperature sensor 44 detects a temperature of ambient air
in the indoor space.
[0075] Information about the temperatures detected by the fourth temperature sensor 46,
the fifth temperature sensor 47, and the sixth temperature sensor 44 is input to the
controller 50 disposed in the outdoor unit 1.
[0076] In the air-conditioning apparatus 100 with the above-described configuration, the
compressor 10, the refrigerant flow switching device 11, the load side heat exchanger
21, the load side expansion device 22, and the heat source side heat exchangers 12a
and 12b connected in parallel are connected in sequence by the pipes to form a main
circuit through which the refrigerant is circulated and a bypass through which part
of the refrigerant discharged from the compressor 10 is allowed to flow to the heat
source side heat exchanger 12, serving as a defrosting target, that is, either the
heat source side heat exchanger 12a or the heat source side heat exchanger 12b.
[0077] Although the case where, as illustrated in Fig. 1, one indoor unit 2 is connected
to one outdoor unit 1 by the refrigerant main pipes 4 is illustrated as an exemplary
configuration in Embodiment 1, the present invention is not limited to this configuration.
The air-conditioning apparatus 100 may include a plurality of indoor units 2. The
indoor units 2 may be connected in parallel with one outdoor unit 1. In addition,
two or more outdoor units may be connected in parallel. Furthermore, the air-conditioning
apparatus 100 may include a refrigerant circuit that enables a cooling and heating
mixed operation, in which the cooling operation or the heating operation can be selected
in each indoor unit, by connecting three extension pipes in parallel or disposing
a switching valve in each indoor unit.
[0078] The air-conditioning apparatus 100 includes the controller 50, which includes a microcomputer.
The controller 50 controls, for example, driving frequency of the compressor 10, a
rotation speed (including ON/OFF) of each air-sending device, switching of the refrigerant
flow switching device 11, opening and closing of the first opening and closing devices
30a and 30b, opening and closing of the third opening and closing devices 31, and
the opening degree of the load side expansion device 22 on the basis of information
about detection results of the individual detecting units and an instruction from
a remote control, thus performing any of the operation modes, which will be described
later.
[0079] Although Fig. 1 illustrates the case where the controller 50 is installed in the
outdoor unit 1, another configuration may be used. For example, the controller 50
may be disposed in each unit or may be disposed in the indoor unit 2. If the controller
50 is disposed in each unit, the controllers 50 may be connected in a wired or wireless
manner to achieve communication and cooperative control.
[0080] The operation modes performed by the air-conditioning apparatus 100 will now be described.
[0081] The operation modes will be described in accordance with the flow of the refrigerant.
[Cooling Only Operation Mode]
[0082] Fig. 3 is a refrigerant circuit diagram illustrating the flow of the refrigerant
in the cooling only operation mode of the air-conditioning apparatus 100. The cooling
only operation mode performed by the air-conditioning apparatus 100 will now be described
with reference to Fig. 3. The cooling only operation mode will be described on the
assumption that, for example, a cooling load is generated in the load side heat exchanger
21 in Fig. 3. In Fig. 3, solid-line arrows indicate the refrigerant flow direction.
[0083] In the cooling only operation mode, the refrigerant flow switching device 11 is switched
to a state illustrated by solid lines in Fig. 2. Each of the first opening and closing
devices 30a and 30b and the second opening and closing device 35 is switched to a
closed state, thus stopping the flow of the refrigerant. Each of the third opening
and closing devices 31 a and 31 b and the flow control devices 32a and 32b is switched
to an open state, thus permitting the flow of the refrigerant.
[0084] When the compressor 10 is driven, low temperature, low pressure refrigerant is compressed
into high temperature, high pressure gas refrigerant and is then discharged. The high
temperature, high pressure gas refrigerant discharged from the compressor 10 flows
through the refrigerant flow switching device 11 and divides into two refrigerant
streams, which flow into the heat source side heat exchangers 12a and 12b. In the
heat source side heat exchangers 12a and 12b, the high temperature, high pressure
gas refrigerant streams that have flowed into the heat source side heat exchangers
12a and 12b transfer heat to outdoor air, so that the refrigerant turns into high
pressure liquid refrigerant. The high pressure liquid refrigerant streams flow out
of the heat source side heat exchangers 12a and 12b, pass through the flow control
devices 32a and 32b, and then merge together. The refrigerant flows out of the outdoor
unit 1.
[0085] The high pressure liquid refrigerant leaving the outdoor unit 1 passes through the
refrigerant main pipe 4, flows into the indoor unit 2, and is expanded by the load
side expansion device 22, so that the refrigerant turns into low temperature, low
pressure two-phase refrigerant. The two-phase refrigerant flows into the load side
heat exchanger 21 operating as an evaporator and removes heat from indoor air to cool
the indoor air, so that the refrigerant turns into low temperature, low pressure gas
refrigerant. The gas refrigerant flows out of the load side heat exchanger 21, passes
through the refrigerant main pipe 4, and again flows into the outdoor unit 1. The
refrigerant that has flowed into the outdoor unit 1 passes through the refrigerant
flow switching device 11 and the accumulator 13 and is again sucked into the compressor
10.
[0086] The controller 50 controls the opening degree of the load side expansion device 22
to provide a constant superheat (degree of superheat). The degree of superheat is
obtained as the difference between a temperature detected by the fourth temperature
sensor 46 and a temperature detected by the fifth temperature sensor 47.
[Heating Only Operation Mode]
[0087] Fig. 4 is a refrigerant circuit diagram illustrating the flow of the refrigerant
in the heating only operation mode of the air-conditioning apparatus 100. The heating
only operation mode performed by the air-conditioning apparatus 100 will now be described
with reference to Fig. 4. The heating only operation mode will be described on the
assumption that a heating load is generated in the load side heat exchanger 21 in
Fig. 4. In Fig. 4, solid-line arrows indicate the refrigerant flow direction.
[0088] In the heating only operation mode, the refrigerant flow switching device 11 is switched
to a state indicated by solid lines in Fig. 3. Each of the first opening and closing
devices 30a and 30b and the second opening and closing device 35 is switched to the
closed state, thus stopping the flow of the refrigerant. Each of the third opening
and closing devices 31 a and 31 b and the flow control devices 32a and 32b is switched
to the open state, thus permitting the flow of the refrigerant.
[0089] When the compressor 10 is driven, low temperature, low pressure refrigerant is compressed
into high temperature, high pressure gas refrigerant and is then discharged. The high
temperature, high pressure gas refrigerant discharged from the compressor 10 passes
through the refrigerant flow switching device 11 and flows out of the outdoor unit
1.
[0090] The high temperature, high pressure gas refrigerant leaving the outdoor unit 1 passes
through the refrigerant main pipe 4 and flows into the indoor unit 2. The refrigerant
transfers heat to indoor air in the load side heat exchanger 21 to heat the indoor
air, so that the refrigerant turns into liquid refrigerant. The liquid refrigerant
flows out of the load side heat exchanger 21 and is then expanded by the load side
expansion device 22, so that the refrigerant turns into low temperature, intermediate
pressure two-phase refrigerant or liquid refrigerant. The refrigerant passes through
the refrigerant main pipe 4 and again flows into the outdoor unit 1.
[0091] The low temperature, intermediate pressure two-phase refrigerant or liquid refrigerant
that has flowed into the outdoor unit 1 passes through the flow control devices 32a
and 32b and flows into the heat source side heat exchangers 12a and 12b. The refrigerant
that has flowed into the heat source side heat exchangers 12a and 12b removes heat
from outdoor air, so that the refrigerant turns into low temperature, low pressure
gas refrigerant. The refrigerant passes through the refrigerant flow switching device
11 and the accumulator 13 and is again sucked into the compressor 10.
[0092] The controller 50 controls the opening degree of the load side expansion device 22
to provide a constant subcooling (degree of subcooling). The degree of subcooling
is obtained as the difference between a saturation temperature converted from a pressure
detected by the first pressure sensor 41 and a temperature detected by the fourth
temperature sensor 46.
[Defrosting Operation Mode]
[0093] The defrosting operation mode is performed when a detection result of each of the
third temperature sensors 48a and 48b arranged on outlet sides of the heat source
side heat exchangers 12a and 12b is less than or equal to a predetermined value. Specifically,
when a detection result of each of the third temperature sensors 48a and 48b is less
than or equal to the predetermined value (for example, less than or equal to approximately
-10 degrees C) in the heating only operation mode, the controller 50 determines that
the fins of the heat source side heat exchangers 12a and 12b have a predetermined
amount of frost, and then performs the defrosting operation mode.
[0094] Another method may be used for frost formation determination. For example, when a
saturation temperature converted from a suction pressure of the compressor 10 significantly
falls as compared with a preset outdoor air temperature, or alternatively, when the
difference between an outdoor air temperature and an evaporating temperature is greater
than or equal to a preset value for a certain period of time, it may be determined
that frost is formed.
[0095] In the defrosting operation mode of the air-conditioning apparatus 100, the heat
source side heat exchanger 12b at the lower level is defrosted and, after that, the
heat source side heat exchanger 12a at the upper level is defrosted. In addition,
the heat source side heat exchanger 12 that is not a defrosting target of the heat
source side heat exchangers 12a and 12b is allowed to operate as an evaporator, and
the load side heat exchanger 21 of the indoor unit 2 is allowed to operate as a condenser,
thus continuing the heating operation.
(Defrosting of Heat Source Side Heat Exchanger 12b)
[0096] Fig. 5 is a refrigerant circuit diagram illustrating the flow of the refrigerant
in the defrosting operation mode of the air-conditioning apparatus 100 in which the
heat source side heat exchanger 12b is defrosted. In Fig. 4, solid-line arrows indicate
the refrigerant flow direction.
[0097] In the defrosting operation mode, the refrigerant flow switching device 11 is maintained
in the state indicated by solid lines in Fig. 5.
[0098] In the defrosting operation mode in which the heat source side heat exchanger 12b
is a defrosting target, the first opening and closing devices 30, the second opening
and closing device 35, the third opening and closing devices 31, and the flow control
devices 32 have the following states.
[0099] The controller 50 controls the states of those devices.
[0100] The first opening and closing device 30b is switched to the open state, thus permitting
the flow of the refrigerant.
[0101] The third opening and closing device 31 b is switched to the closed state, thus stopping
the flow of the refrigerant.
[0102] The first opening and closing device 30a is maintained in the closed state to stop
the flow of the refrigerant.
[0103] The third opening and closing device 31 a is maintained in the open state to permit
the flow of the refrigerant.
[0104] The flow control device 32a is set to a fully open state to permit the flow of the
refrigerant.
[0105] The opening degree of the flow control device 32b is controlled so that a preset
pressure (for example, approximately 0.8 MPa for R410A refrigerant) remains constant.
At the preset pressure, a saturation temperature converted from a saturation pressure
of two-phase refrigerant calculated based on a detection result of the third temperature
sensor 48b is greater than 0 degrees C.
[0106] When either one of a condition that an outdoor air temperature detected by the second
temperature sensor 45 is less than or equal to a second predetermined value (for example,
less than or equal to 0 degrees C) and a condition that a pressure at a suction inlet
of the compressor 10 detected by the second pressure sensor 42 is less than or equal
to a first predetermined value (for example, less than or equal to approximately 0.3
MPa for R410A refrigerant) is satisfied, or alternatively, when both the conditions
are satisfied, the second opening and closing device 35 is maintained in the open
state to permit the flow of the refrigerant.
[0107] The second temperature sensor 45 and the second pressure sensor 42 correspond to
a defrosting mode refrigerant decrease detecting unit in the present invention.
[0108] If either the condition associated with the second temperature sensor 45 or the condition
associated with the second pressure sensor 42 is satisfied in the defrosting operation
mode, a shortage of refrigerant circulated through the main circuit may be determined.
If either one of the sensors breaks down, functions of the defrosting mode refrigerant
decrease detecting unit can be reliably achieved by making the above determination
based on both the conditions.
[0109] Fig. 6 is a graph illustrating a change in enthalpy difference, available for defrosting,
caused by a change in saturation temperature in the heat source side heat exchanger
12 that serves as a defrosting-target heat exchanger in the air-conditioning apparatus
100. In Fig. 6, the horizontal axis represents the saturation temperature in the heat
source side heat exchanger 12 that serves as a defrosting-target heat exchanger. The
left vertical axis represents an average refrigerant density (kg/m
3) in the heat source side heat exchanger 12 that serves as a defrosting-target heat
exchanger. The right vertical axis represents the difference in enthalpy (kJ/kg) between
an inlet and an outlet of the heat source side heat exchanger 12 that serves as a
defrosting-target heat exchanger. In Fig. 6, a solid line represents an average refrigerant
density necessary for the saturation temperature in the heat source side heat exchanger
12 that serves as a defrosting-target heat exchanger. In Fig. 6, a dashed line represents
the difference in enthalpy, or enthalpy difference that is caused by a change in saturation
temperature in the heat source side heat exchanger 12 that serves as a defrosting-target
heat exchanger, and that is available for defrosting.
[0110] In Fig. 6, as indicated by the dashed line, it can be seen that the enthalpy difference
available for defrosting increases at saturation temperatures ranging from above 0
degrees C and to approximately 1 degree C in the heat source side heat exchanger 12
that serves as a defrosting-target heat exchanger, latent heat of two-phase part of
the refrigerant can be used more effectively, and the necessary average refrigerant
density in the heat source side heat exchanger 12 at that time is approximately 600
(kg/m
3) or greater. In other words, when the defrosting operation is performed such that
latent heat of two-phase part of the refrigerant is effectively used, the refrigerant
having an average refrigerant density of approximately 600 (kg/m
3) or greater has to be accumulated in the heat source side heat exchanger 12.
[0111] When the refrigerant having an average refrigerant density of approximately 600 (kg/m
3) or greater is supplied to the heat source side heat exchanger 12 in the defrosting
operation mode, the refrigerant in the load side heat exchanger 21 used as a condenser
for the heating operation moves into the heat source side heat exchanger 12. Consequently,
the amount of refrigerant in the load side heat exchanger 21 decreases, leading to
a decrease in pressure (high pressure) in the load side heat exchanger 21. In addition,
a decreases in the amount of gas refrigerant in the whole cycle results in a decrease
in low pressure. While the load side heat exchanger 21 is used as a condenser, air
supplied to the indoor space has to be at such a temperature that cold air does not
cause user discomfort.
[0112] The indoor air temperature and the saturation temperature converted from the pressure
in the load side heat exchanger 21 have to have a temperature difference of a predetermined
value or greater (for example, 10 degrees C or greater) therebetween. For example,
according to Japanese Industrial Standards JIS B 8616, serving as the standards for
performance evaluation of package air conditioners, when a set temperature of an indoor
environment in the heating operation is 20 degrees C, the saturation temperature converted
from the pressure in the load side heat exchanger 21 has to be at or above 30 degrees
C. In the defrosting operation mode, therefore, a pressure on a low-pressure side
under circumstances where the saturation temperature converted from the pressure in
the load side heat exchanger 21 can be at or above 30 degrees C is approximately 0.3
MPa, which is the first predetermined value.
[0113] Furthermore, in the defrosting operation under conditions where the outdoor air temperature
is at or below approximately 0 degrees C, which is the second predetermined value,
the operation is in a state where the pressure on the low-pressure side is below approximately
0.3 MPa. To accumulate the refrigerant in the heat source side heat exchanger 12 while
a decrease in pressure on the low-pressure side is eliminated or reduced, the refrigerant
that is not used for the heating operation and the defrosting operation has to be
supplied to the heat source side heat exchanger 12.
[0114] The flow of the refrigerant in the defrosting operation mode will now be described
in detail.
[0115] When the compressor 10 is driven, low temperature, low pressure refrigerant is compressed
into high temperature, high pressure gas refrigerant and is then discharged.
[0116] Part of the high temperature, high pressure gas refrigerant discharged from the compressor
10 flows through the first gas bypass pipe 5 and is then depressurized to a pressure
equivalent to greater than 0 degrees C in terms of saturation temperature by the first
opening and closing device 30b, so that the refrigerant turns into intermediate pressure,
high temperature gas refrigerant. The refrigerant flows into the heat source side
heat exchanger 12b. The intermediate pressure, high temperature gas refrigerant that
has flowed into the heat source side heat exchanger 12b turns into intermediate pressure,
low quality two-phase refrigerant or intermediate pressure liquid refrigerant while
melting frost on the heat source side heat exchanger 12b. The refrigerant then passes
through the flow control device 32b. The refrigerant leaving the flow control device
32b merges with intermediate pressure, low temperature, low quality two-phase refrigerant
or liquid refrigerant that has flowed into the outdoor unit 1 from the indoor unit
2 at a point upstream of the flow control device 32a.
[0117] The other part of the high temperature, high pressure gas refrigerant discharged
from the compressor 10 passes through the refrigerant flow switching device 11 and
flows out of the outdoor unit 1. The high temperature, high pressure gas refrigerant
leaving the outdoor unit 1 passes through the refrigerant main pipe 4, flows into
the indoor unit 2, and transfers heat to indoor air in the load side heat exchanger
21, so that the refrigerant turns into liquid refrigerant while heating the indoor
air. The liquid refrigerant flows out of the load side heat exchanger 21 and is expanded
by the load side expansion device 22, so that the refrigerant turns into low temperature,
intermediate pressure two-phase refrigerant or liquid refrigerant. The refrigerant
passes through the refrigerant main pipe 4 and again flows into the outdoor unit 1.
[0118] The low temperature, intermediate pressure two-phase refrigerant or liquid refrigerant
that has flowed into the outdoor unit 1 merges with the refrigerant leaving the flow
control device 32b at the point upstream of the flow control device 32a. The refrigerant
then flows into the heat source side heat exchanger 12a. The refrigerant that has
flowed into the heat source side heat exchanger 12a removes heat from outdoor air,
so that the refrigerant turns into low temperature, low pressure gas refrigerant.
The gas refrigerant flows out of the heat source side heat exchanger 12a, passes through
the refrigerant flow switching device 11 and the accumulator 13, and is again sucked
into the compressor 10.
[0119] The controller 50 controls the opening degree of the flow control device 32b so
that the preset pressure (for example, approximately 0.8 MPa for R410A refrigerant),
at which a saturation temperature converted from a saturation pressure of two-phase
refrigerant calculated based on a detection result of the third temperature sensor
48b is greater than 0 degrees C, remains constant. In other words, the controller
50 controls the opening degree of the flow control device 32b so that the saturation
pressure of the two-phase refrigerant calculated based on the detection result of
the third temperature sensor 48b is greater than a pressure (for example, approximately
0.8 MPa for R410A refrigerant) equivalent to greater than 0 degrees C in terms of
saturation temperature.
[0120] As regards the completion of defrosting of the heat source side heat exchanger 12b,
the completion of defrosting may be determined, for example, after a lapse of a predetermined
period of time, or alternatively, when a temperature detected by the third temperature
sensor 48b is greater than or equal to a predetermined value (e.g., 5 degrees C).
Assuming that the heat source side heat exchanger 12b is fully covered with frost,
the predetermined period of time may be set longer than or equal to the time required
to completely defrost the heat source side heat exchanger 12b by allowing part of
high temperature, high pressure refrigerant to flow into the heat source side heat
exchanger 12b.
[0121] While the second opening and closing device 35 is maintained in the open state by
the controller 50, a branch flow of the high temperature, high pressure gas refrigerant
from a discharge side of the compressor 10 flows through the second gas bypass pipe
7, passes through the second opening and closing device 35, and merges with the low
temperature, low pressure gas refrigerant leaving the heat source side heat exchanger
12a. The refrigerant then flows into the accumulator 13. The refrigerant that has
flowed into the accumulator 13 causes liquid refrigerant accumulating in the accumulator
13 to evaporate. This evaporation increases the amount of gas refrigerant flowing
out of the accumulator 13, thus achieving an increase in density of low pressure gas
refrigerant. Consequently, the pressure of the low pressure gas refrigerant increases,
so that the pressure of the low pressure gas refrigerant can be maintained at a value
(for example, approximately 0.3 MPa for R410A refrigerant) greater than the first
predetermined value.
[0122] If the pressure of the low pressure gas refrigerant is less than or equal to the
first predetermined value (for example, less than or equal to approximately 0.3 MPa
for R410A refrigerant), the density of the low pressure gas refrigerant would decrease
and the amount of refrigerant discharged from the compressor 10 would decrease, leading
to a decrease in heating capacity and defrosting capacity. In the air-conditioning
apparatus 100, however, the second gas bypass pipe 7 is used to increase the amount
of gas refrigerant flowing out of the accumulator 13, so that the pressure of the
low pressure gas refrigerant can be increased. This can eliminate or reduce a decrease
in the amount of refrigerant discharged from the compressor 10, thus eliminating or
reducing a decrease in heating capacity and defrosting capacity.
[0123] In the defrosting operation mode, if the outdoor air temperature detected by the
second temperature sensor 45 is at or below the second predetermined value (e.g.,
at or below 0 degrees C), the pressure of the refrigerant in the heat source side
heat exchanger 12a used as an evaporator would decrease due to a decrease in outdoor
air temperature and frost on the heat source side heat exchanger 12a. The temperature
of the refrigerant in the heat source side heat exchanger 12a may reach approximately
-27 degrees C in terms of saturation temperature (approximately 0.3 MPa as a saturation
pressure) and the pressure of low pressure gas refrigerant at the suction inlet of
the compressor 10 may reach the first predetermined value (e.g., approximately 0.3
MPa for R410A refrigerant). If the outdoor air temperature is at or below the second
predetermined value (e.g., at or below 0 degrees C), therefore, the second opening
and closing device 35 is maintained in the open state by the controller 50, so that
a decrease in the amount of refrigerant discharged from the compressor 10 can be eliminated
or reduced. Thus, a decrease in heating capacity and defrosting capacity can be eliminated
or reduced.
[0124] In addition, since the refrigerant accumulating in the accumulator 13 is supplied
to the suction inlet of the compressor 10, gas refrigerant having a density higher
than that before the second opening and closing device 35 is opened can be sucked
into the compressor 10. This can increase the circulation amount of refrigerant discharged
from the compressor 10.
[0125] As described above, increasing the circulation amount of refrigerant discharged from
the compressor 10 enables much refrigerant to be supplied to the heat source side
heat exchanger 12b while a sufficient amount of gas refrigerant is supplied from the
second gas bypass pipe 7 to the accumulator 13. Consequently, the saturation pressure
of two-phase refrigerant in the heat source side heat exchanger 12b can be increased
to a value equivalent to greater than 0 degrees C in terms of saturation temperature
more rapidly than in a case where high temperature, high pressure gas refrigerant
is not allowed to flow into the accumulator 13 through the second gas bypass pipe
7 and the second opening and closing device 35. Thus, the air-conditioning apparatus
100 can rapidly increase the temperature difference between the frost and the refrigerant
necessary for defrosting, thus shortening the time required for defrosting.
[0126] To defrost the heat source side heat exchanger 12a after the heat source side heat
exchanger 12b is completely defrosted, an operation is performed in a manner obtained
by interchanging the letters "a" and "b" added to the reference numerals in the above
description about the defrosting operation for the heat source side heat exchanger
12b. Specifically, the open and closed states of the first opening and closing devices
30a and 30b and the third opening and closing devices 31 a and 31 b are the opposite
of the above-described states and the refrigerant flow direction in each of the heat
source side heat exchangers 12a and 12b is reversed. In addition, the flow control
device 32b is fully opened and the opening degree of the flow control device 32a is
controlled.
[0127] As described above, the saturation temperature of the refrigerant in the heat source
side heat exchanger 12 functioning as a condenser in the defrosting operation mode
for the heat source side heat exchanger 12 is set at an intermediate pressure (for
example, at or above approximately 0.8 MPa for R410A refrigerant) equivalent to a
temperature greater than the temperature of frost, that is, 0 degrees C. In the air-conditioning
apparatus 100, therefore, a two-phase region (latent heat) of the refrigerant can
be used, so that efficient defrosting can be achieved with a small circulation amount
of refrigerant, a decrease in indoor heating capacity can be eliminated or reduced,
and the indoor space can be kept comfortable.
[0128] The air-conditioning apparatus 100 can defrost the heat source side heat exchangers
12a and 12b while continuing the heating operation by performing the above-described
defrosting operation mode. The heat source side heat exchanger 12b at the lower level
in the housing of the outdoor unit 1 is defrosted and, after that, the heat source
side heat exchanger 12a at the upper level is defrosted. This can eliminate a likelihood
that water produced by defrosting the heat source side heat exchanger 12a may freeze
in the lower heat source side heat exchanger 12b to be defrosted. Efficient defrosting
can be achieved.
[0129] Fig. 7 illustrates a change in heating capacity relative to the saturation temperature
in the heat source side heat exchanger 12 that serves as a defrosting-target heat
exchanger. In Fig. 7, the refrigerant excessively accumulates in the heat source side
heat exchanger 12 at saturation temperatures greater than 10 degrees C. In such a
state, there is no liquid refrigerant accumulating in the accumulator 13, thus causing
a shortage of refrigerant in the whole refrigeration cycle. This leads to a decrease
in heating capacity. To solve such a shortage of refrigerant caused by excessive accumulation
of the refrigerant in the heat source side heat exchanger 12, the saturation temperature
in the heat source side heat exchanger 12 may be in the range from above 0 to 10 degrees
C.
[0130] Fig. 8 is a flowchart of control for operating the second opening and closing device
35 in the defrosting operation mode of the air-conditioning apparatus 100. An operation
of the controller 50 operating the second opening and closing device 35 in the defrosting
operation mode will now be described with reference to Fig. 8.
(CT1)
[0131] When a detection result of each of the third temperature sensors 48a and 48b is less
than or equal to a predetermined value (for example, less than or equal to approximately
-10 degrees C) in the heating operation mode, the controller 50 determines that the
fins of the heat source side heat exchangers 12a and 12b are covered with a predetermined
amount of frost, executes the defrosting operation mode, and proceeds to CT2.
(CT2)
[0132] The controller 50 determines whether an outdoor air temperature detected by the second
temperature sensor 45 is greater than or equal to a predetermined value (e.g., 0 degrees
C). This predetermined value corresponds to the second predetermined value.
[0133] If the value detected by the second temperature sensor 45 is greater than or equal
to the predetermined value, the controller 50 proceeds to CT3.
[0134] If the value detected by the second temperature sensor 45 is not greater than or
equal to the predetermined value, the controller 50 proceeds to CT4.
(CT3)
[0135] The controller 50 determines whether a pressure substantially equal to the refrigerant
pressure at the suction inlet of the compressor 10 detected by the second pressure
sensor 42 is greater than or equal to a predetermined value (for example, greater
than or equal to 0.3 MPa for R410A refrigerant). This predetermined value corresponds
to the first predetermined value.
[0136] If the value detected by the second pressure sensor 42 is greater than or equal to
the predetermined value, the controller 50 proceeds to CT5.
[0137] If the value detected by the second pressure sensor 42 is not greater than or equal
to the predetermined value, the controller 50 proceeds to CT4.
(CT4)
[0138] The controller 50 opens the second opening and closing device 35 to cause a branch
flow of high temperature, high pressure gas refrigerant discharged from the compressor
10 to flow through the second gas bypass pipe 7 and the second opening and closing
device 35 into the accumulator 13. Consequently, liquid refrigerant accumulating in
the accumulator 13 is evaporated to increase the amount of gas refrigerant flowing
out of the accumulator 13, thus achieving an increase in pressure of low pressure
gas refrigerant.
[0139] After opening the second opening and closing device 35, the controller 50 proceeds
to CT6.
(CT5)
[0140] The controller 50 closes the second opening and closing device 35 to close the passage
of the branch flow of the high temperature, high pressure gas refrigerant from the
discharge side of the compressor 10 to the accumulator 13 through the second gas bypass
pipe 7 and the second opening and closing device 35.
[0141] After closing the second opening and closing device 35, the controller 50 proceeds
to CT6.
(CT6)
[0142] The controller 50 determines whether the defrosting operation mode is completed.
[0143] If the defrosting operation mode is not completed, the controller 50 proceeds to
CT2.
[0144] If the defrosting operation mode is completed, the controller 50 proceeds to CT7.
(CT7)
[0145] If the defrosting operation mode is completed, the controller 50 closes the second
opening and closing device 35 to close the passage of the branch flow of the high
temperature, high pressure gas refrigerant from the discharge side of the compressor
10 to the accumulator 13 through the second gas bypass pipe 7 and the second opening
and closing device 35.
[0146] After closing the second opening and closing device 35, the controller 50 shifts
to the heating only operation mode.
[0147] Although the pressure substantially equal to the refrigerant pressure at the suction
inlet of the compressor 10 detected by the second pressure sensor 42 is set at approximately
0.3 MPa for R410A refrigerant in CT3 in Fig. 8, another value may be used. Specifically,
the first predetermined value may be set to a value less than 0.3 MPa, as long as
the difference between an indoor air temperature and a saturation temperature converted
from a pressure in the load side heat exchanger 21 can be provided to the extent that
cold air caused by an operation state does not cause user discomfort, that is, the
temperature difference can be greater than or equal to a predetermined value (for
example, greater than or equal to 10 degrees C). As regards the second pressure sensor
42, a temperature sensor, such as a thermistor, may be used instead of the pressure
sensor. The controller 50 may calculate a saturation pressure based on a value detected
by the temperature sensor and the saturation pressure may be used.
[0148] Although the second opening and closing device 35 is opened in accordance with the
detection result of the defrosting mode refrigerant decrease detecting unit in the
above-described case, the second opening and closing device 35 may be opened at the
time when the opening and closing devices and the flow control devices are switched
between the states upon start of the defrosting operation mode, because a refrigerant
shortage in the refrigerant circuit is expected at this switching time. Consequently,
the refrigerant can be more rapidly supplied to the defrosting-target heat source
side heat exchanger 12, thus shortening the time required for defrosting.
[0149] In the above-described case, when a pressure substantially equal to the refrigerant
pressure at the suction inlet of the compressor 10 detected by the second pressure
sensor 42 is greater than or equal to the first predetermined value (for example,
greater than or equal to 0.3 MPa for R410A refrigerant), the second opening and closing
device 35 is closed. In addition, for example, an increase in refrigerant pressure
at the suction inlet of the compressor 10 in the defrosting operation mode may be
estimated in advance based on examinations and the second opening and closing device
35 may be closed after a lapse of a predetermined period of time. This can prevent
the refrigerant accumulating in the accumulator 13 from being excessively supplied
to the refrigerant circuit if the second pressure sensor 42 breaks down. In other
words, the branch flow of the high temperature, high pressure gas refrigerant from
the discharge side of the compressor 10 can be prevented from being wastefully introduced
into the bypass pipe, thus eliminating or reducing a decrease in heating capacity.
[0150] A duration during which the second opening and closing device 35 is kept opened may
be changed in accordance with an outdoor air temperature. At high outdoor air temperatures,
when the heat source side heat exchanger 12 used as an evaporator is allowed to achieve
a heat exchange amount greater than or equal to that at low outdoor air temperatures
on the assumption that the difference in temperature between the outdoor air and the
refrigerant in the heat source side heat exchanger 12 at high outdoor air temperatures
is substantially equivalent to that at low outdoor air temperatures, the refrigerant
pressure in the heat source side heat exchanger 12 rises and the refrigerant pressure
at the suction inlet of the compressor 10 also rises. Consequently, a large amount
of refrigerant is circulated through the refrigerant circuit. If a small amount of
the refrigerant accumulating in the accumulator 13 is supplied to the refrigerant
circuit by opening the second opening and closing device 35, the defrosting operation
and the heating operation can be adequately performed. At high outdoor air temperatures,
therefore, a short duration during which the second opening and closing device 35
is opened can be set.
[0151] On the other hand, at low outdoor air temperatures, the refrigerant pressure in the
heat source side heat exchanger 12 falls and the refrigerant pressure at the suction
inlet of the compressor 10 also falls. Consequently, a small amount of refrigerant
is circulated through the refrigerant circuit. A large amount of the refrigerant accumulating
in the accumulator 13 has to be supplied to the refrigerant circuit. A long duration
during which the second opening and closing device 35 is opened has to be set.
[0152] In other words, setting the duration during which the second opening and closing
device 35 is opened in accordance with a change in outdoor air temperature prevents
the branch flow of the high temperature, high pressure gas refrigerant from the discharge
side of the compressor 10 from being wastefully introduced into the bypass pipe, particularly,
at high outdoor air temperatures, thus eliminating or reducing a decrease in heating
capacity.
[0153] Fig. 9 is a graph illustrating a change in saturation temperature converted from
a pressure in the load side heat exchanger 21 caused by changing the flow rate of
high temperature, high pressure gas refrigerant flowing into the accumulator 13 in
the defrosting mode of the air-conditioning apparatus 100. Fig. 9 illustrates the
change in saturation temperature converted from the pressure in the load side heat
exchanger 21 caused by changing the flow rate of high temperature, high pressure gas
refrigerant flowing into the accumulator 13 in the defrosting operation mode at an
outdoor air temperature of approximately 0 degrees C and an indoor air temperature
of approximately 20 degrees C. In Fig. 9, the horizontal axis represents a value (hereinafter,
"gas refrigerant flow rate ratio") obtained by dividing the flow rate of high temperature,
high pressure gas refrigerant flowing from the pipe disposed at the discharge outlet
of the compressor 10 through the second gas bypass pipe 7 into the accumulator 13
by the flow rate of the whole of high temperature, high pressure gas refrigerant discharged
from the compressor 10, and the vertical axis represents the saturation temperature
converted from the pressure in the load side heat exchanger 21.
[0154] In Fig. 9, it can be seen that the flow rate of the high temperature, high pressure
gas refrigerant flowing into the accumulator 13 should be increased (shifted to the
right of the horizontal axis in Fig. 9) to more rapidly supply the refrigerant having
an average density of approximately 600 (kg/m
3) or greater from the accumulator 13 to the defrosting-target heat source side heat
exchanger 12. Furthermore, in Fig. 9, it can be seen that the saturation temperature
converted from the pressure in the load side heat exchanger 21 accordingly decreases
(shifts to the bottom of the vertical axis in Fig. 9). To maintain the saturation
temperature converted from the pressure in the load side heat exchanger 21 at or above
30 degrees C so that the difference between the saturation temperature and an indoor
air temperature of approximately 20 degrees C is greater than or equal to 10 degrees
C, the gas refrigerant flow rate ratio has to be set below 0.65. As regards the second
opening and closing device 35, a valve having a size that satisfies the condition
where the gas refrigerant flow rate ratio is less than 0.65 may be used.
(Modified Manner of Gas Supply to Accumulator 13)
[0155] Fig. 10 is a schematic circuit diagram illustrating another example of the circuit
configuration of the air-conditioning apparatus 100. As illustrated in Fig. 10, the
second end of the second gas bypass pipe 7 may be connected to the accumulator 13.
Such a configuration enables the branch flow of the high temperature, high pressure
gas refrigerant discharged from the compressor 10 to directly flow into the accumulator
13 through the second gas bypass pipe 7 and the second opening and closing device
35.
[0156] In the configuration in which the second end of the second gas bypass pipe 7 is connected
to the refrigerant pipe 3 between the refrigerant flow switching device 11 and the
accumulator 13, the branch flow of the high temperature, high pressure gas refrigerant
from the discharge side of the compressor 10 transfers heat to low temperature, low
pressure gas or two-phase refrigerant flowing from the heat source side heat exchanger
12 functioning as an evaporator, so that heat energy decreases. In addition, when
flowing into the accumulator 13, the refrigerant exchanges heat with only upper part
of liquid refrigerant accumulating in the accumulator 13.
[0157] The circuit configuration as illustrated in Fig. 10 enables the gas refrigerant flowing
into the accumulator 13 to efficiently exchange heat with the liquid refrigerant accumulating
in the accumulator 13. Consequently, the refrigerant accumulating in the accumulator
13 can be more rapidly supplied to the defrosting-target heat source side heat exchanger
12 than that in the configuration in which the branch flow of the high temperature,
high pressure gas refrigerant from the discharge side of the compressor 10 flows into
the pipe at an inlet of the accumulator 13, thus achieving defrosting more rapidly.
A decrease in indoor heating capacity can be further eliminated or reduced and the
indoor space can be kept comfortable.
Embodiment 2
[0158] Fig. 11 is a schematic circuit diagram illustrating an example of the circuit configuration
of an air-conditioning apparatus 200 according to Embodiment 2 of the present invention.
[0159] The configuration of the air-conditioning apparatus 200 will now be described in
detail with reference to Fig. 11.
[0160] The following description of Embodiment 2 will be focused on differences from Embodiment
1. The same components as those in Embodiment 1 are designated by the same reference
numerals and an explanation of these components is omitted in the description of Embodiment
2. In Fig. 11, solid-line arrows indicate a refrigerant flow direction in a state
where the heat source side heat exchanger 12b is defrosted.
[0161] As illustrated in Fig. 11, the air-conditioning apparatus 200 further includes a
fourth opening and closing device 33a for closing the refrigerant passage to the heat
source side heat exchanger 12a. The fourth opening and closing device 33a is disposed
in the pipe extending from the heat source side heat exchanger 12a toward the load
side expansion device 22. The air-conditioning apparatus 200 further includes a fourth
opening and closing device 33b for closing the refrigerant passage to the heat source
side heat exchanger 12b. The fourth opening and closing device 33b is similarly disposed
in the pipe extending from the heat source side heat exchanger 12b toward the load
side expansion device 22.
[0162] The air-conditioning apparatus 200 further includes a refrigerant bypass pipe 6.
The refrigerant bypass pipe 6 is connected at a first end to each of the refrigerant
pipe 3 between the heat source side heat exchangers 12a and the third opening and
closing device 31 a and the refrigerant pipe 3 between the heat source side heat exchanger
12b and the third opening and closing device 31 b. The refrigerant bypass pipe 6 is
connected at a second end to the passage between the load side expansion device 22
and the fourth opening and closing devices 33a and 33b. The refrigerant bypass pipe
6 allows the refrigerant in the heat source side heat exchanger 12 functioning as
a condenser in the defrosting operation mode to flow into the refrigerant pipe 3.
[0163] In addition, a fifth opening and closing device 34a and a fifth opening and closing
device 34b for switching between refrigerant passages of the refrigerant bypass pipe
6 are arranged in the first end of the refrigerant bypass pipe 6 connected to the
pipes between the heat source side heat exchangers 12 and the third opening and closing
devices 31. At the second end of the refrigerant bypass pipe 6, the one flow control
device 32b (or flow control device 32a), serving as an expansion device having a variable
opening degree (opening area), for controlling a refrigerant pressure in the heat
source side heat exchanger 12 is disposed.
[0164] The fourth opening and closing device 33a closes the refrigerant passage in the defrosting
operation mode in which the heat source side heat exchanger 12a operates as a condenser
so that low temperature two-phase refrigerant flowing from the indoor unit 2 through
the refrigerant main pipe 4 into the outdoor unit 1 does not flow into the heat source
side heat exchanger 12a.
[0165] The fourth opening and closing device 33b closes the refrigerant passage in the defrosting
operation mode in which the heat source side heat exchanger 12b operates as a condenser
so that low temperature two-phase refrigerant flowing from the indoor unit 2 through
the refrigerant main pipe 4 into the outdoor unit 1 does not flow into the heat source
side heat exchanger 12b.
[0166] Each of the fourth opening and closing devices 33a and 33b may be a component capable
of opening and closing the refrigerant passage, for example, a two-way valve, a solenoid
valve, or an electronic expansion valve.
[0167] In the following description, the fourth opening and closing devices 33a and 33b
may be collectively referred to as fourth opening and closing devices 33.
[0168] The fifth opening and closing device 34a allows the refrigerant flowing from the
heat source side heat exchanger 12a operating as a condenser in the defrosting operation
mode to flow into the refrigerant pipe 3 through the flow control device 32b (or the
flow control device 32a).
[0169] The fifth opening and closing device 34b allows the refrigerant flowing from the
heat source side heat exchanger 12a to flow into the refrigerant pipe 3 through the
flow control device 32b (or the flow control device 32a) while the heat source side
heat exchanger 12b is operating as a condenser in the defrosting operation mode.
[0170] Each of the fifth opening and closing devices 34a and 34b may be a component capable
of opening and closing the refrigerant passage, for example, a two-way valve, a solenoid
valve, or an electronic expansion valve.
[0171] In the following description, the fifth opening and closing devices 34a and 34b may
be collectively referred to as fifth opening and closing devices 34.
[0172] One of the two pipes constituting the second end of the first gas bypass pipe 5 is
connected to the refrigerant pipe 3 between the heat source side heat exchanger 12a
and the fourth opening and closing device 33a, and the other one of them is connected
to the refrigerant pipe 3 between the heat source side heat exchanger 12b and the
fourth opening and closing device 33b.
[0173] The third temperature sensor 48a is disposed in the refrigerant pipe 3 between the
heat source side heat exchanger 12a and the third opening and closing device 31 a.
The third temperature sensor 48b is disposed in the refrigerant pipe 3 between the
heat source side heat exchanger 12b and the third opening and closing device 31 b.
[0174] The third temperature sensor 48a measures a temperature of the refrigerant flowing
from the heat source side heat exchanger 12a operating as an evaporator or the refrigerant
flowing from the heat source side heat exchanger 12a operating as a condenser. The
third temperature sensor 48b measures a temperature of the refrigerant flowing from
the heat source side heat exchanger 12b operating as an evaporator or the refrigerant
flowing from the heat source side heat exchanger 12b operating as a condenser.
[0175] Since the rest of the configuration is the same as that of the air-conditioning apparatus
100 according to Embodiment 1, an explanation of the rest of the configuration is
omitted. As regards Figs. 6 to 9 in the description of Embodiment 1, the same applies
to the air-conditioning apparatus 200.
[0176] In the cooling only operation mode and the heating only operation mode of the air-conditioning
apparatus 200, the fourth opening and closing devices 33a and 33b are opened and the
fifth opening and closing devices 34a and 34b are closed. Since the operations of
the other opening and closing devices and the refrigerant flows are the same as those
in the air-conditioning apparatus 100 according to Embodiment 1, an explanation of
the operations and the refrigerant flows is omitted.
[Defrosting Operation Mode]
[0177] In the defrosting operation mode of the air-conditioning apparatus 200, similarly,
the heat source side heat exchanger 12b disposed at the lower level in the housing
of the outdoor unit 1 is defrosted and, after that, the heat source side heat exchanger
12a disposed at the upper level in the housing of the outdoor unit 1 is defrosted.
[0178] Conditions for starting the defrosting operation mode are the same as those in the
air-conditioning apparatus 100 according to Embodiment 1.
(Defrosting of Heat Source Side Heat Exchanger 12b)
[0179] In the defrosting operation mode, the refrigerant flow switching device 11 is maintained
in the state indicated by solid lines in Fig. 11.
[0180] Additionally, in the defrosting operation mode in which the heat source side heat
exchanger 12b is a defrosting target, the states of the first opening and closing
devices 30, the second opening and closing device 35, the third opening and closing
devices 31, the fourth opening and closing devices 33, the fifth opening and closing
devices 34, and the flow control device 32 are as follows.
[0181] The controller 50 controls the states of those devices.
[0182] The first opening and closing device 30b is switched to the open state, thus permitting
the flow of the refrigerant.
[0183] The third opening and closing device 31 b is switched to the closed state, thus stopping
the flow of the refrigerant.
[0184] The fourth opening and closing device 33b is switched to the closed state, thus stopping
the flow of the refrigerant.
[0185] The fifth opening and closing device 34b is switched to the open state, thus permitting
the flow of the refrigerant.
[0186] The first opening and closing device 30a is maintained in the closed state to stop
the flow of the refrigerant.
[0187] The third opening and closing device 31 a is maintained in the open state to permit
the flow of the refrigerant.
[0188] The fourth opening and closing device 33a is switched to the open state, thus permitting
the flow of the refrigerant.
[0189] The fifth opening and closing device 34a is switched to the closed state, thus stopping
the flow of the refrigerant.
[0190] The opening degree of the flow control device 32b (or the flow control device 32a)
is controlled so that a preset pressure (e.g., approximately 0.8 MPa for R410A refrigerant)
remains constant. At the preset pressure, a saturation temperature converted from
a saturation pressure of two-phase refrigerant calculated based on a detection result
of the third temperature sensor 48b, serving as the "defrosting mode refrigerant decrease
detecting unit", is greater than 0 degrees C.
[0191] When either one of the condition that an outdoor air temperature detected by the
second temperature sensor 45 is less than or equal to the second predetermined value
(for example, less than or equal to 0 degrees C) and the condition that a pressure
at the suction inlet of the compressor 10 detected by the second pressure sensor 42
is less than or equal to the first predetermined value (for example, less than or
equal to approximately 0.3 MPa for R410A refrigerant) is satisfied, or alternatively,
when both the conditions are satisfied, the second opening and closing device 35 is
maintained in the open state to permit the flow of the refrigerant.
[0192] The second temperature sensor 45, the second pressure sensor 42, and the third temperature
sensor 48b correspond to the defrosting mode refrigerant decrease detecting unit in
the present invention.
[0193] The flow of the refrigerant in the defrosting operation mode will now be described
in detail.
[0194] When the compressor 10 is driven, low temperature, low pressure refrigerant is compressed
into high temperature, high pressure gas refrigerant and is then discharged.
[0195] Part of the high temperature, high pressure gas refrigerant discharged from the compressor
10 flows through the first gas bypass pipe 5. In the first opening and closing device
30b, the refrigerant is depressurized to a pressure equivalent to greater than 0 degrees
C in terms of saturation temperature, so that the refrigerant turns into intermediate
pressure, high temperature gas refrigerant. The refrigerant flows into the heat source
side heat exchanger 12b. The intermediate pressure, high temperature gas refrigerant
that has flowed into the heat source side heat exchanger 12b turns into intermediate
pressure, low quality two-phase refrigerant or intermediate pressure refrigerant while
melting frost on the heat source side heat exchanger 12b. The refrigerant then passes
through the fifth opening and closing device 34b. The refrigerant leaving the fifth
opening and closing device 34b is depressurized by the flow control device 32b (or
the flow control device 32a) and then merges with intermediate pressure, low temperature,
low quality two-phase refrigerant or liquid refrigerant that has flowed from the indoor
unit 2 into the outdoor unit 1 at a point upstream of the fourth opening and closing
device 33a.
[0196] Most of the high temperature, high pressure gas refrigerant discharged from the compressor
10 passes through the refrigerant flow switching device 11 and flows out of the outdoor
unit 1. The high temperature, high pressure gas refrigerant leaving the outdoor unit
1 passes through the refrigerant main pipe 4, flows into the indoor unit 2, and transfers
heat to indoor air in the load side heat exchanger 21, so that the refrigerant turns
into liquid refrigerant while heating the indoor air. The liquid refrigerant flows
out of the load side heat exchanger 21 and is then expanded by the load side expansion
device 22, so that the refrigerant turns into low temperature, intermediate pressure
two-phase refrigerant or liquid refrigerant. The refrigerant passes through the refrigerant
main pipe 4 and again flows into the outdoor unit 1.
[0197] The low temperature, intermediate pressure two-phase refrigerant or liquid refrigerant
that has flowed into the outdoor unit 1 merges with the refrigerant flowing from the
flow control device 32b (or the flow control device 32a) at the point upstream of
the fourth opening and closing device 33a. The refrigerant then flows into the heat
source side heat exchanger 12a. The refrigerant that has flowed into the heat source
side heat exchanger 12a removes heat from outdoor air, so that the refrigerant turns
into low temperature, low pressure gas refrigerant. The gas refrigerant flows out
of the heat source side heat exchanger 12a, passes through the third opening and closing
device 31 a, the refrigerant flow switching device 11, and the accumulator 13, and
is again sucked into the compressor 10.
[0198] The controller 50 controls the opening degree of the flow control device 32b (or
the flow control device 32a) so that the preset pressure (for example, approximately
0.8 MPa for R410A refrigerant), at which a saturation temperature converted from a
saturation pressure of two-phase refrigerant calculated based on a detection result
of the third temperature sensor 48b is greater than 0 degrees C, remains constant.
In other words, the controller 50 controls the opening degree of the flow control
device 32b (or the flow control device 32a) so that the saturation temperature converted
from the saturation pressure of the two-phase refrigerant calculated based on the
detection result of the third temperature sensor 48b is greater than 0 degrees C.
[0199] As regards the completion of defrosting of the heat source side heat exchanger 12b,
the completion of defrosting may be determined, for example, after a lapse of a predetermined
period of time, or alternatively, when a temperature detected by the third temperature
sensor 48b is greater than or equal to a predetermined temperature (e.g., 5 degrees
C). Assuming that the heat source side heat exchanger 12b is fully covered with frost,
the predetermined period of time may be set longer than or equal to the time required
to completely defrost the heat source side heat exchanger 12b by allowing part of
high temperature, high pressure refrigerant to flow into the heat source side heat
exchanger 12b.
[0200] The rest of the operation in the defrosting operation mode is the same as that of
the air-conditioning apparatus 100 according to Embodiment 1. Specifically, while
the second opening and closing device 35 is maintained in the open state by the controller
50, a branch flow of the high temperature, high pressure gas refrigerant from the
discharge side of the compressor 10 is allowed to flow into the accumulator 13, so
that the refrigerant accumulating in the accumulator 13 is supplied to the suction
inlet of the compressor 10. Consequently, the air-conditioning apparatus 200 achieves
the same advantages as those of the air-conditioning apparatus 100 according to Embodiment
1. A decrease in indoor heating capacity and defrosting capacity can be eliminated
or reduced.
[0201] Since the controller 50 controls the second opening and closing device 35 in the
same manner as that in the air-conditioning apparatus 100 according to Embodiment
1, a description of the operation of the controller 50 is omitted.
[0202] For example, if the heat source side heat exchanger 12b includes a first heat exchanger
element and a second heat exchanger element and is used as an evaporator, most of
outdoor air will be dehumidified by the fins of the first heat exchanger element disposed
on an outdoor air inlet side of the heat source side heat exchanger 12b, or the fins
of the first heat exchanger element disposed on the air inlet side of the heat source
side heat exchanger 12b. In other words, the fins of the first heat exchanger element
on the air inlet side of the heat source side heat exchanger 12b will be covered with
a large amount of frost and the fins of the second heat exchanger element will be
covered with a small amount of frost.
[0203] Unlike the air-conditioning apparatus 100 according to Embodiment 1, the air-conditioning
apparatus 200 allows part of the high temperature, high pressure gas refrigerant discharged
from the compressor 10 to flow into the heat source side heat exchanger 12b functioning
as a condenser in the same direction as that in the passage of the heat source side
heat exchanger 12b used as an evaporator. Consequently, two-phase refrigerant having
higher heat energy is allowed to flow into the first heat exchanger element covered
with the large amount of frost. Thus, the air-conditioning apparatus 200 achieves
defrosting with higher efficiency than the air-conditioning apparatus 100 according
to Embodiment 1, so that the time required for defrosting can be shortened and a decrease
in indoor heating capacity can be further eliminated or reduced.
[0204] To defrost the heat source side heat exchanger 12a after the heat source side heat
exchanger 12b is completely defrosted, an operation may be performed in a manner obtained
by interchanging the letters "a" and "b" added to the reference numerals in the above
description about the defrosting operation for the heat source side heat exchanger
12b. Specifically, the open and closed states of the first opening and closing devices
30a and 30b, the third opening and closing devices 31 a and 31 b, the fourth opening
and closing devices 33a and 33b, and the fifth opening and closing devices 34a and
34b are the opposite of the above-described states and the refrigerant flow direction
in each of the heat source side heat exchangers 12a and 12b is reversed.
[0205] As described above, the saturation temperature of the refrigerant in the heat source
side heat exchanger 12 functioning as a condenser in the defrosting operation mode
for the heat source side heat exchanger 12 is set at an intermediate pressure (for
example, at or above approximately 0.8 MPa for R410A refrigerant) equivalent to a
temperature greater than the temperature of frost, that is, 0 degrees C. In the air-conditioning
apparatus 200, therefore, a two-phase region (latent heat) of the refrigerant can
be used, so that efficient defrosting can be achieved with a small circulation amount
of refrigerant, a decrease in indoor heating capacity can be eliminated or reduced,
and the indoor space can be kept comfortable.
[0206] The air-conditioning apparatus 200 can defrost the heat source side heat exchangers
12a and 12b while continuing the heating operation by performing the above-described
defrosting operation mode. The heat source side heat exchanger 12b at the lower level
in the housing of the outdoor unit 1 is defrosted and, after that, the heat source
side heat exchanger 12a at the upper level is defrosted. This can eliminate a likelihood
that water produced by defrosting the heat source side heat exchanger 12a may freeze
in the lower heat source side heat exchanger 12b to be defrosted. Efficient defrosting
can be achieved.
[0207] In the above description, the air-conditioning apparatus 200 according to Embodiment
2 is configured such that the branch flow of the high temperature, high pressure gas
refrigerant from the discharge side of the compressor 10 flows into the pipe at the
inlet of the accumulator 13. In addition, for example, the air-conditioning apparatus
200 may have such a circuit configuration that the branch flow of the high temperature,
high pressure gas refrigerant from the discharge side of the compressor 10 directly
flows into the accumulator 13 through the second gas bypass pipe 7 and the second
opening and closing device 35 in a manner similar to the configuration of Fig. 10
of the air-conditioning apparatus 100 according to Embodiment 1. Such a configuration
achieves the same advantages as those of the air-conditioning apparatus 100 according
to Embodiment 1. Efficient defrosting can be performed, a decrease in indoor heating
capacity can be eliminated or reduced, and the indoor space can be kept comfortable.
[Refrigerant]
[0208] As regards the heat source side refrigerant for the air-conditioning apparatus 100
according to Embodiment 1 and the air-conditioning apparatus 200 according to Embodiment
2, a nonflammable refrigerant, such as R410A, R407C, or R22, a refrigerant mixture
containing HFO1234yf, HFO1234ze(E), R32, HC, or R32 and HFO1234yf, a slightly flammable
refrigerant, such as a refrigerant mixture containing any of the above-described refrigerants
as at least one component, a highly flammable refrigerant, such as propane (R290),
or a refrigerant that operates in a supercritical state on a high-pressure side, for
example, CO
2 (R744), can be used as a heat source side refrigerant.
[First Opening and Closing Devices]
[0209] As regards the first opening and closing devices 30a and 30b of each of the air-conditioning
apparatus 100 according to Embodiment 1 and the air-conditioning apparatus 200 according
to Embodiment 2, the solenoid valves are used in the above-described case. In addition,
a valve having a variable opening degree, for example, an electronic expansion valve,
may be used as each of the first opening and closing devices 30a and 30b.
[Second Opening and Closing Device]
[0210] As regards the second opening and closing device 35 of each of the air-conditioning
apparatus 100 according to Embodiment 1 and the air-conditioning apparatus 200 according
to Embodiment 2, the solenoid valve is used in the above-described case. In addition,
a valve having a variable opening degree, for example, an electronic expansion valve,
may be used as the second opening and closing device 35. Furthermore, the air-conditioning
apparatus 100 according to Embodiment 1 and the air-conditioning apparatus 200 according
to Embodiment 2 each include the single second opening and closing device 35 in the
above-described case. In addition, a plurality of solenoid valves arranged in parallel
may be used. Such a configuration achieves the same advantages as those of Embodiments
1 and 2.
[Third Opening and Closing Devices]
[0211] As regards the third opening and closing devices 31 a and 31 b of each of the air-conditioning
apparatus 100 according to Embodiment 1 and the air-conditioning apparatus 200 according
to Embodiment 2, the solenoid valves are used in the above-described case. In addition,
a valve having a variable opening degree, for example, an electronic expansion valve,
may be used as each of the third opening and closing devices 31 a and 31 b.
[Flow Control Devices]
[0212] As regards the flow control devices 32a and 32b of each of the air-conditioning apparatus
100 according to Embodiment 1 and the air-conditioning apparatus 200 according to
Embodiment 2, the expansion device having a variable opening degree (opening area)
is used as each flow control device in the above description. Any device having a
variable passage opening area may be used. For example, the expansion device may be
an electronic expansion valve that is driven by a stepping motor or may include a
plurality of small solenoid valves arranged in parallel such that the opening degree
is changed by switching the solenoid valves.
[0213] In each of the air-conditioning apparatus 100 according to Embodiment 1 and the air-conditioning
apparatus 200 according to Embodiment 2, each of the flow control devices 32a and
32b is the device having a variable passage opening area. In addition, for example,
the flow control device 32a may be a device having a variable passage opening area
and the flow control device 32b may include a plurality of small solenoid valves arranged
in parallel. Such a configuration achieves the same advantages as those of Embodiments
1 and 2.
[Fourth Opening and Closing Devices]
[0214] As regards the fourth opening and closing devices 33 of the air-conditioning apparatus
200 according to Embodiment 2, the solenoid valves are used in the above-described
case. In addition, a valve having a variable opening degree, for example, an electronic
expansion valve, may be used as each of the fourth opening and closing devices 33.
[Fifth Opening and Closing Devices]
[0215] As regards the fifth opening and closing devices 34 of the air-conditioning apparatus
200 according to Embodiment 2, the solenoid valves are used in the above-described
case. In addition, a valve having a variable opening degree, for example, an electronic
expansion valve, may be used as each of the fifth opening and closing devices.
[0216] Assuming that a component having a variable opening degree (opening area), for example,
an electronic expansion valve, is used as each of the opening and closing devices,
the term "opening the opening and closing device" refers to changing the opening degree
to fully or substantially fully open the opening and closing device, and the term
"closing the opening and closing device" refers to changing the opening degree to
fully or substantially fully close the opening and closing device. The same applies
to each of the flow control devices. The term "opening" refers to changing the opening
degree to fully or substantially fully open the flow control device, and the term
"closing the flow control device" refers to changing the opening degree to fully or
substantially fully close the flow control device, that is, changing the opening degree
to a state where little or no refrigerant flows through the device.
[Heat Source Side Heat Exchangers]
[0217] As regards the heat source side heat exchangers 12a and 12b of each of the air-conditioning
apparatus 100 according to Embodiment 1 and the air-conditioning apparatus 200 according
to Embodiment 2, the heat source side heat exchangers are arranged at two levels in
the level arrangement direction (or the top-bottom direction along the length of the
fins aligned so as to face in the same direction) in the above-described case. The
present invention is not limited to such a configuration. For example, as described
above, a plurality of heat source side heat exchangers 12 may be arranged at, for
example, three or more levels in the level arrangement direction (or the top-bottom
direction along the length of the fins aligned so as to face in the same direction).
Furthermore, the arrangement is not limited to that in the top-bottom direction. A
plurality of heat source side heat exchangers 12 may be arranged in the left-right
direction or a front-rear direction.
[0218] As regards each of the air-conditioning apparatus 100 according to Embodiment 1 and
the air-conditioning apparatus 200 according to Embodiment 2, the air-conditioning
apparatus capable of switching between the cooling operation and the heating operation
has been described as an example. In addition, the present invention can be applied
to an air-conditioning apparatus having a circuit configuration that enables the cooling
and heating mixed operation. Furthermore, the present invention can be applied to
an air-conditioning apparatus that does not include the refrigerant flow switching
device 11 and performs only the heating only operation mode and the defrosting operation
mode. The term "heating circuit" refers to the refrigerant circuit configuration formed
in the heating operation mode of each of the air-conditioning apparatus 100 and the
air-conditioning apparatus 200. Reference Signs List
[0219] 1: outdoor unit; 2: indoor unit; 3: refrigerant pipe; 4: refrigerant main pipe; 5:
first gas bypass pipe; 6: refrigerant bypass pipe; 7: second gas bypass pipe; 10:
compressor; 11: refrigerant flow switching device; 12: heat source side heat exchanger;
12a: heat source side heat exchanger; 12b: heat source side heat exchanger; 13: accumulator;
21: load side heat exchanger; 22: load side expansion device; 30: first opening and
closing device; 30a: first opening and closing device; 30b: first opening and closing
device; 31: third opening and closing device; 31 a: third opening and closing device;
31b: third opening and closing device; 32: flow control device; 32a: flow control
device; 32b: flow control device; 33: fourth opening and closing device; 33a: fourth
opening and closing device; 33b: fourth opening and closing device; 34: fifth opening
and closing device; 34a: fifth opening and closing device; 34b: fifth opening and
closing device; 35: second opening and closing device; 41: first pressure sensor;
42: second pressure sensor; 43: first temperature sensor; 44: sixth temperature sensor;
45: second temperature sensor; 46: fourth temperature sensor; 47: fifth temperature
sensor; 48a: third temperature sensor; 48b: third temperature sensor; 50: controller;
51: fin; 52: heat transfer tube; 100: air-conditioning apparatus; and 200: air-conditioning
apparatus.