Technical Field
[0001] The present invention relates to the field of air conditioning and low temperature
storage of commodities, and more specifically, to a refrigeration system and a control
method thereof.
Background Art
[0002] At present, at least two refrigeration systems need to be provided in a place like
a conventional convenience store. One refrigeration system is used for providing refrigerating
capacity to a refrigerated display cabinet for exhibition and sales of commodities,
and the other refrigeration system is used for providing the application place with
the cooling/heating air-conditioning effect according to the change in seasons. Since
the outdoor unit of the refrigerated display cabinet is constantly in a heat dissipation
state, the heat utilization rate will be undoubtedly improved if the heat dissipated
by the outdoor unit can be utilized to provide some heat when the air conditioning
system needs to work in a heating mode.
[0003] However, how to couple the two refrigeration systems with independent functions and
provide a heat recovery function becomes a technical problem to be solved urgently.
Summary of the Invention
[0004] This application is aimed at providing a refrigeration system and a control method
thereof, so as to improve the utilization rate of energy between refrigeration circulation
for air conditioning and refrigeration circulation for refrigerating or freezing products.
[0005] According to one aspect of this application, a refrigeration system is provided,
including: a refrigeration circuit including a compressor, a condenser and an evaporation
portion provided with a throttle element that are sequentially connected to form a
circuit, wherein the evaporation portion includes a first-type evaporation branch
and a second-type evaporation branch that are connected in parallel, the first-type
evaporation branch is used for air conditioning, and the second-type evaporation branch
is used for refrigerating or freezing products; and a heat recovery branch having
a first end and a second end that are connected into the refrigeration circuit from
between the downstream section of the compressor and the upstream section of the condenser,
and a heat-recovery heat exchanger disposed thereon, wherein the first-type evaporation
branch has a first evaporator and a first fan for driving air to flow through the
first evaporator, and the heat-recovery heat exchanger is disposed upstream or downstream
of the first evaporator in the direction of air flowing through the first evaporator.
[0006] Optionally, the refrigeration system further includes a flow path switching portion
controlled to switch on or switch off the heat recovery branch.
[0007] Optionally, the flow path switching portion includes a three-way valve disposed at
the first end or the second end of the heat recovery branch.
[0008] Optionally, the flow path switching portion includes a first switch valve and a second
switch valve, wherein the first switch valve is disposed on the heat recovery branch,
and the second switch valve is disposed on a refrigeration circuit section between
the first end and the second end.
[0009] Optionally, the refrigeration system further includes an evaporation pressure regulator
disposed on the first-type evaporation branch and located downstream of the first
evaporator.
[0010] Optionally, the refrigeration system further includes a gas-liquid separator disposed
on the refrigeration circuit upstream of an air suction port of the compressor.
[0011] Optionally, the evaporation portion has a plurality of throttle elements, and throttle
elements of the first-type evaporation branch and the second-type evaporation branch
have different throttling degrees.
[0012] Optionally, the evaporation portion has a plurality of switch valves that are each
used for controlling on/off state of the first-type evaporation branch and/or on/off
state of the second-type evaporation branch.
[0013] Optionally, the refrigeration system further includes a one-way valve disposed on
the refrigeration circuit between an exhaust port of the compressor and the first
end of the heat recovery branch.
[0014] According to another aspect of this application, a control method of a refrigeration
system for the aforementioned refrigeration system is further provided. The control
method includes: in a first mode S100, switching off the heat recovery branch, so
that a refrigerant sequentially flows through the compressor, the condenser, and the
first-type evaporation branch and the second-type evaporation branch that are connected
in parallel; in a second mode S200, switching on the heat recovery branch, so that
the refrigerant sequentially flows through the compressor, the heat recovery branch,
the condenser, and the second-type evaporation branch; in a third mode S300, switching
on the heat recovery branch, so that the refrigerant sequentially flows through the
compressor, the heat recovery branch, the condenser, and the first-type evaporation
branch and the second-type evaporation branch that are connected in parallel; and
in a fourth mode S400, switching off the heat recovery branch, so that the refrigerant
sequentially flows through the compressor, the condenser, and the second-type evaporation
branch.
[0015] Optionally, the first mode S100 is performed when an outlet air temperature of the
first evaporator is not less than a first pre-set temperature; and/or the second mode
S200 is performed when the outlet air temperature of the first evaporator is less
than a second pre-set temperature.
[0016] Optionally, the third mode S300 is performed when the outlet air temperature of the
first evaporator is not greater than a third pre-set temperature while performing
the first mode S100; and/or the first mode S100 is maintained when the outlet air
temperature of the first evaporator is greater than the third pre-set temperature.
[0017] Optionally, the first mode S100 is performed when the outlet air temperature of the
first evaporator is not less than the third pre-set temperature while performing the
third mode S300; and/or the third mode S300 is maintained when the outlet air temperature
of the first evaporator is less than the third pre-set temperature.
[0018] Optionally, the first fan is kept on and the heat recovery branch is switched off
when the outlet air temperature of the first evaporator is not less than a fourth
pre-set temperature while performing the second mode S200; and/or the second mode
S200 is maintained when the outlet air temperature of the first evaporator is less
than the fourth pre-set temperature.
[0019] Optionally, the first pre-set temperature is 23°C to 26°C.
[0020] Optionally, the second pre-set temperature is 8°C to 10°C.
[0021] Optionally, the third pre-set temperature is 13°C to 16°C.
[0022] Optionally, the fourth pre-set temperature is 16°C to 23°C.
[0023] According to the refrigeration system and the control method thereof in this application,
heat recycling is realized by disposing, on a refrigeration circuit, a heat recovery
branch having a first end and a second end that are connected into the refrigeration
circuit from between the downstream section of a compressor and the upstream section
of a condenser, arranging a heat-recovery heat exchanger disposed on the heat recovery
branch and a first evaporator at upstream and downstream positions in an air flow
direction, and controlling on/off state of a flow path, thereby effectively achieving
low temperature preservation of commodities in a refrigerated display cabinet, air
conditioning for a commercial environment (such as a convenience store) where the
refrigerated display cabinet is located, and energy efficiency improvement for the
whole refrigeration system at the same time.
Brief Description of the Drawings
[0024]
FIG. 1 is a schematic diagram of a system flow direction of a refrigeration system
in a first mode.
FIG. 2 is a schematic diagram of a system flow direction of a refrigeration system
in a second mode.
FIG. 3 is a schematic diagram of a system flow direction of a refrigeration system
in a third mode.
FIG. 4 is a schematic diagram of a system flow direction of a refrigeration system
in a fourth mode.
Detailed description
[0025] As shown in FIG. 1 to FIG. 3, according to an embodiment of this application, a refrigeration
system is provided, which includes a refrigeration circuit for providing a refrigerating
capacity. The refrigeration circuit is formed by sequentially connecting a compressor
4, a condenser 1 and an evaporation portion provided with a throttle element. The
evaporation portion includes a first-type evaporation branch and a second-type evaporation
branch that are connected in parallel. The first-type evaporation branch here mainly
refers to a type of evaporation branch for air conditioning, and it is feasible to
arrange a plurality of such evaporation branches or arrange a plurality of evaporators
on such an evaporation branch according to an actual refrigerating capacity demand
or a refrigeration area demand. The second-type evaporation branch here mainly refers
to a type of evaporation branch for refrigerating or freezing products. Similarly,
it is feasible to arrange a plurality of such evaporation branches or arrange a plurality
of evaporators on such an evaporation branch according to an actual refrigerating
capacity demand or a refrigeration area demand. In addition, the refrigeration system
further includes a heat recovery branch. The heat recovery branch has a first end
and a second end that are connected into the refrigeration circuit from between the
downstream section of the compressor 4 and the upstream section of the condenser 1,
and a heat-recovery heat exchanger 8 is disposed on the heat recovery branch. Because
the refrigeration circuit used for refrigerating or freezing products needs to stay
in a refrigerating state constantly, heat thereof can be recovered and used for air
conditioning. Therefore, the heat-recovery heat exchanger 8 needs to be disposed at
a heat exchange part passing through the first-type evaporation branch. For example,
since the first-type evaporation branch has a first evaporator 9 and a first fan for
driving air to flow through the first evaporator 9, the heat-recovery heat exchanger
8 may be disposed downstream or upstream of the first evaporator 9. Hence, the heat-recovery
heat exchanger 8 and the first evaporator 9 can share an air outlet 7 of the first
evaporator. In this case, when air conditioning is needed to provide heat, the heat
recovery branch can be switched on while the first-type evaporation branch is switched
off, and then the air outlet 7 will blow hot air. Or when air conditioning is needed
for refrigeration while ambient temperature and humidity need to be controlled, the
heat recovery branch can be switched on while the first-type evaporation branch is
switched on; therefore, the air outlet 7 can blow cold air generally, with the temperature
and humidity thereof changing in a certain degree. Through the foregoing arrangement,
heat recovery of the whole system is taken into account while refrigeration of commodities
and air conditioning are realized, thus improving the comprehensive energy efficiency
ratio.
[0026] Many details of the refrigeration system are further changed here, such as specific
implementation forms of various functional components or a connection relationship
between components, which will be illustrated exemplarily below.
[0027] For example, the heat-recovery heat exchanger 8 is disposed downstream the first
evaporator 9 in the direction of air flowing through the first evaporator 9, that
is, the heat-recovery heat exchanger 8 is disposed closer to the air outlet of the
first evaporator.
[0028] For another example, in order to realize switching of the refrigeration system between
a main circuit and the heat recovery circuit, the refrigeration system should further
include a flow path switching portion that can be controlled to switch on or switch
off the heat recovery branch. As an example, the flow path switching portion includes
a three-way valve 6. The three-way valve 6 is disposed at the first end or the second
end of the heat recovery branch. Then the heat recovery branch can be switched on
or off by opening or closing the three-way valve 6. Although not shown in the figure,
as another example, the flow path switching portion may include a first switch valve
and a second switch valve. The first switch valve is disposed on the heat recovery
branch to control on/off state of the heat recovery branch. The second switch valve
is disposed on a refrigeration circuit section between the first end and the second
end to control on/off state of the refrigeration circuit section.
[0029] In addition, the refrigeration system may further include an evaporation pressure
regulator 12 disposed on the first-type evaporation branch and located downstream
of the first evaporator 9. Because air conditioning and refrigeration of commodities
have different requirements on the operating evaporation temperature needed by the
evaporator, the evaporation pressure regulator 12 disposed here can desirably adjust
the temperature of the evaporator on the first-type evaporation branch for air conditioning.
[0030] Besides, the refrigeration system further includes a gas-liquid separator 3 disposed
on the refrigeration circuit upstream of an air suction port of the compressor 4 to
perform gas-liquid separation on a refrigerant flowing into the compressor, thus preventing
the liquid refrigerant from entering the compressor to cause liquid hammering. Optionally,
a one-way valve 5 can further be disposed on the refrigeration circuit between an
exhaust port of the compressor 4 and the first end of the heat recovery branch to
avoid refrigerant backflow.
[0031] In addition, the evaporation portion has a plurality of throttle elements, for example,
a first thermostatic expansion valve 10 and second thermostatic expansion valves 14
and 18. Throttle elements of the first-type evaporation branch and the second-type
evaporation branch have different throttling degrees to meet requirements corresponding
to different refrigeration capabilities in different application situations. Moreover,
a plurality of switch valves can further be disposed on the evaporation portion. For
example, a first solenoid valve 11 and second solenoid valves 13 and 17 are each used
for controlling on/off state of the first-type evaporation branch and/or on/off state
of the second-type evaporation branch, so as to implement on/off control over each
circuit as required.
[0032] In addition, to better manage and control the refrigeration system in the foregoing
embodiment so that the system can realize heat recovery while meeting actual refrigeration
and ventilation requirements, a control method of the refrigeration system is further
provided correspondingly. The control method includes: a first mode S100, in which
the heat recovery branch is switched off so that a refrigerant sequentially flows
through the compressor 4, the condenser 1, and the first evaporation branch and the
second evaporation branch that are connected in parallel, where functions of air-conditioning
refrigeration and commodity refrigeration can be realized at the same time in this
mode; a second mode S200, in which the heat recovery branch is switched on so that
the refrigerant sequentially flows through the compressor 4, the heat recovery branch,
the condenser 1, and the second evaporation branch, where functions of air-conditioning
heating and commodity refrigeration can be realized at the same time in this mode;
a third mode S300, in which the heat recovery branch is switched on so that the refrigerant
sequentially flows through the compressor 4, the heat recovery branch, the condenser
1, and the first evaporation branch and the second evaporation branch that are connected
in parallel, where functions of air conditioning and commodity refrigeration can be
realized at the same time in this mode; and a fourth mode S400, in which the heat
recovery branch is switched off so that the refrigerant sequentially flows through
the compressor, the condenser, and the second evaporation branch, where the function
of commodity refrigeration can be realized alone in this mode.
[0033] It should be noted that the foregoing operating modes can be switched manually or
switched under automatic control. In an actual application, excessively dry or humid
air will cause physical discomfort. Besides, the humidity of air also has a double-sided
influence on preservation of refrigerated commodities. For example, if the air is
too humid, bacteria easily grow in the commodities (especially foods); if the air
is too dry, foods are easily dehydrated. Therefore, an operator can selectively switch
the mode according to the foregoing influence to meet the actual application situation.
In addition, when the form of automatic control is adopted, corresponding switching
conditions need to be provided. Switching conditions of the operating modes will be
illustrated exemplarily below.
[0034] First, when an outlet air temperature of the first evaporator 9 is not less than
a first pre-set temperature, e.g., 27°C, it indicates that an ambient temperature
in an application scenario is too high at this time, and the first mode S100 should
be performed; or when the outlet air temperature of the first evaporator 9 is less
than a second pre-set temperature, e.g., 7°C, it indicates that the ambient temperature
in the application scenario is too low at this time, and the second mode S200 should
be performed.
[0035] After that, if it is already in the first mode S100, when the outlet air temperature
of the first evaporator 9 is not greater than a third pre-set temperature, e.g., 11°C,
it indicates that an air refrigerating temperature is too low at this time, and the
third mode S300 should be performed, thereby achieving a reheating and dehumidification
effect; or when the outlet air temperature of the first evaporator 9 is greater than
the third pre-set temperature, it indicates that the air refrigerating temperature
is appropriate at this time, and the first mode S100 can be maintained.
[0036] After that, if it is already in the third mode S300, when the outlet air temperature
of the first evaporator 9 is not less than the third pre-set temperature, e.g., 18°C,
it indicates that the air refrigerating temperature has been adjusted to the appropriate
range at this time, and the first mode S100 can be performed again; or when the outlet
air temperature of the first evaporator 9 is less than the third pre-set temperature,
it indicates that the air refrigerating temperature is still low at this time, and
the third mode S300 can be maintained.
[0037] In addition, if it is already in the second mode S200, when the outlet air temperature
of the first evaporator 9 is not less than a fourth pre-set temperature, it indicates
that an air heating temperature is already in an appropriate range at this time, and
the first fan can be kept on and the heat recovery branch can be switched off; or
when the outlet air temperature of the first evaporator 9 is less than the fourth
pre-set temperature, it indicates that the air heating temperature is still low at
this time, and the second mode S200 can be maintained.
[0038] The following will describe operating processes of the refrigeration system in different
modes respectively as well as technical effects on a product application environment
(such as a convenience store) with reference to FIG. 1 to FIG. 4. In the figures,
a solid line represents that the flow path is in an on-state, and a dashed line represents
that the flow path is in an off-state. The bold solid arrow at the heat exchanger
represents the flow direction of air, and the thin solid arrow on the pipeline of
the refrigeration system represents the flow direction of the refrigerant.
[0039] Referring to FIG. 1, when the first mode S100 is run, the heat recovery branch is
switched off, while the first-type evaporation branch and the second-type evaporation
branch are switched on. In this case, the high-pressure high-temperature refrigerant
flows out from the exhaust port of the compressor 4, and flows into the condenser
1 through the one-way valve 5 and the closed three-way valve 6 to dissipate heat to
the air flow that is driven by the fan 2 to flow through the condenser 1. The high-pressure
medium-temperature refrigerant that flows out thereafter is divided into two parts
that continue to move on. One part of the refrigerant flows into the first-type evaporation
branch and becomes low in pressure and low in temperature after being throttled by
the switched-on first solenoid valve 11 and first thermostatic expansion valve 10,
and then enters the first evaporator 9 to absorb heat. In this case, the temperature
of the air flow that is driven by the fan to flow through the first evaporator 9 can
be reduced, and the air flow is blown into the convenience store through the air outlet
7 to provide a shopping environment with comfortable temperature and humidity for
consumers and shop assistants. The low-pressure medium-temperature refrigerant that
flows out after absorbing heat will flow back to the air suction port of the compressor
4 through the gas-liquid separator 3, thus completing circulation of this part. Besides,
the other part of the refrigerant will flow into the second-type evaporation branch.
For example, in this embodiment, there are two second-type branches. The refrigerant
becomes low in pressure and low in temperature after being throttled by the switched-on
second solenoid valves 13 and 17 as well as second thermostatic expansion valves 14
and 18, and then enters the second evaporators 15 and 19 to absorb heat. In this case,
the temperature of the air flow that is driven by the fans 16 and 20 to flow through
the second evaporators 15 and 19 can be reduced, and is blown to exhibited commodities
stored in the refrigerated display cabinet, thus providing a preservation environment
with suitable temperature and humidity for the commodities. The low-pressure medium-temperature
refrigerant that flows out after absorbing heat will flow back to the air suction
port of the compressor 4 through the gas-liquid separator 3, thus completing circulation
of this part. Hence, one round of circulation of the first mode is completed.
[0040] Referring to FIG. 2, when the second mode S200 is run, the heat recovery branch is
switched on, the first-type evaporation branch is switched off, and the second-type
evaporation branch is switched on. In this case, the high-pressure high-temperature
refrigerant flows out from the exhaust port of the compressor 4 and flows into the
heat-recovery heat exchanger 8 through the one-way valve 5 and the opened three-way
valve 6. In this case, the temperature of the air flow that is driven by the fan to
flow through the heat-recovery heat exchanger 8 can be increased and is blown in to
the convenience store through the air outlet 7 to provide a shopping environment with
comfortable temperature and humidity for consumers and shop assistants. After that,
the refrigerant flows into the condenser 1, to dissipate heat to the air flow that
is driven by the fan 2 to flow through the condenser 1. The high-pressure medium-temperature
refrigerant that flows out thereafter will flow into the second-type evaporation branch.
For example, in this embodiment, there are two second-type branches. The refrigerant
becomes low in pressure and low in temperature after being throttled by the switched-on
second solenoid valves 13 and 17 as well as second thermostatic expansion valves 14
and 18, and then enters the second evaporators 15 and 19 to absorb heat. In this case,
the temperature of the air flow that is driven by the fans 16 and 20 to flow through
the second evaporators 15 and 19 can be reduced, and is blown to exhibited commodities
stored in the refrigerated display cabinet, thus providing a preservation environment
with suitable temperature and humidity for the commodities. The low-pressure medium-temperature
refrigerant that flows out after absorbing heat will flow back to the air suction
port of the compressor 4 through the gas-liquid separator 3, thus completing one round
of circulation of the second mode.
[0041] Referring to FIG. 3, when the third mode S300 is run, the heat recovery branch, the
first-type evaporation branch, and the second-type evaporation branch are switched
on. In this case, the high-pressure high-temperature refrigerant flows out from the
exhaust port of the compressor 4, and flows into the heat-recovery heat exchanger
8 through the one-way valve 5 and the opened three-way valve 6, to provide a temperature
and humidity regulation space for the air flow that is subsequently driven by the
fan to pass through the first evaporator 9 and the heat-recovery heat exchanger 8
sequentially. After that, the refrigerant flows into the condenser 1 to dissipate
heat to the air flow that is driven by the fan 2 to flow through the condenser 1.
The high-pressure medium-temperature refrigerant that flows out thereafter is divided
into two parts that continue to move on. One part of the refrigerant flows into the
first-type evaporation branch and becomes low in pressure and low in temperature after
being throttled by the switched-on first solenoid valve 11 and first thermostatic
expansion valve 10, and then enters the first evaporator 9 to absorb heat. In this
case, the temperature of the air flow that is driven by the fan to flow through the
first evaporator 9 can be reduced. The air flow continues to flow through the heat-recovery
heat exchanger 8 so that the temperature is increased by some degrees to make the
outlet air more comfortable. Then, the air flow is blown into the convenience store
through the air outlet 7 to provide a shopping environment with comfortable temperature
and humidity for consumers and shop assistants. The low-pressure medium-temperature
refrigerant that flows out after absorbing heat will flow back to the air suction
port of the compressor 4 through the gas-liquid separator 3, thus completing circulation
of this part. Besides, the other part of the refrigerant will flow into the second-type
evaporation branch. For example, in this embodiment, there are two second-type branches.
The refrigerant becomes low in pressure and low in temperature after being throttled
by the switched on second solenoid valves 13 and 17 as well as second thermostatic
expansion valves 14 and 18, and then enters the second evaporators 15 and 19 to absorb
heat. In this case, the temperature of the air flow that is driven by the fans 16
and 20 to flow through the second evaporators 15 and 19 can be reduced, and is blown
to exhibited commodities stored in the refrigerated display cabinet, thus providing
a preservation environment with suitable temperature and humidity for the commodities.
The low-pressure medium-temperature refrigerant that flows out after absorbing heat
will flow back to the air suction port of the compressor 4 through the gas-liquid
separator 3, thus completing circulation of this part. Hence, one round of circulation
of the third mode is completed.
[0042] Referring to FIG. 4, when the fourth mode S400 is run, the heat recovery branch is
switched off, the first-type evaporation branch is switched off, and the second-type
evaporation branch is switched on. In this case, the high-pressure high-temperature
refrigerant flows out from the exhaust port of the compressor 4, and flows into the
condenser 1 through the one-way valve 5 and the opened three-way valve 6, to dissipate
heat to the air flow that is driven by the fan 2 to flow through the condenser 1.
The high-pressure medium-temperature refrigerant that flows out thereafter will flow
into the second-type evaporation branch. For example, in this embodiment, there are
two second-type branches. The refrigerant becomes low in pressure and low in temperature
after being throttled by the switched-on second solenoid valves 13 and 17 as well
as second thermostatic expansion valves 14 and 18, and then enters the second evaporators
15 and 19 to absorb heat. In this case, the temperature of the air flow that is driven
by the fans 16 and 20 to flow through the second evaporators 15 and 19 can be reduced,
and is blown to exhibited commodities stored in the refrigerated display cabinet,
thus providing a preservation environment with suitable temperature and humidity for
the commodities. The low-pressure medium-temperature refrigerant that flows out after
absorbing heat will flow back to the air suction port of the compressor 4 through
the gas-liquid separator 3, thus completing one round of circulation of the fourth
mode.
[0043] Although the foregoing embodiment shows that the heat-recovery heat exchanger 8 is
disposed downstream of the first evaporator 9 in the direction of air flowing through
the first evaporator 9, those of ordinary skill in the art should understand that
the heat-recovery heat exchanger 8 can also be disposed upstream the first evaporator
9 in the direction of air flowing through the first evaporator 9.
[0044] The examples above mainly illustrate the refrigeration system and the control method
thereof in the present invention. Although only some implementations of the present
invention are described, those of ordinary skill in the art should understand that
the present invention can be implemented in many other forms without departing from
the subject and scope of the present invention. Therefore, the examples and implementations
shown are regarded as illustrative rather than limitative, and the present invention
can cover various modifications and replacements without departing from the scope
of the present invention as defined in the appended claim.
1. A refrigeration system, comprising:
a refrigeration circuit comprising a compressor (4), a condenser (1) and an evaporation
portion provided with a throttle element that are sequentially connected to form a
circuit, wherein the evaporation portion comprises a first-type evaporation branch
and a second-type evaporation branch that are connected in parallel, the first-type
evaporation branch is used for air conditioning, and the second-type evaporation branch
is used for refrigerating or freezing products; and
a heat recovery branch having a first end and a second end that are connected into
the refrigeration circuit from between the downstream section of the compressor and
the upstream section of the condenser, and a heat-recovery heat exchanger (8) disposed
thereon,
wherein the first-type evaporation branch has a first evaporator (9) and a first fan
for driving air to flow through the first evaporator, and the heat-recovery heat exchanger
is disposed upstream or downstream of the first evaporator in the direction of air
flowing through the first evaporator.
2. The refrigeration system according to Claim 1, characterised by further comprising a flow path switching portion controlled to switch on or switch
off the heat recovery branch.
3. The refrigeration system according to Claims 1 or 2, characterised in that the flow path switching portion comprises a three-way valve (6) disposed at the first
end or the second end of the heat recovery branch.
4. The refrigeration system according to any of Claims 1 to 3, characterised in that the flow path switching portion comprises a first switch valve and a second switch
valve, wherein the first switch valve is disposed on the heat recovery branch, and
the second switch valve is disposed on a refrigeration circuit section between the
first end and the second end.
5. The refrigeration system according to any of Claims 1 to 4, characterised by further comprising an evaporation pressure regulator (12) disposed on the first-type
evaporation branch and located downstream of the first evaporator.
6. The refrigeration system according to any preceding claim, characterised by further comprising a gas-liquid separator (3) disposed on the refrigeration circuit
upstream of an air suction port of the compressor.
7. The refrigeration system according to any preceding claim, characterised in that the evaporation portion has a plurality of throttle elements (10), and throttle elements
of the first-type evaporation branch and the second-type evaporation branch have different
throttling degrees.
8. The refrigeration system according to any preceding claim, characterised in that the evaporation portion has a plurality of switch valves (11) that are each used
for controlling on/off state of the first-type evaporation branch and/or on/off state
of the second-type evaporation branch.
9. The refrigeration system according to any preceding claim, characterised by further comprising a one-way valve (5) disposed on the refrigeration circuit between
an exhaust port of the compressor and the first end of the heat recovery branch.
10. A control method of a refrigeration system for the refrigeration system according
to any of Claims 1 to 9, comprising:
in a first mode S100, switching off the heat recovery branch, so that a refrigerant
sequentially flows through the compressor, the condenser, and the first-type evaporation
branch and the second-type evaporation branch that are connected in parallel;
in a second mode S200, switching on the heat recovery branch, so that the refrigerant
sequentially flows through the compressor, the heat recovery branch, the condenser,
and the second-type evaporation branch;
in a third mode S300, switching on the heat recovery branch, so that the refrigerant
sequentially flows through the compressor, the heat recovery branch, the condenser,
and the first-type evaporation branch and the second-type evaporation branch that
are connected in parallel; and
in a fourth mode S400, switching off the heat recovery branch, so that the refrigerant
sequentially flows through the compressor, the condenser, and the second-type evaporation
branch.
11. The control method according to Claim 10, characterised in that the first mode S100 is performed when an outlet air temperature of the first evaporator
is not less than a first pre-set temperature; and/or the second mode S200 is performed
when the outlet air temperature of the first evaporator is less than a second pre-set
temperature; and/or the third mode S300 is performed when the outlet air temperature
of the first evaporator is not greater than a third pre-set temperature while performing
the first mode S100; and/or the first mode S100 is maintained when the outlet air
temperature of the first evaporator is greater than the third pre-set temperature.
12. The control method according to any of Claims 10 or 11, characterised in that the first mode S100 is performed when the outlet air temperature of the first evaporator
is not less than the third pre-set temperature while performing the third mode S300;
and/or the third mode S300 is maintained when the outlet air temperature of the first
evaporator is less than the third pre-set temperature.
13. The control method according to any of Claims 10 or 11, characterised in that the first fan is kept on and the heat recovery branch is switched off when the outlet
air temperature of the first evaporator is not less than a fourth pre-set temperature
while performing the second mode S200; and/or the second mode S200 is maintained when
the outlet air temperature of the first evaporator is less than the fourth pre-set
temperature.
14. The control method according to any of Claims 10 to 12, characterised in that the first pre-set temperature is 23°C to 26°C, the second pre-set temperature is
8°C to 10°C, and/or
the third pre-set temperature is 13°C to 16°C.
15. The control method according to any of Claims 10 or 13, characterised in that the fourth pre-set temperature is 16°C to 23°C.