TECHNICAL FIELD
[0002] The present application relates to the field of air conditioning technologies, and
in particular, to an air conditioning system and a method for determining the energy
efficiency ratio thereof.
BACKGROUND
[0003] A central air conditioning system is widely used in public buildings, a water chilling
unit is one of main energy consumption devices of the central air conditioning system,
the operating performance of the water chilling unit is influenced by a plurality
of factors, the energy efficiency of the water chilling unit is greatly influenced
by a cooling load, and the operating performance of the water chilling unit can be
improved by reasonably adjusting and controlling an operating strategy of the water
chilling unit according to the cooling load.
SUMMARY
[0004] In a first aspect, an air conditioning system is provided, and the air conditioning
system includes a water chilling unit, a refrigerant circulation loop, a first temperature
sensor, a second temperature sensor, and a controller. The refrigerant circulation
loop is configured for circulating a refrigerant in a loop including a compressor,
a condenser, and an evaporator. The first temperature sensor is configured for detecting
a condensation temperature of the condenser. The second temperature sensor is configured
for detecting an evaporation temperature of the evaporator. The controller is configured
for: using the first temperature sensor to obtain a first condensation temperature
in an n-th detection period, and using the second temperature sensor to obtain a first
evaporation temperature in the n-th detection period, n being an integer greater than
1; obtaining operating parameters of the water chilling unit, and based on the operating
parameters, determining a second condensation temperature of the condenser in the
n-th detection period and a second evaporation temperature of the evaporator in the
n-th detection period; determining a first energy efficiency ratio in the n-th detection
period according to the first condensation temperature and the first evaporation temperature;
determining a second energy efficiency ratio in the n-th detection period according
to the second condensation temperature and the second evaporation temperature; and
determining an ideal energy efficiency ratio in the n-th detection period according
to the first energy efficiency ratio in the n-th detection period and the second energy
efficiency ratio in the n-th detection period.
[0005] In a second aspect, a method for determining the energy efficiency ratio of an air
conditioning system is provided, the air conditioning system includes a water chilling
unit, and the method is applied to the water chilling unit. The method includes: using
a first temperature sensor to obtain a first condensation temperature of a condenser
in an n-th detection period, and using a second temperature sensor to obtain a first
evaporation temperature of an evaporator in the n-th detection period, n being an
integer greater than 1; obtaining operating parameters of the water chilling unit,
and based on the operating parameters, determining a second condensation temperature
of the condenser in the n-th detection period and a second evaporation temperature
of the evaporator in the n-th detection period; determining a first energy efficiency
ratio in the n-th detection period according to the first condensation temperature
and the first evaporation temperature; determining a second energy efficiency ratio
in the n-th detection period according to the second condensation temperature and
the second evaporation temperature; and determining an ideal energy efficiency ratio
in the n-th detection period according to the first energy efficiency ratio in the
n-th detection period and the second energy efficiency ratio in the n-th detection
period.
[0006] In a third aspect, an air conditioning system is provided, and the air conditioning
system includes: an evaporator, a condenser, and a controller. The controller is configured
for: obtaining an evaporation temperature of the air conditioning system, a condensation
temperature of the air conditioning system, a first energy efficiency ratio of the
air conditioning system, and a load ratio of the air conditioning system according
to operating data of the evaporator and the condenser in a preset duration; obtaining
a second energy efficiency ratio of the air conditioning system and a first corresponding
relationship between the second energy efficiency ratio and the load ratio of the
air conditioning system according to the evaporation temperature of the air conditioning
system, the condensation temperature of the air conditioning system, the first energy
efficiency ratio of the air conditioning system, and the load ratio of the air conditioning
system; obtaining a second corresponding relationship between the second energy efficiency
ratio and the load ratio of the air conditioning system by using a back propagation
neural network model; and obtaining a third corresponding relationship between a target
energy efficiency ratio of the air conditioning system and the load ratio of the air
conditioning system by using the first corresponding relationship and the second corresponding
relationship based on a mean clustering algorithm.
[0007] In a fourth aspect, a method for controlling an air conditioning system is provided,
including: obtaining an evaporation temperature of the air conditioning system, a
condensation temperature of the air conditioning system, a first energy efficiency
ratio of the air conditioning system, and a load ratio of the air conditioning system
according to operating data of an evaporator and a condenser in a preset duration;
obtaining a second energy efficiency ratio of the air conditioning system and a first
corresponding relationship between the second energy efficiency ratio and the load
ratio of the air conditioning system according to the evaporation temperature of the
air conditioning system, the condensation temperature of the air conditioning system,
the first energy efficiency ratio of the air conditioning system, and the load ratio
of the air conditioning system; obtaining a second corresponding relationship between
the second energy efficiency ratio and the load ratio of the air conditioning system
by using a back propagation neural network model; and obtaining a third corresponding
relationship between a target energy efficiency ratio of the air conditioning system
and the load ratio of the air conditioning system by using the first corresponding
relationship and the second corresponding relationship based on a mean clustering
algorithm.
BRIEF DESCRIPTION OF THE DRAWINGS
[0008]
FIG. 1 is a schematic structural diagram of a water chilling unit according to some
embodiments of the present application;
FIG. 2 is a schematic structural diagram of another water chilling unit according
to some embodiments of the present application;
FIG. 3 is a block diagram of a hardware configuration of a water chilling unit according
to some embodiments of the present application;
FIG. 4 is a schematic interaction diagram of a controller of a water chilling unit
and a terminal device according to some embodiments of the present application;
FIG. 5 is a schematic diagram of a management interface of a water chilling unit according
to some embodiments of the present application;
FIG. 6 is a schematic flowchart of a method for determining an energy efficiency ratio
of an air conditioning system according to some embodiments of the present application;
FIG. 7 is a schematic flowchart of another method for determining an energy efficiency
ratio of an air conditioning system according to some embodiments of the present application;
FIG. 8 is a schematic flowchart of another method for determining an energy efficiency
ratio of an air conditioning system according to some embodiments of the present application;
FIG. 9 is a schematic flowchart of another method for determining an energy efficiency
ratio of an air conditioning system according to some embodiments of the present application;
FIG. 10 is a schematic flowchart of another method for determining an energy efficiency
ratio of an air conditioning system according to some embodiments of the present application;
FIG. 11 is a schematic flowchart of a method for controlling an air conditioning system
according to some embodiments of the present application;
FIG. 12 is a schematic flowchart of another method for controlling an air conditioning
system according to some embodiments of the present application;
FIG. 13 is a schematic flowchart of yet another method for controlling an air conditioning
system according to some embodiments of the present application;
FIG. 14 is a schematic flowchart of yet another method for controlling an air conditioning
system according to some embodiments of the present application;
FIG. 15 is a schematic flowchart of yet another method for controlling an air conditioning
system according to some embodiments of the present application;
FIG. 16 is a schematic flowchart of yet another method for controlling an air conditioning
system according to some embodiments of the present application;
FIG. 17 is a schematic flowchart of yet another method for controlling an air conditioning
system according to some embodiments of the present application;
FIG. 18 is a schematic flowchart of yet another method for controlling an air conditioning
system according to some embodiments of the present application;
FIG. 19 is a structural diagram of a neural network of a model for predicting the
performance of a water chilling unit according to some embodiments of the present
application; and
FIG. 20 is a schematic diagram of a hardware structure of a controller according to
some embodiments of the present application.
DETAILED DESCRIPTION
[0009] Some embodiments of the present disclosure are clearly and completely described below
with reference to the accompanying drawings, and apparently, the described embodiments
are not all but only a part of the embodiments of the present disclosure. All other
embodiments obtained by a person of ordinary skill in the art based on the embodiments
of the present disclosure shall fall within the protection scope of the present disclosure.
[0010] Unless required otherwise in the context, throughout the specification and the claims,
the term "comprise" and its other forms such as "comprises" and "comprising" are interpreted
as open and inclusive meaning "including, but not limited to". In the description
of the specification, the terms "one embodiment", "some embodiments", "exemplary embodiments",
"example", "specific example", "some examples", or the like, are intended to indicate
that a particular feature, structure, material, or characteristic related to the embodiment
or example is included in at least one embodiment or example of the present disclosure.
The schematic representations of the above terms do not necessarily refer to the same
embodiment or example. In addition, the particular feature, structure, material, or
characteristic may be included in any suitable manner in any one or more embodiments
or examples.
[0011] The use of "adapted to" or "configured for" herein means open and inclusive languages
and does not exclude devices adapted to or configured for performing additional tasks
or steps.
[0012] Additionally, since a process, step, calculation, or other action that is "based
on" one or more stated conditions or values may, in practice, be based on additional
conditions or exceed the stated values, the use of "based on" is open and inclusive.
[0013] The operating performance of a water chilling unit may be improved by adjusting an
operating strategy of the water chilling unit according to a cooling load, so that
the higher the accuracy of the determined cooling load is, the greater the benefit
for improving the operating performance of the water chilling unit is. Currently,
the cooling load is determined according to the energy efficiency ratio of the water
chilling unit, and in the related art, the energy efficiency ratio of the water chilling
unit is determined only according to a condensation temperature of a condenser and
an evaporation temperature of an evaporator in the water chilling unit detected by
temperature sensors. However, in the operating process of the water chilling unit,
the temperature sensor is easily affected by various measurement noises, abnormal
values or system errors, resulting in a low accuracy of the detected condensation
temperature of the condenser and the detected evaporation temperature of the evaporator,
, which in turn leading to a low accuracy of the cooling load determined according
to the inaccuracy condensation temperature of the condenser and the evaporation temperature
of the evaporator, and therefore, the operating strategy of the water chilling unit
cannot be reasonably regulated and controlled, thus affecting the operating performance
of the water chilling unit.
[0014] Based on this, some embodiments of the present application provide a method for determining
the energy efficiency ratio of an air conditioning system, and the air conditioning
system includes a water chilling unit. On the one hand, a detected value of an evaporation
temperature of an evaporator and a detected value of a condensation temperature of
a condenser are obtained through temperature sensors, and then, a detected value of
the energy efficiency ratio is determined according to the detected value of the evaporation
temperature and the detected value of the condensation temperature. On the other hand,
a calculated value of an evaporation temperature of the evaporator and a calculated
value of a condensation temperature of the condenser are determined according to the
operating parameters of the water chilling unit, and then, a calculated value of the
energy efficiency ratio is determined according to the calculated value of the evaporation
temperature and the calculated value of the condensation temperature. Then, according
to the detected value of the energy efficiency ratio and the calculated value of the
energy efficiency ratio, different energy efficiency ratios are selected as ideal
energy efficiency ratios under different conditions, which can minimize the influences
of the abnormity of the temperature sensor on the determination of the ideal energy
efficiency ratio as much as possible, thus enhancing the reasonability and accuracy
of the determination of the ideal energy efficiency ratio. Further, when the cooling
load of the water chilling unit is determined according to the ideal energy efficiency
ratio with high accuracy, the cooling load with high accuracy can be obtained, thus
improving the accuracy of the determined cooling load of the water chilling unit.
[0015] FIG. 1 shows a schematic structural diagram of a water chilling unit in an exemplary
embodiment of the present application. It should be noted that the water chilling
unit in some embodiments of the present application may include different types of
water chilling units such as an air-cooled water chilling unit and a water-cooled
water chilling unit. The water chilling unit may be further classified into a screw
water chilling unit, a vortex water chilling unit, a centrifugal water chilling unit,
or the like, according to the type of a compressor. For convenience of description,
different types of water chilling units are illustrated by using the schematic structural
diagram of the water chilling unit shown in FIG. 1 as an example.
[0016] As shown in FIG. 1, the water chilling unit 1 includes a compressor 10, a condenser
11, a throttling member 12, an evaporator 13, and a controller 14 (see FIG. 3). The
compressor 10, the condenser 11, the throttling member 12, and the evaporator 13 are
sequentially connected to form a refrigerant circulation loop. It should be noted
that, in some embodiments of the present application, the sequential connection only
illustrates the sequential relationship of the connections between the devices, and
other devices may also be included between the devices. For example, as shown in FIG.
2, a stop valve 15, or the like, may be arranged on a pipeline between the compressor
10 and the condenser 11.
[0017] During cooling, the compressor 10 compresses low-temperature and low-pressure refrigerant
gas into high-temperature and high-pressure refrigerant gas, and discharges the high-temperature
and high-pressure refrigerant gas to the condenser 11. The high-temperature and high-pressure
refrigerant gas exchanges heat with outdoor air flow in the condenser 11, a refrigerant
releases heat, the released heat is brought to outdoor ambient air by the air flow,
and the refrigerant then undergoes a phase change to be condensed into a liquid or
a mixture of gas and liquid refrigerant. The refrigerant flows out of the condenser
11, enters the throttling member 12 to be cooled and depressurized into low-temperature
and low-pressure refrigerant. The low-temperature and low-pressure refrigerant enters
the evaporator 13, and the refrigerant absorbs heat of chilled water in the evaporator
13 to lower the temperature of the chilled water in the evaporator 13, so as to achieve
the cooling effect. The refrigerant undergoes a phase change to be evaporated into
low-temperature and low-pressure refrigerant gas, and the low-temperature and low-pressure
refrigerant gas flows back into the compressor 10, so that the refrigerant is recycled.
The evaporator 13 in the present embodiment is also connected to a user side, and
after the temperature of the chilled water in the evaporator 13 is lowered, the chilled
water enters the user side, and the chilled water in the evaporator 13 can be replenished
from the user side.
[0018] In some embodiments, the chilled water in the water chilling unit 1 enters the evaporator
13 and absorbs cold energy evaporated by the refrigerant, the temperature of the chilled
water is lowered, and the chilled water becomes cold water which enters a water separator,
then enters a surface cooler or a cooling coil, exchanges heat with the treated air,
and then returns to the water chilling unit 1 for recycling treatment.
[0019] In some embodiments, the water chilling unit 1 further includes cooling water (also
called cooling liquid). During the operating process of the water chilling unit 1,
a large amount of heat may be brought by operation of the components, and if the heat
is not taken away in time, high-temperature components are easily damaged by the excessive
temperature. By utilizing the effect of heat conduction, when the cooling water flows
through the high-temperature component, the heat is conducted into the cooling water
from the high-temperature component, the water temperature rises, and the heat can
be continuously taken away by the continuous cooling water, so as to cool the high-temperature
component.
[0020] In some embodiments, the heat exchange of the water chilling unit 1 includes four
processes: (1) heat exchange between the chilled water and air in an occasion where
cooling is required. (2) Heat exchange between the chilled water and the refrigerant
in the evaporator. (3) Heat exchange between the cooling water and the refrigerant
in the condenser. (4) Heat exchange between the cooling water and air in a cooling
tower.
[0021] In some embodiments, the compressor 10 may be a screw compressor.
[0022] In some embodiments, a plurality of compressors 10 may be provided, and the plurality
of compressors are connected in parallel.
[0023] In some embodiments, the evaporator 13 may be a flooded evaporator or a falling film
evaporator.
[0024] In some embodiments, the throttling member 12 may be an electronic expansion valve,
a capillary tube, or the like.
[0025] In some embodiments, the controller 14 is an apparatus capable of generating an operation
control signal according to an instruction operation code and a timing signal, and
instructing the multi-split air conditioning system to execute a control instruction.
For example, the controller may be a central processing unit (CPU), a general-purpose
processor, a network processor (NP), a digital signal processor (DSP), a microcontroller
unit (MCU), or any combination thereof.
[0026] In addition, the controller 14 can be configured for controlling the components in
the water chilling unit 1 to work, so as to cause the components of the water chilling
unit 1 to operate to achieve predetermined functions of the water chilling unit 1.
[0027] In some embodiments, the controller 14 can obtain electric power and a cooling load
ratio of the water chilling unit 1 during operation of the water chilling unit 1.
[0028] In some embodiments, the controller 14 can calculate the cooling load ratio of the
water chilling unit according to a real-time load value of the water chilling unit
1 and a rated load value of the water chilling unit 1. That is, a ratio of the real-time
load value to the rated load value is used as the cooling load ratio.
[0029] FIG. 3 shows a block diagram of a hardware configuration of a water chilling unit
in an exemplary embodiment of the present application, as shown in FIG. 3.
[0030] In some embodiments, the water chilling unit 1 may include a first temperature sensor
21, and the first temperature sensor 21 may be arranged around the condenser 11 and
configured for detecting a condensation temperature of the condenser 11.
[0031] In some embodiments, the water chilling unit 1 may include a second temperature sensor
22, and the second temperature sensor 22 may be arranged around the evaporator 13
and configured for detecting an evaporation temperature of the evaporator 13.
[0032] In some embodiments, the water chilling unit 1 may include a third temperature sensor
23, and the third temperature sensor 23 may be arranged on a chilled water supply
pipeline of the water chilling unit 1 and configured for detecting a supply water
temperature value of the chilled water.
[0033] In some embodiments, the water chilling unit 1 may include a fourth temperature sensor
24, and the fourth temperature sensor 24 may be arranged on a chilled water return
pipeline of the water chilling unit 1 and configured for detecting a return water
temperature value of the chilled water.
[0034] In some embodiments, the controller 14 may determine a temperature difference between
supply water temperature and return water temperature of the chilled water according
to the supply water temperature value of the chilled water detected by the third temperature
sensor 23 and the return water temperature value of the chilled water detected by
the fourth temperature sensor 24.
[0035] In some embodiments, the water chilling unit 1 may include a fifth temperature sensor
25, and the fifth temperature sensor 25 may be arranged on a cooling water supply
pipeline of the water chilling unit 1 and configured for detecting a supply water
temperature value of the cooling water.
[0036] In some embodiments, the water chilling unit 1 may include a sixth temperature sensor
26, and the sixth temperature sensor 26 may be arranged on a cooling water return
pipeline of the water chilling unit 1 and configured for detecting a return water
temperature value of the cooling water.
[0037] In some embodiments, the controller 14 may determine a temperature difference between
the supply water temperature and return water temperature of the cooling water according
to the supply water temperature value of the cooling water detected by the fifth temperature
sensor 25 and the return water temperature value of the cooling water detected by
the sixth temperature sensor 26.
[0038] In some embodiments, in order to improve the accuracy of the determined energy efficiency
ratio, the temperature difference between supply water temperature and return water
temperature of the chilled water and the temperature difference between supply water
temperature and return water temperature of the cooling water when the water chilling
unit 1 operates at full load may be obtained.
[0039] In some embodiments, the water chilling unit 1 may include a seventh temperature
sensor 27, and the seventh temperature sensor 27 may be arranged at a water outlet
of the water chilling unit 1 and configured for detecting an outlet water temperature
of the water chilling unit 1.
[0040] In some embodiments, the controller 14 may determine a heat exchange temperature
difference of the condenser 11 according to the condensation temperature of the condenser
11 detected by the first temperature sensor 21 and the outlet water temperature detected
by the seventh temperature sensor 27. The heat exchange temperature difference of
the condenser 11 is configured for representing a heat exchange performance of the
condenser 11.
[0041] In some embodiments, the water chilling unit 1 may include an eighth temperature
sensor 27, and the eighth temperature sensor 27 may be arranged on the evaporator
13 and configured for detecting an environment temperature of an environment in which
the evaporator 13 is located. The environment in which the evaporator 13 is located
may be the atmosphere or other fluids.
[0042] In some embodiments, the controller 14 may determine a heat exchange temperature
difference of the evaporator 13 according to the evaporation temperature of the evaporator
13 detected by the second temperature sensor 22 and the environment temperature detected
by the eighth temperature sensor 28. The heat exchange temperature difference of the
evaporator 13 is configured for representing a heat exchange performance of the evaporator
13.
[0043] In some embodiments, the water chilling unit 1 may include a communicator 29 configured
for establishing a communication connection with other network entities such as a
terminal device.
[0044] In some embodiments, the water chilling unit 1 may include a memory 30 configured
for storing software programs and data. The controller 14 executes various functions
of the water chilling unit 1 and data processing by executing the software programs
or data stored in the memory 30.
[0045] FIG. 4 shows a schematic interaction diagram of the controller of a water chilling
unit and a terminal device in some embodiments of the present application. As shown
in FIG. 4, the terminal device 300 can establish a communication connection with the
controller 14. Exemplarily, the establishment of the communication connection may
be realized using any known network communication protocol. It should be noted that
the terminal device 300 shown in FIG. 4 is only one example of the terminal device.
The terminal device 300 in the present application may be a remote controller, a mobile
phone, a tablet computer, a personal computer (PC), a personal digital assistant (PDA),
or the like, and the specific form of the terminal device is not specifically limited
in the present application.
[0046] Exemplarily, when the terminal device 300 is a mobile phone, a user may download
a water chilling unit management APP on the mobile phone, and the water chilling unit
management APP may be configured for managing the water chilling unit. The user can
select the water chilling unit 1, which is an online device, and select a control
function required to be performed on the water chilling unit 1 from management options
of the water chilling unit 1. Exemplarily, FIG. 5 shows a schematic diagram of a management
interface of a water chilling unit in an exemplary embodiment of the present application,
and the management options of the water chilling unit 1 displayed on the water chilling
unit management APP may include control functions such as startup, shutdown, and temperature
adjustment. If it is detected that the user clicks the startup option of the water
chilling unit 1 in the water chilling unit management APP, the mobile phone can send
a startup instruction to the water chilling unit 1. In response to the startup instruction,
the controller controls the components in the water chilling unit to start working.
[0047] As shown in FIG. 6, some embodiments of the present application provide a method
for determining the energy efficiency ratio of an air conditioning system, the method
may be applied to the controller 14 of the above water chilling unit 1, and the method
includes the following steps.
[0048] In S101: a first condensation temperature of the condenser in an n-th detection period
is obtained through the first temperature sensor, and a first evaporation temperature
of the evaporator in the n-th detection period is obtained through the second temperature
sensor.
[0049] In some embodiments, in the operating process of the water chilling unit, after the
controller receives a control instruction for determining a cooling load issued by
a user, in response to the control instruction for determining the cooling load, the
controller uses the first temperature sensor to obtain the first condensation temperature
of the condenser in the n-th detection period, and uses the second temperature sensor
to obtain the first evaporation temperature of the evaporator in the n-th detection
period, where n is a positive integer, e.g., 20. The detection period may be preset
when the water chilling unit is manufactured, or may be set by a manager of the water
chilling unit through a terminal device. For example, one detection period is 5 seconds
and is not limited herein.
[0050] The n-th detection period may be understood as a current detection period, and n-1
detection periods before the n-th detection period may be understood as historical
detection periods before the current detection period.
[0051] In some embodiments, the detection period may be a time point. That is, the first
condensation temperature of the condenser at the current time point and the first
evaporation temperature of the evaporator at the current time point are obtained.
[0052] It is easy to understand that the first condensation temperature and the first evaporation
temperature are both detected by the corresponding temperature sensors, the first
condensation temperature can be understood as a detected value of a condensation temperature
of the condenser, and the first evaporation temperature can be understood as a detected
value of an evaporation temperature of the evaporator.
[0053] In some embodiments, during the operating process of the water chilling unit, the
controller can periodically use the first temperature sensor to obtain the first condensation
temperature of the condenser in the n-th detection period and use the second temperature
sensor to obtain the first evaporation temperature of the evaporator in the n-th detection
period, so as to determine the ideal energy efficiency ratio of the water chilling
unit timely, then determine the cooling load of the water chilling unit timely, and
then adjust an operating strategy of the water chilling unit timely according to the
cooling load of the water chilling unit, which facilitates the improvement of the
operating performance of the water chilling unit.
[0054] Exemplarily, the first condensation temperature of the condenser in the n-th detection
period may be denoted as T
c1, and the first evaporation temperature of the evaporator in the n-th detection period
may be denoted as T
e1.
[0055] In S102: operating parameters of the water chilling unit are obtained, and based
on the operating parameters, a second condensation temperature of the condenser in
the n-th detection period and a second evaporation temperature of the evaporator in
the n-th detection period are determined.
[0056] It should be understood that the operating parameters of the water chilling unit
are parameters generated by the components of the water chilling unit during the operating
process of the water chilling unit. With one detection period as a unit, the operating
parameters of the water chilling unit include a temperature difference between supply
water temperature and return water temperature of chilled water, a temperature difference
between the supply water temperature and return water temperature of cooling water,
a heat exchange temperature difference of the evaporator, a heat exchange temperature
difference of the condenser, a supply water temperature of the chilled water, a return
water temperature of the cooling water, a cooling load ratio of the water chilling
unit, electric power of the water chilling unit, or the like.
[0057] It should be noted that, in order to improve the accuracy of subsequent determination
of the ideal energy efficiency ratio, values of the operating parameters of the water
chilling unit are all obtained from values of the water chilling unit in a fully-loaded
state.
[0058] In some embodiments, as shown in FIG. 7, determining the second condensation temperature
of the condenser in the n-th detection period and the second evaporation temperature
of the evaporator in the n-th detection period based on the operating parameters may
include the following steps S1021 and S1022.
[0059] In S1021: the second condensation temperature of the condenser in the n-th detection
period is determined according to the temperature difference between the supply water
temperature and return water temperature of the cooling water in the n-th detection
period, the heat exchange temperature difference of the condenser in the n-th detection
period, and the cooling load ratio of the water chilling unit in the n-th detection
period.
[0060] Exemplarily, the relationship between the temperature difference between the supply
water temperature and return water temperature of the cooling water in the n-th detection
period, the heat exchange temperature difference of the condenser in the n-th detection
period, and the cooling load ratio of the water chilling unit in the n-th detection
period and the second condensation temperature of the condenser in the n-th detection
period may be shown in the following formula (1):

where T
c2 is the second condensation temperature of the condenser in the n-th detection period,
PLR is the cooling load ratio of the water chilling unit in the n-th detection period,
T
c-rtn is the return water temperature of the cooling water in the n-th detection period,
and T
c-exc is the heat exchange temperature difference of the condenser in the n-th detection
period.
[0061] In S 1022: the second evaporation temperature of the evaporator in the n-th detection
period is obtained according to the temperature difference between the supply water
temperature and return water temperature of the chilled water in the n-th detection
period, the heat exchange temperature difference of the evaporator in the n-th detection
period, the supply water temperature of the chilled water in the n-th detection period,
and the cooling load ratio of the water chilling unit in the n-th detection period.
[0062] Exemplarily, the relationship between the temperature difference between the supply
water temperature and return water temperature of the chilled water in the n-th detection
period, the heat exchange temperature difference of the evaporator in the n-th detection
period, the supply water temperature of the chilled water in the n-th detection period,
and the cooling load ratio of the water chilling unit in the n-th detection period
and the second evaporation temperature of the evaporator in the n-th detection period
may be shown in the following formula (2):

where T
e2 is the second evaporation temperature of the evaporator in the n-th detection period,
T
e-sup is the supply water temperature of the chilled water in the n-th detection period,
T
e-em is the temperature difference between supply water temperature and return water temperature
of the chilled water in the n-th detection period, and T
c-exc is the heat exchange temperature difference of the evaporator in the n-th detection
period.
[0063] It is easy to understand that the second condensation temperature can be understood
as a calculated value of the condensation temperature of the condenser, and the second
evaporation temperature can be understood as a calculated value of the evaporation
temperature of the evaporator.
[0064] In S103: a first energy efficiency ratio in the n-th detection period is determined
according to the first condensation temperature and the first evaporation temperature.
[0065] In some embodiments, the first energy efficiency ratio may be represented as a COP
(coefficient of performance) and refers to the amount of cooling produced per unit
of power consumed. After the first condensation temperature of the condenser in the
n-th detection period and the first evaporation temperature of the evaporator in the
n-th detection period are obtained, the first energy efficiency ratio in the n-th
detection period may be determined according to the first condensation temperature
of the condenser in the n-th detection period and the first evaporation temperature
of the evaporator in the n-th detection period.
[0066] Exemplarily, the relationship between the first condensation temperature, the first
evaporation temperature, and the first energy efficiency ratio may be shown in the
following formula (3):

where K
1 is the first energy efficiency ratio in the n-th detection period.
[0067] In S104: a second energy efficiency ratio in the n-th detection period is determined
according to the second condensation temperature and the second evaporation temperature.
[0068] In some embodiments, after the second condensation temperature of the condenser in
the n-th detection period is obtained through step S1021 and the second evaporation
temperature of the evaporator in the n-th detection period is obtained through step
S1022, the second energy efficiency ratio in the n-th detection period may be determined
according to the second condensation temperature of the condenser in the n-th detection
period and the second evaporation temperature of the evaporator in the n-th detection
period.
[0069] Exemplarily, the relationship between the second condensation temperature, the second
evaporation temperature, and the second energy efficiency ratio may be shown in the
following formula (4):

where K
2 is the second energy efficiency ratio in the n-th detection period.
[0070] It should be noted that the execution order of step S103 and step S104 is not limited
in some embodiments of the present application. For example, step S103 is executed
first, and step S104 is then executed. Alternatively, step S104 is executed first,
and step S103 is then executed. Still alternatively, step S103 and step S104 are executed
simultaneously.
[0071] In S105: an ideal energy efficiency ratio in the n-th detection period is determined
according to the first energy efficiency ratio in the n-th detection period and the
second energy efficiency ratio in the n-th detection period.
[0072] It is easy to understand that the first energy efficiency ratio is obtained according
to the first condensation temperature and the first evaporation temperature, and the
first condensation temperature and the first evaporation temperature are detected
by the temperature sensors, so that the first energy efficiency ratio can be understood
as a detected value of the energy efficiency ratio. The second energy efficiency ratio
is obtained according to the second condensation temperature and the second evaporation
temperature, and the second condensation temperature and the second evaporation temperature
are calculated according to the operating parameters of the water chilling unit, so
that the second energy efficiency ratio can be understood as a calculated value of
the energy efficiency ratio.
[0073] Then, the detected value of the energy efficiency ratio or the calculated value of
the energy efficiency ratio can be selected as the ideal energy efficiency ratio in
different situations. This approach, compared to the related art in which only the
detected value of the energy efficiency ratio is used as the ideal energy efficiency
ratio, can avoid the influences of abnormity of the temperature sensor on the determination
of the ideal energy efficiency ratio, thereby improving the reasonability and accuracy
of the determination of the ideal energy efficiency ratio.
[0074] Compared to the related art in which the ideal energy efficiency ratio is determined
only according to the detected value of the condensation temperature of the condenser
and the detected value of the evaporation temperature of the evaporator detected by
the temperature sensors, in the method for determining the energy efficiency ratio
of an air conditioning system according to some embodiments of the present application,
the ideal energy efficiency ratio in the n-th detection period is determined by comparing
the detected value of the energy efficiency ratio with the calculated value of the
energy efficiency ratio, so that influences of an error of the temperature sensor
on the accuracy of the ideal energy efficiency ratio can be reduced, and the reasonability
and accuracy of the determination of the ideal energy efficiency ratio are improved.
Further, by determining the cooling load of the water chilling unit according to the
ideal energy efficiency ratio with high accuracy, the cooling load with high accuracy
can be obtained, thus improving the accuracy of the determined cooling load of the
water chilling unit.
[0075] In some embodiments, as shown in FIG. 8, an implementation of step S105 may include
the following steps.
[0076] In S201: the ideal energy efficiency ratio in the n-th detection period is determined
according to the first energy efficiency ratio in the n-th detection period, the second
energy efficiency ratio in the n-th detection period, a first value range, and a second
value range.
[0077] The first value range is determined according to an average value and a standard
deviation of the first energy efficiency ratios in n detection periods, and the second
value range is determined according to an average value and a standard deviation of
the second energy efficiency ratios in the n detection periods.
[0078] A manner of determining the first energy efficiency ratio in each of the n detection
periods can be referred to the description of the above step S103, and a manner of
determining the second energy efficiency ratio in each of the n detection periods
reference can be referred to the description of the above step S104, which are not
repeated herein.
[0079] Exemplarily, the average value of the first energy efficiency ratios in the n detection
periods may be as shown in the following formula (5):

where K
1 is the average value of the first energy efficiency ratios in the n detection periods,
and K
1i is the first energy efficiency ratio in the i-th detection period among the n detection
periods.
[0080] Exemplarily, the standard deviation of the first energy efficiency ratios in the
n detection periods may be as shown in the following formula (6):

where σ
1 is the standard deviation of the first energy efficiency ratios in the n detection
periods.
[0081] Exemplarily, the average value of the second energy efficiency ratios in the n detection
periods may be as shown in the following formula (7):

where K
2 is the average value of the second energy efficiency ratios in the n detection periods,
and K
2i is the second energy efficiency ratio in the i-th detection period among the n detection
periods.
[0082] Exemplarily, the standard deviation of the second energy efficiency ratios in the
n detection periods may be as shown in the following formula (8):

where σ
2 is the standard deviation of the second energy efficiency ratios in the n detection
periods.
[0083] In some embodiments, the first value range and the second value range may be preset
by the manager of the water chilling unit according to an operating condition of the
water chilling unit and stored in the memory.
[0084] In some embodiments, the first value range and the second value range may alternatively
be calculated by the controller in real time according to a preset rule and the operating
parameters of the water chilling unit. For example, the first value range may be (K
1-σ
1, K
1+σ
1), and the second value range may be (K
2-σ
1, K
2+σ
1). For another example, the first value range may be (K
1-2σ
1, K
1+2σ
1), the second value range may be (K
2-2σ
1, K
2+2σ
1), and setting ranges of the first value range and the second value range are not
limited in some embodiments of the present application.
[0085] In some embodiments, as shown in FIG. 9, an implementation of step S201 may include
the following steps.
[0086] In S2011: when the first energy efficiency ratio in the n-th detection period is
not within the first value range and the second energy efficiency ratio in the n-th
detection period is not within the second value range, an average value of the first
energy efficiency ratio in the n-th detection period and the second energy efficiency
ratio in the n-th detection period is taken as the ideal energy efficiency ratio in
the n-th detection period.
[0087] It can be understood that, when the first energy efficiency ratio in the n-th detection
period is not within the first value range and the second energy efficiency ratio
in the n-th detection period is not within the second value range, neither the first
energy efficiency ratio nor the second energy efficiency ratio can effectively reflect
the ideal energy efficiency ratio in the n-th detection period, so that the average
value of the first energy efficiency ratio in the n-th detection period and the second
energy efficiency ratio in the n-th detection period is used as the ideal energy efficiency
ratio in the n-th detection period. Compared to the related technologies where the
energy efficiency ratio is determined according to the evaporation temperature and
the condensation temperature detected by the sensors, this approach enhances the rationality
and accuracy of determining the ideal energy efficiency ratio.
[0088] In S2012: when the first energy efficiency ratio in the n-th detection period is
within the first value range and the second energy efficiency ratio in the n-th detection
period is not within the second value range, the first energy efficiency ratio in
the n-th detection period is taken as the ideal energy efficiency ratio in the n-th
detection period.
[0089] It can be understood that when the first energy efficiency ratio in the n-th detection
period is within the first value range and the second energy efficiency ratio in the
n-th detection period is not within the second value range, it indicates that errors
of the temperature sensors are small, and the first condensation temperature of the
condenser and the first evaporation temperature of the evaporator detected by the
corresponding temperature sensors are accurate. That is to say, a calculation result
of the first energy efficiency ratio is better than a calculation result of the second
energy efficiency ratio, and the first energy efficiency ratio can better reflect
the ideal energy efficiency ratio in the n-th detection period than the second energy
efficiency ratio, so that the first energy efficiency ratio in the n-th detection
period is taken as the ideal energy efficiency ratio in the n-th detection period.
[0090] In S2013: when the second energy efficiency ratio in the n-th detection period is
within the second value range, the second energy efficiency ratio in the n-th detection
period is taken as the ideal energy efficiency ratio in the n-th detection period.
[0091] As can be seen from the above description, the second energy efficiency ratio is
calculated according to the operating parameters of the water chilling unit, and when
it is detected that the second energy efficiency ratio is within the second value
range, the second energy efficiency ratio can better reflect the ideal energy efficiency
ratio in the n-th detection period, so that the second energy efficiency ratio in
the n-th detection period is taken as the ideal energy efficiency ratio in the n-th
detection period.
[0092] Exemplarily, a value of the ideal energy efficiency ratio in the n-th detection period
under different conditions may be as shown in the following formula (9):

where K
F is the ideal energy efficiency ratio in the n-th detection period.
[0093] Exemplarily, the following table 1 provides some values of K
1, K
2, K
1, K
2, σ
1, σ
2, and K
F in the exemplary embodiment of the present application.
Table 1
| Detection period |
K1 |
K2 |
K1 |
K2 |
σ1 |
σ2 |
KF |
| 1 |
0.6754 |
0.6765 |
0.6754 |
0.6765 |
0.0000 |
0.0000 |
0.6760 |
| 2 |
0.6500 |
0.6533 |
0.6627 |
0.6649 |
0.0090 |
0.0082 |
0.6516 |
| 3 |
0.6577 |
0.6628 |
0.6611 |
0.6642 |
0.0076 |
0.0068 |
0.6603 |
| 4 |
0.6394 |
0.6228 |
0.6556 |
0.6538 |
0.0104 |
0.0166 |
0.6311 |
| 5 |
0.6312 |
0.6430 |
0.6508 |
0.6516 |
0.0128 |
0.0153 |
0.6371 |
| 6 |
0.6268 |
0.6337 |
0.6468 |
0.6487 |
0.0142 |
0.0153 |
0.6303 |
| 7 |
0.6501 |
0.6537 |
0.6472 |
0.6494 |
0.0132 |
0.0142 |
0.6519 |
| 8 |
0.6244 |
0.6507 |
0.6444 |
0.6496 |
0.0143 |
0.0133 |
0.6375 |
| 9 |
0.6364 |
0.6007 |
0.6435 |
0.6441 |
0.0136 |
0.0192 |
0.6186 |
| 10 |
0.6402 |
0.6660 |
0.6432 |
0.6463 |
0.0130 |
0.0192 |
0.6531 |
[0094] The above embodiment emphasizes the manner for determining the ideal energy efficiency
ratio in the n-th detection period. In some embodiments, the method for determining
the energy efficiency ratio of an air conditioning system according to some embodiments
of the present application further involves usage of the ideal energy efficiency ratio.
As shown in FIG. 10, after step S105, the method further includes the following steps.
[0095] In S301: the cooling load of the water chilling unit in the n-th detection period
is determined according to the electric power of the water chilling unit in the n-th
detection period, the cooling load ratio of the water chilling unit in the n-th detection
period and the ideal energy efficiency ratio in the n-th detection period.
[0096] For example, the relationship between the electric power of the water chilling unit
in the n-th detection period, the cooling load ratio of the water chilling unit in
the n-th detection period, the ideal energy efficiency ratio in the n-th detection
period, and the cooling load of the water chilling unit in the n-th detection period
may be as shown in the following formula (10):

where Q
i is the cooling load of the water chilling unit in the n-th detection period, PLR
is the cooling load ratio of the water chilling unit in the n-th detection period,
P
W is the electric power of the water chilling unit in the n-th detection period, and
a, b, and c are all constants.
[0097] Here, a, b, and c are obtained by performing training based on data of the water
chilling unit, data training is to collect operating data of the water chilling unit
for a period of time, use PLR as the horizontal axis, use a ratio of the energy efficiency
ratio (the coefficient of performance, COP) of the water chilling unit to K
F as the vertical axis, and perform curve fitting on the data to obtain a, b and c.
[0098] The relationship between the COP and K
F may be as shown in the following formula (11):

[0099] The embodiment shown in FIG. 9 brings at least the following beneficial effects:
compared to the related art in which the ideal energy efficiency ratio of the water
chilling unit is obtained according to the condensation temperature and the evaporation
temperature detected by the temperature sensors, the method for determining the energy
efficiency ratio of an air conditioning system according to some embodiments of the
present application not only determines the first energy efficiency ratio of the water
chilling unit according to the first condensation temperature and the first evaporation
temperature detected by the temperature sensors, but also determines the second condensation
temperature and the second evaporation temperature according to the operating parameters
of the water chilling unit, then determines the second energy efficiency ratio of
the water chilling unit, and selects different energy efficiency ratios as the ideal
energy efficiency ratio of the water chilling unit under different conditions, thereby
reducing the influences of the errors of the temperature sensors on the accuracy of
the determination of the ideal energy efficiency ratio, and improving the reasonability
and accuracy of the determination of the ideal energy efficiency ratio. Then, the
cooling load of the water chilling unit is determined according to the ideal energy
efficiency ratio with high accuracy, thus improving the accuracy of the determination
of the cooling load of the water chilling unit.
[0100] In addition, in the method for determining the energy efficiency ratio of an air
conditioning system according to some embodiments of the present application, when
determining the cooling load of the water chilling unit according to the ideal energy
efficiency ratio, the electric power of the water chilling unit is introduced to serve
as a determination basis of the cooling load of the water chilling unit. It can be
understood that, compared to the electric power of the water chilling unit, the temperature
detected by the temperature sensor has a delay and error to a certain extent and is
also easily influenced by various noises. In contrast, detection of the electric power
of the water chilling unit is more stable, so that the accuracy and stability of the
determination of the cooling load of the water chilling unit are improved by taking
the electric power of the water chilling unit as one of bases for calculating the
cooling load of the water chilling unit.
[0101] Further, the manager of the water chilling unit adjusts the operating strategy of
the water chilling unit according to the cooling load with higher accuracy, and the
accuracy of the adjustment of the operating strategy is higher, which facilitates
the improvement of the operating performance of the water chilling unit.
[0102] Based on the above air conditioning system, as shown in FIG. 11, some embodiments
of the present application provide a method for controlling an air conditioning system,
and the method may include the following steps.
[0103] S111: the air conditioning system obtains an evaporation temperature of the air conditioning
system, a condensation temperature of the air conditioning system, a first energy
efficiency ratio of the air conditioning system, and a load ratio of the air conditioning
system according to operating data of the evaporator and the condenser in a preset
duration.
[0104] In some embodiments, the operating data includes a supply chilled water temperature,
a return chilled water temperature, a chilled water flow rate, and an evaporator evaporation
temperature of the evaporator, a supply cooling water temperature, a return cooling
water temperature, a cooling water flow rate, and a condenser condensation temperature
of the condenser, and a water chilling unit load ratio, water chilling unit power
of the air conditioning system, or the like.
[0105] In some embodiments, the preset duration may be half a year, one year, or the like,
the operating data corresponding to each time point in the preset duration may form
one data set, and a time interval for obtaining the operating data may be 5 minutes,
10 minutes, or the like. For example, one data set is acquired every 5 minutes, and
one data set may include the supply chilled water temperature, the return chilled
water temperature, the chilled water flow rate, and the evaporator evaporation temperature
of the evaporator, the supply cooling water temperature, the return cooling water
temperature, the cooling water flow rate, and the condenser condensation temperature
of the condenser, and the water chilling unit load ratio, the water chilling unit
power, or the like, of the air conditioning system at this time point.
[0106] S112: the air conditioning system obtains a second energy efficiency ratio and a
first corresponding relationship between the second energy efficiency ratio and the
load ratio of the air conditioning system according to the evaporation temperature,
the condensation temperature, and the first energy efficiency ratio.
[0107] In some embodiments, the second energy efficiency ratio is a DCOP (dynamic coefficient
of performance), and also represents an internal energy efficiency of the air conditioning
system, which mainly reflects a deviation between a COP and an ICOP (ideal coefficient
of performance), and the DCOP can be used to determine a reason for a low operating
efficiency of the air conditioning system.
[0108] In some embodiments, the first corresponding relationship may be an air conditioning
system DCOP performance model established between the DCOP of the air conditioning
system and a PLR (part load ratio) of the air conditioning system. Since the first
corresponding relationship is obtained or established based on actual operating data,
the DCOP performance model correspondingly represented by the first corresponding
relationship can reflect a real energy efficiency of the air conditioning system.
[0109] S113: the air conditioning system obtains a second corresponding relationship between
the second energy efficiency ratio and the load ratio of the air conditioning system
by using a back propagation neural network model.
[0110] In some embodiments, the second corresponding relationship may be an air conditioning
system DCOP performance prediction model established between the DCOP of the air conditioning
system and the PLR of the air conditioning system. Since the second corresponding
relationship is established through learning and prediction of a back propagation
neural network, the energy efficiency of the air conditioning system can be predicted
by the DCOP performance prediction model correspondingly represented by the second
corresponding relationship.
[0111] In some embodiments, the back propagation neural network model has a BP (back propagation)
neural network structure, and the BP neural network is a multi-layer feedforward neural
network trained according to an error back propagation algorithm.
[0112] In some embodiments, the water chilling unit load ratio of the air conditioning system
and a temperature difference between the evaporation temperature and the condensation
temperature of the air conditioning system in the operating data may be input into
the back propagation neural network model to obtain the second energy efficiency ratio
and the second corresponding relationship between the second energy efficiency ratio
and the load ratio of the air conditioning system.
[0113] Exemplarily, the BP neural network structure is established, and has three layers.
Input neurons of the neural network are the water chilling unit load ratio, and the
difference between the condensation temperature and the evaporation temperature. The
number of network nodes of a network hidden layer is seven. An output neuron is the
DCOP. A trainlm (Levenberg-Marquarelt) learning algorithm is used in the BP neural
network model, a network hidden layer transfer function is a tansig function (bipolar
S function), an output layer is a Pureline function (linear function), a learning
rate of the BP neural network model can be set to be 0.05, a maximum number of learning
steps can be set to be 1,000, and a training target error can be set to be 0.003,
so that the above DCOP prediction model can be obtained through data training.
[0114] S114: the air conditioning system obtains a third corresponding relationship between
a target energy efficiency ratio of the air conditioning system and the load ratio
of the air conditioning system by using the first corresponding relationship and the
second corresponding relationship based on a mean clustering algorithm.
[0115] In some embodiments, the third corresponding relationship represents a target performance
model of the air conditioning system that can realize the target energy efficiency
ratio.
[0116] In some embodiments, the mean clustering algorithm is a K-means clustering algorithm.
The K-means algorithm is a classic distance-based clustering algorithm, and a distance
is used as an evaluation index of similarity. That is, the closer the two objects
are, the greater the similarity of the two objects is.
[0117] In some embodiments, the establishment of the third corresponding relationship according
to the first corresponding relationship means that the performance of an operating
state of the air conditioning system at a current time is predicted according to the
DCOP performance model established by using the real operating data of the air conditioning
system, and the performance can be represented by the target energy efficiency ratio;
the establishment of the third corresponding relationship according to the second
corresponding relationship means that the performance of the operating state of the
air conditioning system at the current time is predicted according to the DCOP performance
prediction model of the air conditioning system established by the BP neural network,
and the performance can be represented by the target energy efficiency ratio.
[0118] According to the operating data of the evaporator and the condenser within the preset
duration, the first energy efficiency ratio and the second energy efficiency ratio
of the air conditioning system are obtained, and then, the first corresponding relationship
between the second energy efficiency ratio and the load ratio of the air conditioning
system is established. Then, the second corresponding relationship between the second
energy efficiency ratio and the load ratio of the air conditioning system is predicted
through the back propagation neural network model. Whether the third corresponding
relationship is established according to the first corresponding relationship or the
second corresponding relationship is then determined based on the mean clustering
algorithm. In the control method according to the present application, the plurality
of corresponding relationships between the energy efficiency ratio of the air conditioning
system and the load ratio of the air conditioning system can be obtained in different
ways, and the more appropriate corresponding relationship is selected from the corresponding
relationships to determine the target energy efficiency ratio. A more accurate cooling
capacity can be determined according to the target energy efficiency ratio, thereby
lowering operating energy consumption of the air conditioning system. In addition,
the prediction precision of the energy efficiency ratio of the air conditioning system
can be improved, and the problem that the precision of prediction of the energy efficiency
ratio by the performance model of the air conditioning system in the related art is
low is solved. Meanwhile, premises are provided for energy consumption simulation,
energy efficiency monitoring and formulation of a reasonable energy-saving control
strategy of the air conditioning system.
[0119] In some embodiments, a first performance ratio, the evaporation temperature, and
a cooling temperature of the air conditioning system may be further obtained by obtaining
a water chilling unit direct load and a water chilling unit cooling amount. Therefore,
as shown in FIG. 12, the step S111 may include the following steps.
[0120] In S211, the water chilling unit direct load is obtained according to a specific
heat capacity of water and the chilled water flow rate, the return chilled water temperature,
and the supply chilled water temperature in a target data set in the operating data.
[0121] In some embodiments, the water chilling unit direct load may be obtained using formula
(12):

where Q
d represents the water chilling unit direct load, c represents the specific heat capacity
of water, m
e represents the chilled water mass flow rate, T
e-rtn represents the return chilled water temperature, and T
e-sup represents the supply chilled water temperature.
[0122] In S212: the water chilling unit cooling amount is obtained according to the specific
heat capacity of water and the cooling water flow rate, the return cooling water temperature,
and the supply cooling water temperature in the target data set in the operating data.
[0123] In some embodiments, the water chilling unit cooling amount may be obtained using
formula (13):

where Q
c represents the water chilling unit cooling amount, m
c represents the cooling water flow rate, T
c-sup represents the supply cooling water temperature, and T
c-rtn represents the return cooling water temperature.
[0124] In some embodiments, in consideration of an error in time measurement, a load unbalance
ratio can be obtained according to the water chilling unit power, the water chilling
unit direct load, and the water chilling unit cooling amount. Under the condition
that the load unbalance ratio is greater than or equal to a preset load unbalance
ratio, the data set corresponding to the load unbalance ratio in the operating data
is deleted, so as to reduce an error of data acquisition. Exemplarily, the load unbalance
ratio may be calculated using formula (14):

where B
a represents the load unbalance ratio, and P
w represents the water chilling unit power.
[0125] Exemplarily, the preset load unbalance ratio may be 15%. That is, when the load unbalance
ratio calculated according to some data in one data set is greater than or equal to
15%, all data in the data set corresponding to the load unbalance ratio is removed
from the operating data.
[0126] In the above embodiment, the data set in the operating data corresponding to the
abnormal load unbalance ratio is removed, so that interference of the abnormal data
set in the establishment of the performance model of the air conditioning system is
reduced, the data set in the operating data is more accurate, and a foundation is
laid for the subsequent improvement of the precision of the model of the air conditioning
system.
[0127] In some embodiments, as shown in FIG. 13, removing the data set corresponding to
an abnormal data value of the first energy efficiency ratio may include the following
steps.
[0128] In S311, the first energy efficiency ratio of the air conditioning system is obtained
according to the water chilling unit direct load and the water chilling unit power
in the target data set in the operating data.
[0129] In some embodiments, the water chilling unit cooling amount may be obtained using
formula (15):

where the COP represents the first energy efficiency ratio.
[0130] In S312, the data in the target data set is deleted from the operating data under
the condition that the first energy efficiency ratio is outside a preset interval.
[0131] Exemplarily, the preset interval may be (µ1-2σ1, µ1+2σ1), µ1 is an average value
of the COPs in a current month and σ1 is a standard deviation of the COPs in the current
month. That is, when a value of the COP is outside the interval (µ1-2σ1, µ1+2σ1),
the value is an abnormal value, and all the data in the target data set corresponding
to the value of the COP is removed from the operating data.
[0132] In the above embodiment, when the first energy efficiency ratio is outside the preset
interval, the data set in the operating data corresponding to the first energy efficiency
ratio is deleted. In this embodiment, the data set in the operating data corresponding
to the abnormal first energy efficiency ratio is removed, so that the interference
of the abnormal data set in the establishment of the performance model of the air
conditioning system is reduced, the data in the operating data is more accurate, and
the foundation is laid for the subsequent improvement of the precision of the model
of the air conditioning system.
[0133] In some embodiments, as shown in FIG. 14, obtaining the evaporation temperature of
the air conditioning system may include the following steps.
[0134] In S411, an evaporator logarithmic mean temperature difference corresponding to the
target data set is obtained according to a temperature difference between the supply
chilled water temperature and the evaporator evaporation temperature in the target
data set and a temperature difference between the return chilled water temperature
and the evaporator evaporation temperature in the target data set.
[0135] In some embodiments, the evaporator logarithmic mean temperature difference may be
obtained using formulas (16) and (17):

where Δt
e2 and Δt
e1 represent the temperature difference between the supply chilled water temperature
and the evaporator evaporation temperature and the temperature difference between
the return chilled water temperature and the evaporator evaporation temperature, respectively,
Δt
m,e represents the evaporator logarithmic mean temperature difference, and Δt
ch,e represents a temperature difference between inlet and outlet of the evaporator.
[0136] In S412, an evaporator heat transfer coefficient corresponding to the target data
set is obtained according to the water chilling unit direct load and the evaporator
logarithmic mean temperature difference.
[0137] In some embodiments, the evaporator heat transfer coefficient may be obtained using
formula (18):

where K
eF
e represents the evaporator heat transfer coefficient.
[0138] In S413, an evaporator target heat transfer coefficient is obtained by performing
fitting according to the evaporator heat transfer coefficients corresponding to different
data sets.
[0139] In some embodiments, the evaporator target heat transfer coefficient may be obtained
by performing regression fitting using formula (19):

where a
1, b
1, c
1, d
1, e
1 and f
1 represent parameters of a fitted evaporator model.
[0140] In some embodiments, by obtaining the evaporator target heat transfer coefficient
by performing the regression fitting, the evaporation temperature of the air conditioning
system can be quantitatively depicted in a curve mode, so that the evaporation temperature
of the air conditioning system is more comprehensive and accurate.
[0141] In S414, the evaporation temperature of the air conditioning system is obtained according
to a density of water, the specific heat capacity of water, the evaporator target
heat transfer coefficient, the water chilling unit direct load, the chilled water
flow rate, and the supply chilled water temperature.
[0142] In some embodiments, the evaporation temperature of the air conditioning system may
be obtained using formula (20):

where ρ represents the density of water, and T
e represents the evaporation temperature.
[0143] In the above embodiment, the evaporator target heat transfer coefficient is obtained
by performing fitting based on the evaporator heat transfer coefficients corresponding
to different data sets in the operating data, which can help to establish a heat transfer
model of the evaporator, so that obtained evaporation temperature data of the air
conditioning system is more comprehensive and accurate.
[0144] In some embodiments, as shown in FIG. 15, obtaining the condensation temperature
of the air conditioning system may include the following steps.
[0145] In S511, a condenser logarithmic mean temperature difference corresponding to the
target data set is obtained according to a temperature difference between the supply
cooling water temperature and the condenser condensation temperature in the target
data set and a temperature difference between the return cooling water temperature
and the condenser condensation temperature in the target data set.
[0146] In some embodiments, the condenser logarithmic mean temperature difference may be
obtained using formulas (21) and (22):


where Δt
c2 represents the temperature difference between a supply cooling water temperature
and the condenser condensation temperature, Δt
c1 represents the temperature difference between the return cooling water temperature
and the condenser condensation temperature, Δt
m,c represents the condenser logarithmic mean temperature difference, and Δt
ch,c represents a temperature difference the inlet and outlet of the condenser.
[0147] In S512, a condenser heat transfer coefficient corresponding to the target data set
is obtained according to the water chilling unit direct load and the condenser logarithmic
mean temperature difference.
[0148] In some embodiments, the condenser heat transfer coefficient may be obtained using
formula (23):

where K
cF
c represents the condenser heat transfer coefficient.
[0149] In S513, a condenser target heat transfer coefficient is obtained by performing fitting
based on the condenser heat transfer coefficients corresponding to different data
sets.
[0150] In some embodiments, the condenser target heat transfer coefficient may be obtained
by performing fitting using formula (24):

where a
2, b
2, c
2, d
2, e
2 and f
2 represent parameters of a fitted condenser model.
[0151] In some embodiments, by obtaining the condenser target heat transfer coefficient
by performing the regression fitting, the condensation temperature of the air conditioning
system can be quantitatively depicted in a curve mode, so that the condensation temperature
of the air conditioning system is more comprehensive and accurate.
[0152] In S514, the condensation temperature of the air conditioning system is obtained
according to the density of water, the specific heat capacity of water, the condenser
target heat transfer coefficient, the water chilling unit direct load, the cooling
water flow rate, and the return cooling water temperature.
[0153] In some embodiments, the condensation temperature of the air conditioning system
may be obtained using formula (25):

where ρ represents the density of water, and T
c represents the condensation temperature.
[0154] In the above embodiment, the condenser target heat transfer coefficient is obtained
by performing fitting according to the condenser heat transfer coefficients corresponding
to different data sets in the operating data, which can help to establish a heat transfer
model of the condenser, so that obtained condensation temperature data of the air
conditioning system is more comprehensive and accurate.
[0155] In some embodiments, the first corresponding relationship between the second energy
efficiency ratio and the load ratio of the air conditioning system may be a first
corresponding relationship of the air conditioning system represented by a curve.
Therefore, as shown in FIG. 16, the step S112 may include the following steps.
[0156] In S611, with the second energy efficiency ratio as an abscissa and the load ratio
corresponding to the second energy efficiency ratio as an ordinate, a scatter diagram
composed of a plurality of data points is generated.
[0157] In some embodiments, a value of the ICOP of the air conditioning system may be calculated
using formula (26), and a value of the DCOP may be calculated using formula (27):

where the ICOP represents the ideal energy efficiency ratio, and the DCOP represents
the second energy efficiency ratio.
[0158] In some embodiments, the value of the DCOP may be used as the abscissa, and the water
chilling unit load ratio PLR corresponding to the value of the DCOP may be used as
the ordinate, so as to generate the scatter diagram composed of the plurality of data
points, and the scatter diagram may visually represent a relationship between the
value of the DCOP of the air conditioning system and the load ratio PLR corresponding
thereto.
[0159] In S602: the first corresponding relationship represented by the curve is obtained
by fitting the data points on the scatter diagram.
[0160] In some embodiments, the obtained first corresponding relationship represented by
the curve may be the air conditioning system DCOP performance model established by
performing regression fitting on the data. Exemplarily, the regression fitting may
be performed using formula (28) to identify and obtain model coefficients, so as to
obtain the air conditioning system DCOP performance model:

where the PLR is the water chilling unit load ratio; A, B, and C are parameters of
the fitted model of the air conditioning system.
[0161] In the above embodiment, the air conditioning system DCOP performance model curve
obtained based on the large amount of actual operating data is one of bases for optimizing
operation of the air conditioning system, and with the air conditioning system DCOP
performance model obtained by data regression fitting, construction of the performance
model of the air conditioning system is more complete, so that the air conditioning
system DCOP performance model can be selectively suitable for air conditioning systems
in different actual environments, thus improving prediction precision of the energy
efficiency ratio of the air conditioning system.
[0162] In some embodiments, the third corresponding relationship of the air conditioning
system may be obtained by selectively using the first corresponding relationship or
the second corresponding relationship according to data similarity between a newly
added current data set and the target data set in the operating data. Therefore, as
shown in FIG. 17, the step S114 may include the following steps.
[0163] In S711, the data similarity between the current data set and the target data set
in the operating data is obtained based on the water chilling unit load ratio and
the temperature difference between the evaporation temperature and the condensation
temperature of the air conditioning system.
[0164] The current data set includes operating data obtained after the preset duration,
and may also represent operating data at the current time.
[0165] In some embodiments of the present application, the target data set may represent
any data set in the operating data. In some embodiments, input data may be clustered
by using a K-means clustering analysis method, and an optimal number k of clustering
centers is found in a preset interval by using an elbow method, so as to obtain the
clustering centers p
1, p
2, ..., and p
k. Exemplarily, the water chilling unit load ratio and the temperature difference between
the evaporation temperature and the condensation temperature are clustered by using
the K-means clustering analysis method, and the optimal number k of the clustering
centers is found in the interval [2,10] by using the elbow method, so as to obtain
the clustering centers p
1, p
2, ..., and p
k. Then, Euclidean distances d
1, d
2, ..., and d
k from the water chilling unit load ratio and the temperature difference between the
evaporation temperature and the condensation temperature to the clustering centers
are calculated by using formula (29):

where x
j is an n-dimensional input parameter, p
i is the clustering center, and d
i is the Euclidean distance from the input parameter to the clustering center p
i.
[0166] In some embodiments, the data similarity may be data proximity, and the data similarity
between the current data set and the target data set in the operating data may be
calculated using formula (30):

where I is the data similarity between the current data set and the target data set
in the operating data.
[0167] In S712, the third corresponding relationship is established according to the first
corresponding relationship under the condition that the data similarity is smaller
than or equal to preset similarity; and the third corresponding relationship is established
according to the second corresponding relationship under the condition that the data
similarity is greater than the preset similarity.
[0168] In some embodiments, the established third corresponding relationship may also represent
a target performance model of the air conditioning system. The target performance
model may be obtained using formula (31) to obtain the target energy efficiency ratio
from the target performance model.

[0169] The COP in the formula (31) may represent the target energy efficiency ratio.
[0170] In some embodiments, the current data set may include the water chilling unit operating
load ratio, the condensation temperature of the air conditioning system, and the evaporation
temperature of the air conditioning system in the operating data obtained after the
preset duration. The data of the target data set in the operating data is input neurons
in the BP neural network: the water chilling unit load ratio, and the difference between
the condensation temperature and the evaporation temperature. Similarity between the
current input data and the input neuron in the BP neural network can be calculated
by using the formula (19), I' (preset similarity) is taken as a boundary, and when
the similarity is higher than I', the current data set is close to the input neuron
in the BP neural network, so that the air conditioning system DCOP performance prediction
model established by using the BP neural network is selected to establish the target
performance model of the air conditioning system. When the similarity is smaller than
or equal to I', the precision of prediction by using the air conditioning system DCOP
performance model is higher, so that the air conditioning system DCOP performance
model is selected to establish the target performance model of the air conditioning
system. In the above embodiment, data similarity between a first data set and the
current data set is obtained through the mean clustering algorithm, and whether the
first corresponding relationship or the second corresponding relationship is used
to establish the third corresponding relationship is determined according to the similarity,
so that the establishment of the performance model of the air conditioning system
is based on an actual situation of the current data, the prediction precision of the
model of the air conditioning system is improved, and the more accurate target energy
efficiency ratio and cooling capacity can be obtained, so as to achieve efficient,
safe and energy-saving operating targets of the air conditioning system.
[0171] The control method according to some embodiments of the present application is described
below by taking a centrifugal water chilling unit with a rated cooling capacity of
440kW as an example. The compressor is a centrifugal compressor, the evaporator and
the condenser are both shell-and-tube heat exchangers, water flows in tubes, a refrigerant
R134a flows outside the tubes, and an electronic expansion valve is used. As shown
in FIG. 18, steps for establishing the performance model of the water chilling unit
are as follows.
[0172] In S811of collecting data by sensors: a large amount of actual operating data of
the water chilling unit is collected through the sensors, and operating data of ten
features in a certain year is obtained: a supply chilled water temperature, a return
chilled water temperature, a water chilling unit cooling load ratio, water chilling
unit power, a chilled water flow rate, a supply cooling water temperature, a return
cooling water temperature, a cooling water flow rate, an evaporator evaporation temperature,
and a condenser condensation temperature.
[0173] In S812 of performing data screening: data screening is performed by taking all data
of continuous months as a set of operating data.
- 1) Calculating a load unbalance ratio: a water chilling unit direct load is calculated
by using the formula (12), a water chilling unit cooling mount is calculated by using
the formula (13), and then, the load unbalance ratio is calculated by using the formula
(14).
- 2) calculating a COP of the water chilling unit: the water chilling unit direct load
is calculated using the formula (12), and then, the COP of the water chilling unit
is calculated using the formula (15).
- 3) performing data removal.
[0174] A rule for identifying an abnormal unbalance ratio is as follows:
when the unbalance ratio exceeds 15%, the unbalance ratio is an abnormal value, that
is, when the load unbalance ratio calculated at a certain time point is greater than
or equal to 15%, a data set at the time point corresponding to the load unbalance
ratio is removed from the operating data.
[0175] A rule for identifying an abnormal COP value is as follows:
when the COP value is outside the interval (µ1-2σ1, µ1+2σ1), the value is an abnormal
value and is removed, µ1 is an average value of the COPs in a current month, and σ1
is a standard deviation of the COPs in the current month. That is, when the COP value
calculated at a time point is outside the interval (µ1-2σ1, µ1+2σ1), the COP value
is an abnormal value, and a data set at the time point corresponding to the COP value
is removed from the operating data.
[0176] In S813, an evaporation temperature and a condensation temperature are calculated
by using the data values that has been screened.
1) Calculating the evaporation temperature: a temperature difference between the supply
chilled water temperature and the evaporator evaporation temperature and a temperature
difference between the return chilled water temperature and the evaporator evaporation
temperature are calculated, an evaporator logarithmic mean temperature difference
and a temperature difference between inlet and outlet of the evaporator are calculated
through the formulas (15) and (17) respectively, and then, an evaporator heat transfer
coefficient K
eF
e is calculated by utilizing the formula (18). The evaporator heat transfer coefficient
is subjected to regression fitting by using the formula (19), the evaporator heat
transfer coefficient K
eF
e is quantitatively depicted, and the evaporation temperature is calculated by using
the formula (20). The calculated regression fitting coefficient is shown in table
2 below.
Table 2. Calculation results of fitting coefficients for evaporator heat transfer
model
| a1 |
b1 |
c1 |
d1 |
e1 |
f1 |
| -3.30E+01 |
-4.80E-03 |
-3.14E-04 |
5.01E+03 |
6.75E-01 |
-190311.015 |
2) Calculating the condensation temperature: a temperature difference between the
return cooling water temperature and the condenser condensation temperature and a
temperature difference between a supply cooling water temperature and the condenser
condensation temperature are calculated, a condenser logarithmic mean temperature
difference and a temperature difference between inlet and outlet of the condenser
are calculated through the formulas (21) and (22) respectively, a condenser heat transfer
coefficient K
cF
c is then calculated by using the formula (23), the condenser heat transfer coefficient
is subjected to regression fitting by using the formula (24), the condenser heat transfer
coefficient K
cF
c is quantitatively depicted, and the condensation temperature is calculated by using
the formula (25). The calculated regression fitting coefficient is shown in table
3 below.
Table 3. Calculation results of fitting coefficients for condenser heat transfer model
| a2 |
b2 |
c2 |
d2 |
e2 |
f2 |
| -3.65E-01 |
-1.11E-02 |
-2.39E-04 |
6.94E+01 |
1.26E+00 |
-3227.177731 |
[0177] In S814, a DCOP performance model of the water chilling unit is established.
[0178] The evaporation temperature and the condensation temperature of the water chilling
unit are calculated through the formulas (20) and (25), an ideal COP value of the
water chilling unit is calculated through the formula (26) and is defined as an ICOP
value, and a DCOP value is calculated through the formula (27), the DCOP value is
a degree of the actual COP value of the water chilling unit approaching the ideal
COP value, which is called a water chilling unit performance coefficient. Finally,
a load ratio PLR is taken as an abscissa, the water chilling unit performance coefficient
DCOP is take as an ordinate, and corresponding data points are listed in a coordinate
system to form a dense scatter diagram. Regression fitting is then performed through
the formula (28) to identify and obtain a model coefficient, so as to obtain a water
chilling unit DCOP performance model. The calculated regression fitting coefficients
and corresponding model evaluation indexes are shown in table 4 below.
Table 4. Calculation results of fitting coefficients for DCOP performance model
| A |
B |
C |
| -0.6578 |
0.8922 |
0.3294 |
| MAPE (mean absolute percentage error) |
RMSE (root mean square error) |
R2 (determination coefficient) |
| 1.2663% |
0.0108 |
0.7490 |
[0179] Newly added water chilling unit operating data is input into the trained DCOP performance
model for calculation, so as to obtain model error evaluation indexes shown in the
following table 5.
Table 5. DCOP performance model newly added data error evaluation index
| MAPE (mean absolute percentage error) |
RMSE (root mean square error) |
R2 (determination coefficient) |
| 1.4828% |
0.0185 |
0.7325 |
[0180] For input data which is not trained by the model, a prediction result of the DCOP
performance model is still close to an actual measurement result, and the generalization
capacity of the DCOP performance model is good.
[0181] In S815, a DCOP performance prediction model of the water chilling unit is established
through a BP neural network model.
[0182] A BP neural network structure is established and has three layers, as shown in FIG.
19, and input neurons of a neural network are the operating load ratio PLR of the
water chilling unit and the difference T
c-T
e between the condensation temperature and the evaporation temperature. The number
of network nodes of a network hidden layer is 7. An output neuron is a DCOP. A trainlm
learning algorithm is used in the BP neural network model, a network hidden layer
transfer function is a tansig function, an output layer is a Pureline function, a
learning rate of the BP neural network model is set to be 0.05, a maximum number of
learning steps is set to be 1,000, and a training target error is set to be 0.003,
so that the DCOP prediction model of the water chilling unit is obtained through data
training.
[0183] Through calculation, training data error evaluation indexes for the DCOP prediction
result and the DCOP actual measurement calculation result are shown in table 6. Newly
added water chilling unit operating data is input into the trained DCOP prediction
model for calculation, so as to obtain model error evaluation indexes shown in the
following table 7. It can be seen that the DCOP performance prediction model established
by the neural network has higher precision, but when the newly added input data deviates
from training data of the model, an error is reduced, which indicates that the generalization
capacity of the model is poor.
Table 6. DCOP prediction model training data error evaluation index
| MAPE (mean absolute percentage error) |
RMSE (root mean square error) |
R2 (determination coefficient) |
| 0.6043% |
0.0059 |
0.9073 |
Table 7. DCOP prediction model newly added data error evaluation index
| MAPE (mean absolute percentage error) |
RMSE (root mean square error) |
R2 (determination coefficient) |
| 2.0949% |
0.0182 |
0.6492 |
[0184] In S816, the DCOP performance model and the COP performance prediction model of the
water chilling unit are fused based on a K-means clustering algorithm, and the water
chilling unit model is established.
1) Performing clustering to obtain clustering centers: the input data of the DCOP
prediction model is clustered by using a K-means clustering analysis method, and an
optimal number k of the clustering centers is found in the interval [2, 10] by using
an elbow method to obtain the clustering centers p
1, p
2, ..., and p
k. In this embodiment, the number k of the clustering centers calculated through the
elbow method is 5, and Euclidean distances d
1, d
2, ..., and d
k from input parameters to the clustering centers are calculated through the formula
(18). Coordinates of the clustering centers p
1, p
2, p
3, p
4, p
5, p
6 and p
7 are shown in table 8.
Table
8. Clustering center calculation result
| Clustering center 1 |
Clustering center 2 |
Clustering center 3 |
Clustering center 4 |
| (0.673, 29.412) |
(0.841, 32.571) |
(0.588, 26.479) |
(0.461, 22.689) |
| Clustering center 5 |
Clustering center 6 |
Clustering center 7 |
|
| (0.676, 30.819) |
(0.638, 28.014) |
(0.609, 24.835) |
|
2) Calculating clustering center proximity I by using the newly added data.
3) Taking I' (preset similarity) as a boundary, where when the proximity is higher
than I', the current data set is close to the input neuron in the BP neural network,
so that the air conditioning system DCOP performance prediction model established
by using the BP neural network is selected; when the proximity is less than or equal
to I', the precision of prediction by using the air conditioning system DCOP performance
model established by using parameter identification is higher, so that the air conditioning
system DCOP performance model established by using the parameter identification is
selected. In this embodiment, I' is 0.8. Newly added data error evaluation indexes
are shown in table 9.
Table 9. Water chilling unit model newly added data error evaluation index
| MAPE (mean absolute percentage error) |
RMSE (root mean square error) |
R2 (determination coefficient) |
| 1.6328% |
0.0133 |
0.8362 |
4) Constructing the water chilling unit performance model.
[0185] The energy efficiency ratio COP of the water chilling unit is calculated by using
the formula (20). Newly added data error evaluation indexes are shown in table 10.
Therefore, the finally established water chilling unit model has higher prediction
precision, and a generalization capacity and a self-adaption capacity of the model
are also better.
Table 10. Water chilling unit model COP prediction error evaluation index
| MAPE (mean absolute percentage error) |
RMSE (root mean square error) |
R2 (determination coefficient) |
| 1.6318% |
0.1553 |
0.8735 |
[0186] As can be seen from the above examples, in the control method according to some embodiments
of the present application, the evaporation temperature and the condensation temperature
of the water chilling unit can be quantitatively depicted in the curve manner by counting
the actual energy efficiency ratios of the water chilling unit under different weather
conditions and different cooling load ratios, the ideal energy efficiency ratios in
various situations, the target heat transfer coefficients of the evaporator and the
target heat transfer coefficients of the condenser of the water chilling unit. Based
on a physical framework of the water chilling unit, the actual performance model of
the water chilling unit is established by using the actual data, the water chilling
unit performance prediction model is then established through the BP neural network,
and finally, the actual performance model of the water chilling unit is combined with
the high-precision prediction interval of the performance prediction model by using
the K-means clustering method to obtain the water chilling unit target performance
model. The target performance model obtained by the solution is completely based on
the actual data, so that the actual performance of the water chilling unit under different
load ratios can be well reflected, the prediction precision of the water chilling
unit model is greatly improved, and the problems that a traditional water chilling
unit performance curve cannot be applied to actual projects, and an existing water
chilling unit performance model is not high in prediction precision and poor in self-adaptation
capacity and universality are solved. The target energy efficiency ratio can be obtained
according to the target performance model, so that a more reasonable and more accurate
cooling capacity can be determined according to the target energy efficiency ratio,
thus effectively lowering operating energy consumption of the water chilling unit.
[0187] In some embodiments of the present application, functional modules of the controller
may be divided according to the above method examples. For example, each functional
module may be divided corresponding to each function, or two or more functions may
be integrated into one processing module. The integrated module can be realized in
the form of hardware or a software functional module. In some embodiments of the present
application, the division of the modules is schematic, and is only logical function
division, and there may be another division manner in actual implementation.
[0188] Some embodiments of the present application further provide a schematic diagram of
a hardware structure of an air conditioner, as shown in FIG. 20, the air conditioner
3000 includes a processor 3001, and in some embodiments, further includes a memory
3002 and a communication interface 3003 connected to the processor 3001. The processor
3001, the memory 3002, and the communication interface 3003 are connected by a bus
3004.
[0189] The processor 3001 may be a central processing unit (CPU), a general-purpose processor,
a network processor (NP), a digital signal processor (DSP), a microprocessor, a microcontroller,
a programmable logic device (PLD), or any combination thereof.
[0190] The memory 3002 may be a read-only memory (ROM) or other types of static storage
devices that may store static information and instructions, a random access memory
(RAM) or other types of dynamic storage devices that may store information and instructions,
an electrically erasable programmable read-only memory (EEPROM), a compact disc read-only
memory (CD-ROM), or other optical storages.
[0191] The communication interface 3003 may be configured for being in communication with
other devices or communication networks.
[0192] The bus 3004 may be a peripheral component interconnect (PCI) bus, an extended industry
standard architecture (EISA) bus, or the like. The bus 3004 may be divided into an
address bus, a data bus, a control bus, or the like. For ease of illustration, the
bus is represented only by one thick line in FIG. 20, but which does not indicate
only one bus or one type of buses.
[0193] The one or more memories 3002 are configured for storing computer program codes including
computer instructions, and when the one or more processors 3002 execute the computer
instructions, the controller executes the method for controlling an air conditioning
system and the method for determining the ideal energy efficiency ratio of a water
chilling unit provided in the above possible implementations. Reference may be made
to the foregoing for specific implementation, which is not explained herein.
[0194] It will be understood by those skilled in the art that the scope of the disclosure
of the present application is not limited to the particular embodiments described
above, and that modifications and substitutions of certain elements of the embodiments
may be made without departing from the spirit of the application. The scope of the
present application is limited by the appended claims.
1. An air conditioning system, comprising:
a water chilling unit;
a refrigerant circulation loop configured for circulating a refrigerant in a loop
comprising a compressor, a condenser, and an evaporator;
a first temperature sensor configured for detecting a condensation temperature of
the condenser;
a second temperature sensor configured for detecting an evaporation temperature of
the evaporator; and
a controller configured for:
using the first temperature sensor to obtain a first condensation temperature in an
n-th detection period, and using the second temperature sensor to obtain a first evaporation
temperature in the n-th detection period, n being an integer greater than 1;
obtaining operating parameters of the water chilling unit, and based on the operating
parameters, determining a second condensation temperature of the condenser in the
n-th detection period and a second evaporation temperature of the evaporator in the
n-th detection period;
determining a first energy efficiency ratio in the n-th detection period according
to the first condensation temperature and the first evaporation temperature;
determining a second energy efficiency ratio in the n-th detection period according
to the second condensation temperature and the second evaporation temperature; and
determining an ideal energy efficiency ratio in the n-th detection period according
to the first energy efficiency ratio in the n-th detection period and the second energy
efficiency ratio in the n-th detection period.
2. The air conditioning system according to claim 1, wherein the controller is further
configured for:
determining the ideal energy efficiency ratio in the n-th period according to the
first energy efficiency ratio in the n-th detection period, the second energy efficiency
ratio in the n-th detection period, a first value range, and a second value range;
wherein the first value range is determined according to an average value and a standard
deviation of first energy efficiency ratios in n detection periods, and the second
value range is determined according to an average value and a standard deviation of
second energy efficiency ratios in the n detection periods.
3. The air conditioning system according to claim 2, wherein the controller is further
configured for:
when the first energy efficiency ratio in the n-th detection period is not within
the first value range and the second energy efficiency ratio in the n-th detection
period is not within the second value range, taking an average value of the first
energy efficiency ratio in the n-th detection period and the second energy efficiency
ratio in the n-th detection period as the ideal energy efficiency ratio in the n-th
detection period; or
when the first energy efficiency ratio in the n-th detection period is within the
first value range and the second energy efficiency ratio in the n-th detection period
is not within the second value range, taking the first energy efficiency ratio in
the n-th period as the ideal energy efficiency ratio in the n-th period; or
when the second energy efficiency ratio in the n-th detection period is within the
second value range, taking the second energy efficiency ratio in the n-th detection
period as the ideal energy efficiency ratio in the n-th period.
4. The air conditioning system according to any one of claims 1 to 3, wherein the water
chilling unit comprises chilled water and cooling water;
the operating parameters of the water chilling unit comprise: a temperature difference
between a supply water temperature and return water temperature of the chilled water
in each detection period, a temperature difference between a supply water temperature
and return water temperature of the cooling water in each detection period, a heat
exchange temperature difference of the evaporator in each detection period, a heat
exchange temperature difference of the condenser in each detection period, a supply
water temperature of the chilled water in each detection period, a return water temperature
of the cooling water in each detection period, and a cooling load ratio of the water
chilling unit in each detection period;
the controller is further configured for:
determining the second condensation temperature of the condenser in the n-th detection
period according to the water temperature difference between the supply water temperature
and return water temperature of the cooling water in the n-th detection period, the
heat exchange temperature difference of the condenser in the n-th detection period,
the return water temperature of the cooling water in the n-th detection period, and
the cooling load ratio of the water chilling unit in the n-th detection period; and
determining the second evaporation temperature of the evaporator in the n-th detection
period according to the temperature difference between the supply water temperature
and return water temperature of the chilled water in the n-th detection period, the
heat exchange temperature difference of the evaporator in the n-th detection period,
the supply water temperature of the chilled water in the n-th detection period, and
the cooling load ratio of the water chilling unit in the n-th detection period.
5. The air conditioning system according to claim 4, wherein the operating parameters
of the water chilling unit further comprise electric power of the water chilling unit
in each detection period;
the controller is further configured for:
after determining the ideal energy efficiency ratio in the n-th detection period,
determining a cooling load of the water chilling unit in the n-th detection period
according to the electric power of the water chilling unit in the n-th detection period,
the cooling load ratio of the water chilling unit in the n-th detection period, and
the ideal energy efficiency ratio in the n-th detection period.
6. An air conditioning system, comprising:
an evaporator;
a condenser; and
a controller electrically connected to the evaporator and the condenser, the controller
being configured for:
obtaining an evaporation temperature of the air conditioning system, a condensation
temperature of the air conditioning system, a first energy efficiency ratio of the
air conditioning system, and a load ratio of the air conditioning system according
to operating data of the evaporator and the condenser in a preset duration;
obtaining a second energy efficiency ratio of the air conditioning system and a first
corresponding relationship between the second energy efficiency ratio and the load
ratio of the air conditioning system according to the evaporation temperature of the
air conditioning system, the condensation temperature of the air conditioning system,
the first energy efficiency ratio of the air conditioning system, and the load ratio
of the air conditioning system;
obtaining a second corresponding relationship between the second energy efficiency
ratio and the load ratio of the air conditioning system by using a back propagation
neural network model; and
obtaining a third corresponding relationship between a target energy efficiency ratio
of the air conditioning system and the load ratio of the air conditioning system by
using the first corresponding relationship and the second corresponding relationship
based on a mean clustering algorithm.
7. The air conditioning system according to claim 6, wherein the operating data of the
evaporator and the condenser in the preset duration comprises a supply chilled water
temperature, a return chilled water temperature, a chilled water flow rate, and an
evaporator evaporation temperature of the evaporator, a supply cooling water temperature,
a return cooling water temperature, a cooling water flow rate, and a condenser condensation
temperature of the condenser, and a water chilling unit load ratio and water chilling
unit power of the air conditioning system;
wherein the operating data corresponding to each time point in the preset duration
forms a data set.
8. The air conditioning system according to claim 7, wherein the controller is further
configured for:
obtaining a water chilling unit direct load according to a specific heat capacity
of water and the chilled water flow rate, the return chilled water temperature, and
the supply chilled water temperature in a target data set in the operating data;
obtaining a water chilling unit cooling amount according to the specific heat capacity
of water and the cooling water flow rate, the return cooling water temperature, and
the supply cooling water temperature in the target data set in the operating data;
obtaining an evaporator logarithmic mean temperature difference corresponding to the
target data set according to a temperature difference between the supply chilled water
temperature and the evaporator evaporation temperature in the target data set and
a temperature difference between the return chilled water temperature and the evaporator
evaporation temperature in the target data set;
obtaining an evaporator heat transfer coefficient corresponding to the target data
set according to the water chilling unit direct load and the evaporator logarithmic
mean temperature difference;
performing fitting according to the evaporator heat transfer coefficients corresponding
to different data sets to obtain an evaporator target heat transfer coefficient; and
obtaining the evaporation temperature of the air conditioning system according to
a density of water, the specific heat capacity of water, the evaporator target heat
transfer coefficient, the water chilling unit direct load, the chilled water flow
rate, and the supply chilled water temperature.
9. The air conditioning system according to claim 7, wherein the controller is further
configured for:
obtaining a water chilling unit direct load according to a specific heat capacity
of water and the chilled water flow rate, the return chilled water temperature, and
the supply chilled water temperature in a target data set in the operating data;
obtaining a water chilling unit cooling amount according to the specific heat capacity
of water and the cooling water flow rate, the return cooling water temperature, and
the supply cooling water temperature in the target data set in the operating data;
obtaining a condenser logarithmic mean temperature difference corresponding to the
target data set according to a temperature difference between the supply cooling water
temperature and the condenser condensation temperature in the target data set and
a temperature difference between the return cooling water temperature and the condenser
condensation temperature in the target data set;
obtaining a condenser heat transfer coefficient corresponding to the target data set
according to the water chilling unit direct load and the condenser logarithmic mean
temperature difference;
performing fitting according to the condenser heat transfer coefficients corresponding
to different data sets to obtain a condenser target heat transfer coefficient; and
obtaining the condensation temperature of the air conditioning system according to
the density of water, the specific heat capacity of water, the condenser target heat
transfer coefficient, the water chilling unit direct load, the cooling water flow
rate, and the return cooling water temperature.
10. The air conditioning system according to claim 8 or 9, wherein the controller is further
configured for:
obtaining a load unbalance ratio according to the water chilling unit direct load,
the water chilling unit cooling amount, and the water chilling unit power in the target
data set in the operating data; and
deleting data in the target data set from the operating data under a condition that
the load unbalance ratio is greater than or equal to a preset load unbalance ratio.
11. The air conditioning system according to claim 8 or 9, wherein the controller is further
configured for:
obtaining the first energy efficiency ratio of the air conditioning system according
to the water chilling unit direct load and the water chilling unit power in the target
data set in the operating data; and
deleting the data in the target data set from the operating data under a condition
that the first energy efficiency ratio is outside a preset interval.
12. The air conditioning system according to claim 6 or 7, wherein the controller is further
configured for:
obtaining the second energy efficiency ratio of the air conditioning system according
to the evaporation temperature, the condensation temperature, the first energy efficiency
ratio, and the load ratio;
with the second energy efficiency ratio as an abscissa and the load ratio corresponding
to the second energy efficiency ratio as an ordinate, generating a scatter diagram
composed of a plurality of data points, each data point corresponding to one second
energy efficiency ratio and one load ratio; and
fitting the data points on the scatter diagram to obtain the first corresponding relationship
represented by a curve.
13. The air conditioning system according to claim 6 or 7, wherein the controller is further
configured for:
inputting the water chilling unit load ratio and a temperature difference between
the evaporation temperature and the condensation temperature of the air conditioning
system in the operating data into the back propagation neural network model to obtain
the second energy efficiency ratio and the second corresponding relationship between
the second energy efficiency ratio and the load ratio of the air conditioning system.
14. The air conditioning system according to claim 6 or 7, wherein the controller is further
configured for:
obtaining data similarity between a current data set and the target data set in the
operating data based on the water chilling unit load ratio and the temperature difference
between the evaporation temperature and the condensation temperature of the air conditioning
system; the current data set comprising operating data obtained after the preset duration;
establishing the third corresponding relationship according to the first corresponding
relationship under a condition that the data similarity is smaller than or equal to
preset similarity; and
establishing the third corresponding relationship according to the second corresponding
relationship under a condition that the data similarity is greater than the preset
similarity.
15. A method for determining the energy efficiency ratio of an air conditioning system,
the method being applied to a water chilling unit in the air conditioning system,
and the method comprising:
using a first temperature sensor to obtain a first condensation temperature of a condenser
in an n-th detection period, and using a second temperature sensor to obtain a first
evaporation temperature of an evaporator during the n-th detection period, n being
an integer greater than 1;
obtaining operating parameters of the water chilling unit, and based on the operating
parameters, determining a second condensation temperature of the condenser in the
n-th detection period and a second evaporation temperature of the evaporator in the
n-th detection period;
determining a first energy efficiency ratio in the n-th detection period according
to the first condensation temperature and the first evaporation temperature;
determining a second energy efficiency ratio in the n-th detection period according
to the second condensation temperature and the second evaporation temperature; and
determining an ideal energy efficiency ratio in the n-th detection period according
to the first energy efficiency ratio in the n-th detection period and the second energy
efficiency ratio in the n-th detection period.
16. A method for controlling an air conditioning system, comprising:
obtaining an evaporation temperature of the air conditioning system, a condensation
temperature of the air conditioning system, a first energy efficiency ratio of the
air conditioning system, and a load ratio of the air conditioning system according
to operating data of an evaporator and a condenser in a preset duration;
obtaining a second energy efficiency ratio of the air conditioning system and a first
corresponding relationship between the second energy efficiency ratio and the load
ratio of the air conditioning system according to the evaporation temperature of the
air conditioning system, the condensation temperature of the air conditioning system,
the first energy efficiency ratio of the air conditioning system, and the load ratio
of the air conditioning system;
obtaining a second corresponding relationship between the second energy efficiency
ratio and the load ratio of the air conditioning system by using a back propagation
neural network model; and
obtaining a third corresponding relationship between a target energy efficiency ratio
of the air conditioning system and the load ratio of the air conditioning system by
using the first corresponding relationship and the second corresponding relationship
based on a mean clustering algorithm.