TECHNICAL FIELD
[0001] The present invention relates to a function to judge the adequacy of the refrigerant
quantity in a refrigerant circuit of an air conditioner. More specifically, the present
invention relates to a function to judge the adequacy of the refrigerant quantity
in a refrigerant circuit of an air conditioner configured by the interconnection of
a heat source unit and a utilization unit via a refrigerant communication pipe.
BACKGROUND ART
[0002] Conventionally, in a separate type air conditioner configured by the interconnection
of a heat source unit and a utilization unit via a refrigerant communication pipe,
information on the length and the like of the refrigerant communication pipe is input
in order to accurately judge the excess or deficiency of the refrigerant quantity
in a refrigerant circuit (for example, see Patent Document 1).
<Patent Document 1>
DISCLOSURE OF THE INVENTION
[0004] However, the above described work to input information on the refrigerant communication
pipe is extremely laborious work. In addition, there is a problem that an input error
easily occurs.
[0005] An object of the present invention is to minimize the labor of inputting information
on a refrigerant communication pipe before operating a separate type air conditioner,
and at the same time, to enable a highly accurate judgment of the adequacy of the
refrigerant quantity in a refrigerant circuit.
[0006] An air conditioner according to a first aspect of the present invention includes
a refrigerant circuit configured by the interconnection of a heat source unit and
a utilization unit via a refrigerant communication pipe, and a pipe volume calculating
means. The pipe volume calculating means calculates the volume of the refrigerant
communication pipe based on an additional charging quantity that is a refrigerant
quantity to be additionally charged after the refrigerant circuit is configured by
the interconnection of the heat source unit and the utilization unit via the refrigerant
communication pipe.
[0007] In this air conditioner, the volume of the refrigerant communication pipe is calculated
based on the additional charging quantity that is the refrigerant quantity to be additionally
charged after the refrigerant circuit is configured by the interconnection of the
heat source unit and the utilization unit via the refrigerant communication pipe.
Thus, even when the volume of the refrigerant communication pipe is unknown, it is
possible to calculate the volume of the refrigerant communication pipe by inputting
a value of the additional charging quantity. Accordingly, it is possible to determine
the volume of the refrigerant communication pipe while minimizing the labor of inputting
information on the refrigerant communication pipe. As a result, it is possible to
judge the adequacy of the refrigerant quantity in the refrigerant circuit with high
accuracy.
[0008] An air conditioner according to a second aspect of the present invention is the air
conditioner according to the first aspect of the present invention, further including
a refrigerant quantity judging means to judge whether or not the refrigerant quantity
charged in the refrigerant circuit has reached a target charging quantity based on
an operation state quantity of constituent equipment or refrigerant flowing in the
refrigerant circuit in an automatic refrigerant charging operation in which the refrigerant
is additionally charged into the refrigerant circuit. The additional charging quantity
is the refrigerant quantity additionally charged into the refrigerant circuit in the
automatic refrigerant charging operation.
[0009] In this air conditioner, whether or not the target charging quantity is reached can
be judged based on the operation state quantity of constituent equipment or refrigerant
flowing in the refrigerant circuit, so that it is possible to reliably perform additional
refrigerant charging, and at the same time, it is possible to determine a value of
the additional charging quantity required for the calculation of the volume of the
refrigerant communication pipe by performing the automatic refrigerant charging operation.
[0010] An air conditioner according to a third aspect of the present invention includes
a refrigerant circuit configured by the interconnection of a heat source unit and
a utilization unit via a refrigerant communication pipe, and a pipe volume calculating
means. The pipe volume calculating means calculates the volume of the refrigerant
communication pipe based on a communication pipe refrigerant quantity that is a refrigerant
quantity in the refrigerant communication pipe. The communication pipe refrigerant
quantity is determined by subtracting an inside-unit refrigerant quantity that is
a refrigerant quantity in the refrigerant circuit excluding the refrigerant communication
pipe from a total charged refrigerant quantity that is a refrigerant quantity in the
entire refrigerant circuit after the refrigerant is additionally charged thereinto.
[0011] In this air conditioner, the volume of the refrigerant communication pipe is calculated
based on the communication pipe refrigerant quantity that is the refrigerant quantity
in the refrigerant communication pipe. The communication pipe refrigerant quantity
is determined by subtracting the inside-unit refrigerant quantity that is the refrigerant
quantity in the refrigerant circuit excluding the refrigerant communication pipe from
the total charged refrigerant quantity that is the refrigerant quantity in the entire
refrigerant circuit after the refrigerant is additionally charged thereinto. Thus,
even when the volume of the refrigerant communication pipe is unknown, it is possible
to calculate the volume of the refrigerant communication pipe by inputting a value
of the additional charging quantity. Accordingly, it is possible to determine the
volume of the refrigerant communication pipe while minimizing the labor of inputting
information on the refrigerant communication pipe. As a result, it is possible to
judge the adequacy of the refrigerant quantity in the refrigerant circuit with high
accuracy.
[0012] An air conditioner according to a fourth aspect of the present invention is the air
conditioner according to the second aspect of the present invention, further including
a refrigerant quantity calculating means to calculate an inside-unit refrigerant quantity
that is a refrigerant quantity in the refrigerant circuit excluding the refrigerant
pipe from the operation state quantity of constituent equipment or refrigerant flowing
in the refrigerant circuit in the automatic refrigerant charging operation. The pipe
volume calculating means determines a total charged refrigerant quantity that is a
refrigerant quantity in the entire refrigerant circuit immediately after the automatic
refrigerant charging operation, by adding the additional charging quantity to an initial
charging quantity that is a refrigerant quantity charged in the refrigerant circuit
before the automatic refrigerant charging operation. Then, the pipe volume calculating
means determines a communication pipe refrigerant quantity that is a refrigerant quantity
in the refrigerant communication pipe by subtracting the inside-unit refrigerant quantity
from the total charged refrigerant quantity, and calculates a density of the refrigerant
flowing through the refrigerant communication pipe from the operation state quantity
of constituent equipment or refrigerant flowing in the refrigerant circuit. Then,
the pipe volume calculating means calculates the volume of the refrigerant communication
pipe based on the communication pipe refrigerant quantity and the density.
[0013] In this air conditioner, it is possible to calculate the communication pipe refrigerant
quantity present with high accuracy during the automatic refrigerant charging operation
by subtracting the inside-unit refrigerant quantity calculated based on the operation
state quantity of constituent equipment or refrigerant flowing in the refrigerant
circuit in the automatic refrigerant charging operation, from the total charged refrigerant
quantity determined by adding the additional charging quantity to the initial charging
quantity. Thus, the volume of the refrigerant communication pipe can be calculated
with high accuracy.
[0014] An air conditioner according to a fifth aspect of the present invention is the air
conditioner according to the fourth aspect of the present invention, wherein the refrigerant
communication pipe includes a liquid refrigerant communication pipe and a gas refrigerant
communication pipe. The pipe volume calculating means calculates a liquid refrigerant
density that is a density of liquid refrigerant flowing through the liquid refrigerant
communication pipe and a gas density that is a density of gas refrigerant flowing
through the gas refrigerant communication pipe. Then, the pipe volume calculating
means calculates the volume of the liquid refrigerant communication pipe and the volume
of the gas refrigerant communication pipe based on the communication pipe refrigerant
quantity, a volume ratio between the liquid refrigerant communication pipe and the
gas refrigerant communication pipe, the liquid refrigerant density, and the gas refrigerant
density.
[0015] The liquid refrigerant communication pipe and the gas refrigerant communication pipe
are provided so as to interconnect the utilization unit and the heat source unit,
so that these pipes have substantially the same pipe length but different pipe diameters,
i.e., different flow passage cross-sectional areas, due to the different densities
of the refrigerant flowing through the pipes. Therefore, the volume ratio between
the liquid refrigerant communication pipe and the gas refrigerant communication pipe
will substantially correspond to a flow passage cross-sectional area ratio between
these pipes, and furthermore, this volume ratio will be within a certain range because
the flow passage cross-sectional area ratio is predetermined based on the capacities
and models of the utilization unit and the heat source unit. Further, if the volume
ratio between the liquid refrigerant communication pipe and the gas refrigerant communication
pipe is known, it will be possible to calculate both the volume of the liquid refrigerant
communication pipe and the volume of the gas refrigerant communication pipe, because
a total value obtained by adding a value of the multiplication between the volume
of the liquid refrigerant communication pipe and the liquid refrigerant density to
a value of the multiplication between the volume of the gas refrigerant communication
pipe and the gas refrigerant density will be equal to the communication pipe refrigerant
quantity.
[0016] Consequently, in this air conditioner, it is possible to easily calculate both the
volume of the liquid refrigerant communication pipe and the volume of the gas refrigerant
communication pipe by predetermining the volume ratio between the liquid refrigerant
communication pipe and the gas refrigerant communication pipe.
[0017] An air conditioner according to a sixth aspect of the present invention is the air
conditioner according to the fourth or fifth aspect of the present invention, wherein
the refrigerant quantity calculating means calculates a total calculated refrigerant
quantity that is a refrigerant quantity in the entire refrigerant circuit based on
the volume of the refrigerant communication pipe calculated by the pipe volume calculating
means and based on the operation state quantity of constituent equipment or refrigerant
flowing in the refrigerant circuit in a refrigerant leak detection operation in which
whether or not there is a refrigerant leak from the refrigerant circuit is judged.
The refrigerant quantity judging means judges whether or not there is a refrigerant
leak from the refrigerant circuit by comparing the total calculated refrigerant quantity
with a reference refrigerant quantity that serves as a reference for judging whether
or not there is a refrigerant leak from the refrigerant circuit.
[0018] In this air conditioner, the pipe volume calculating means can calculate the volume
of the refrigerant communication pipe, so that even if the volume of the refrigerant
communication pipe is unknown, it is possible to calculate the refrigerant quantity
in the refrigerant circuit in the refrigerant leak detection operation using the volume
of the refrigerant communication pipe calculated by the pipe volume calculating means.
Accordingly, it is possible to determine, with high accuracy, whether or not there
is a refrigerant leak from the refrigerant circuit while minimizing the labor of inputting
information on the refrigerant communication pipe.
[0019] An air conditioner according to a seventh aspect of the present invention is the
air conditioner according to the second aspect of the present invention, wherein the
pipe volume calculating means calculates a density of the refrigerant flowing through
the refrigerant communication pipe from the operation state quantity of constituent
equipment or refrigerant flowing in the refrigerant circuit, and calculates the volume
of the refrigerant communication pipe based on the additional charging quantity and
the density.
[0020] In this air conditioner, for example, the refrigerant whose quantity is substantially
equal to an inside-unit refrigerant quantity that is a refrigerant quantity in the
refrigerant circuit excluding the refrigerant communication pipe and that is present
when the refrigerant quantity in the refrigerant circuit is reached the target charging
quantity by the automatic refrigerant charging operation, is charged as an initial
charging quantity into the refrigerant circuit before the automatic refrigerant charging
operation is performed, and thereby the refrigerant quantity to be additionally charged
into the refrigerant circuit in the automatic refrigerant charging operation can be
regarded as a refrigerant quantity corresponding to the refrigerant quantity present
in the refrigerant communication pipe. Accordingly, it is possible to calculate the
volume of the refrigerant communication pipe with high accuracy based on the additional
charging quantity and the density.
[0021] An air conditioner according to an eighth aspect of the present invention is the
air conditioner according to the seventh aspect of the present invention, wherein
the refrigerant communication pipe includes a liquid refrigerant communication pipe
and a gas refrigerant communication pipe. The pipe volume calculating means calculates
a liquid refrigerant density that is a density of liquid refrigerant flowing through
the liquid refrigerant communication pipe and a gas refrigerant density that is a
density of gas refrigerant flowing through the gas refrigerant communication pipe.
Then, the pipe volume calculating means calculates the volume of the liquid refrigerant
communication pipe and the volume of the gas refrigerant communication pipe based
on the additional charging quantity, a volume ratio between the liquid refrigerant
communication pipe and the gas refrigerant communication pipe, the liquid refrigerant
density, and the gas refrigerant density.
[0022] The liquid refrigerant communication pipe and the gas refrigerant communication pipe
are provided so as to interconnect the utilization unit and the heat source unit,
so that these pipes have substantially the same pipe length but different pipe diameters,
i.e., different flow passage cross-sectional areas, due to the different densities
of the refrigerant flowing through the pipes. Therefore, the volume ratio between
the liquid refrigerant communication pipe and the gas refrigerant communication pipe
substantially corresponds to a flow passage cross-sectional area ratio between these
pipes, and further more, this volume ratio will be within a certain range because
the flow passage cross-sectional area ratio is predetermined based on the capacities
and models of the utilization unit and the heat source unit. Further, if the volume
ratio between the liquid refrigerant communication pipe and the gas refrigerant communication
pipe is known, it will be possible to calculate both the volume of the liquid refrigerant
communication pipe and the volume of the gas refrigerant communication pipe because
a total value obtained by adding a value of the multiplication between the volume
of the liquid refrigerant communication pipe and the liquid refrigerant density to
a value of the multiplication between the volume of the gas refrigerant communication
pipe and the gas refrigerant density will be equal to the additional charging quantity.
[0023] Consequently, in this air conditioner, it is possible to easily calculate both the
volume of the liquid refrigerant communication pipe and the volume of the gas refrigerant
communication pipe by predetermining the volume ratio between the liquid refrigerant
communication pipe and the gas refrigerant communication pipe.
[0024] An air conditioner according to a ninth aspect of the present invention is the air
conditioner according to the seventh or eighth aspect of the present invention, further
including a refrigerant quantity calculating means to calculate a total calculated
refrigerant quantity that is a refrigerant quantity in the entire refrigerant circuit
based on the volume of the refrigerant communication pipe calculated by the pipe volume
calculating means and based on the operation state quantity of constituent equipment
or refrigerant flowing in the refrigerant circuit in a refrigerant leak detection
operation in which whether or not there is a refrigerant leak from the refrigerant
circuit is judged, The refrigerant quantity judging means judges whether or not there
is a refrigerant leak from the refrigerant circuit by comparing the total calculated
refrigerant quantity with a reference refrigerant quantity that serves as a reference
for judging whether or not there is a refrigerant leak from the refrigerant circuit.
[0025] In this air conditioner, the pipe volume calculating means can calculate the volume
of the refrigerant communication pipe, so that even when the volume of the refrigerant
communication pipe is unknown, it is possible to calculate the refrigerant quantity
in the refrigerant circuit in the refrigerant leak detection operation using the volume
of the refrigerant communication pipe calculated by the pipe volume calculating means.
Accordingly, it is possible to determine, with high accuracy, whether or not there
is a refrigerant leak from the refrigerant circuit while minimizing the labor of inputting
information on the refrigerant communication pipe.
BRIEF DESCRIPTION OF THE DRAWINGS
[0026]
Figure 1 is a schematic configuration view of an air conditioner according to an embodiment
of the present invention.
Figure 2 is a control block diagram of the air conditioner.
Figure 3 is a flowchart of a test operation mode.
Figure 4 is a flowchart of an automatic refrigerant charging operation.
Figure 5 is a schematic diagram to show a state of refrigerant flowing in a refrigerant
circuit in a refrigerant quantity judging operation (illustrations of a four-way switching
valve and the like are omitted).
Figure 6 is a flowchart of a pipe volume calculation process.
Figure 7 is a flowchart of a refrigerant leak detection operation mode.
DESCRIPTION OF THE REFERENCE SYMBOLS
[0027]
- 1
- Air conditioner
- 2
- Outdoor unit (heat source unit)
- 4, 5
- Indoor unit (utilization unit)
- 6
- Liquid refrigerant communication pipe (refrigerant communication pipe)
- 7
- Gas refrigerant communication pipe (refrigerant communication pipe)
- 10
- Refrigerant circuit
BEST MODE FOR CARRYING OUT THE INVENTION
[0028] In the following, an embodiment of an air conditioner according to the present invention
is described based on the drawings.
(1) CONFIGURATION OF THE AIR CONDITIONER
[0029] Figure 1 is a schematic configuration view of an air conditioner 1 according to an
embodiment of the present invention. The air conditioner 1 is a device that is used
to cool and heat a room in a building and the like by performing a vapor compression-type
refrigeration cycle operation. The air conditioner 1 mainly includes one outdoor unit
2 as a heat source unit, indoor units 4 and 5 as a plurality (two in the present embodiment)
of utilization units connected in parallel thereto, and a liquid refrigerant communication
pipe 6 and a gas refrigerant communication pipe 7 as refrigerant communication pipes
which interconnect the outdoor unit 2 and the indoor units 4 and 5. In other words,
the vapor compression-type refrigerant circuit 10 of the air conditioner 1 in the
present embodiment is configured by the interconnection of the outdoor unit 2, the
indoor units 4 and 5, and the liquid refrigerant communication pipe 6 and the gas
refrigerant communication pipe 7.
<INDOOR UNIT>
[0030] The indoor units 4 and 5 are installed by being embedded in or hung from a ceiling
of a room in a building and the like or by being mounted or the like on a wall surface
of a room. The indoor units 4 and 5 are connected to the outdoor unit 2 via the liquid
refrigerant communication pipe 6 and the gas refrigerant communication pipe 7, and
configure a part of the refrigerant circuit 10.
[0031] Next, the configurations of the indoor units 4 and 5 are described. Note that, because
the indoor units 4 and 5 have the same configuration, only the configuration of the
indoor unit 4 is described here, and in regard to the configuration of the indoor
unit 5, reference numerals in the 50s are used instead of reference numerals in the
40s representing the respective portions of the indoor unit 4, and descriptions of
those respective portions are omitted.
[0032] The indoor unit 4 mainly includes an indoor side refrigerant circuit 10a (an indoor
side refrigerant circuit 10b in the case of the indoor unit 5) that configures a part
of the refrigerant circuit 10. The indoor side refrigerant circuit 10a mainly includes
an indoor expansion valve 41 as an expansion mechanism and an indoor heat exchanger
42 as a utilization side heat exchanger.
[0033] In the present embodiment, the indoor expansion valve 41 is an electrically powered
expansion valve connected to a liquid side of the indoor heat exchanger 42 in order
to adjust the flow rate or the like of the refrigerant flowing in the indoor side
refrigerant circuit 10a.
[0034] In the present embodiment, the indoor heat exchanger 42 is a cross fin-type fin-and-tube
type heat exchanger configured by a heat transfer tube and numerous fins, and is a
heat exchanger that functions as an evaporator for the refrigerant during a cooling
operation to cool the room air and functions as a condenser for the refrigerant during
a heating operation to heat the room air.
[0035] In the present embodiment, the indoor unit 4 includes an indoor fan 43 as a ventilation
fan for taking in room air into the unit, causing the air to heat exchange with the
refrigerant in the indoor heat exchanger 42, and then supplying the air to the room
as supply air. The indoor fan 43 is a fan capable of varying an air flow rate Wr of
the air which is supplied to the indoor heat exchanger 42, and in the present embodiment,
is a centrifugal fan, multi-blade fan, or the like, which is driven by a motor 43a
comprising a DC fan motor.
[0036] In addition, various types of sensors are disposed in the indoor unit 4. A liquid
side temperature sensor 44 that detects the temperature of the refrigerant (i.e.,
the refrigerant temperature corresponding to a condensation temperature Tc during
the heating operation or an evaporation temperature Te during the cooling operation)
is disposed at the liquid side of the indoor heat exchanger 42. A gas side temperature
sensor 45 that detects a temperature Teo of the refrigerant is disposed at a gas side
of the indoor heat exchanger 42. A room temperature sensor 46 that detects the temperature
of the room air that flows into the unit (i.e., a room temperature Tr) is disposed
at a room air intake side of the indoor unit 4. In the present embodiment, the liquid
side temperature sensor 44, the gas side temperature sensor 45, and the room temperature
sensor 46 comprise thermistors. In addition, the indoor unit 4 includes an indoor
side controller 47 that controls the operation of each portion constituting the indoor
unit 4. Additionally, the indoor side controller 47 includes a microcomputer and a
memory and the like disposed in order to control the indoor unit 4, and is configured
such that it can exchange control signals and the like with a remote controller (not
shown) for individually operating the indoor unit 4 and can exchange control signals
and the like with the outdoor unit 2 via a transmission line 8a.
<OUTDOOR UNIT>
[0037] The outdoor unit 2 is installed outside of a building and the like, is connected
to the indoor units 4 and 5 via the liquid refrigerant communication pipe 6 and the
gas refrigerant communication pipe 7, and configures the refrigerant circuit 10 with
the indoor units 4 and 5.
[0038] Next, the configuration of the outdoor unit 2 is described. The outdoor unit 2 mainly
includes an outdoor side refrigerant circuit 10c that configures a part of the refrigerant
circuit 10. This outdoor side refrigerant circuit 10c mainly includes a compressor
21, a four-way switching valve 22, an outdoor heat exchanger 23 as a heat source side
heat exchanger, an outdoor expansion valve 38 as an expansion mechanism, an accumulator
24, a subcooler 25 as a temperature adjustment mechanism; a liquid side stop valve
26, and a gas side stop valve 27.
[0039] The compressor 21 is a compressor whose operation capacity can be varied, and in
the present embodiment, is a positive displacement-type compressor driven by a motor
21a whose rotation frequency Rm is controlled by an inverter. In the present embodiment,
only one compressor 21 is provided, but it is not limited thereto, and two or more
compressors may be connected in parallel according to the number of connected units
of indoor units and the like.
[0040] The four-way switching valve 22 is a valve for switching the direction of the flow
of the refrigerant such that, during the cooling operation, the four-way switching
valve 22 is capable of connecting a discharge side of the compressor 21 and a gas
side of the outdoor heat exchanger 23 and connecting a suction side of the compressor
21 (specifically, the accumulator 24) and the gas refrigerant communication pipe 7
(see the solid lines of the four-way switching valve 22 in Figure 1) to cause the
outdoor heat exchanger 23 to function as a condenser for the refrigerant compressed
in the compressor 21. and to cause the indoor heat exchangers 42 and 52 to function
as evaporators for the refrigerant condensed in the outdoor heat exchanger 23; and
such that, during the heating operation, the four-way switching valve 22 is capable
of connecting the discharge side of the compressor 21 and the gas refrigerant communication
pipe 7 and connecting the suction side of the compressor 21 and the gas side of the
outdoor heat exchanger 23 (see the dotted lines of the four-way switching valve 22
in Figure 1) to cause the indoor heat exchangers 42 and 52 to function as condensers
for the refrigerant compressed in the compressor 21 and to cause the outdoor heat
exchanger 23 to function as an evaporator for the refrigerant condensed in the indoor
heat exchangers 42 and 52.
[0041] In the present embodiment, the outdoor heat exchanger 23 is a cross-fin type fin-and-tube
type heat exchanger configured by a heat transfer tube and numerous fins, and is a
heat exchanger that functions as a condenser for the refrigerant during the cooling
operation and as an evaporator for the refrigerant during the heating operation. The
gas side of the outdoor heat exchanger 23 is connected to the four-way switching valve
22, and the liquid side thereof is connected to the liquid refrigerant communication
pipe 6.
[0042] In the present embodiment, the outdoor expansion valve 38 is an electrically powered
expansion valve connected to a liquid side of the outdoor heat exchanger 23 in order
to adjust the pressure, flow rate, or the like of the refrigerant flowing in the outdoor
side refrigerant circuit 10c.
[0043] In the present embodiment, the outdoor unit 2 includes an outdoor fan 28 as a ventilation
fan for taking in outdoor air into the unit, causing the air to exchange heat with
the refrigerant in the outdoor heat exchanger 23, and then exhausting the air to the
outside. The outdoor fan 28 is a fan capable of varying an air flow rate Wo of the
air which is supplied to the outdoor heat exchanger 23, and in the present embodiment,
is a propeller fan or the like driven by a motor 28a comprising a DC fan motor.
[0044] The accumulator 24 is connected between the four-way switching valve 22 and the compressor
21, and is a container capable of accumulating excess refrigerant generated in the
refrigerant circuit 10 in accordance with the change in the operation load of the
indoor units 4 and 5 and the like.
[0045] In the present embodiment, the subcooler 25 is a double tube heat exchanger, and
is disposed to cool the refrigerant sent to the indoor expansion valves 41 and 51
after the refrigerant is condensed in the outdoor heat exchanger 23. In the present
embodiment, the subcooler 25 is connected between the outdoor expansion valve 38 and
the liquid side stop valve 26.
[0046] In the present embodiment, a bypass refrigerant circuit 61 as a cooling source of
the subcooler 25 is disposed. Note that, in the description below, a portion corresponding
to the refrigerant circuit 10 excluding the bypass refrigerant circuit 61 is referred
to as a main refrigerant circuit for convenience sake.
[0047] The bypass refrigerant circuit 61 is connected to the main refrigerant circuit so
as to cause a portion of the refrigerant sent from the outdoor heat exchanger 23 to
the indoor expansion valves 41 and 51 to branch from the main refrigerant circuit
and return to the suction side of the compressor 21. Specifically, the bypass refrigerant
circuit 61 includes a branch circuit 61 a connected so as to branch a portion of the
refrigerant sent from the outdoor expansion valve 38 to the indoor expansion valves
41 and 51 at a position between the outdoor heat exchanger 23 and the subcooler 25,
and a merging circuit 61b connected to the suction side of the compressor 21 so as
to return a portion of refrigerant from an outlet on a bypass refrigerant circuit
side of the subcooler 25 to the suction side of the compressor 21. Further, the branch
circuit 61a is disposed with a bypass expansion valve 62 for adjusting the flow rate
of the refrigerant flowing in the bypass refrigerant circuit 61. Here, the bypass
expansion valve 62 comprises an electrically operated expansion valve. In this way,
the refrigerant sent from the outdoor heat exchanger 23 to the indoor expansion valves
41 and 51 is cooled in the subcooler 25 by the refrigerant flowing in the bypass refrigerant
circuit 61 which has been depressurized by the bypass expansion valve 62. In other
words, performance of the subcooler 25 is controlled by adjusting the opening degree
of the bypass expansion valve 62.
[0048] The liquid side stop valve 26 and the gas side stop valve 27 are valves disposed
at ports connected to external equipment and pipes (specifically, the liquid refrigerant
communication pipe 6 and the gas refrigerant communication pipe 7). The liquid side
stop valve 26 is connected to the outdoor heat exchanger 23. The gas side stop valve
27 is connected to the four-way switching valve 22.
[0049] In addition, various sensors are disposed in the outdoor unit 2. Specifically, disposed
in the outdoor unit 2 are an suction pressure sensor 29 that detects a suction pressure
Ps of the compressor 21, a discharge pressure sensor 30 that detects a discharge pressure
Pd of the compressor 21, a suction temperature sensor 31 that detects a suction temperature
Ts of the compressor 21, and a discharge temperature sensor 32 that detects a discharge
temperature Td of the compressor 21. The suction temperature sensor 31 is disposed
at a position between the accumulator 24 and the compressor 21. A heat exchanger temperature
sensor 33 that detects the temperature of the refrigerant flowing through the outdoor
heat exchanger 23 (i.e., the refrigerant temperature corresponding to the condensation
temperature Tc during the cooling operation or the evaporation temperature Te during
the heating operation) is disposed in the outdoor heat exchanger 23. A liquid side
temperature sensor 34 that detects a refrigerant temperature Tco is disposed at the
liquid side of the outdoor heat exchanger 23. A liquid pipe temperature sensor 35
that detects the temperature of the refrigerant (i.e., a liquid pipe temperature T1p)
is disposed at the outlet on the main refrigerant circuit side of the subcooler 25.
The merging circuit 61b of the bypass refrigerant circuit 61 is disposed with a bypass
temperature sensor 63 for detecting the temperature of the refrigerant flowing through
the outlet on the bypass refrigerant circuit side of the subcooler 25. An outdoor
temperature sensor 36 that detects the temperature of the outdoor air that flows into
the unit (i.e., an outdoor temperature Ta) is disposed at an outdoor air intake side
of the outdoor unit 2. In the present embodiment, the suction temperature sensor 31,
the discharge temperature sensor 32, the heat exchanger temperature sensor 33, the
liquid side temperature sensor 34, the liquid pipe temperature sensor 35, the outdoor
temperature sensor 36, and the bypass temperature sensor 63 comprise thermistors.
In addition, the outdoor unit 2 includes an outdoor side controller 37 that controls
the operation of each portion constituting the outdoor unit 2. Additionally, the outdoor
side controller 37 includes a microcomputer and a memory disposed in order to control
the outdoor unit 2, an inverter circuit that controls the motor 21a. and the like,
and is configured such that it can exchange control signals and the like with the
indoor side controllers 47 and 57 of the indoor units 4 and 5 via the transmission
line 8a. In other words, a controller 8 that performs the operation control of the
entire air conditioner 1 is configured by the indoor side controllers 47 and 57, the
outdoor side controller 37, and the transmission line 8a that interconnects the controllers
37, 47, and 57.
[0050] As shown in Figure 2, the controller 8 is connected so as to be able to receive detection
signals of sensors 29 to 36, 44 to 46, 54 to 56, and 63 and also to be able to control
various equipment and valves 21, 22, 24, 28a, 38, 41, 43a, 51, 53a, and 62 based on
these detection signals and the like. In addition, the controller 8 is provided with
an input unit 9a such that a set value for each type of control can be input and changed
and such that the total charged refrigerant quantity including the refrigerant quantity
additionally charged into the refrigerant circuit 10 in an automatic refrigerant charging
operation (described later) and an initial charging quantity can be input. In addition,
a display 9b comprising LEDs and the like is connected to the controller 8. The display
9b is configured to indicate that additional charging is completed in the automatic
refrigerant charging operation (described later) and that a refrigerant leak is detected
in a refrigerant leak detection operation (described later). Here, Figure 2 is a control
block diagram of the air conditioner 1. Note that the input unit 9a is not limited
to the one provided to the controller 8, but may be the one that is connected to the
controller 8 as needed when inputting the additional charging quantity and the total
charged refrigerant quantity.
<REFRIGERANT COMMUNICATION PIPE>
[0051] The refrigerant communication pipes 6 and 7 are refrigerant pipes that are arranged
on site when installing the air conditioner 1 at an installation site such as a building.
As the refrigerant communication pipes 6 and 7, pipes having various lengths and diameters
are used according to the installation conditions such as an installation site, combination
of an outdoor unit and an indoor unit, and the like. Accordingly, for example, when
installing a new air conditioner, in order to calculate the additional charging quantity
of the refrigerant, it is necessary to obtain accurate information regarding the lengths,
diameters and the like of the refrigerant communication pipes 6 and 7. However, such
information management and the calculation itself of the refrigerant quantity are
difficult. In addition, when utilizing an existing pipe to renew an indoor unit and
an outdoor unit, information regarding the lengths, diameters and the like of the
refrigerant communication pipes 6 and 7 may have been lost in some cases.
[0052] As described above, the refrigerant circuit 10 of the air conditioner 1 is configured
by the interconnection of the indoor side refrigerant circuits 10a and 10b, the outdoor
side refrigerant circuit 10c, and the refrigerant communication pipes 6 and 7. In
addition, it can also be that this refrigerant circuit 10 is configured by the bypass
refrigerant circuit 61 and the main refrigerant circuit excluding the bypass refrigerant
circuit 61. Additionally, the controller 8 constituted by the indoor side controllers
47 and 57 and the outdoor side controller 37 allows the air conditioner 1 in the present
embodiment to switch and operate between the cooling operation and the heating operation
by the four-way switching valve 22 and to control each equipment of the outdoor unit
2 and the indoor units 4 and 5 according to the operation load of each of the indoor
units 4 and 5.
(2) OPERATION OF THE AIR CONDITIONER
[0053] Next, the operation of the air conditioner 1 in the present embodiment is described.
[0054] The operation modes of the air conditioner 1 in the present embodiment include: a
normal operation mode where control of constituent equipment of the outdoor unit 2
and the indoor units 4 and 5 is performed according to the operation load of each
of the indoor units 4 and 5; a test operation mode where a test operation is performed
after installation of constituent equipment of the air conditioner 1 is performed
(specifically, it is not limited to after the first installation of equipment: it
also includes, for example, after modification by adding or removing constituent equipment
such as an indoor unit, after repair of damaged equipment); and a refrigerant leak
detection operation mode where, after the test operation is finished and the normal
operation has started, whether or not there is a refrigerant leak from the refrigerant
circuit 10 is judged. The normal operation mode mainly includes the cooling operation
for cooling the room and the heating operation for heating the room. In addition,
the test operation mode mainly includes the automatic refrigerant charging operation
to charge refrigerant into the refrigerant circuit 10, and a pipe volume calculation
process to calculate the volumes of the refrigerant communication pipes 6 and 7.
[0055] Operation in each operation mode of the air conditioner 1 is described below.
<NORMAL OPERATION MODE>
(COOLING OPERATION)
[0056] First, the cooling operation in the normal operation mode is described with reference
to Figures 1 and 2.
[0057] During the cooling operation, the four-way switching valve 22 is in the state represented
by the solid lines in Figure 1, i.e., a state where the discharge side of the compressor
21 is connected to the gas side of the outdoor heat exchanger 23 and also the suction
side of the compressor 21 is connected to the gas sides of the indoor heat exchangers
42 and 52 via the gas side stop valve 27 and the gas refrigerant communication pipe
7. The outdoor expansion valve 38 is in a fully opened state. The liquid side stop
valve 26 and the gas side stop valve 27 are in an opened state. The opening degree
of each of the indoor expansion valves 41 and 51 is adjusted such that a superheat
degree SHr of the refrigerant at the outlets of the indoor heat exchangers 42 and
52 (i.e., the gas sides of the indoor heat exchangers 42 and 52) becomes constant
at a target superheat degree SHrs. In the present embodiment, the superheat degree
SHr of the refrigerant at the outlet of each of the indoor heat exchangers 42 and
52 is detected by subtracting the refrigerant temperature (which corresponds to the
evaporation temperature Te) detected by the liquid side temperature sensors 44 and
54 from the refrigerant temperature detected by the gas side temperature sensors 45
and 55, or is detected by converting the suction pressure Ps of the compressor 21
detected by the suction pressure sensor 29 to saturated temperature corresponding
to the evaporation temperature Te, and subtracting this saturated temperature of the
refrigerant from the refrigerant temperature detected by the gas side temperature
sensors 45 and 55. Note that, although it is not employed in the present embodiment,
a temperature sensor that detects the temperature of the refrigerant flowing through
each of the indoor heat exchangers 42 and 52 may be disposed such that the superheat
degree SHr of the refrigerant at the outlet of each of the indoor heat exchangers
42 and 52 is detected by subtracting the refrigerant temperature corresponding to
the evaporation temperature Te which is detected by this temperature sensor from the
refrigerant temperature detected by the gas side temperature sensors 45 and 55. In
addition, the opening degree of the bypass expansion valve 62 is adjusted such that
a superheat degree SHb of the refrigerant at the outlet on the bypass refrigerant
circuit side of the subcooler 25 becomes a target superheat degree SHbs. In the present
embodiment, the superheat degree SHb of the refrigerant at the outlet on the bypass
refrigerant circuit side of the subcooler 25 is detected by converting the suction
pressure Ps of the compressor 21 detected by the suction pressure sensor 29 to saturated
temperature corresponding to the evaporation temperature Te, and subtracting this
saturated temperature of the refrigerant from the refrigerant temperature detected
by the bypass temperature sensor 63. Note that, although it is not employed in the
present embodiment, a temperature sensor may be disposed at an inlet on the bypass
refrigerant circuit side of the subcooler 25 such that the superheat degree SHb of
the refrigerant at the outlet on the bypass refrigerant circuit side of the subcooler
25 is detected by subtracting the refrigerant temperature detected by this temperature
sensor from the refrigerant temperature detected by the bypass temperature sensor
63.
[0058] When the compressor 21, the outdoor fan 28, the indoor fans 43 and 53 are started
in this state of the refrigerant circuit 10, low-pressure gas refrigerant is sucked
into the compressor 21 and compressed into high-pressure gas refrigerant. Subsequently,
the high-pressure gas refrigerant is sent to the outdoor heat exchanger 23 via the
four-wary switching valve 22, exchanges heat with the outdoor air supplied by the
outdoor fan 28, and becomes condensed into high-pressure liquid refrigerant. Then,
this high-pressure liquid refrigerant passes through the outdoor expansion valve 38,
flows into the subcooler 25, exchanges heat with the refrigerant flowing in the bypass
refrigerant circuit 61, is further cooled, and becomes subcooled. At this time, a
portion of the high-pressure liquid refrigerant condensed in the outdoor heat exchanger
23 is branched into the bypass refrigerant circuit 61 and is depressurized by the
bypass expansion valve 62. Subsequently, it is returned to the suction side of the
compressor 21. Here, the refrigerant that passes through the bypass expansion valve
62 is depressurized close to the suction pressure Ps of the compressor 21 and thereby
a portion of the refrigerant evaporates. Then, the refrigerant flowing from the outlet
of the bypass expansion valve 62 of the bypass refrigerant circuit 61 toward the suction
side of the compressor 21 passes through the subcooler 25 and exchanges heat with
high-pressure liquid refrigerant sent from the outdoor heat exchanger 23 on the main
refrigerant circuit side to the indoor units 4 and 5.
[0059] Then, the high-pressure liquid refrigerant that has become subcooled is sent to the
indoor unites 4 and 5 via the liquid side stop valve 26 and the liquid refrigerant
communication pipe 6. The high-pressure liquid refrigerant sent to the indoor units
4 and 5 is depressurized close to the suction pressure Ps of the compressor 21 by
the indoor expansion valves 41 and 51, becomes refrigerant in a low-pressure gas-liquid
two-phase state, is sent to the indoor heat exchangers 42 and 52, exchanges heat with
the room air in the indoor heat exchangers 42 and 52, and is evaporated into low-pressure
gas refrigerant.
[0060] This low-pressure gas refrigerant is sent to the outdoor unit 2 via the gas refrigerant
communication pipe 7, and flows into the accumulator 24 via the gas side stop valve
27 and the four-way switching valve 22. Then, the low-pressure gas refrigerant that
flowed into the accumulator 24 is again sucked into the compressor 21.
(HEATING OPERATION)
[0061] Next, the heating operation in the normal operation mode is described.
[0062] During the heating operation, the four-way switching valve 22 is in a state represented
by the dotted lines in Figure 1, i.e., a state where the discharge side of the compressor
21 is connected to the gas sides of the indoor heat exchangers 42 and 52 via the gas
side stop valve 27 and the gas refrigerant communication pipe 7 and also the suction
side of the compressor 21 is connected to the gas side of the outdoor heat exchanger
23. The opening degree of the outdoor expansion valve 38 is adjusted so as to be able
to depressurize the refrigerant that flows into the outdoor heat exchanger 23 to a
pressure where the refrigerant can evaporate (i.e., evaporation pressure Pe) in the
outdoor heat exchanger 23. In addition, the liquid side stop valve 26 and the gas
side stop valve 27 are in an opened state. The opening degree of the indoor expansion
valves 41 and 51 is adjusted such that a subcooling degree SCr of the refrigerant
at the outlets of the indoor heat exchangers 42 and 52 becomes constant at the target
subcooling degree SCrs. In the present embodiment, a subcooling degree SCr of the
refrigerant at the outlets of the indoor heat exchangers 42 and 52 is detected by
converting the discharge pressure Pd of the compressor 21 detected by the discharge
pressure sensor 30 to saturated temperature corresponding to the condensation temperature
Tc, and subtracting the refrigerant temperature detected by the liquid side temperature
sensors 44 and 54 from this saturated temperature of the refrigerant. Note that, although
it is not employed in the present embodiment, a temperature sensor that detects the
temperature of the refrigerant flowing through each of the indoor heat exchangers
42 and 52 may be disposed such that the subcooling degree SCr of the refrigerant at
the outlets of the indoor heat exchangers 42 and 52 is detected by subtracting the
refrigerant temperature corresponding to the condensation temperature Tc which is
detected by this temperature sensor from the refrigerant temperature detected by the
liquid side temperature sensors 44 and 54. In addition, the bypass expansion valve
62 is closed.
[0063] When the compressor 21, the outdoor fan 28, the indoor fans 43 and 53 are started
in this state of the refrigerant circuit 10, low-pressure gas refrigerant is sucked
into the compressor 21, compressed into high-pressure gas refrigerant, and sent to
the indoor units 4 and 5 via the four-way switching valve 22, the gas side stop valve
27, and the gas refrigerant communication pipe 7.
[0064] Then, the high-pressure gas refrigerant sent to the indoor units 4 and 5 exchanges
heat with the room air in the indoor heat exchangers 42 and 52 and is condensed into
high-pressure liquid refrigerant. Subsequently, it is depressurized according to the
opening degree of the indoor expansion valves 41 and 51 when passing through the indoor
expansion valves 41 and 51.
[0065] The refrigerant that passed through the indoor expansion valves 41 and 51 is sent
to the outdoor unit 2 via the liquid refrigerant communication pipe 6, is further
depressurized via the liquid side stop valve 26, the subcooler 25, and the outdoor
expansion valve 38, and then flows into the outdoor heat exchanger 23. Then, the refrigerant
in a low-pressure gas-liquid two-phase state that flowed into the outdoor heat exchanger
23 exchanges heat with the outdoor air supplied by the outdoor fan 28, is evaporated
into low-pressure gas refrigerant, and flows into the accumulator 24 via the four-way
switching valve 22. Then, the low-pressure gas refrigerant that flowed into the accumulator
24 is again sucked into the compressor 21.
[0066] Such operation control as described above in the normal operation mode is performed
by the controller 8 (more specifically, the indoor side controllers 47 and 57, the
outdoor side controller 37, and the transmission line 8a that connects between the
controllers 37, 47 and 57) that functions as a normal operation controlling means
to perform the normal operation that includes the cooling operation and the heating
operation.
<TEST OPERATION MODE>
[0067] Next, the test operation mode is described with reference to Figures 1 to 3. Here,
Figure 3 is a flowchart of the test operation mode. In the present embodiment, in
the test operation mode, first, the automatic refrigerant charging operation in Step
51 is performed, and subsequently, the pipe volume calculation process in Step 52
is performed.
[0068] In the present embodiment, an example of a case is described where, the outdoor unit
2 in which the refrigerant is charged in advance and the indoor units 4 and 5 are
installed at an installation site such as a building, and the outdoor unit 2, the
indoor units 4, 5 are interconnected via the liquid refrigerant communication pipe
6 and the gas refrigerant communication pipe 7 to configure the refrigerant circuit
10, and subsequently additional refrigerant is charged into the refrigerant circuit
10 whose refrigerant quantity is insufficient according to the volumes of the liquid
refrigerant communication pipe 6 and the gas refrigerant communication pipe 7.
(STEP S1: AUTOMATIC REFRIGERANT CHARGING OPERATION)
[0069] First, the liquid side stop valve 26 and the gas side stop valve 27 of the outdoor
unit 2 are opened and the refrigerant circuit 10 is filled with the refrigerant that
is charged in the outdoor unit 2 in advance.
[0070] Next, when a worker performing the test operation connects a refrigerant cylinder
for additional charging to a service port (not shown) of the refrigerant circuit 10
and issues a command to start the test operation directly to the controller 8 or remotely
by a remote controller (not shown) and the like, the controller 8 starts the process
from Step S11 to Step S13 shown in Figure 4. Here, Figure 4 is a flowchart of the
automatic refrigerant charging operation.
(STEP S 11: REFRIGERANT QUANTITY JUDGING OPERATION)
[0071] When a command to start the automatic refrigerant charging operation is issued, the
refrigerant circuit 10, with the four-way switching valve 22 of the outdoor unit 2
in the state represented by the solid lines in Figure 1, becomes a state where the
indoor expansion valves 41 and 51 of the indoor units 4 and 5 and the outdoor expansion
valve 38 are opened. Then, the compressor 21, the outdoor fan 28, and the indoor fans
43 and 53 are started, and the cooling operation is forcibly performed in all of the
indoor units 4 and 5 (hereinafter referred to as "all indoor unit operation").
[0072] Consequently, as shown in Figure 5, in the refrigerant circuit 10, the high-pressure
gas refrigerant compressed and discharged in the compressor 21 flows along a flow
path from the compressor 21 to the outdoor heat exchanger 23 that functions as a condenser
(see the portion from the compressor 21 to the outdoor heat exchanger 23 in the hatching
area indicated by the diagonal line in Figure 5); the high-pressure refrigerant that
undergoes phase-change from a gas state to a liquid state by heat exchange with the
outdoor air flows in the outdoor heat exchanger 23 that functions as a condenser (see
the portion corresponding to the outdoor heat exchanger 23 in the hatching area indicated
by the diagonal line and the black-lacquered hatching area in Figure 5); the high-pressure
liquid refrigerant flows along a flow path from the outdoor heat exchanger 23 to the
indoor expansion valves 41 and 51 including the outdoor expansion valve 38, the portion
corresponding to the main refrigerant circuit side of the subcooler 25 and the liquid
refrigerant communication pipe 6, and a flow path from the outdoor heat exchanger
23 to the bypass expansion valve 62 (see the portions from the outdoor heat exchanger
23 to the indoor expansion valves 41 and 51 and to the bypass expansion valve 62 in
the area indicated by the black hatching in Figure 5); the low-pressure refrigerant
that undergoes phase-change from a gas-liquid two-phase state to a gas state by heat
exchange with the room air flows in the portions corresponding to the indoor heat
exchangers 42 and 52 that function as evaporators and the portion corresponding to
the bypass refrigerant circuit side of the subcooler 25 (see the portions corresponding
to the indoor heat exchangers 42 and 52 and the portion corresponding to the subcooler
25 in the area indicated by the lattice hatching and the hatching indicated by the
diagonal line in Figure 5); and the low-pressure gas refrigerant flows along a flow
path from the indoor heat exchangers 42 and 52 to the compressor 21 including the
gas refrigerant communication pipe 7 and the accumulator 24 and a flow path from the
portion corresponding to the bypass refrigerant circuit side of the subcooler 25 to
the compressor 21 (see the portion from the indoor heat exchangers 42 and 52 to the
compressor 21 and the portion from the portion corresponding to the bypass refrigerant
circuit side of the subcooler 25 to the compressor 21 in the hatching area indicated
by the diagonal line in Figure 5). Figure 5 is a schematic diagram to show a state
of the refrigerant flowing in the refrigerant circuit 10 in a refrigerant quantity
judging operation (illustrations of the four-way switching valve 22 and the like are
omitted).
[0073] Next, equipment control as described below is performed to proceed to operation to
stabilize the state of the refrigerant circulating in the refrigerant circuit 10.
Specifically, the indoor expansion valves 41 and 51 are controlled such that the superheat
degree SHr of the indoor heat exchangers 42 and 52 that function as evaporators becomes
constant (hereinafter referred to as "super heat degree control"); the operation capacity
of the compressor 21 is controlled such that an evaporation pressure Pe becomes constant
(hereinafter referred to as "evaporation pressure control"); the air flow rate Wo
of outdoor air supplied to the outdoor heat exchanger 23 by the outdoor fan 28 is
controlled such that a condensation pressure Pc of the refrigerant in the outdoor
heat exchanger 23 becomes constant (hereinafter referred to as "condensation pressure
control"); the operation capacity of the subcooler 25 is controlled such that the
temperature of the refrigerant sent from the subcooler 25 to the indoor expansion
valves 41 and 51 becomes constant (hereinafter referred to as "liquid pipe temperature
control"); and the air flow rate Wr of room air supplied to the indoor heat exchangers
42 and 52 by the indoor fans 43 and 53 is maintained constant such that the evaporation
pressure Pe of the refrigerant is stably controlled by the above described evaporation
pressure control.
[0074] Here, the reason to perform the evaporation pressure control is that the evaporation
pressure Pe of the refrigerant in the indoor heat exchangers 42 and 52 that function
as evaporators is greatly affected by the refrigerant quantity in the indoor heat
exchangers 42 and 52 where low-pressure refrigerant flows while undergoing a phase
change from a gas-liquid two-phase state to a gas state as a result of heat exchange
with the room air (see the portions corresponding to the indoor heat exchangers 42
and 52 in the area indicated by the lattice hatching and hatching indicated by the
diagonal line in Figure 5, which is hereinafter referred to as "evaporator portion
C"). Consequently, here, a state is created in which the refrigerant quantity in the
evaporator portion C changes mainly by the evaporation pressure Pe by causing the
evaporation pressure Pe of the refrigerant in the indoor heat exchangers 42 and 52
to become constant and by stabilizing the state of the refrigerant flowing in the
evaporator portion C as a result of controlling the operation capacity of the compressor
21 by the motor 21a whose rotation frequency Rm is controlled by an inverter. Note
that, the control of the evaporation pressure Pe by the compressor 21 in the present
embodiment is achieved in the following manner: the refrigerant temperature (which
corresponds to the evaporation temperature Te) detected by the liquid side temperature
sensors 44 and 54 of the indoor heat exchangers 42 and 52 is converted to saturation
pressure; the operation capacity of the compressor 21 is controlled such that the
saturation pressure becomes constant at a target low pressure Pes (in other words,
the control to change the rotation frequency Rm of the motor 21a is performed); and
then a refrigerant circulation flow rate Wc flowing in the refrigerant circuit 10
is increased or decreased. Note that, although it is not employed in the present embodiment,
the operation capacity of the compressor 21 may be controlled such that the suction
pressure Ps of the compressor 21 detected by the suction pressure sensor 29, which
is the operation state quantity equivalent to the pressure of the refrigerant at the
evaporation pressure Pe of the refrigerant in the indoor heat exchangers 42 and 52,
becomes constant at the target low pressure Pes, or the saturation temperature (which
corresponds to the evaporation temperature Te) corresponding to the suction pressure
Ps becomes constant at a target low pressure Tes. Also, the operation capacity of
the compressor 21 may be controlled such that the refrigerant temperature (which corresponds
to the evaporation temperature Te) detected by the liquid side temperature sensors
44 and 54 of the indoor heat exchangers 42 and 52 becomes constant at the target low
pressure Tes.
[0075] Then, by performing such evaporation pressure control, the state of the refrigerant
flowing in the refrigerant pipes from the indoor heat exchangers 42 and 52 to the
compressor 21 including the gas refrigerant communication pipe 7 and the accumulator
24 (see the portion from the indoor heat exchangers 42 and 52 to the compressor 21
in the hatching area indicated by the diagonal line in Figure 5, which is hereinafter
referred to as "gas refrigerant distribution portion D") becomes stabilized, creating
a state where the refrigerant quantity in the gas refrigerant distribution portion
D changes mainly by the evaporation pressure Pe (i.e., the suction pressure Ps), which
is the operation state quantity equivalent to the pressure of the refrigerant in the
gas refrigerant distribution portion D.
[0076] In addition, the reason to perform the condensation pressure control is that the
condensation pressure Pc of the refrigerant is greatly affected by the refrigerant
quantity in the outdoor heat exchanger 23 where high-pressure refrigerant flows while
undergoing a phase change from a gas state to a liquid state as a result of heat exchange
with the outdoor air (see the portions corresponding to the outdoor heat exchanger
23 in the area indicated by the diagonal line hatching and the black hatching in Figure
5, which is hereinafter referred to as "condenser portion A"). The condensation pressure
Pc of the refrigerant in the condenser portion A greatly changes due to the effect
of the outdoor temperature Ta. Therefore, the air flow rate Wo of the room air supplied
from the outdoor fan 28 to the outdoor heat exchanger 23 is controlled by the motor
28a, and thereby the condensation pressure Pc of the refrigerant in the outdoor heat
exchanger 23 is maintained constant and the state of the refrigerant flowing in the
condenser portion A is stabilized, creating a state where the refrigerant quantity
in condenser portion A changes mainly by a subcooling degree SCo at the liquid side
of the outdoor heat exchanger 23 (hereinafter regarded as the outlet of the outdoor
heat exchanger 23 in the description regarding the refrigerant quantity judging operation).
Note that, for the control of the condensation pressure Pc by the outdoor fan 28 in
the present embodiment, the discharge pressure Pd of the compressor 21 detected by
the discharge pressure sensor 30, which is the operation state quantity equivalent
to the condensation pressure Pc of the refrigerant in the outdoor heat exchanger 23,
or the temperature of the refrigerant flowing through the outdoor heat exchanger 23
(i.e., the condensation temperature Tc) detected by the heat exchanger temperature
sensor 33 is used.
[0077] Then, by performing such condensation pressure control, the high-pressure liquid
refrigerant flows along a flow path from the outdoor heat exchanger 23 to the indoor
expansion valves 41 and 51 including the outdoor expansion valve 38, the portion on
the main refrigerant circuit side of the subcooler 25, and the liquid refrigerant
communication pipe 6 and a flow path from the outdoor heat exchanger 23 to the bypass
expansion valve 62 of the bypass refrigerant circuit 61; the pressure of the refrigerant
in the portions from the outdoor heat exchanger 23 to the indoor expansion valves
41 and 51 and to the bypass expansion valve 62 (see the area indicated by the black
hatching in Figure 5, which is hereinafter referred to as "liquid refrigerant distribution
portion B") also becomes stabilized; and the liquid refrigerant distribution portion
B is sealed by the liquid refrigerant, thereby becoming a stable state.
[0078] In addition, the reason to perform the liquid pipe temperature control is to prevent
a change in the density of the refrigerant in the refrigerant pipes from the subcooler
25 to the indoor expansion valves 41 and 51 including the liquid refrigerant communication
pipe 6 (see the portion from the subcooler 25 to the indoor expansion valves 41 and
51 in the liquid refrigerant distribution portion B shown in Figure 5). Performance
of the subcooler 25 is controlled by increasing or decreasing the flow rate of the
refrigerant flowing in the bypass refrigerant circuit 61 such that the refrigerant
temperature Tlp detected by the liquid pipe temperature sensor 35 disposed at the
outlet on the main refrigerant circuit side of the subcooler 25 becomes constant at
a target liquid pipe temperature Tlps, and by adjusting the quantity of heat exchange
between the refrigerant flowing through the main refrigerant circuit side and the
refrigerant flowing through the bypass refrigerant circuit side of the subcooler 25.
Note that, the flow rate of the refrigerant flowing in the bypass refrigerant circuit
61 is increased or decreased by adjustment of the opening degree of the bypass expansion
valve 62. In this way, the liquid pipe temperature control is achieved in which the
refrigerant temperature in the refrigerant pipes from the subcooler 25 to the indoor
expansion valves 41 and 51 including the liquid refrigerant communication pipe 6 becomes
constant.
[0079] Then, by performing such liquid pipe temperature constant control, even when the
refrigerant temperature Tco at the outlet of the outdoor heat exchanger 23 (i.e.,
the subcooling degree SCo of the refrigerant at the outlet of the outdoor heat exchanger
23) changes along with a gradual increase in the refrigerant quantity in the refrigerant
circuit 10 by charging refrigerant into the refrigerant circuit 10, the effect of
a change in the refrigerant temperature Tco at the outlet of the outdoor heat exchanger
23 will remain only within the refrigerant pipes from the outlet of the outdoor heat
exchanger 23 to the subcooler 25, and the effect will not extend to the refrigerant
pipes from the subcooler 25 to the indoor expansion valves 41 and 51 including the
liquid refrigerant communication pipe 6 in the liquid refrigerant distribution portion
B.
[0080] Further, the reason to perform the superheat degree control is because the refrigerant
quantity in the evaporator portion C greatly affects the quality of wet vapor of the
refrigerant at the outlets of the indoor heat exchangers 42 and 52. The superheat
degree SHr of the refrigerant at the outlets of the indoor heat exchangers 42 and
52 is controlled such that the superheat degree SHr of the refrigerant at the gas
sides of the indoor heat exchangers 42 and 52 (hereinafter regarded as the outlets
of the indoor heat exchangers 42 and 52 in the description regarding the refrigerant
quantity judging operation) becomes constant at the target superheat degree SHrs (in
other words, the gas refrigerant at the outlets of the indoor heat exchangers 42 and
52 is in a superheat state) by controlling the opening degree of the indoor expansion
valves 41 and 51, and thereby the state of the refrigerant flowing in the evaporator
portion C is stabilized.
[0081] Consequently, by performing such superheat degree control, a state is created in
which the gas refrigerant reliably flows into the gas refrigerant communication portion
D.
[0082] By various control described above, the state of the refrigerant circulating in the
refrigerant circuit 10 becomes stabilized, and the distribution of the refrigerant
quantity in the refrigerant circuit 10 becomes constant. Therefore, when refrigerant
starts to be charged into the refrigerant circuit 10 by additional refrigerant charging,
which is subsequently performed, it is possible to create a state where a change in
the refrigerant quantity in the refrigerant circuit 10 mainly appears as a change
of the refrigerant quantity in the outdoor heat exchanger 23 (hereinafter this operation
is referred to as "refrigerant quantity judging operation").
[0083] Such operation control as described above is performed as the process in Step S11
by the controller 8 (more specifically, the indoor side controllers 47, 57, the outdoor
side controller 37, and the transmission line 8a that connects between the controllers
37, 47 and 57) that functions as a normal operation controlling means to perform the
refrigerant quantity judging operation.
(STEP S12: REFRIGERANT QUANTITY CALCULATION)
[0084] Next, additional refrigerant is charged into the refrigerant circuit 10 during performing
the above described refrigerant quantity judging operation. At this time, the controller
8 that functions as refrigerant quantity calculating means calculates the refrigerant
quantity in the refrigerant circuit 10 from the operation state quantity of constituent
equipment or refrigerant flowing in the refrigerant circuit 10 during additional refrigerant
charging in Step S 12.
[0085] First, the refrigerant quantity calculating means in the present embodiment is described.
The refrigerant quantity calculating means divides the refrigerant circuit 10 into
a plurality of portions, calculates the refrigerant quantity for each divided portions,
and thereby calculates the refrigerant quantity in the refrigerant circuit 10. More
specifically, a relational expression between the refrigerant quantity in each portion
and the operation state quantity of constituent equipment or refrigerant flowing in
the refrigerant circuit 10 is set for each divided portion, and the refrigerant quantity
in each portion can be calculated by using these relational expressions. In the present
embodiment, in a state where the four-way switching valve 22 is represented by the
solid lines in Figure 1, i.e., a state where the discharge side of the compressor
21 is connected to the gas side of the outdoor heat exchanger 23 and where the suction
side of the compressor 21 is connected to the outlets of the indoor heat exchangers
42 and 52 via the gas side stop valve 27 and the gas refrigerant communication pipe
7, the refrigerant circuit 10 is divided into the following portions and a relational
expression is set for each portion: a portion corresponding to the compressor 21 and
a portion from the compressor 21 to the outdoor heat exchanger 23 including the four-way
switching valve 22 (not shown in Figure 5) (hereinafter referred to as "high-pressure
gas pipe portion E"); a portion corresponding to the outdoor heat exchanger 23 (i.e.,
the condenser portion A); a portion from the outdoor heat exchanger 23 to the subcooler
25 and an inlet side half of the portion corresponding to the main refrigerant circuit
side of the subcooler 25 in the liquid refrigerant distribution portion B (hereinafter
referred to as "high temperature side liquid pipe portion B1"); an outlet side half
of a portion corresponding to the main refrigerant circuit side of the subcooler 25
and a portion from the subcooler 25 to the liquid side stop valve 26 (not shown in
Figure 5) in the liquid refrigerant distribution portion B (hereinafter referred to
as "low temperature side liquid pipe portion B2"); a portion corresponding to the
liquid refrigerant communication pipe 6 in the liquid refrigerant distribution portion
B (hereinafter referred to as "liquid refrigerant communication pipe portion B3");
a portion from the liquid refrigerant communication pipe 6 in the liquid refrigerant
distribution portion B to the gas refrigerant communication pipe 7 in the gas refrigerant
distribution portion D including portions corresponding to the indoor expansion valves
41 and 51 and the indoor heat exchangers 42 and 52 (i.e., the evaporator portion C)
(hereinafter referred to as "indoor unit portion F"); a portion corresponding to the
gas refrigerant communication pipe 7 in the gas refrigerant distribution portion D
(hereinafter referred to as "gas refrigerant communication pipe portion G"); a portion
from the gas side stop valve 27 (not shown in Figure 5) in the gas refrigerant distribution
portion D to the compressor 21 including the four-way switching valve 22 and the accumulator
24 (hereinafter referred to as "low-pressure gas pipe portion H"); and a portion from
the high temperature side liquid pipe portion B 1 in the liquid refrigerant distribution
portion B to the low-pressure gas pipe portion H including the bypass expansion valve
62 and a portion corresponding to the bypass refrigerant circuit side of the subcooler
25 (hereinafter referred to as "bypass circuit portion I"). Next, the relational expressions
set for each portion described above are described.
[0086] In the present embodiment, a relational expression between a refrigerant quantity
Mog1 in the high-pressure gas pipe portion. E and the operation state quantity of
constituent equipment or refrigerant flowing in the refrigerant circuit 10 is, for
example, expressed by

which is a function expression in which a volume Vog1 of the high-pressure gas pipe
portion E in the outdoor unit 2 is multiplied by the density pd of the refrigerant
in high-pressure gas pipe portion E. Note that, the volume Vog1 of the high-pressure
gas pipe portion E is a value that is known prior to installation of the outdoor unit
2 at the installation site and is stored in advance in the memory of the controller
8. In addition, a density ρd of the refrigerant in the high-pressure gas pipe portion
E is obtained by converting the discharge temperature Td and the discharge pressure
Pd.
[0087] A relational expression between a refrigerant quantity Mc in the condenser portion
A and the operation state quantity of constituent equipment or refrigerant flowing
in the refrigerant circuit 10 is, for example, expressed by

which is a function expression of the outdoor temperature Ta, the condensation temperature
Tc, a compressor discharge superheat degree SHm, the refrigerant circulation flow
rate Wc, the saturated liquid density ρc of the refrigerant in the outdoor heat exchanger
23, and the density ρco of the refrigerant at the outlet of the outdoor heat exchanger
23. Note that, the parameters kc1 to kc7 in the above described relational expression
are derived from a regression analysis of results of tests and detailed simulations
and are stored in advance in the memory of the controller 8. In addition, the compressor
discharge superheat degree SHm is a superheat degree of the refrigerant at the discharge
side of the compressor, and is obtained by converting the discharge pressure Pd to
refrigerant saturation temperature and subtracting this refrigerant saturation temperature
from the discharge temperature Td. The refrigerant circulation flow rate Wc is expressed
as a function of the evaporation temperature Te and the condensation temperature Tc
(i.e., Wc = f(Te, Tc)). A saturated liquid density ρc of the refrigerant is obtained
by converting the condensation temperature Tc. A density ρco of the refrigerant at
the outlet of the outdoor heat exchanger 23 is obtained by converting the condensation
pressure Pc which is obtained by converting the condensation temperature Tc and the
refrigerant temperature Tco.
[0088] A relational expression between a refrigerant quantity Mol1 in the high temperature
liquid pipe portion B1 and the operation state quantity of constituent equipment or
refrigerant flowing in the refrigerant circuit 10 is, for example, expressed by

which is a function expression in which a volume Vol1 of the high temperature liquid
pipe portion B1 in the outdoor unit 2 is multiplied by the density ρco of the refrigerant
in the high temperature liquid pipe portion B1 (i.e., the above described density
of the refrigerant at the outlet of the outdoor heat exchanger 23). Note that, the
volume Vol1 of the high-pressure liquid pipe portion B1 is a value that is known prior
to installation of the outdoor unit 2 at the installation site and is stored in advance
in the memory of the controller 8.
[0089] A relational expression between a refrigerant quantity Mol2 in the low temperature
liquid pipe portion B2 and the operation state quantity of constituent equipment or
refrigerant flowing in the refrigerant circuit 10 is, for example, expressed by

which is a function expression in which a volume Vol2 of the low temperature liquid
pipe portion B2 in the outdoor unit 2 is multiplied by a density ρlp of the refrigerant
in the low temperature liquid pipe portion B2. Note that, the volume Vol2 of the low
temperature liquid pipe portion B2 is a value that is known prior to installation
of the outdoor unit 2 at the installation site and is stored in advance in the memory
of the controller 8. In addition, the density ρlp of the refrigerant in the low temperature
liquid pipe portion B2 is the density of the refrigerant at the outlet of the subcooler
25, and is obtained by converting the condensation pressure Pc and the refrigerant
temperature Tlp at the outlet of the subcooler 25.
[0090] A relational expression between a refrigerant quantity Mlp in the liquid refrigerant
communication pipe portion B3 and the operation state quantity of constituent equipment
or refrigerant flowing in the refrigerant circuit 10 is, for example, expressed by

which is a function expression in which a volume Vlp of the liquid refrigerant communication
pipe 6 is multiplied by the density ρlp of the refrigerant in the liquid refrigerant
communication pipe portion B3 (i.e., the density of the refrigerant at the outlet
of the subcooler 25).
[0091] A relational expression between a refrigerant quantity Mr in the indoor unit portion
F and the operation state quantity of constituent equipment or refrigerant flowing
in the refrigerant circuit 10 is, for example, expressed by

which is a function expression of the refrigerant temperature Tlp at the outlet of
the subcooler 25, a temperature difference ΔT in which the evaporation temperature
Te is subtracted from the room temperature Tr, the superheat degree SHr of the refrigerant
at the outlets of the indoor heat exchangers 42 and 52, and the air flow rate Wr of
the indoor fans 43 and 53. Note that, the parameters kr1 to kr5 in the above described
relational expression are derived from a regression analysis of results of tests and
detailed simulations and are stored in advance in the memory of the controller 8.
Note that, here, the relational expression for the refrigerant quantity Mr is set
for each of the two indoor units 4 and 5, and the total refrigerant quantity in the
indoor unit portion F is calculated by adding the refrigerant quantity Mr in the indoor
unit 4 to the refrigerant quantity Mr in the indoor unit 5. Note that relational expressions
in each portion having parameters kr1 to kr5 with different values will be used when
the indoor unit 4 and the indoor unit 5 are different in terms of the model and the
capacity.
[0092] A relational expression between a refrigerant quantity Mgp in the gas refrigerant
communication pipe portion G and the operation state quantity of constituent equipment
or refrigerant flowing in the refrigerant circuit 10 is, for example, expressed by

which is a function expression in which a volume Vgp of the gas refrigerant communication
pipe 7 is multiplied by a density pgp of the refrigerant in the gas refrigerant communication
pipe portion H. In addition, the density pgp of the refrigerant in the gas refrigerant
communication pipe portion G is an average value between a density ps of the refrigerant
at the suction side of the compressor 21 and a density peo of the refrigerant at the
outlets of the indoor heat exchangers 42 and 52 (i.e., the inlet of the gas refrigerant
communication pipe 7). The density ps of the refrigerant is obtained by converting
the suction pressure Ps and the suction temperature Ts, and a density peo of the refrigerant
is obtained by converting the evaporation pressure Pe, which is a converted value
of the evaporation temperature Te, and the outlet temperature Teo of the indoor heat
exchangers 42 and 52.
[0093] A relational expression between a refrigerant quantity Mog2 in the low-pressure gas
pipe portion H and the operation state quantity of constituent equipment or refrigerant
flowing in the refrigerant circuit 10 is, for example, expressed by

which is a function expression in which a volume Vog2 of the low-pressure gas pipe
portion H in the outdoor unit 2 is multiplied by the density ps of the refrigerant
in the low-pressure gas pipe portion H. Note that, the volume Vog2 of the low-pressure
gas pipe portion H is a value that is known prior to shipment to the installation
site and is stored in advance in the memory of the controller 8.
[0094] A relational expression between a refrigerant quantity Mob in the bypass circuit
portion I and the operation state quantity of constituent equipment or refrigerant
flowing in the refrigerant circuit 10 is, for example, expressed by

which is a function expression of a density ρco of the refrigerant at the outlet of
the outdoor heat exchanger 23, and the density ps and evaporation pressure Pe of the
refrigerant at the outlet on the bypass circuit side of the subcooler 25. Note that,
the parameters kob1 to kob3 in the above described relational expression are derived
from a regression analysis of results of tests and detailed simulations and are stored
in advance in the memory of the controller 8. In addition, the refrigerant quantity
Mob of the bypass circuit portion I may be calculated using a simpler relational expression
because the refrigerant quantity there is smaller compared to the other portions.
For example, it is expressed as follows;

which is a function expression in which a volume Vob of the bypass circuit portion
I is multiplied by the saturated liquid density pe at the portion corresponding to
the bypass circuit side of the subcooler 25 and a correct coefficient kob 5. Note
that, the volume Vob of the bypass circuit portion I is a value that is known prior
to installation of the outdoor unit 2 at the installation site and is stored in advance
in the memory of the controller 8. In addition, the saturated liquid density pe at
the portion corresponding to the bypass circuit side of the subcooler 25 is obtained
by converting the suction pressure Ps or the evaporation temperature Te.
[0095] Note that, in the present embodiment, one outdoor unit 2 is provided. However, when
a plurality of outdoor units are connected, as for the refrigerant quantity in the
outdoor unit such as Mog1, Mc, Mol1, Mol2, Mog2, and Mob, the relational expression
for the refrigerant quantity in each portion is set for each of the plurality of outdoor
units, and the entire refrigerant quantity in the outdoor units is calculated by adding
the refrigerant quantity in each portion of the plurality of the outdoor units.
[0096] As described above, in the present embodiment, by using the relational expressions
for each portion in the refrigerant circuit 10, the refrigerant quantity in each portion
is calculated from the operation state quantity of constituent equipment or refrigerant
flowing in the refrigerant circuit 10 in the refrigerant quantity judging operation,
and thereby the refrigerant quantity in the refrigerant circuit 10 can be calculated.
[0097] Further, this Step S12 is repeated until the condition for judging the adequacy of
the refrigerant quantity in the below described Step S13 is satisfied. Therefore,
in the period from the start to the completion of additional refrigerant charging,
the refrigerant quantity in each portion is calculated from the operation state quantity
during refrigerant charging by using the relational expressions for each portion in
the refrigerant circuit 10. More specifically, a refrigerant quantity Mo in the outdoor
unit 2 and the refrigerant quantity Mr in each of the indoor units 4 and 5 (i.e.,
the refrigerant quantity in each portion in the refrigerant circuit 10 excluding the
refrigerant communication pipes 6 and 7) necessary for judgment of the adequacy of
the refrigerant quantity in the below described Step S 13 are calculated. Here, the
refrigerant quantity Mo in the outdoor unit 2 is calculated by adding Mog1, Mc, Mol1,
Mol2, Mog2, and Mob described above, each of which is the refrigerant quantity in
each portion in the outdoor unit 2.
[0098] In this way, the process in Step S12 is performed by the controller 8 that functions
as the refrigerant quantity calculating means for calculating the refrigerant quantity
in each portion in the refrigerant circuit 10 from the operation state quantity of
constituent equipment or refrigerant flowing in the refrigerant circuit 10 in the
automatic refrigerant charging operation.
(STEP S13: JUDGMENT OF THE ADEQUACY OF THE REFRIGERANT QUANTITY)
[0099] As described above, when additional refrigerant charging into the refrigerant circuit
10 starts, the refrigerant quantity in the refrigerant circuit 10 gradually increases.
Here, when the volumes of the refrigerant communication pipes 6 and 7 are unknown,
the refrigerant quantity that should be charged into the refrigerant circuit 10 after
additional refrigerant charging cannot be prescribed as a total charging refrigerant
quantity Mt that is a refrigerant quantity in the entire refrigerant circuit 10. However,
when the focus is placed only on the outdoor unit 2 and the indoor units 4 and 5 (i.e.,
the refrigerant circuit 10 excluding the refrigerant communication pipes 6 and 7),
it is possible to know in advance the optimal refrigerant quantity Mo in the outdoor
unit 2 and the optimal refrigerant quantities Mr in the indoor units 4 and 5 by tests
and detailed simulations. Therefore, additional refrigerant can be charged by the
following manner: a refrigerant quantity that satisfies these optimal refrigerant
quantities is stored in advance in the memory of the controller 8 as a target charging
value Ms; the refrigerant quantity Mo in the outdoor unit 2 and the refrigerant quantities
Mr in the indoor units 4 and 5 are calculated from the operation state quantity of
constituent equipment or refrigerant flowing in the refrigerant circuit 10 in the
automatic refrigerant charging operation by using the above described relational expressions;
and additional refrigerant is charged until a value (hereinafter referred to as an
inside-unit refrigerant quantity Mu) of the refrigerant quantity obtained by adding
the refrigerant quantity Mo to the refrigerant quantities Mr (i.e., the refrigerant
quantity in the refrigerant circuit 10 excluding the refrigerant communication pipes
6 and 7) reaches the target charging value Ms. In other words, Step S13 is a process
to judge the adequacy of the refrigerant quantity charged in the refrigerant circuit
10, by additional refrigerant charging by judging whether or not the inside-unit refrigerant
quantity Mu in the automatic refrigerant charging operation has reached the target
charging value Ms.
[0100] Further, in Step S13, when a value of the inside-unit refrigerant quantity Mu is
smaller than the target charging value Ms and additional refrigerant charging has
not been completed, the process in Step S13 is repeated until the target charging
value Ms is reached. In addition, when the inside-unit refrigerant quantity Mu reaches
the target charging value Ms, the display 9b displays a message indicating that the
additional refrigerant charging is completed, the refrigerant supply from the refrigerant
cylinder is stopped, and Step S 1 as the automatic refrigerant charging operation
process is completed.
[0101] In this way, the process in Step S 13 is performed by the controller 8 that functions
as an automatic refrigerant charging judging means which is one of the refrigerant
quantity judging means to judge the adequacy of the refrigerant quantity in the refrigerant
circuit 10 in the refrigerant quantity judging operation of the automatic refrigerant
charging operation (i.e., to judge whether or not the refrigerant quantity has reached
the target charging value Ms). Then, by this automatic refrigerant charging operation,
a state is reached where the total charged refrigerant quantity Mt is charged in the
refrigerant circuit 10. the total charged refrigerant quantity Mt is the refrigerant
quantity obtained by adding an additional charging quantity Ma that is a refrigerant
quantity additionally charged to an initial charging quantity Mi that is a refrigerant
quantity that has been charged into the refrigerant circuit 10 before the automatic
refrigerant charging operation (i.e., the refrigerant quantity charged in the outdoor
unit 2 in advance).
(STEP S2: PIPE VOLUME CALCULATION)
[0102] When the above described automatic refrigerant charging operation in Step S1 is completed,
the process proceeds to the pipe volume calculation process in Step S2. In this pipe
volume calculation process, the process from Steps S21 to S24 shown in Figure 6 is
performed by the controller 8 that functions as a pipe volume calculating means that
calculates the volumes of the refrigerant communication pipes 6 and 7 based on the
additional charging quantity Ma. Here, Figure 6 is a flowchart of the pipe volume
calculation process.
(STEPS S21, S22: STORING DATA FROM THE AUTOMATIC REFRIGERANT CHARGING OPERATION AND
INPUTTING ADDITIONAL CHARGING QUANTITY)
[0103] In Step S21, the operation data from the above described automatic refrigerant charging
operation is stored in the memory of the controller 8 such that the density of the
refrigerant flowing through the refrigerant communication pipes 6 and 7 can be calculated
in the below described Step S23. Here, the data stored in the memory of the controller
8 includes: condensation pressure Pc and temperature Tlp of the refrigerant at the
outlet of the subcooler 25 required for the calculation of the density ρlp of the
refrigerant in the liquid refrigerant communication pipe portion B3; suction pressure
Ps, suction temperature Ts, evaporation pressure Pe, and outlet temperature Teo required
for the calculation of the density pgp of the refrigerant in the gas refrigerant communication
pipe portion H; and the inside-unit refrigerant quantity Mu at the time of completion
of the automatic refrigerant charging operation.
[0104] In Step S22, a value of the additional charging quantity Ma or a value of the total
charged refrigerant quantity Mt including the additional charging quantity Ma is input
in the memory of the controller 8 through the input unit 9a. Here, the additional
charging quantity Ma is a value of the refrigerant quantity obtained from the change
in the weight of the refrigerant cylinder and the like in the automatic refrigerant
charging operation. The additional charging quantity Ma may be manually input in the
memory of the controller 8 through the input unit 9a provided in the controller 8
by an operator or the like who performs additional charging, or may be automatically
input in the memory of the controller 8 by connecting a scale for measuring the change
in the weight of the refrigerant cylinder as the input unit 9a to the controller 8.
[0105] Note that, here, the process of Steps S21 and S22 is performed in the process of
the pipe volume calculation, however, the process may be performed in the process
of the above described automatic refrigerant charging operation.
(STEPS S23, S24: CALCULATION OF COMMUNICATION PIPE REFRIGERANT QUANTITY, CALCULATION
OF DENSITY, CALCULATION OF PIPE VOLUME)
[0106] In Step S23, first, the total charged refrigerant quantity Mt, which is the refrigerant
quantity in the entire refrigerant circuit 10 immediately after the automatic refrigerant
charging operation, is obtained by adding the additional charging quantity Ma input
in the controller 8 in Step S22 to the initial charging quantity Mi that is the refrigerant
quantity that has been charged in the refrigerant circuit 10 before the automatic
refrigerant charging operation. Here, the initial charging quantity Mi is stored in
the memory of the controller 8. Next, the inside-unit refrigerant quantity Mu (or
the target charging quantity Ms) stored in the controller 8 in Step S21 is subtracted
from the total charged refrigerant quantity Mt, and thereby the communication pipe
refrigerant quantity Mp that is the refrigerant quantity in the refrigerant communication
pipes 6 and 7 is determined.
[0107] In addition, in Step S23, based on the condensation pressure Pc and the temperature
Tlp of the refrigerant at the outlet of the subcooler 25 stored in the controller
8 in Step S21, the density ρlp of liquid refrigerant flowing through the liquid refrigerant
communication pipe portion B3 (i.e., the liquid refrigerant communication pipe 6)
during the automatic refrigerant charging operation is determined. In addition, based
on the suction pressure Ps, the suction temperature Ts, the evaporation pressure Pe,
and the outlet temperature Teo stored in the controller 8 in Step S21, the density
pgp of gas refrigerant flowing through the gas refrigerant communication pipe portion
H (i.e., the gas refrigerant communication pipe 7) during the automatic refrigerant
charging operation is determined (note that the calculation of these densities ρlp
and pgp is the same as the calculation of the densities ρlp and pgp for the calculation
of the refrigerant quantity in Step S12 of the above described automatic refrigerant
charging operation, and thus the description thereof is omitted here).
[0108] In Step S24, the volumes of the refrigerant communication pipes 6 and 7 (more specifically,
the volume Vlp of the liquid refrigerant communication pipe 6 and the volume Vgp of
the gas refrigerant communication pipe) are calculated based on the communication
pipe refrigerant quantity Mp and the densities ρlp and pgp determined in Step S23.
[0109] Here, first, the calculation method of the volumes of the refrigerant communication
pipes 6 and 7 in the present embodiment is described.
[0110] The liquid refrigerant communication pipe 6 and the gas refrigerant communication
pipe 7 are provided so as to interconnect the indoor units 4 and 5 and the outdoor
unit 2, so that these pipes have substantially the same pipe length but different
pipe diameters, i.e., different flow passage cross-sectional areas, due to the different
densities of the refrigerant flowing through the pipes. Therefore, the volume ratio
between the liquid refrigerant communication pipe 6 and the gas refrigerant communication
pipe 7 (in the description below , a value of Vgp/Vlp in which the gas refrigerant
communication pipe Vgp is divided by the volume Vlp of liquid refrigerant communication
pipe 6 is referred to as a volume ratio Rv) will substantially correspond to the flow
passage cross-sectional area ratio between these pipes, and furthermore, this volume
ratio Rv will be within a certain range because the flow passage cross-sectional area
ratio is predetermined based on the capacities and models of the indoor units 4 and
5 and the outdoor unit 2.
[0111] Further, if the volume ratio Rv between the liquid refrigerant communication pipe
6 and the gas refrigerant communication pipe 7 is known, a total value obtained by
adding a value of the multiplication between the volume Vlp of the liquid refrigerant
communication pipe 6 and the liquid refrigerant density ρlp to a value of the multiplication
between the volume Vgp of the gas refrigerant communication pipe 7 and the gas refrigerant
density pgp will be equal to the communication pipe refrigerant quantity Mp, as in
the following expression:

Thereby, the volume Vlp of the liquid refrigerant communication pipe can be calculated
as follows:

and the volume Vgp of the gas refrigerant communication pipe 7 can be calculated as
follows:

[0112] In addition, in the present embodiment, the volume ratio Rv between the liquid refrigerant
communication pipe 6 and the gas refrigerant communication pipe 7 is stored in the
memory of the controller 8 in advance as a value corresponding to the capacities and
models of the indoor units 4, 5 and the outdoor unit 2, then the volumes of the refrigerant
communication pipes 6 and 7 (more specifically, the volume Vlp of the liquid refrigerant
communication pipe 6 and the volume Vgp of the gas refrigerant communication pipe)
are calculated using the above described calculation equations, based on the communication
pipe refrigerant quantity Mp, the densities ρlp and pgp determined in Step S23 and
the volume ratio Rv.
<REFRIGERANT LEAK DETECTION OPERATION MODE>
[0113] Next, the refrigerant leak detection operation mode is described with reference to
Figures 1, 2, 5, and 7. Here, Figure 7 is a flowchart of the refrigerant leak detection
operation mode.
[0114] In the present embodiment, an example of a case is described where, whether or not
the refrigerant in the refrigerant circuit 10 is leaking to the outside due to an
unforeseen factor is detected periodically (for example, during a period of time such
as on a holiday or in the middle of the night when air conditioning is not needed).
(STEP S31: REFRIGERANT QUANTITY JUDGING OPERATION)
[0115] First, when operation in the normal operation mode such as the above described cooling
operation and heating operation has gone on for a certain period of time (for example,
half a year to a year), the normal operation mode is automatically or manually switched
to the refrigerant leak detection operation mode, and as is the case with the refrigerant
quantity judging operation of the initial refrigerant quantity detection operation,
the refrigerant quantity judging operation, including the all indoor unit operation,
condensation pressure control, liquid pipe temperature control, superheat degree control,
and evaporation pressure control, is performed. Here, as a rule, values that are the
same as the target values in Step S11 of the refrigerant quantity judging operation
of the automatic refrigerant charging operation are used for the target liquid pipe
temperature Tlps in the liquid pipe temperature control, the target superheat degree
SHrs in the superheat degree control, and the target low pressure Pes in the evaporation
pressure control.
[0116] Note that, this refrigerant quantity judging operation is performed for each time
the refrigerant leak detection operation is performed. Even when the refrigerant temperature
Tco at the outlet of the outdoor heat exchanger 23 fluctuates due to the different
operating conditions, for example, such as when the condensation pressure Pc is different
or when there is a refrigerant leak, the refrigerant temperature Tlp in the liquid
refrigerant communication pipe 6 is maintained constant at the same target liquid
pipe temperature Tlps by the liquid pipe temperature control.
[0117] In this way, the process in Step S31 is performed by the controller 8 that functions
as the refrigerant quantity judging operation controlling means for performing the
refrigerant quantity judging operation, including the all indoor unit operation, condensation
pressure control, liquid pipe temperature control, superheat degree control, and evaporation
pressure control.
(STEP S32: REFRIGERANT QUANTITY CALCULATION)
[0118] Next, the refrigerant quantity in the refrigerant circuit 10 is calculated from the
operation state quantity of constituent equipment or refrigerant flowing in the refrigerant
circuit 10 in the refrigerant leak detection operation in Step S32 by the controller
8 that functions as the refrigerant quantity calculating means during performing the
above described refrigerant quantity judging operation. Calculation of the refrigerant
quantity in the refrigerant circuit 10 is performed by using the above described relational
expression between the refrigerant quantity in each portion in the refrigerant circuit
10 and the operation state quantity of constituent equipment or refrigerant flowing
in the refrigerant circuit 10. However, at this time, the volumes Vlp and Vgp of the
refrigerant communication pipes 6 and 7, which were unknown at the time of after installation
of constituent equipment of the air conditioner 1, have been calculated and the values
thereof are known by the above described pipe volume calculation process. Thus, by
multiplying the volumes Vlp and Vgp of the refrigerant communication pipes 6 and 7
by the density of the refrigerant, the refrigerant quantities Mlp, Mgp in the refrigerant
communication pipes 6 and 7 can be calculated, and further by adding the refrigerant
quantity in each of the other portions (for the calculation of the refrigerant in
each of other portions, see Step S12 of the automatic refrigerant charging operation),
the refrigerant quantity in the entire refrigerant circuit 10 (hereinafter referred
to as "tonal calculated refrigerant quantity M") can be calculated,
[0119] Here, as described above, the refrigerant temperature Tlp in the liquid refrigerant
communication pipe 6 is maintained constant at the target liquid pipe temperature
Tlps by the liquid pipe temperature control. Therefore, regardless the difference
in the operating conditions for the refrigerant leak detection operation, the refrigerant
quantity Mlp in the liquid refrigerant communication pipe portion B3 will be maintained
constant even when the refrigerant temperature Tco at the outlet of the outdoor heat
exchanger 23 changes.
[0120] In this way, the process in Step S32 is performed by the controller 8 that functions
as the refrigerant quantity calculating means for calculating the refrigerant quantity
at each portion in the refrigerant circuit 10 from the operation state quantity of
constituent equipment or refrigerant flowing in the refrigerant circuit 10 in the
refrigerant leak detection operation.
(STEPS S33, S34: ADEQUACY JUDGMENT OF THE REFRIGERANT QUANTITY, WARNING DISPLAY)
[0121] When refrigerant leaks from the refrigerant circuit 10, the refrigerant quantity
in the refrigerant circuit 10 decreases. Then, when the refrigerant quantity in the
refrigerant circuit 10 decreases, mainly, a tendency of a decrease in the subcooling
degree SC
o at the outlet of the outdoor heat exchanger 23 appears. Along with this, the refrigerant
quantity Mc in the outdoor heat exchanger 23 decreases, and the refrigerant quantities
in other portions tend to be maintained substantially constant. Consequently, when
there is a refrigerant leak from the refrigerant circuit 10, the total calculated
refrigerant quantity M calculated in the above described Step S32 is smaller than
the total charged refrigerant quantity Mt that is the refrigerant quantity in the
entire refrigerant circuit 10 immediately after the automatic refrigerant charging
operation is completed and that serves as a reference refrigerant quantity for judging
whether or not there is a refrigerant leak; whereas when there is no refrigerant leak
from the refrigerant circuit 10, the total calculated refrigerant quantity M has substantially
the same value as the total charged refrigerant quantity Mt.
[0122] By utilizing the above described characteristics, whether or not there is a refrigerant
leak is judged in Step S33. When it is judged in Step S33 that there is no refrigerant
leak from the refrigerant circuit 10, the refrigerant leak detection operation mode
is finished.
[0123] On the other hand, when it is judged in Step S33 that there is a refrigerant leak
from the refrigerant circuit 10, the process proceeds to Step S34, and a warning indicating
that a refrigerant leak is detected is displayed on the display 9b. Subsequently,
the refrigerant leak detection operation mode is finished.
[0124] In this way, the process from Steps S32 to S34 is performed by the controller 8 that
functions as the refrigerant leak detection means, which is one of the refrigerant
quantity judging means, and which detects whether or not there is a refrigerant leak
by judging the adequacy of the refrigerant quantity in the refrigerant circuit 10
during performing the refrigerant quantity judging operation in the refrigerant leak
detection operation mode.
[0125] As described above, in the air conditioner 1 in the present embodiment, the controller
8 functions as the refrigerant quantity judging operation means, the refrigerant quantity
calculating means, the refrigerant quantity judging means, and the pipe volume calculating
means, and thereby configures the refrigerant quantity judging system for judging
the adequacy of the refrigerant quantity charged into the refrigerant circuit 10.
(3) CHARACTERISTICS OF THE AIR CONDITIONER
[0126] The air conditioner 1 in the present embodiment has the following characteristics.
(A)
In the air conditioner 1 of the present embodiment, the volume of each of the refrigerant
communication pipes 6 and 7 is calculated based on the additional charging quantity
Ma that is the refrigerant quantity to be additionally charged after the refrigerant
circuit 10 is configured by the interconnection of the outdoor unit 2 and the indoor
units 4 and 5 via the refrigerant communication pipes 6 and 7. Thus, even if the volumes
of the refrigerant communication pipes 6 and 7 are unknown, it is possible to calculate
the volumes of the refrigerant communication pipes 6 and 7 by inputting a value of
the additional charging quantity Ma. Accordingly, it is possible to determine the
volume of each of the refrigerant communication pipes 6 and 7 while minimizing the
labor of inputting information on the refrigerant communication pipes 6 and 7. As
a result, it is possible to judge the adequacy of the refrigerant quantity in the
refrigerant circuit 10 with high accuracy. More specifically, it is possible to judge
whether or not there is a refrigerant leak from the refrigerant circuit 10 with high
accuracy.
(B)
In the air conditioner 1 of the present embodiment, the automatic refrigerant charging
operation can be performed in which whether or not the target charging quantity Ms
is reached is judged based on the operation state quantity of constituent equipment
or refrigerant flowing in the refrigerant circuit 10, so that it is possible to reliably
perform additional refrigerant charging, and at the same time, it is possible to determine
a value of the additional charging quantity Ma required for the calculation of the
volumes of the refrigerant communication pipes 6 and 7 by performing the automatic
refrigerant charging operation.
(C)
In the air conditioner 1 of the present embodiment, it is possible to calculate the
communication pipe refrigerant quantity Mp that is present with high accuracy during
the automatic refrigerant charging operation by subtracting the inside-unit refrigerant
quantity Mu calculated based on the operation state quantity of constituent equipment
or refrigerant flowing in the refrigerant circuit 10 in the automatic refrigerant
charging operation from the total charged refrigerant quantity Mt determined by adding
the additional charging quantity Ma to the initial charging quantity Mi that is the
refrigerant quantity that has been charged in the refrigerant circuit 10 before the
automatic refrigerant charging operation. Thus, the volumes of the refrigerant communication
pipes 6 and 7 can be calculated with high accuracy. In addition, in the air conditioner
1 of the present embodiment, it is possible to easily calculate both the volume Vlp
of the liquid refrigerant communication pipe 6 and the volume Vgp of the gas refrigerant
communication pipe 7 by predetermining the volume ratio Rv between the liquid refrigerant
communication pipe 6 and the gas refrigerant communication pipe 7 as a value corresponding
to the capacities and models of the indoor units 4, 5 and the outdoor unit 2.
(4) ALTERNATIVE EMBODIMENT
[0127] In the above described embodiment, the communication pipe refrigerant quantity Mp
required for the calculation of the volumes of the refrigerant communication pipes
6 and 7 is determined by calculating the inside-unit refrigerant quantity Mu determined
by the calculation above from the operation state quantity of constituent equipment
or refrigerant flowing in the refrigerant circuit 10 in the automatic refrigerant
charging operation and subtracting the inside-unit refrigerant quantity Mu from the
total charged refrigerant quantity Mt. However, the refrigerant whose quantity is
substantially equal to the inside-unit refrigerant quantity Mu that is present when
the refrigerant quantity in the refrigerant circuit 10 is reached the target charging
quantity Ms by the automatic refrigerant charging operation may be charged as the
initial charging quantity Mi into the refrigerant circuit 10 before the automatic
refrigerant charging operation (in other words, into the indoor units 4, 5 and the
outdoor unit 2 to be shipped to the installation site) is performed.
[0128] In this case, although a slight error will be generated depending on the capacities
and models of the indoor units 4 and 5 or the number of units and the like, the additional
charging quantity Ma that is the refrigerant quantity to be additionally charged into
the refrigerant circuit 10 in the automatic refrigerant charging operation can be
regarded as being corresponding to the communication pipe refrigerant quantity Mp
that is refrigerant quantity present in the refrigerant communication pipes 6 and
7. Therefore, unlike the above described embodiment, the need to calculate the communication
pipe refrigerant quantity Mp using the inside-unit refrigerant quantity Mu and the
total charged refrigerant quantity Mt will be eliminated, and thus the volumes of
the refrigerant communication pipes 6 and 7 can be easily calculated.
[0129] Meanwhile, even if the refrigerant whose quantity is different from the refrigerant
quantity corresponding to the inside-unit refrigerant quantity Mu that is present
when the refrigerant quantity in the refrigerant circuit 10 is reached the target
charging quantity Ms by the automatic refrigerant charging operation is charged as
the initial charging quantity Mi in the refrigerant circuit 10 before the automatic
refrigerant charging operation (in other words, into the indoor units 4 and 5 and
the outdoor unit 2 to be shipped to the installation site), in the above described
embodiment, as described above, the inside-unit refrigerant quantity Mu is calculated
from the operation state quantity of constituent equipment or refrigerant flowing
in the refrigerant circuit 10 in the automatic refrigerant charging operation. Therefore,
even under various conditions of the initial charging quantity Mi, it is possible
to determine a correct value of the communication pipe refrigerant quantity Mp, and
it is possible to calculate the volumes of the refrigerant communication pipes 6 and
7 with high accuracy.
(5) OTHER EMBODIMENT
[0130] While a preferred embodiment of the present invention has been described with reference
to the figures, the scope of the present invention is not limited to the above embodiment,
and the various changes and modifications may be made without departing from the scope
of the present invention.
[0131] For example, in the above described embodiment, an example in which the present invention
is applied to an air conditioner capable of switching and performing the cooling operation
and heating operation is described. However, it is not limited thereto, and the present
invention may be applied to different types of air conditioners such as a cooling
only air conditioner and the like. In addition, in the above described embodiment,
an example in which the present invention is applied to an air conditioner including
a single outdoor unit is described. However, it is not limited thereto, and the present
invention may be applied to an air conditioner including a plurality of outdoor units.
INDUSTRIAL APPLICABILITY
[0132] When the present invention is used, the labor of inputting information on the refrigerant
communication pipe before the operation of a separate type air conditioner is minimized,
and at the same time, the adequacy of the refrigerant quantity in the refrigerant
circuit can be judged with high accuracy.