CROSS-REFERENCE TO RELATED APPLICATION
[0001] This application is based on and claims priority to Chinese patent application No.
201810606528.1, filed on June 13, 2018, the content of which is incorporated herein by reference in its entirety.
FIELD
[0002] The present disclosure relates to the technical field of cooling, in particular to
a method for controlling oil return of a multi-split air conditioning system, a device
for controlling oil return of a multi-split air conditioning system, and a multi-split
air conditioning system.
BACKGROUND
[0003] With the constant increase of multi-split air conditioner models (multi-split air
conditioner for short), the multi-split air conditioner is increasingly widely used
in large buildings and villas owing to the advantages of energy saving, intelligent
regulation, accurate temperature control, high automation degree, flexible use, convenient
management and the like. Generally, a multi-split air conditioner has a long tube,
and numbers of oil storage positions. With the increase of system operation time,
more and more lubricating oil will be accumulated in the tube of the system. If the
oil is not returned in time, then a compressor will be damaged due to the shortage
of the lubricating oil.
[0004] With regard to the above-described problem, a conventional method is to perform an
oil return operation after the multi-split air conditioner operates for a fixed period
of time; the oil return operation is generally an operation switched to a cooling
mode, so as to carry the lubricating oil in the tube of the system back to an outdoor
unit, and avoid the compressor from operating in short of oil.
[0005] However, the operation conditions of the multi-split air conditioner are inconsistent,
and the oil discharge amount during operation is also inconsistent. If the oil discharge
amount is great and the oil return amount is small under the operation condition,
the compressor may also operate in short of oil in a fixed time.
SUMMARY
[0006] The objects of the present disclosure are to solve at least one of the technical
problems in the related art to a certain extent. Therefore, a first object of the
present disclosure is to provide a method for controlling oil return of a multi-split
air conditioning system. The present disclosure can ensure that the compressor will
not operate in short of oil due to great oil discharge amount and small oil return
amount, and can effectively improve the capability and energy efficiency of the multi-split
air conditioning system; furthermore, the method is simple and feasible.
[0007] A second object of the present disclosure is to provide a non-transitory computer
readable storage medium.
[0008] A third object of the present disclosure is to provide a device for controlling oil
return of a multi-split air conditioning system.
[0009] A fourth object of the present disclosure is to provide a multi-split air conditioning
system.
[0010] To achieve the above objects, in a first aspect, an embodiment of the present disclosure
provides a method for controlling oil return of a multi-split air conditioning system,
the multi-split air conditioning system including an outdoor unit and a plurality
of indoor units, wherein the outdoor unit includes a compressor; the method includes:
acquiring a minimum refrigerant flux required for carrying a lubricating oil in the
system back to the outdoor unit and a current refrigerant flux of the system every
a first preset time during operation of the system; detecting and determining that
the current refrigerant flux is less than or equal to the minimum refrigerant flux;
acquiring a total oil discharge amount of the compressor since last time oil return;
detecting and determining that the total oil discharge amount is greater than a maximum
safe oil discharge amount; and controlling the system to return oil.
[0011] According to an embodiment of the present disclosure, the method for controlling
oil return of a multi-split air conditioning system includes: acquiring a minimum
refrigerant flux required for carrying a lubricating oil in the system back to an
outdoor unit and a current refrigerant flux of the system every a first preset time
during operation of the system, detecting and determining that the current refrigerant
flux is less than or equal to the minimum refrigerant flux; acquiring a total oil
discharge amount of the compressor since last time oil; detecting and determining
that the total oil discharge amount is greater than a maximum safe oil discharge amount;
and controlling system to return oil. Therefore, the present disclosure can ensure
that the compressor will not operate in short of oil due to great oil discharge amount
and small oil return amount, and can effectively improve the capability and energy
efficiency of the multi-split air conditioning system; furthermore, the method is
simple and feasible.
[0012] According to an embodiment of the present disclosure, the method further includes:
detecting and determining that a duration of the current refrigerant flux being greater
than the minimum refrigerant flux is greater than a second preset time when the current
refrigerant flux is greater than the minimum refrigerant flux; zero-clearing the total
oil discharge amount, detecting and determining that a duration since last time oil
return is greater than a third preset time; and controlling the system to return oil,
wherein the third preset time > the second preset time > the first preset time.
[0013] According to an embodiment of the present disclosure, the method for controlling
oil return of a multi-split air conditioning system further includes: acquiring a
current operation mode of the system; controlling the system to return oil in a cooling
mode when the current operation mode is determined to be the cooling mode; and controlling
the system to return oil in a heating mode when the current operation mode is determined
to be the heating mode.
[0014] According to an embodiment of the present disclosure, acquiring a minimum refrigerant
flux required for carrying a lubricating oil in the system back to the outdoor unit
in the cooling mode includes: acquiring a saturation evaporation temperature of the
system, and acquiring a saturation evaporation pressure of the system according to
the saturation evaporation temperature; acquiring a concentration of the lubricating
oil, a density of the lubricating oil, and an inner diameter of a refrigerant air
tube in the system; and acquiring the minimum refrigerant flux from a preset table
according to the saturation evaporation pressure, the concentration of the lubricating
oil, the density of the lubricating oil, and the inner diameter of the refrigerant
air tube.
[0015] According to an embodiment of the present disclosure, acquiring a minimum refrigerant
flux required for carrying a lubricating oil in the system back to the outdoor unit
in the heating mode includes: acquiring an exhaust pressure of the system; acquiring
a concentration of the lubricating oil, a density of the lubricating oil, and an inner
diameter of a refrigerant air tube in the system; and acquiring the minimum refrigerant
flux from a preset table according to the exhaust pressure, the concentration of the
lubricating oil, the density of the lubricating oil, and the inner diameter of the
refrigerant air tube.
[0016] According to an embodiment of the present disclosure, the acquiring a current refrigerant
flux of the system includes: acquiring an exhaust pressure and an air return pressure
of the system, and a current operation frequency of the compressor; acquiring a saturation
exhaust temperature of the system according to the exhaust pressure; acquiring a saturation
air return temperature of the system according to the air return pressure; and acquiring
the current refrigerant flux according to the saturation exhaust temperature, the
saturation air return temperature and the current operation frequency.
[0017] According to an embodiment of the present disclosure, the current refrigerant flux
is acquired by the following formula:

wherein G2 is the current refrigerant flux; S is the saturation air return temperature;
D is the saturation exhaust temperature; C0 to C9 are calculating coefficients and
are acquired according to the current operation frequency.
[0018] To achieve the above objects, in a second aspect, an embodiment of the present disclosure
provides a non-transitory computer readable storage medium having stored therein a
computer program that, when executed by a processor, causes the processor to realize
the method for controlling oil return of a multi-split air conditioning system.
[0019] The non-transitory computer readable storage medium according to the embodiment of
the present disclosure, by means of the method for controlling oil return of a multi-split
air conditioning system, can ensure that the compressor will not operate in short
of oil due to great oil discharge amount and small oil return amount, and can effectively
improve the capability and energy efficiency of the multi-split air conditioning system;
furthermore, the method is simple and feasible.
[0020] To achieve the above objects, in a third aspect, an embodiment of the present disclosure
provides a device for controlling oil return of a multi-split air conditioning system,
the multi-split air conditioning system including an outdoor unit and a plurality
of indoor units, wherein the outdoor unit includes a compressor; the device includes:
a first acquisition module, configured to acquire a minimum refrigerant flux required
for carrying a lubricating oil in the system back to the outdoor unit every a first
preset time during operation of the system; a second acquisition module, configured
to acquire a current refrigerant flux of the system every the first preset time during
operation of the system; and a control module, configured to detect and determine
that the current refrigerant flux is less than or equal to the minimum refrigerant
flux, acquire a total oil discharge amount of the compressor since last time oil return,
detect and determine that the total oil discharge amount is greater than a maximum
safe oil discharge amount, and control the system to return oil.
[0021] In the device for controlling oil return of a multi-split air conditioning system
according to the embodiment of the present disclosure, the first acquisition module
acquires the minimum refrigerant flux required for carrying the lubricating oil in
the system back to the outdoor unit every the first preset time during operation of
the system; the second acquisition module acquires the current refrigerant flux of
the system every the first preset time during operation of the system; and the control
module detects and determines that the current refrigerant flux is less than or equal
to the minimum refrigerant flux, acquires the total oil discharge amount of the compressor
since last time oil return, detects and determines that the total oil discharge amount
is greater than the maximum safe oil discharge amount, and controls the system to
return oil. Therefore, the present disclosure can ensure that the compressor will
not operate in short of oil due to great oil discharge amount and small oil return
amount, and can effectively improve the capability and energy efficiency of the multi-split
air conditioning system; furthermore, the method is simple and feasible.
[0022] According to an embodiment of the present disclosure, the control module is further
specifically configured to: detect and determine, when the current refrigerant flux
is greater than the minimum refrigerant flux, that a duration of the current refrigerant
flux being greater than the minimum refrigerant flux is greater than a second preset
time; zero-clear the total oil discharge amount, detect and determine that a duration
since last time oil return is greater than a third preset time, and control the system
to return oil, wherein the third preset time > the second preset time > the first
preset time.
[0023] According to an embodiment of the present disclosure, the device for controlling
oil return of a multi-split air conditioning system further includes: a third acquisition
module, configured to acquire a current operation mode of the system; wherein the
control module is further configured to control the system to return oil in a cooling
mode when the current operation mode is determined to be the cooling mode, and control
the system to return oil in a heating mode when the current operation mode is determined
to be the heating mode.
[0024] According to an embodiment of the present disclosure, when the current operation
mode is determined to be the cooling mode, the first acquisition module is specifically
configured to: acquire a saturation evaporation temperature of the system, and acquire
a saturation evaporation pressure of the system according to the saturation evaporation
temperature; acquire a concentration of the lubricating oil, a density of the lubricating
oil, and an inner diameter of a refrigerant air tube in the system; and acquire the
minimum refrigerant flux from a preset table according to the saturation evaporation
pressure, the concentration of the lubricating oil, the density of the lubricating
oil, and the inner diameter of the refrigerant air tube.
[0025] According to an embodiment of the present disclosure, when the current operation
mode is determined to be the heating mode, the first acquisition module is specifically
configured to: acquire an exhaust pressure of the system; acquire a concentration
of the lubricating oil, a density of the lubricating oil, and an inner diameter of
a refrigerant air tube in the system; and acquire the minimum refrigerant flux from
a preset table according to the exhaust pressure, the concentration of the lubricating
oil, the density of the lubricating oil, and the inner diameter of the refrigerant
air tube.
[0026] According to an embodiment of the present disclosure, the second acquisition module
is specifically configured to: acquire an exhaust pressure and an air return pressure
of the system, and a current operation frequency of the compressor; acquire a saturation
exhaust temperature of the system according to the exhaust pressure; acquire a saturation
air return temperature of the system according to the air return pressure; and acquire
the current refrigerant flux according to the saturation exhaust temperature, the
saturation air return temperature and the current operation frequency.
[0027] According to an embodiment of the present disclosure, the second acquisition module
acquires the current refrigerant flux by the following formula:

wherein G2 is the current refrigerant flux; S is the saturation air return temperature;
D is the saturation exhaust temperature; C0 to C9 are calculating coefficients and
are acquired according to the current operation frequency.
[0028] To achieve the above objects, in a fourth aspect, an embodiment of the present disclosure
provides multi-split air conditioning system, including the device for controlling
oil return of a multi-split air conditioning system.
[0029] The multi-split air conditioning system according to the embodiment of the present
disclosure, by means of the device for controlling oil return of a multi-split air
conditioning system, can ensure that the compressor will not operate in short of oil
due to great oil discharge amount and small oil return amount, and can effectively
improve the capability and energy efficiency of the multi-split air conditioning system;
furthermore, the method is simple and feasible.
[0030] A part of additional aspects and advantages of the present disclosure will be provided
in the descriptions hereafter, and the other part will become apparent from the descriptions
hereafter, or can be understood through the practice of the present disclosure.
BRIEF DESCRIPTION OF THE DRAWINGS
[0031]
Fig. 1 is a flow chart of the method for controlling oil return of a multi-split air
conditioning system according to one embodiment of the present disclosure;
Fig. 2 is a flow chart of acquiring the minimum refrigeration flux in the cooling
mode according to one embodiment of the present disclosure;
Fig. 3 is a flow chart of acquiring the minimum refrigeration flux in the heating
mode according to one embodiment of the present disclosure;
Fig. 4 is a flow chart of the method for controlling oil return of a multi-split air
conditioning system in the cooling mode according to one embodiment of the present
disclosure;
Fig. 5 is a flow chart of the method for controlling oil return of a multi-split air
conditioning system in the heating mode according to one embodiment of the present
disclosure; and
Fig. 6 is a block diagram of the device for controlling oil return of a multi-split
air conditioning system according to one embodiment of the present disclosure.
DETAILED DESCRIPTION
[0032] The embodiments of the present disclosure will be described in detail hereafter,
and the examples of the embodiments are shown in the drawings, wherein the same or
similar signs from beginning to end denote the same or similar elements or the elements
having the same or similar functions. The embodiments described below with reference
to the drawings are for illustration only, and are intended to explain the present
disclosure, but not to limit the present disclosure.
[0033] The method for controlling oil return of a multi-split air conditioning system, the
non-transitory computer readable storage medium, the device for controlling oil return
of a multi-split air conditioning system, and the multi-split air conditioning system
provided according to the embodiments of the present disclosure will be described
hereafter with reference to the drawings.
[0034] Fig. 1 is a flow chart of the method for controlling oil return of a multi-split
air conditioning system according to one embodiment of the present disclosure.
[0035] In the embodiment of the present disclosure, the multi-split air conditioning system
may include an outdoor unit and a plurality of indoor units, wherein the outdoor unit
includes a compressor.
[0036] As shown in Fig. 1, the method for controlling oil return of a multi-split air conditioning
system according to the embodiment of the present disclosure may include:
S1, acquiring a minimum refrigerant flux required for carrying a lubricating oil in
the system back to the outdoor unit and a current refrigerant flux of the system every
a first preset time during operation of the system, wherein the first preset time
can be calibrated according to practical situations.
[0037] To be specific, the minimum refrigerant flux required for carrying the lubricating
oil in the system back to the outdoor unit and the current refrigerant flux of the
system can be acquired according to an operation parameter of the system during operation
of the system.
[0038] According to an embodiment of the present disclosure, as shown in Fig. 2, acquiring
a minimum refrigerant flux required for carrying a lubricating oil in the system back
to the outdoor unit in the cooling mode includes:
S201, acquiring a saturation evaporation temperature of the system, and acquiring
a saturation evaporation pressure of the system according to the saturation evaporation
temperature.
[0039] To be specific, during operation of the system in the cooling mode, a temperature
of an indoor heat exchanger tube of each indoor unit in an operating state in the
plurality of indoor units is respectively acquired, so as to acquire the temperatures
of a plurality of indoor heat exchanger tubes; and then the temperatures of the plurality
of indoor heat exchanger tubes are averaged, so as to acquire the saturation evaporation
temperature of the system. For example, assuming that ten indoor units in the plurality
of indoor units are in the operating state, the temperature of the indoor heat exchanger
tubes of five indoor units is 7°C, and the temperature of the indoor heat exchanger
tubes of the other five indoor units is 8°C, then the acquired saturation evaporation
temperature of the system is (5
∗7+8
∗5)/10=7.5. The saturation evaporation pressure of the system is acquired by querying
a relationship table between saturation evaporation temperatures and saturation evaporation
pressures according to the saturation evaporation temperature.
[0040] S202, acquiring a concentration of the lubricating oil, a density of the lubricating
oil, and an inner diameter of a refrigerant air tube in the system.
[0041] S203, acquiring the minimum refrigerant flux from a preset table according to the
saturation evaporation pressure, the concentration of the lubricating oil, the density
of the lubricating oil, and the inner diameter of the refrigerant air tube.
[0042] Specifically, after the system is completely mounted, the concentration of the lubricating
oil, the density of the lubricating oil, and the inner diameter of the refrigerant
air tube can be pre-stored in the system. During operation of the system in the cooling
mode, the saturation evaporation temperature of the system is acquired; then the saturation
evaporation pressure of the system is acquired according to the saturation evaporation
temperature; and finally the minimum refrigerant flux (equivalent to a minimum gas
circulation amount in the refrigeration air tube) is acquired from the preset table
according to the saturation evaporation pressure, the concentration of the lubricating
oil, the density of the lubricating oil, and the inner diameter of the refrigerant
air tube.
[0043] The preset table can be pre-acquired through a large number of experiments and tests.
For example, table 1 shows the minimum refrigeration flux under different tube diameters
in the cooling mode when the saturation evaporation pressure is 1200MPa.
Table 1
Cooling mode |
Saturation evaporation temperature Te |
16.3 |
|
Concentration of the lubricating oil |
1.0% |
Saturation evaporation pressure Pe |
1200.0 |
|
Density of the lubricating oil |
930.0 |
Density of gaseous refrigerant ρg |
50.8 |
|
Density of a mixture of the lubricating oil and liquid refrigerant ρl |
1098.7 |
Density of liquid refrigerant p |
1100.4 |
|
|
|
|
Air tube |
Minimum refrigerant flow rate |
Minimum refrigerant flux |
Outer diameter |
Wall thickness |
Inner diameter |
m/s |
kg/h |
ϕ15.9 |
1.0 |
13.9 |
1.72 |
47.64 |
ϕ19.1 |
1.0 |
17.1 |
1.90 |
79.97 |
ϕ22.2 |
1.0 |
20.2 |
2.07 |
121.28 |
ϕ25.4 |
1.0 |
23.4 |
2.23 |
175.17 |
ϕ28.6 |
1.2 |
26.2 |
2.36 |
232.37 |
ϕ31.8 |
1.2 |
29.4 |
2.50 |
309.95 |
ϕ34.9 |
1.3 |
32.3 |
2.62 |
392.13 |
ϕ38.1 |
1.4 |
35.3 |
2.73 |
489.63 |
ϕ41.3 |
1.5 |
38.3 |
2.85 |
600.38 |
ϕ44.5 |
1.7 |
41.1 |
2.95 |
716.20 |
ϕ54.1 |
1.9 |
50.3 |
3.26 |
1186.72 |
[0044] As shown in Fig. 1, in the cooling mode, when the acquired saturation evaporation
temperature of the system is 16.3°C, the corresponding saturation evaporation pressure
of the system would be 1200MPa; if the concentration of the lubricating oil is 1.0%,
the density of the lubricating oil is 930.0kg/m
3, and the inner diameter of the refrigeration air tube is 32.3cm, then the current
minimum refrigerant flux required for carrying the lubricating oil in the system back
to the outdoor unit would be 392.13kg/h.
[0045] According to an embodiment of the present disclosure, as shown in Fig. 3, acquiring
a minimum refrigerant flux required for carrying a lubricating oil in the system back
to the outdoor unit in the heating mode includes:
S301, acquiring an exhaust pressure of the system.
[0046] Specifically, the exhaust pressure of the system can be acquired by acquiring a pressure
at an exhaust port of the compressor.
[0047] It should be noted that in the heating mode, the exhaust pressure of the system is
also a condensation pressure of the system which can be directly acquired via a pressure
sensor disposed at the exhaust port of the compressor; alternatively, the exhaust
pressure can also be acquired by the following means: first, an exhaust temperature,
that is the condensation temperature of the system, is acquired via a temperature
sensor disposed at the exhaust port of the compressor, and then a condensation temperature
of the system, that is the exhaust pressure, is acquired according to the condensation
temperature.
[0048] S302, acquiring a concentration of the lubricating oil, a density of the lubricating
oil, and an inner diameter of a refrigerant air tube in the system.
[0049] S303, acquiring the minimum refrigerant flux from a preset table according to the
exhaust pressure, the concentration of the lubricating oil, the density of the lubricating
oil, and the inner diameter of the refrigerant air tube.
[0050] Specifically, after the system is completely mounted, the concentration of the lubricating
oil, the density of the lubricating oil, and the inner diameter of the refrigerant
air tube can be pre-stored in the system. During operation of the system in the heating
mode, the exhaust pressure of the system is acquired; and then the minimum refrigerant
flux (equivalent to a minimum gas circulation amount in the refrigeration air tube)
is acquired from the preset table according to the exhaust pressure, the concentration
of the lubricating oil, the density of the lubricating oil, and the inner diameter
of the refrigerant air tube.
[0051] The preset table can be pre-acquired through a large number of experiments and tests.
For example, table 2 shows the minimum refrigeration flux under different tube diameters
in the heating mode when the exhaust pressure is 2200MPa.
Table 2
Heating mode |
Condensation temperature Tc |
38.0 |
|
Concentration of the lubricating oil |
1.0% |
Condensation pressure Pc |
2200.0 |
|
Density of the lubricating oil |
930.0 |
Density of gaseous refrigerant pg |
97.1 |
|
Density of a mixture of the lubricating oil and liquid refrigerant ρ1 |
987.2 |
Density of liquid refrigerant ρ |
987.7 |
|
|
|
|
Air tube |
Minimum refrigerant flow rate |
Minimum refrigerant flux |
Outer diameter |
Wall thickness |
Inner diameter |
m/s |
kg/hr |
ϕ15.9 |
1.0 |
13.9 |
1.18 |
62.43 |
ϕ19.1 |
1.0 |
17.1 |
1.31 |
104.79 |
ϕ22.2 |
1.0 |
20.2 |
1.42 |
158.93 |
ϕ25.4 |
1.0 |
23.4 |
1.53 |
229.54 |
ϕ28.6 |
1.2 |
26.2 |
1.62 |
304.50 |
ϕ31.8 |
1.2 |
29.4 |
1.71 |
406.16 |
ϕ34.9 |
1.3 |
32.3 |
1.79 |
513.85 |
ϕ38.1 |
1.4 |
35.3 |
1.88 |
641.60 |
ϕ41.3 |
1.5 |
38.3 |
1.95 |
786.73 |
ϕ44.5 |
1.7 |
41.1 |
2.02 |
938.50 |
ϕ54.1 |
1.9 |
50.3 |
2.24 |
1555.06 |
[0052] As shown in Fig. 2, in the heating mode, when the acquired exhaust pressure of the
system is 2200MPa, if the concentration of the lubricating oil is 1.0%, the density
of the lubricating oil is 930.0kg/m
3, and the inner diameter of the refrigeration air tube is 32.3cm, then the current
minimum refrigerant flux required for carrying the lubricating oil in the system back
to the outdoor unit would be 392.13kg/h.
[0053] According to an embodiment of the present disclosure, the acquiring a current refrigerant
flux of the system includes: acquiring an exhaust pressure and an air return pressure
of the system, and a current operation frequency of the compressor; acquiring a saturation
exhaust temperature of the system according to the exhaust pressure; acquiring a saturation
air return temperature of the system according to the air return pressure; and acquiring
the current refrigerant flux according to the saturation exhaust temperature, the
saturation air return temperature and the current operation frequency.
[0054] According to an embodiment of the present disclosure, the current refrigerant flux
can be acquired by the following formula (1):

wherein G2 is the current refrigerant flux; S is the saturation air return temperature;
D is the saturation exhaust temperature; C0 to C9 are calculating coefficients and
are acquired according to the current operation frequency.
[0055] Specifically, during operation of the system, the saturation air return temperature
and the saturation exhaust temperature can be first calculated according to the air
return pressure and exhaust pressure of the compressor; and then ten coefficients
provided by a compressor manufacturer are utilized to calculate the current refrigerant
flux, that is the actual gas circulation amount, according to the operation frequency
of the compressor.
[0056] For example, table 3 shows ten coefficients provided by a certain compressor manufacturer.
Table 3
Reference number |
Capability C |
Primary side power P |
Primary side current A |
Mass flow M |
C0 |
157083.7038 |
-147.4029839 |
5.22452E-05 |
506.1576401 |
C1 |
5461.243994 |
-15.66866598 |
3.17939E-05 |
20.23765343 |
C2 |
-0.070791694 |
290.0853125 |
0.32866752 |
10.88823094 |
C3 |
56.50627815 |
-0.598613169 |
0.001438798 |
0.336176128 |
C4 |
-0.189212999 |
0.855442311 |
0.000855527 |
0.215924562 |
C5 |
-19.38408202 |
0.618120874 |
0.007960909 |
-0.159218374 |
C6 |
0.016318866 |
-0.000650971 |
1.89498E-05 |
-0.00096547 |
C7 |
-0.025955152 |
-0.004744646 |
-5.70037E-05 |
-0.000151881 |
C8 |
-0.452236172 |
0.003124316 |
-1.11086E-05 |
-0.002222256 |
C9 |
0.068265115 |
-0.00785332 |
-5.86867E-05 |
0.000640792 |
[0057] It should be noted that the calculating coefficients C0 to C9 in the formula (1)
are respectively the values corresponding to capability C in table 3.
[0058] In practical use, different compressor operation frequencies correspond to different
ten coefficients; a compressor manufacturer generally will provide ten coefficients
under a plurality of operation frequencies, for example the ten coefficients under
the operation frequencies of 30Hz, 60Hz, 75Hz, 90Hz and the like. In this case, first,
the ten coefficients under the current operation frequency can be acquired through
an interpolation algorithm according to the ten coefficients under different operation
frequencies; and then the current refrigerant flux of the system is acquired through
calculation by the formula (1) according to the ten coefficients under the current
operation frequency. For example, assuming that the current operation frequency of
the compressor is 70Hz, first, the ten coefficients under the operation frequency
70Hz can be acquired through the interpolation algorithm according to the ten coefficients
under the operation frequencies 60Hz and 75Hz, wherein the values corresponding to
the capability C in the ten coefficients are respectively the calculating coefficients
C0 to C9 under the operation frequency; and then the current refrigerant flux of the
system is acquired through calculation by the formula (1) according to the calculating
coefficients C0 to C9, the acquired saturation air return temperature and the saturation
exhaust temperature.
[0059] Certainly, the following calculation method is also acceptable: first, the refrigerant
flux of the system under the operation frequency 60Hz is acquired through calculation
by the formula (1) according to the ten coefficients under the operation frequency
60Hz, the acquired saturation air return temperature and the saturation exhaust temperature;
and the refrigerant flux of the system under the operation frequency 75Hz is acquired
through calculation by the formula (1) according to the ten coefficients under the
operation frequency 75Hz, the acquired saturation air return temperature and the saturation
exhaust temperature; then, the refrigerant flux of the system under the operation
frequency 70Hz, that is the current refrigerant flux of the system, is calculated
through the interpolation algorithm. It can be understood that compared with the former
method, the calculation amount of the latter method is greatly reduced. Therefore,
the latter method is preferably adopted.
[0060] It should be noted that the acquisition methods of the current refrigeration flux
under the cooling mode and the heating mode are the same.
[0061] S2, it is detected and determined that the current refrigerant flux is less than
or equal to the minimum refrigerant flux.
[0062] S3, a total oil discharge amount of the compressor since last time oil return is
acquired.
[0063] Specifically, each time the compressor operates, oil will be discharged; and the
oil discharge rate (equivalent to an oil drainage rate) of the compressor is known.
Therefore, the total oil discharge amount of the compressor can be acquired through
calculation according to the oil discharge rate of the compressor.
[0064] For example, the rate discharge rate of the compressor can be provided by a compressor
manufacturer, as shown in table 4.
Table 4
Minimum oil amount |
350ml |
Ex-factory oil amount |
500ml |
Safe oil drainage amount for calculation |
470cm3 |
Compressor exhaust volume |
36cm3/rev |
Oil dilution limit |
0.4 |
Minimum rotating speed |
30rps |
Maximum rotating speed |
90rps |
30rps oil drainage rate (%) |
0.41% |
60rps oil drainage rate (%) |
0.73% |
90rps oil drainage rate (%) |
1.56% |
120rps oil drainage rate (%) |
2.00% |
[0065] Table 4 provides different oil drainage rates under different rotating speeds; rotating
speeds are proportional to operation frequencies; therefore, oil drainage rates under
different rotating speeds can be acquired according to the proportional relationship
therebetween; then the oil drainage rate under the current operation frequency can
be acquired through the interpolation algorithm; and finally the total oil discharge
amount of the compressor can be acquired according to the oil drainage rate under
the current operation frequency, the current refrigerant flux, an operation time of
the compressor, and the density of the lubricating oil. For example, the total oil
discharge amount of the compressor = the oil drainage rate under the current operation
frequency
∗ the current refrigerant flux
∗ the operation time of the compressor / the density of the lubricating oil.
[0066] It should be noted that for a system provided with an oil separator, the total oil
discharge amount can also be acquired according to a separation efficiency of the
oil separator. For example, the total oil discharge amount of the compressor = the
oil drainage rate under the current operation frequency
∗ the current refrigerant flux
∗ (1- the separation efficiency of the oil separator)
∗ the operation time of the compressor / the density of the lubricating oil, wherein
the separation efficiency of the oil separator is generally 90%.
[0067] S4, it is detected and determined that the total oil discharge amount is greater
than a maximum safe oil discharge amount.
[0068] The maximum safe oil discharge amount can be acquired from data provided by the compressor
manufacturer. As shown in table 4, the maximum safe oil discharge amount of the compressor
is 470ml.
[0069] S5, the system is controlled to return oil.
[0070] To be specific, the minimum refrigerant flux required for carrying the lubricating
oil in the system back to the outdoor unit and the current refrigerant flux of the
system are acquired in real time during operation of the system; and whether the current
refrigerant flux is less than or equal to the minimum refrigerant flux is determined.
If so, then the current refrigerant flux is too low, and the lubricating oil cannot
normally return to the outdoor unit; in this case, the summarized oil discharge amount,
that is the total oil discharge amount of the compressor, is calculated, and whether
the total oil discharge amount is greater than a maximum safe oil discharge amount;
if so, then the current oil discharge amount is too great, which would be easy to
cause the compressor to operate in short of oil; therefore, the system is controlled
to return oil, so as to ensure that the compressor would not be damaged due to operation
in short of oil. Therefore, the present disclosure can ensure that the compressor
will not operate in short of oil due to great oil discharge amount and small oil return
amount, and can effectively improve the capability and energy efficiency of the multi-split
air conditioning system; furthermore, the method is simple and feasible.
[0071] Further, according to an embodiment of the present disclosure, the method further
includes: detecting and determining whether a duration of the current refrigerant
flux being greater than the minimum refrigerant flux is greater than a second preset
time when the current refrigerant flux is greater than the minimum refrigerant flux;
zero-clearing the total oil discharge amount, detecting and determining that a duration
since last time oil return is greater than a third preset time; and controlling the
system to return oil, wherein the third preset time > second preset time > the first
preset time; the first preset time, the second preset time and the third preset time
can be calibrated according to practical situations.
[0072] To be specific, if the current refrigerant flux is greater than the minimum refrigerant
flux and the duration is greater than the second preset time, then the current refrigerant
flux is sufficient; in this case, the lubricating oil can normally return to the outdoor
unit without specifically controlling oil return; and when the operation time of the
system since last time oil return is greater than the third preset time, the system
is controlled to return oil. Therefore, under the situation that the refrigerant flux
of the system is sufficient, special oil return processes should be reduced as few
as possible, so as to ensure indoor comfort.
[0073] According to an embodiment of the present disclosure, the method for controlling
oil return of a multi-split air conditioning system further includes: acquiring a
current operation mode of the system; controlling the system to return oil in a cooling
mode when the current operation mode is determined to be the cooling mode; and controlling
the system to return oil in a heating mode when the current operation mode is determined
to be the heating mode.
[0074] To be specific, if the system is currently in the cooling mode, then the system returns
oil in the cooling mode directly; and if the system is currently in the heating mode,
then the system returns oil in the heating mode directly, which can be realized by
utilizing the prior art, thus effectively avoiding the influence on indoor comfort
during oil return. For example, in the heating mode, when oil return is required,
if the system is switched to the cooling mode, then the indoor temperature would reduce,
and the indoor comfort would be influenced.
[0075] Further, in order to enable a person skilled in the art to more clearly understand
the present disclosure, the specific steps of the method for controlling oil return
of a multi-split air conditioning system in the cooling mode and in the heating mode
will be respectively described in detail hereafter. Fig. 4 is a flow chart of the
method for controlling oil return of a multi-split air conditioning system in the
cooling mode according to one embodiment of the present disclosure. As shown in Fig.
4, the method for controlling oil return of a multi-split air conditioning system
may include:
S401, the multi-split air conditioning system operates in a cooling mode;
S402, acquiring a temperature of an indoor heat exchanger tube of the indoor unit;
S403, calculating the minimum refrigerant flux G1;
S404, acquiring an air return pressure Pe and an air return temperature Te;
S405, calculating the current refrigerant flux G2;
S406, determining whether the current refrigerant flux G2 is greater than the minimum
refrigerant flux G1; if so, then executing the step S407; and if not, then executing
the step S411;
S407, determining whether a duration of the current refrigerant flux G2 being greater
than the minimum refrigerant flux G1 is greater than t1; if so, then executing the
step S408; and if not, then executing the step S402;
S408, zero-clearing the total oil discharge amount;
S409, determining whether a duration since last time oil return is greater than t2;
if so, then executing the step S410; and if not, then executing the step S402;
S410, returning oil in the cooling mode;
S411, acquiring a total oil discharge amount of the compressor since last time oil
return;
S412, determining whether the total oil discharge amount is greater than a maximum
safe oil discharge amount; if so, then executing the step S410; and if not, then executing
the step S402.
[0076] Fig. 5 is a flow chart of the method for controlling oil return of a multi-split
air conditioning system in the heating mode according to one embodiment of the present
disclosure. As shown in Fig. 5, the method for controlling oil return of a multi-split
air conditioning system may include:
S501, the multi-split air conditioning system operates in the heating mode;
S502, acquiring an exhaust pressure Pc;
S503, calculating the minimum refrigerant flux G1;
S504, acquiring an air return pressure Pe and an air return temperature Te;
S505, calculating the current refrigerant flux G2;
S506, determining whether the current refrigerant flux G2 is greater than the minimum
refrigerant flux G1; if so, then executing the step S507; and if not, then executing
the step S511;
S507, determining whether a duration of the current refrigerant flux G2 being greater
than the minimum refrigerant flux G1 is greater than t1; if so, then executing the
step S508; and if not, then executing the step S502;
S508, zero-clearing the total oil discharge amount;
S509, determining whether a duration since last time oil return is greater than t2;
if so, then executing the step S510; and if not, then executing the step S502;
S510, returning oil in the heating mode;
S511, acquiring a total oil discharge amount of the compressor since last time oil
return;
S512, determining whether the total oil discharge amount is greater than a maximum
safe oil discharge amount; if so, then executing the step S510; and if not, then executing
the step S502.
[0077] In the method for controlling oil return of a multi-split air conditioning system
according to the embodiment of the present disclosure, the minimum refrigerant flux
required for carrying the lubricating oil in the system back to the outdoor unit and
the current refrigerant flux of the system are acquired every the first preset time
during operation of the system; whether the current refrigerant flux is less than
or equal to the minimum refrigerant flux is detected and determined; the total oil
discharge amount of the compressor since last time oil return is acquired; whether
the total oil discharge amount is greater than the maximum safe oil discharge amount
is detected and determined; the system is controlled to return oil. Therefore, the
present disclosure can ensure that the compressor will not operate in short of oil
due to great oil discharge amount and small oil return amount, and can effectively
improve the capability and energy efficiency of the multi-split air conditioning system;
furthermore, the method is simple and feasible.
[0078] In addition, an embodiment of the present disclosure further provides a non-transitory
computer readable storage medium having stored therein a computer program that, when
executed by a processor, causes the processor to realize the method for controlling
oil return of a multi-split air conditioning system.
[0079] The non-transitory computer readable storage medium provided according to the embodiment
of the present disclosure, by means of the method for controlling oil return of a
multi-split air conditioning system, can ensure that the compressor will not operate
in short of oil due to great oil discharge amount and small oil return amount, and
can effectively improve the capability and energy efficiency of the multi-split air
conditioning system; furthermore, the method is simple and feasible.
[0080] Fig. 6 is a block diagram of the device for controlling oil return of a multi-split
air conditioning system according to one embodiment of the present disclosure.
[0081] In the embodiment of the present disclosure, the multi-split air conditioning system
includes an outdoor unit and a plurality of indoor units, wherein the outdoor unit
includes a compressor.
[0082] As shown in Fig. 6, the device for controlling oil return of a multi-split air conditioning
system according to the embodiment of the present disclosure may include: a first
acquisition module 100, a second acquisition module 200 and a control module 300.
[0083] The first acquisition module 100 is configured to acquire a minimum refrigerant flux
required for carrying a lubricating oil in the system back to the outdoor unit every
a first preset time during operation of the system; the second acquisition module
200 is configured to acquire a current refrigerant flux of the system every the first
preset time during operation of the system; and the control module 300 is configured
to detect and determine that the current refrigerant flux is less than or equal to
the minimum refrigerant flux, acquire a total oil discharge amount of the compressor
since last time oil return, detect and determine that the total oil discharge amount
is greater than a maximum safe oil discharge amount, and control the system to return
oil.
[0084] According to an embodiment of the present disclosure, the control module 300 is further
specifically configured to: detect and determine, when the current refrigerant flux
is greater than the minimum refrigerant flux, that a duration of the current refrigerant
flux being greater than the minimum refrigerant flux is greater than a second preset
time; zero-clear the total oil discharge amount, detect and determine that a duration
since last time oil return is greater than a third preset time, and control the system
to return oil, wherein the third preset time > the second preset time > the first
preset time.
[0085] According to an embodiment of the present disclosure, the device for controlling
oil return of a multi-split air conditioning system further includes: a third acquisition
module (not shown in the figure), wherein the third acquisition module is configured
to acquire a current operation mode of the system; the control module 300 is further
configured to control the system to return oil in a cooling mode when the current
operation mode is determined to be the cooling mode, and control the system to return
oil in a heating mode when the current operation mode is determined to be the heating
mode.
[0086] According to an embodiment of the present disclosure, when the current operation
mode is determined to be the cooling mode, the first acquisition module 100 is specifically
configured to: acquire a saturation evaporation temperature of the system, and acquire
a saturation evaporation pressure of the system according to the saturation evaporation
temperature; acquire a concentration of the lubricating oil, a density of the lubricating
oil, and an inner diameter of a refrigerant air tube in the system; and acquire the
minimum refrigerant flux from a preset table according to the saturation evaporation
pressure, the concentration of the lubricating oil, the density of the lubricating
oil, and the inner diameter of the refrigerant air tube.
[0087] According to an embodiment of the present disclosure, when the current operation
mode is determined to be the heating mode, the first acquisition module 100 is specifically
configured to: acquire an exhaust pressure of the system; acquire a concentration
of the lubricating oil, a density of the lubricating oil, and an inner diameter of
a refrigerant air tube in the system; and acquire the minimum refrigerant flux from
a preset table according to the exhaust pressure, the concentration of the lubricating
oil, the density of the lubricating oil, and the inner diameter of the refrigerant
air tube.
[0088] According to an embodiment of the present disclosure, the second acquisition module
200 is specifically configured to: acquire an exhaust pressure and an air return pressure
of the system, and a current operation frequency of the compressor; acquire a saturation
exhaust temperature of the system according to the exhaust pressure; acquire a saturation
air return temperature of the system according to the air return pressure; and acquire
the current refrigerant flux according to the saturation exhaust temperature, the
saturation air return temperature and the current operation frequency.
[0089] According to an embodiment of the present disclosure, the second acquisition module
200 acquires the current refrigerant flux by the following formula:

wherein G2 is the current refrigerant flux; S is the saturation air return temperature;
D is the saturation exhaust temperature; C0 to C9 are calculating coefficients and
are acquired according to the current operation frequency.
[0090] In the device for controlling oil return of a multi-split air conditioning system
according to the embodiment of the present disclosure, the first acquisition module
acquires the minimum refrigerant flux required for carrying the lubricating oil in
the system back to the outdoor unit every the first preset time during operation of
the system; the second acquisition module acquires the current refrigerant flux of
the system every the first preset time during operation of the system; and the control
module detects and determines that the current refrigerant flux is less than or equal
to the minimum refrigerant flux, acquires the total oil discharge amount of the compressor
since last time oil return, detects and determines that the total oil discharge amount
is greater than the maximum safe oil discharge amount, and
controls the system to return oil. Therefore, the present disclosure can ensure that
the compressor will not operate in short of oil due to great oil discharge amount
and small oil return amount, and can effectively improve the capability and energy
efficiency of the multi-split air conditioning system; furthermore, the method is
simple and feasible.
[0091] In addition, an embodiment of the present disclosure further provides a multi-split
air conditioning system, the multi-split air conditioning system including the device
for controlling oil return of a multi-split air conditioning system.
[0092] The multi-split air conditioning system provided according to the embodiment of the
present disclosure, by means of the device for controlling oil return of a multi-split
air conditioning system, can ensure that the compressor will not operate in short
of oil due to great oil discharge amount and small oil return amount, and can effectively
improve the capability and energy efficiency of the multi-split air conditioning system;
furthermore, the method is simple and feasible.
[0093] In addition, In the descriptions of the present disclosure, the azimuth or position
relationships indicated by the terms "center", "longitudinal", "transverse", "length",
"width", "thickness", "upper", "lower", "front", "back", "left", "right", "vertical",
"horizontal", "top", "bottom", "inside", "outside", "clockwise", "anticlockwise",
"axial direction", "radial direction", "circumferential" and the like are on the basis
of the azimuth and position relationships as shown in the drawings, and are only intended
to facilitate and simplify the description of the present disclosure, but not intended
to indicate or imply that the designated devices or elements must have a specific
azimuth or are constructed and operated in a specific azimuth. Therefore, the terms
cannot be considered to limit the present disclosure.
[0094] In addition, the terms "first" and "second" are used for the purpose of description
only, but cannot be considered to indicate or imply relative importance or implicitly
indicate the number of the indicated technical features. Therefore, a feature defined
by "first" or "second" may explicitly or implicitly include at least one of the features.
In the description of the present disclosure, unless otherwise stated, "a plurality
of' means at least two, for example, two, three and the like.
[0095] In the present disclosure, unless otherwise specified and stated, a first feature
being "on" or "under" a second feature means that the first feature and the second
feature can be in direct contact, or in indirect contact via an intermediate medium.
Furthermore, the first feature being "on", "above" and "over" the second feature means
that the first feature can be right above or obliquely above the second feature, or
only denotes that the horizontal height of the first feature is greater than that
of the second feature. The first feature being "under", "below" and "underneath" the
second feature means that the first feature can be right below or obliquely below
the second feature, or only denotes that the horizontal height of the first feature
is less than that of the second feature.
[0096] In the description of the specification, the reference terms "one embodiment", "some
embodiments", "example", "a specific example" or "some examples" and the like mean
that the specific characteristic, structure, material or feature described in combination
with the embodiment or the example are contained in at least one embodiment or example
of the present disclosure. In the specification, the schematic recitation of the above-described
terms does not necessarily refer to the same embodiment or example. Furthermore, the
described specific characteristic, structure, material or feature can be combined
in an appropriate manner in any one or more embodiments or examples. In addition,
under the situation of having no conflict, a person skilled in the art can combine
or incorporate different embodiments or examples described in the specification and
the features of the different embodiments or examples.
[0097] Although the embodiments of the present disclosure have been shown and described
hereabove, it can be understood that the above-described embodiments are only for
illumination, but not intended to limit the present disclosure. And a person skilled
in the art can make various changes, modifications, substitutions and variations to
the above-described embodiments in the scope of the present disclosure.
1. A method for controlling oil return of a multi-split air conditioning system, the
multi-split air conditioning system comprising an outdoor unit and a plurality of
indoor units, wherein the outdoor unit comprises a compressor; the method comprises:
acquiring a minimum refrigerant flux required for carrying a lubricating oil in the
system back to the outdoor unit and a current refrigerant flux of the system every
a first preset time during operation of the system;
detecting and determining that the current refrigerant flux is less than or equal
to the minimum refrigerant flux;
acquiring a total oil discharge amount of the compressor since last time oil return;
detecting and determining that the total oil discharge amount is greater than a maximum
safe oil discharge amount; and
controlling the system to return oil.
2. The method for controlling oil return of a multi-split air conditioning system according
to claim 1, further comprising:
detecting and determining that a duration of the current refrigerant flux being greater
than the minimum refrigerant flux is greater than a second preset time when the current
refrigerant flux is greater than the minimum refrigerant flux;
zero-clearing the total oil discharge amount, detecting and determining that a duration
since last time oil return is greater than a third preset time; and
controlling the system to return oil, wherein the third preset time > the second preset
time > the first preset time.
3. The method for controlling oil return of a multi-split air conditioning system according
to claim 1 or 2, further comprising:
acquiring a current operation mode of the system;
controlling the system to return oil in a cooling mode when the current operation
mode is determined to be the cooling mode; and
controlling the system to return oil in a heating mode when the current operation
mode is determined to be the heating mode.
4. The method for controlling oil return of a multi-split air conditioning system according
to claim 3, wherein acquiring a minimum refrigerant flux required for carrying a lubricating
oil in the system back to the outdoor unit in the cooling mode comprises:
acquiring a saturation evaporation temperature of the system, and acquiring a saturation
evaporation pressure of the system according to the saturation evaporation temperature;
acquiring a concentration of the lubricating oil, a density of the lubricating oil,
and an inner diameter of a refrigerant air tube in the system; and
acquiring the minimum refrigerant flux from a preset table according to the saturation
evaporation pressure, the concentration of the lubricating oil, the density of the
lubricating oil, and the inner diameter of the refrigerant air tube.
5. The method for controlling oil return of a multi-split air conditioning system according
to claim 3, wherein acquiring a minimum refrigerant flux required for carrying a lubricating
oil in the system back to the outdoor unit in the heating mode comprises:
acquiring an exhaust pressure of the system;
acquiring a concentration of the lubricating oil, a density of the lubricating oil,
and an inner diameter of a refrigerant air tube in the system; and
acquiring the minimum refrigerant flux from a preset table according to the exhaust
pressure, the concentration of the lubricating oil, the density of the lubricating
oil, and the inner diameter of the refrigerant air tube.
6. The method for controlling oil return of a multi-split air conditioning system according
to claim 1 or 2, wherein the acquiring the current refrigerant flux of the system
comprises:
acquiring an exhaust pressure and an air return pressure of the system, and a current
operation frequency of the compressor;
acquiring a saturation exhaust temperature of the system according to the exhaust
pressure;
acquiring a saturation air return temperature of the system according to the air return
pressure; and
acquiring the current refrigerant flux according to the saturation exhaust temperature,
the saturation air return temperature and the current operation frequency.
7. The method for controlling oil return of a multi-split air conditioning system according
to claim 6, wherein the current refrigerant flux is acquired by the following formula:

wherein G2 is the current refrigerant flux; S is the saturation air return temperature;
D is the saturation exhaust temperature; C0 to C9 are calculating coefficients and
are acquired according to the current operation frequency.
8. A non-transitory computer readable storage medium having stored therein a computer
program that, when executed by a processor, causes the processor to realize the method
for controlling oil return of a multi-split air conditioning system according to any
one of claims 1 to 7.
9. A device for controlling oil return of a multi-split air conditioning system, the
multi-split air conditioning system comprising an outdoor unit and a plurality of
indoor units, wherein the outdoor unit comprises a compressor; the device comprises:
a first acquisition module, configured to acquire a minimum refrigerant flux required
for carrying a lubricating oil in the system back to the outdoor unit every a first
preset time during operation of the system;
a second acquisition module, configured to acquire a current refrigerant flux of the
system every the first preset time during operation of the system; and
a control module, configured to detect and determine that the current refrigerant
flux is less than or equal to the minimum refrigerant flux, acquire a total oil discharge
amount of the compressor since last time oil return, detect and determine that the
total oil discharge amount is greater than a maximum safe oil discharge amount, and
control the system to return oil.
10. The device for controlling oil return of a multi-split air conditioning system according
to claim 9, wherein the control module is further specifically configured to: detect
and determine, when the current refrigerant flux is greater than the minimum refrigerant
flux, that a duration of the current refrigerant flux being greater than the minimum
refrigerant flux is greater than a second preset time; zero-clear the total oil discharge
amount, detect and determine that a duration since last time oil return is greater
than a third preset time, and control the system to return oil, wherein the third
preset time > the second preset time > the first preset time.
11. The device for controlling oil return of a multi-split air conditioning system according
to claim 9 or 10, wherein the device further comprises:
a third acquisition module, configured to acquire a current operation mode of the
system,
wherein the control module is further configured to control the system to return oil
in a cooling mode when the current operation mode is determined to be the cooling
mode, and control the system to return oil in a heating mode when the current operation
mode is determined to be the heating mode.
12. The device for controlling oil return of a multi-split air conditioning system according
to claim 11, wherein when the current operation mode is determined to be the cooling
mode, the first acquisition module is specifically configured to
acquire a saturation evaporation temperature of the system, and acquire a saturation
evaporation pressure of the system according to the saturation evaporation temperature;
acquire a concentration of the lubricating oil, a density of the lubricating oil,
and an inner diameter of a refrigerant air tube in the system; and
acquire the minimum refrigerant flux from a preset table according to the saturation
evaporation pressure, the concentration of the lubricating oil, the density of the
lubricating oil, and the inner diameter of the refrigerant air tube.
13. The device for controlling oil return of a multi-split air conditioning system according
to claim 11, wherein when the current operation mode is determined to be the heating
mode, the first acquisition module is specifically configured to
acquire an exhaust pressure of the system;
acquire a concentration of the lubricating oil, a density of the lubricating oil,
and an inner diameter of a refrigerant air tube in the system; and
acquire the minimum refrigerant flux from a preset table according to the exhaust
pressure, the concentration of the lubricating oil, the density of the lubricating
oil, and the inner diameter of the refrigerant air tube.
14. The device for controlling oil return of a multi-split air conditioning system according
to claim 9 or 10, wherein the second acquisition module is specifically configured
to
acquire an exhaust pressure and an air return pressure of the system, and a current
operation frequency of the compressor;
acquire a saturation exhaust temperature of the system according to the exhaust pressure;
acquire a saturation air return temperature of the system according to the air return
pressure; and
acquire the current refrigerant flux according to the saturation exhaust temperature,
the saturation air return temperature and the current operation frequency.
15. The device for controlling oil return of a multi-split air conditioning system according
to claim 14, wherein the second acquisition module is configured to acquire the current
refrigerant flux by the following formula:

wherein G2 is the current refrigerant flux; S is the saturation air return temperature;
D is the saturation exhaust temperature; C0 to C9 are calculating coefficients and
are acquired according to the current operation frequency.
16. A multi-split air conditioning system, comprising the device for controlling oil return
of a multi-split air conditioning system according to any one of claims 9 to 15.