[Technical Field]
[0001] The present invention relates to a refrigeration cycle apparatus and a hydronic heater
having the refrigeration cycle apparatus.
[Background Technique]
[0002] Generally, when a heating operation is carried out under an extremely low temperature
condition where an outdoor temperature is - 20°C or the like, a discharge temperature
of a compressor extremely rises in the case of a general refrigeration cycle apparatus
because an evaporating pressure is reduced and a high condensation temperature is
required.
Especially in a transient operation state of the refrigeration cycle apparatus when
its operation is started or when a variation in an indoor load is large, the apparatus
receives an influence of uneven distribution of refrigerant in the refrigeration cycle
or an amount of operation of an opening degree of an expansion valve, and a temperature
of a refrigerant (discharge temperature) discharged from the compressor abruptly rises
until the refrigeration cycle is stabilized in some cases.
According to patent document 1 for example, to solve the discharge temperature rise
of such a compressor, a refrigerant pipe extending from a condenser to an expansion
valve and a suction refrigerant pipe of a compressor are connected to each other by
means of a bypass pipe through the expansion valve and a supercooling heat exchanger,
and the compressor sucks a liquid refrigerant.
[0003] Fig. 6 shows a conventional refrigeration cycle apparatus described in patent document
1.
As shown in Fig. 6, in a refrigeration cycle in which a compressor 101, a four-way
valve 102, a condenser 103, a bridge circuit 104 and an evaporator 105 are annularly
connected to one another, the condenser 103 is connected to a first input terminal
of the bridge circuit 104. One of first output terminals of the bridge circuit 104
is connected to a second input terminal of the bridge circuit 104 through a supercooling
heat exchanger 106 and decompressing means 107, and a second output terminal of the
bridge circuit 104 is connected to the evaporator 105. The other first output terminal
of the bridge circuit 104 is connected to a suction refrigerant pipe of the compressor
101 by means of a bypass pipe 108 through the supercooling heat exchanger 106. A flow
rate adjusting valve 109 for the supercooling heat exchanger is connected to the bypass
pipe 108 at a location upstream of the supercooling heat exchanger 106. A discharge
pipe of the compressor 101 includes a discharge temperature sensor 110.
An opening degree of the flow rate adjusting valve 109 is adjusted based on a discharge
temperature detected by the discharge temperature sensor 110, and an amount of a refrigerant
flowing to the bypass pipe 108 is controlled.
[Prior Art Document]
[Patent Document]
[0004] [Patent Document 1] Japanese Patent Publication No.
3440910
[Summary of the Invention]
[Problem to be Solved by the Invention]
[0005] According to the conventional configuration, however, a liquid refrigerant which
reduces the discharge temperature once passes through the supercooling heat exchanger
106, a portion of latent heat of the liquid refrigerant is absorbed by the supercooling
heat exchanger 106. Hence, there is a problem that an abrupt discharge temperature
rise generated in a transient operating state can not swiftly be suppressed.
[0006] The present invention has been accomplished to solve the problem, and it is an object
of the invention to provide a refrigeration cycle apparatus capable of swiftly suppressing
the abrupt discharge temperature rise while maintaining a stable operation of the
refrigeration cycle.
[Means for Solving the Problem]
[0007] To solve the conventional problem, the present invention provides a refrigeration
cycle apparatus in which a compressor, a condenser, decompressing means and an evaporator
are annularly connected to one another through pipes in order, thereby forming a refrigeration
cycle, a supercooling heat exchanger is disposed between the condenser and the decompressing
means, one end of a first bypass pipe is connected to a portion of the pipe extending
from the supercooling heat exchanger to the decompressing means, first flow rate adjusting
means is connected to the first bypass pipe, heat of a refrigerant which flows out
from the first flow rate adjusting means is exchanged with heat of a refrigerant which
flows through the supercooling heat exchanger, the other end of the first bypass pipe
is connected to the compressor or connected to the portion of the pipe extending from
the evaporator to the compressor, the refrigeration cycle apparatus also includes
a temperature sensor which detects a discharge temperature of the compressor,
characterized in that the refrigeration cycle apparatus further comprises a second bypass pipe, one end
of the second bypass pipe is connected to the portion of the pipe extending from the
supercooling heat exchanger to the decompressing means, the other end of the second
bypass pipe is connected to the portion of the pipe extending from the evaporator
to the compressor, and second flow rate adjusting means is disposed in the second
bypass pipe, and the refrigeration cycle apparatus further comprises control means
which operates the decompressing means and the second flow rate adjusting means by
means of a temperature detected by the temperature sensor.
According to the configuration of the refrigeration cycle apparatus of the first aspect
of the invention, a liquid refrigerant which sufficiently secures a supercooled state
in a high pressure liquid pipe can be made to directly bypass the compressor suction
pipe through the second bypass pipe. It is possible to vary an amount of a refrigerant
flowing through the decompressing means in accordance with a variation in the amount
of the refrigerant flowing through the second bypass pipe such that a total sum of
amounts of refrigerants flowing through the decompressing means and the second bypass
pipe is constantly maintained.
[0008] According to the refrigeration cycle apparatus of a second aspect of the invention,
when a temperature detected by the temperature sensor is higher than a first predetermined
value, the control means operates the decompressing means in its closing direction
and operates the second flow rate adjusting means in its opening direction.
According to the configuration of the refrigeration cycle apparatus of the second
aspect, it is possible to reduce an amount of a refrigerant flowing through the decompressing
means in accordance with an increased amount of the refrigerant flowing through the
second bypass pipe such that the total sum of amounts of the refrigerants flowing
through the decompressing means and the second bypass pipe is constantly maintained.
As a result, even if the discharge temperature from the compressor abruptly increases,
it is possible to swiftly lower the discharge temperature by the bypassing operation
of liquid, and reliability can be enhanced.
Further, even if the bypassing amount of liquid is increased to restrain the discharge
temperature from rising, since an amount of a refrigerant flowing to the compressor
is constantly maintained, it is possible to suppress the variation in high and low
pressures of the refrigeration cycle. That is, it is possible to stably maintain the
refrigeration cycle, and to suppress the efficiency deterioration of the refrigeration
cycle apparatus to the minimum level.
[0009] According to the refrigeration cycle apparatus of the third aspect of the invention,
when a temperature detected by the temperature sensor is lower than a second predetermined
value, the control means operates the decompressing means in its opening direction
and operates the second flow rate adjusting means in its closing direction.
According to the configuration of the refrigeration cycle apparatus of the third aspect,
it is possible to increase the amount of a refrigerant flowing through the decompressing
means in accordance with a reduction amount of the refrigerant flowing through the
second bypass pipe such that the total sum of the amounts of the refrigerants flowing
through the decompressing means and the second bypass pipe is constantly maintained.
As a result, it is possible to restrain a liquid refrigerant from returning to the
compressor which configures the refrigerant circuit. Hence, moisture compression can
be prevented and the reliability can be enhanced.
Even if the bypassing amount of liquid is reduced, since the amount of the refrigerant
which flows into the compressor is constantly maintained, a variation in the suction
pressure of the compressor can be suppressed. That is, since it is possible to suppress
the variation in high and low pressures of the refrigeration cycle caused by the bypassing
operation of liquid, it is possible to stably maintain the refrigeration cycle. According
to this, it is possible to suppress the efficiency deterioration of the hydronic heater
to the minimum level.
[0010] According to the refrigeration cycle apparatus of the fourth aspect of the invention,
the radiator in the refrigeration cycle apparatus according to any one of the first
to third aspects is a heat exchanger which heats water by exchanging heat between
a refrigerant and water. Therefore, the present invention can be applied not only
to a case where the radiator is a heat exchanger between refrigerant and air, but
also to a case where the radiator is a heat exchanger between refrigerant and water.
In addition, the same effect as that of the first or second aspect can be obtained.
Further, the refrigeration cycle apparatus of the invention is
characterized in that the condenser is a heat exchanger which heats water by exchanging heat between the
refrigerant and the water, and hot water heated by the condenser is used for heating
a room.
[Effect of the Invention]
[0011] According to the invention, it is possible to provide a refrigeration cycle apparatus
capable of swiftly suppressing the abrupt discharge temperature rise while maintaining
a stable operation of the refrigeration cycle.
[Brief Description of the Drawings]
[0012]
Fig. 1 is a circuit diagram of a refrigeration cycle apparatus according to a first
embodiment of the present invention;
Fig. 2 is a control flowchart of a flow rate adjusting valve;
Fig. 3 is a control conceptual diagram when control of the flow rate adjusting valve
is started;
Fig. 4 is a control conceptual diagram of a variation in a discharge temperature and
control of an opening degree of the flow rate adjusting valve;
Fig. 5 is a control conceptual diagram during control of the flow rate adjusting valve;
and
Fig. 6 is a circuit diagram of a conventional refrigeration cycle apparatus.
[Explanation of Symbols]
[0013]
3 compressor
5 condenser (radiator)
6 expansion valve (decompressing means)
7 evaporator
8 supercooling heat exchanger
9 first bypass pipe
11 first flow rate adjusting valve (first flow rate adjusting means)
12 second flow rate adjusting valve (second flow rate adjusting means)
13 second bypass pipe
15 discharge temperature sensor
16 control means
[Mode for Carrying Out the Invention]
[0014] An embodiment of the present invention will be explained with reference to the drawings.
The invention is not limited to the embodiment.
[0015] Fig. 1 is a circuit diagram of a refrigeration cycle apparatus according to a first
embodiment of the present invention. Fig. 2 is a control flowchart of a flow rate
adjusting valve. Fig. 3 is a control conceptual diagram when control of the flow rate
adjusting valve is started. Fig. 4 is a control conceptual diagram of a variation
in a discharge temperature and control of an opening degree of the flow rate adjusting
valve. Fig. 5 is a control conceptual diagram during control of the flow rate adjusting
valve. As a refrigerant, it is possible to use a zeotropic refrigerant mixture such
as R407C, a pseudo-azeotropic refrigerant mixture such as R410A or a single refrigerant.
[0016] In Fig. 1, the refrigeration cycle apparatus of the embodiment includes an outdoor
unit 1 and an indoor unit 2.
The refrigeration cycle is formed by annularly connecting the following members to
one another through pipes: that is, a compressor 3 which compresses a refrigerant,
a four-way valve 4 which switches between flowing directions of the refrigerant, a
condenser (radiator) 5 (when the indoor unit 2 is used for a heating operation) which
condenses and liquefies a high-temperature and high-pressure refrigerant, and expansion
valve 6 (decompressing means) which decompresses and expands a high-pressure liquid
refrigerant, and an evaporator 7 (when the indoor unit 2 is used for the heating operation)
which evaporates and vaporizes a low-temperature two-phase refrigerant.
The indoor unit 2 includes the condenser 5, and the outdoor unit 1 includes the compressor
3, the four-way valve 4, the expansion valve 6 and the evaporator 7.
By switching the four-way valve 4, it is possible to switch a normal heating operation
to a cooling operation, or from the normal heating operation to a defrosting operation.
[0017] A supercooling heat exchanger 8 is disposed between the condenser 5 and the expansion
valve 6. The outdoor unit 1 includes the supercooling heat exchanger 8.
One end of a first bypass pipe 9 is connected to a pipe extending from the supercooling
heat exchanger 8 to the expansion valve 6. First flow rate adjusting means 11 is connected
to the first bypass pipe 9. The first flow rate adjusting valve 11 adjusts a bypassing
amount of a refrigerant flowing to the first bypass pipe 9.
The other end of the first bypass pipe 9 is connected to a pipe extending from the
evaporator 7 to the compressor 3. The other end of the first bypass pipe 9 may be
connected to a compression chamber of the compressor 3. A refrigerant which flows
out from the first flow rate adjusting valve 11 exchanges heat with a refrigerant
which flows through the supercooling heat exchanger 8 and then, the refrigerant is
supplied to a suction pipe 10 of the compressor 3.
In the supercooling heat exchanger 8, heat is exchanged between a high-pressure refrigerant
which flows out from the condenser 5 and a low-pressure bypassing refrigerant which
flows out from the first flow rate adjusting valve 11.
[0018] One end of a second bypass pipe 13 is connected to a pipe extending from the supercooling
heat exchanger 8 to the expansion valve 6. A second flow rate adjusting valve 12 is
connected to the second bypass pipe 13. The second flow rate adjusting valve 12 adjusts
a bypassing amount of a refrigerant which flows to the second bypass pipe 13.
The other end of the second bypass pipe 13 is connected to a pipe extending from the
evaporator 7 to the compressor 3. The other end of the second bypass pipe 13 may be
connected to the compression chamber of the compressor 3. A refrigerant which flows
out from the second bypass pipe 13 is supplied to the suction pipe 10 of the compressor
3 without exchanging heat with a refrigerant which flows through the supercooling
heat exchanger 8.
[0019] A discharge temperature sensor 15 which detects a discharge temperature of the compressor
3 is connected to the discharge pipe 14 of the compressor 3.
Control means 16 controls an - of the second flow rate adjusting valve 12 and an opening
degree of the expansion valve 6 in accordance with a temperature detected by the discharge
temperature sensor 15. The opening degree of the expansion valve 6 is controlled in
accordance with a controlled amount of the opening degree of the second flow rate
adjusting valve 12.
[0020] First, in the refrigeration cycle shown in Fig. 1, a high-pressure gas refrigerant
discharged from the compressor 3 flows from the discharge pipe 14 and reaches the
four-way valve 4. When the indoor unit 2 is used for the heating operation, the high-pressure
gas refrigerant flows into the condenser 5, radiates heat, and is condensed and liquefied.
The condensed and liquefied high-pressure liquid refrigerant is supercooled by the
supercooling heat exchanger 8, the refrigerant is decompressed and expanded by the
expansion valve 6 and becomes a low-temperature and low-pressure two-phase refrigerant.
Then, the low-temperature low-pressure two-phase refrigerant flows into the evaporator
7, and evaporates and vaporizes. Thereafter, the refrigerant again passes through
the four-way valve 4 and is sucked from the suction pipe 10 into the compressor 3.
[0021] The control means 16 adjusts an opening degree of the first flow rate adjusting valve
11 such that an outlet state of the first bypass pipe 9 becomes a saturated gas refrigerant.
According to this adjustment, performance of the supercooling heat exchanger 8 is
sufficiently exerted, and the supercooled state of a liquid refrigerant in the refrigerant
pipe which connects the supercooling heat exchanger 8 and the expansion valve 6 to
each other is sufficiently secured.
In the second bypass pipe 13 which branches off from between the supercooling heat
exchanger 8 and the decompressing means (expansion valve 6), and which is connected
to a portion between the compressor 3 and the evaporator 7 through second flow rate
adjusting means (second flow rate adjusting valve 12), a discharge temperature of
the compressor 3 is detected by a discharge temperature sensor 15 disposed in the
discharge pipe 14, and when the discharge temperature becomes equal to or higher than
a preset predetermined temperature, the second flow rate adjusting valve 12 disposed
at the second bypass pipe 13 is opened by a predetermined opening degree by the control
means 16, and the expansion valve 6 is closed by a predetermined opening degree by
the control means 16 in accordance with the opening degree of the second flow rate
adjusting valve 12.
Similarly, in the second bypass pipe 13, a discharge temperature of the compressor
3 is detected by the discharge temperature sensor 15 disposed in the discharge pipe
14, and when the discharge temperature becomes equal to or lower than a preset predetermined
temperature, the second flow rate adjusting valve 12 disposed at the second bypass
pipe 13 is closed by a predetermined opening degree by the control means 16, and the
expansion valve 6 is opened by a predetermined opening degree by the control means
16 in accordance with the opening degree of the second flow rate adjusting valve 12.
[0022] Next, a control operation and effect with respect to a variation in a discharge temperature
will be explained using Figs. 2 to 5.
According to the refrigeration cycle apparatus of the embodiment, a bypassing refrigerant
is made to flow to the first bypass pipe 9 at the time of a normal operation, thereby
carrying out the operation using the supercooling heat exchanger 8.
At the time of the normal operation, a discharge temperature Td is detected by the
discharge temperature sensor 15 (step 101).
At this time, a refrigerant in the pipe which connects the supercooling heat exchanger
8 and the expansion valve 6 to each other is sufficiently supercooled by the supercooling
heat exchanger 8.
[0023] Next, a discharge temperature Td and a previously set first set temperature TdH are
compared with each other (step 102). At that time, the first set temperature TdH is
set in accordance with a specification of the compressor 3. It is preferable that
the first set temperature TdH is set to a normal discharge temperature, or a temperature
which is lower than an upper limit discharge temperature by a predetermined temperature,
i.e., a temperature at which reliability of the compressor 3 can not be deteriorated
when the compressor 3 is used.
In step 102, if the detected discharge temperature Td is lower than the first set
temperature TdH, it is determined whether the refrigeration cycle apparatus keeps
operating (step 103), and if the apparatus keeps operating, the procedure is again
returned to step 101, and the discharge temperature Td is detected.
[0024] If the detected discharge temperature Td is equal to or higher than the first set
temperature TdH, the second flow rate adjusting valve 12 is opened by the predetermined
opening degree, and the expansion valve 6 is closed by the predetermined opening degree
in accordance with the opening degree of the second flow rate adjusting valve 12 (step
104).
The operation in step 104 is shown in Fig. 3. In Fig. 3, a lateral axis shows valve
opening degrees of the expansion valve 6 and the second flow rate adjusting valve
12, and a vertical axis shows refrigerant flow rates of these valves 11 and 12.
The second flow rate adjusting valve 12 is opened from a closed state PLSLO to a predetermined
opening degree PLSL1. An opening operation of the expansion valve 6 is carried out
simultaneously with the opening operation of the second flow rate adjusting valve
12.
A flow rate variation amount Gl is generated when the opening degree of the second
flow rate adjusting valve 12 is varied from PLSLO to PLSL1.
Therefore, the expansion valve 6 is closed by varying the opening degree from PLSSO
to PLSS1 so that a flow rate variation amount Gs (absolute value) which is equal to
the flow rate variation amount Gl is generated.
[0025] Next, a variation state of the discharge temperature generated by operation of step
103 is determined (step 105).
In step 105, in a state where the discharge temperature Td is equal to or higher than
a set temperature TdH, if the discharge temperature Td is rising, the second flow
rate adjusting valve 12 is opened by the predetermined opening degree, and the expansion
valve 6 is closed by the predetermined opening degree (step 106).
If the discharge temperature Td is lowering in step 105 on the contrary, the second
flow rate adjusting valve 12 is closed by the predetermined opening degree and the
expansion valve 6 is opened by the predetermined opening degree (step 107).
Fig. 4 shows a variation in the discharge temperature. A case where the discharge
temperature Td is lowering will be explained. As shown in Fig. 4, a discharge temperature
Td before a predetermined time discharge temperature and a variation amount dTd of
the discharge temperature Td after the predetermined time dT are compared with each
other, and if the variation amount is lower than 0°C, it is determined that the discharge
temperature Td is lowering.
[0026] An operation in step 107 is shown in Fig. 5.
The second flow rate adjusting valve 12 is controlled into the closing direction by
the predetermined opening degree. The expansion valve 6 is controlled into the opening
direction by the predetermined opening degree. That is, the second flow rate adjusting
valve 12 is closed by ΔG1 from the opening degree PLSL1 to the opening degree PLSL2.
The expansion valve 6 is opened by ΔGs from the opening degree PLSS1 to PLSS2 so that
the flow rate variation amount of the expansion valve 6 becomes equal to a reverse
direction of the flow rate variation amount of the second flow rate adjusting valve
12.
[0027] Next, the discharge temperature Td is detected, and this is compared with a second
set temperature TdL (step 108).
If the discharge temperature Td is equal to or higher than the second set temperature
TdL in step 108, operations from step 105 to step 107 are repeated. If the discharge
temperature Td is lower than the second set temperature TdL, a variation state of
the discharge temperature Td is determined (step 109). This determining operation
of the variation state in step 109 is the same as that in step 105.
If the discharge temperature Td is in the lowering state based on the determination
result in step 109, the second flow rate adjusting valve 12 is closed by the predetermined
opening degree. The expansion valve 6 is opened by the predetermined opening degree
(step 110).
After step 110, operation in step 103 is checked, and if the operation is stopped,
the control is completed. If the discharge temperature Td is in the rising state on
the contrary, the second flow rate adjusting valve 12 is opened by the predetermined
opening degree. The expansion valve 6 is closed by the predetermined opening degree
(step 111).
After step 111, the operation in step 103 is checked, and if the operation is stopped,
the control is completed.
[0028] By repeating the operations from step 101 to step 111, even if the discharge temperature
abruptly rises when a load is varied, it is possible to bypass the liquid refrigerant
from the high pressure liquid refrigerant pipe between the radiator 5 and the decompressing
means 6 to the suction pipe of the compressor 3 by the second bypass pipe 13. Hence,
it is possible to swiftly lower the discharge temperature. At the same time, even
when the refrigerant flow rate of the second bypass pipe 13 becomes excessively large,
the second flow rate adjusting valve 12 is controlled into the closing direction and
the expansion valve 6 is controlled into the opening direction. Therefore, it is possible
to prevent a liquid refrigerant from returning to the compressor, and to enhance the
reliability.
A refrigerant state at an inlet of the second bypass pipe 13 is a liquid refrigerant
whose supercooled state is sufficiently secured after the refrigerant passes through
the supercooling heat exchanger 8. Therefore, even under a low outside air temperature
condition of even when a heating load is abruptly increased, it is possible to bypass
the liquid refrigerant from the high pressure liquid refrigerant pipe between the
condenser 5 and the decompressing means 6 to the suction pipe of the compressor 3.
Hence, it is possible to lower the discharge temperature in a wide operation range,
and to enhance the reliability of the compressor 3.
The expansion valve 6 is controlled into the reverse direction in accordance with
a refrigerant flow rate of the second flow rate adjusting valve 12 of the second bypass
pipe 13, and it is possible to reduce a variation amount of a total sum of the flow
rates of a refrigerants flowing through the expansion valve 6 and the second bypass
pipe 13. Therefore, it is possible to suppress a variation in high and low pressures
at the time of the bypassing operation, to stably maintain the refrigeration cycle,
and to suppress the deterioration in efficiency of the refrigeration cycle apparatus
of the present application to the minimum.
Further, it is not absolutely necessary that the first bypass pipe 9 branches off
from between the supercooling heat exchanger 8 and the expansion valve 6, and the
first bypass pipe 9 may branch off from the refrigerant circuit 2 between the radiator
5 and the supercooling heat exchanger 8.
It is not absolutely necessary that a connected portion of the first bypass pipe 9
is the suction pipe of the compressor 3. In the case of a compressor having an injection
mechanism, the first bypass pipe 9 may be connected to an injection port.
[Industrial Applicability]
[0029] As described above, according to the refrigeration cycle apparatus of the invention,
even when a discharge temperature abruptly rises when a load is varied, it is possible
to suppress a discharge temperature rise while stably maintaining the refrigeration
cycle. Therefore, the refrigeration cycle apparatus can also be applied to a general
air conditioner, a heat pump hydronic heater, a professional-use freezing machine,
and a heat pump hot water supply apparatus.