CN117006560A - Water-cooling integrated water chilling unit with natural cooling function and control method - Google Patents
Water-cooling integrated water chilling unit with natural cooling function and control method Download PDFInfo
- Publication number
- CN117006560A CN117006560A CN202311011731.1A CN202311011731A CN117006560A CN 117006560 A CN117006560 A CN 117006560A CN 202311011731 A CN202311011731 A CN 202311011731A CN 117006560 A CN117006560 A CN 117006560A
- Authority
- CN
- China
- Prior art keywords
- cooling
- water
- temperature
- low
- cooling water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000001816 cooling Methods 0.000 title claims abstract description 356
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 312
- 238000000034 method Methods 0.000 title claims abstract description 27
- 239000000498 cooling water Substances 0.000 claims abstract description 282
- 230000002829 reductive effect Effects 0.000 claims abstract description 36
- 238000007710 freezing Methods 0.000 claims description 80
- 230000008014 freezing Effects 0.000 claims description 79
- 239000003507 refrigerant Substances 0.000 claims description 41
- 238000005057 refrigeration Methods 0.000 claims description 27
- 238000009833 condensation Methods 0.000 claims description 13
- 230000005494 condensation Effects 0.000 claims description 13
- 239000007788 liquid Substances 0.000 claims description 13
- 238000009826 distribution Methods 0.000 claims description 9
- 238000004378 air conditioning Methods 0.000 abstract description 8
- 238000010276 construction Methods 0.000 abstract description 3
- 238000005265 energy consumption Methods 0.000 description 5
- 230000010354 integration Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000002238 attenuated effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000003889 chemical engineering Methods 0.000 description 1
- -1 chemical engineering Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000011217 control strategy Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 230000000670 limiting effect Effects 0.000 description 1
- 238000005461 lubrication Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 230000036961 partial effect Effects 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F5/00—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater
- F24F5/0046—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater using natural energy, e.g. solar energy, energy from the ground
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F11/00—Control or safety arrangements
- F24F11/30—Control or safety arrangements for purposes related to the operation of the system, e.g. for safety or monitoring
- F24F11/46—Improving electric energy efficiency or saving
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F11/00—Control or safety arrangements
- F24F11/62—Control or safety arrangements characterised by the type of control or by internal processing, e.g. using fuzzy logic, adaptive control or estimation of values
- F24F11/63—Electronic processing
- F24F11/65—Electronic processing for selecting an operating mode
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F11/00—Control or safety arrangements
- F24F11/70—Control systems characterised by their outputs; Constructional details thereof
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F5/00—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater
- F24F5/0007—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater cooling apparatus specially adapted for use in air-conditioning
- F24F5/001—Compression cycle type
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B41/00—Fluid-circulation arrangements
- F25B41/20—Disposition of valves, e.g. of on-off valves or flow control valves
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B41/00—Fluid-circulation arrangements
- F25B41/30—Expansion means; Dispositions thereof
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B41/00—Fluid-circulation arrangements
- F25B41/40—Fluid line arrangements
Landscapes
- Engineering & Computer Science (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Combustion & Propulsion (AREA)
- Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Life Sciences & Earth Sciences (AREA)
- Thermal Sciences (AREA)
- Sustainable Development (AREA)
- Signal Processing (AREA)
- Sustainable Energy (AREA)
- Fuzzy Systems (AREA)
- Mathematical Physics (AREA)
- Other Air-Conditioning Systems (AREA)
Abstract
The application relates to the technical field of air conditioners, in particular to a water-cooling integrated water chilling unit with a natural cooling function and a control method. The water cooling integrated water chilling unit integrates the modules, is convenient to install and maintain, and is functionally equivalent to an integrated air conditioning cold collection station; the distance between the condenser and the cooling tower as well as between the condenser and the cooling water pump is short, the resistance of the cooling water system is small, and the power consumption of the cooling water pump can be saved by about 33%; the unit does not need to start a compressor in winter, and can directly utilize the low temperature of the outdoor air to realize cooling of chilled water, so that the refrigerating energy efficiency of the unit is obviously improved; the water-cooling integrated water chilling unit is directly arranged outdoors, a special air conditioner room is omitted, and the construction cost can be further reduced.
Description
Technical Field
The application relates to the technical field of air conditioners, in particular to a water-cooling integrated water chilling unit with a natural cooling function and a control method.
Background
The traditional water cooling chiller unit must be provided with a special air conditioner room, and the cooling water pump has higher lift and power consumption because the cooling tower is far away from the chiller unit and the cooling water pipeline is longer. Meanwhile, in actual engineering projects, a chilled water pump, a cooling water pump and a cooling tower are often excessively configured, so that the energy consumption of an air conditioning system is high.
Because the water chiller, the chilled water pump, the cooling water pump and the cooling tower are purchased from different equipment manufacturers, a centralized control system is absent. The air conditioning system is in a partial load operation state 99% of the time, and when the compressor of the water chilling unit is unloaded or stopped, the chilled water pump, the cooling water pump and the cooling tower are still in a full load operation state, so that the operation efficiency of the air conditioning system is low. According to actual measurement statistics of a large number of air conditioning engineering projects, the sum of the power of the chilled water pump, the cooling water pump and the cooling tower only accounts for about 16% of the installed capacity of the whole air conditioning system, but the actual running energy consumption accounts for about 45%, and therefore the integration and linkage control between the water chilling unit and the chilled water pump, and between the cooling water pump and the cooling tower are extremely important.
The process water cooling and cooling water units in the industries of data centers, medicines, chemical engineering, rubber, photovoltaics and the like often need refrigeration operation all year round so as to meet the requirements of production process parameters. When the outdoor air temperature is lower, the high pressure and condensation temperature of the unit can be reduced, and the pressure difference between the front and the rear of the throttle valve is too small, so that the circulation capacity of the throttle valve and the liquid supply amount to the evaporator are greatly reduced, and finally the refrigerating capacity and the refrigerating energy efficiency of the unit are seriously attenuated. Meanwhile, when the pressure difference between the high pressure and the low pressure of the compressor is too low, the oil supply circulation quantity of the compressor is insufficient, the lubrication condition of the bearing is deteriorated, the loading speed is too slow, and the operation reliability of the compressor is seriously affected.
The cooling water outlet temperature of the condenser is generally increased by reducing the flow rate of cooling water in winter, so that the condensation temperature of the unit is kept above 30 ℃, the circulation capacity of a throttle valve and the minimum oil supply pressure difference required by oil supply in the compressor are maintained, and the refrigerating energy efficiency of the unit is low and the running power consumption is high. At this time, the outdoor air temperature may be far lower than the chilled water temperature, and if the chilled water can be directly cooled by utilizing the low-temperature characteristic of the outdoor air, the operation energy consumption of the unit can be greatly reduced.
Disclosure of Invention
Aiming at the technical problems that a compressor of a water cooling main machine of a traditional water cooling air conditioning system is poor in linkage with a chilled water pump, a cooling water pump and a cooling tower, the resistance of the cooling water system is high, the power consumption of the cooling water pump is high, the compressor still needs to operate when the outdoor air temperature is far lower than the chilled water temperature, the operation power consumption of a unit is high, the cold energy contained in the outdoor low-temperature air cannot be utilized, and the like, the application discloses a water cooling integrated water chilling unit with a natural cooling function and a control method.
On one hand, the application provides a water-cooling integrated water chilling unit with a natural cooling function, which comprises a water-cooling water chilling unit module 5, a freezing hydraulic power module 12, a natural cooling heat exchanger module 13, a cooling heat rejection module 19 and a centralized controller module 15 for sending control instructions to the modules; the water-cooling chiller module 5 comprises a compressor 1, a water-cooling condenser 2, a throttling device 3 and an evaporator 4 which are sequentially connected and form a circulation loop; the freezing hydraulic module 12 comprises a freezing water filter 8, a freezing water pump 9, a first control valve 10 and a second control valve 14, wherein the outlet of the freezing water pump 9 is respectively connected with the freezing water inlets of the first control valve 10 and the second control valve 14 through a freezing water pipe 6, the freezing water outlet of the first control valve 10 is respectively connected with the freezing water inlet of the evaporator 4 and the freezing water outlet of the natural cooling heat exchanger module 13 through the freezing water pipe 6, and the freezing water outlet of the second control valve 14 is connected with the freezing water inlet of the natural cooling heat exchanger module 13 through the freezing water pipe 6; the cooling heat rejection module 19 comprises a third control valve 16, a cooling water pump 17 and a cooling tower 18, wherein an inlet of the cooling water pump 17 is connected with a cooling water outlet positioned at the bottom of the cooling tower 18 through a cooling water pipe 7, the third control valve 16 controls cooling water at an outlet of the cooling water pump 17 to flow to the water-cooled condenser 2 and/or the natural cooling heat exchanger module 13, and the cooling water outlet of the water-cooled condenser 2 and the cooling water outlet of the natural cooling heat exchanger module 13 are connected to a top water inlet of the cooling tower 18 through the cooling water pipe 7; the freezing water outlet of the freezing water pump 9, the freezing water inlet and the freezing water outlet of the evaporator 4, the cooling water inlet and the cooling water outlet of the natural cooling heat exchanger module 13, the cooling water outlet of the water cooling condenser 2 and the air inlet side of the cooling tower 18 are all provided with temperature sensors; the centralized controller module 15 controls the fans of the compressor 1, the chilled water pump 9, the cooling water pump 17, and the cooling tower 18, the first control valve 10, the second control valve 14, the third control valve 16, and the throttle device 3 based on the data acquired by the sensors.
In particular, the compressor 1 is selected from screw compressors, scroll compressors, centrifugal compressors or other types of compressors.
In particular, the throttling device 3 is selected from a thermostatic expansion valve, an electronic expansion valve, an electric butterfly valve or other type of throttling element.
In particular, the first control valve 10 and the second control valve 14 are selected from a switch type electric two-way valve or a proportional type electric two-way valve, so as to realize that the chilled water output by the chilled water pump 9 in different operation modes directly enters the evaporator 4 or firstly enters the natural cooling heat exchanger module 13 and then enters the evaporator 4; or the freezing hydraulic module 12 further comprises an expansion tank 11.
In particular, the third control valve 16 is an electric three-way valve or two electric two-way valves respectively leading to the water-cooled condenser 2 and the natural cooling heat exchanger module 13, so as to control the flow distribution ratio of the cooling water delivered by the cooling water pump 17 between the natural cooling heat exchanger module 13 and the water-cooled condenser 2.
In particular, the cooling tower 18 is selected from an open cooling tower, a closed cooling tower, or other types of cooling towers.
On the other hand, the application also provides a control method of the water-cooling integrated water chilling unit with the natural cooling function, the water-cooling integrated water chilling unit is as described above, and the centralized controller module 15 is used for controlling the water chilling unit according to the inlet air wet bulb temperature t of the cooling tower WB And a target value t of the total water temperature of freezing W3S The running mode of the unit is controlled by the difference of the cooling system, and the unit comprises a mechanical refrigeration mode, a natural cooling precooling mode, a mechanical refrigeration sub-cooling mode and a natural cooling mode.
In particular, the mechanical refrigeration mode, when t WB ≥t W3S -Δt 1 At Deltat 1 The compressor 1 is operated at the temperature of-3 ℃ to 9 ℃, preferably 3 ℃, the first control valve 10 is electrified, the second control valve 14 is powered off, and the cooling water pump 17 and the cooling tower 18 are in an operation state; chilled water entering the unit passes through a chilled water filter 8, is sequentially conveyed to a first control valve 10 and an evaporator 4 by a chilled water pump 9, and exchanges heat with low-temperature low-pressure refrigerant which is relatively low in temperature and flows from a throttling device 3 in the evaporator 4; the low-temperature low-pressure gas refrigerant coming out of the evaporator 4 enters the compressor 1, is compressed into high-temperature high-pressure gas, then enters the water-cooled condenser 2, discharges a large amount of heat released in the condensation process to the cooling water to heat the cooling water, and is condensed into high-pressure liquid; then, the high-pressure liquid refrigerant enters a throttling device 3, throttled and depressurized into low-temperature low-pressure refrigerant, then enters an evaporator 4, absorbs the relatively high-temperature chilled water heat to cool the low-pressure refrigerant, evaporates into low-pressure gas, and then returns to the compressor 1 again to be compressed into high-temperature high-pressure gas, so that the high-pressure refrigerant is repeatedly circulated; the cooling water absorbs condensation heat discharged by the high-temperature high-pressure refrigerant in the water-cooling condenser 2, then the temperature rises, the cooling water is led to the cooling tower 18 from a cooling water outlet of the water-cooling condenser 2 through the cooling water pipe 7, the cooling water temperature is reduced after the heat is discharged to outdoor air in the cooling tower 18, and then the cooling water is conveyed to the third control valve 16 by the cooling water pump 17 and then enters the water-cooling condenser 2, and the circulation is repeated; the unit centralized controller module 15 is cooled according to the water-cooled condenser 2 Water temperature t W6 To control the number and frequency of fan operations of cooling tower 18, when t W6 <t W6S At time t W6S The fan operation number and operation frequency of the cooling tower 18 are gradually reduced for the lowest cooling water outlet temperature, the range is 20-30 ℃, and the preferable range is 25 ℃; if only 1 fan is operated at the lowest frequency, t is still satisfied W6 <t W6S If the conditions are that the flow distribution proportion of the cooling water is controlled by the third control valve 16, the flow of the cooling water entering the water-cooled condenser 2 is gradually reduced, namely, the flow of the cooling water entering the natural cooling heat exchanger module 13 is gradually increased until t W6 ≥t W6S 。
In particular, the unit is in a natural cooling precooling mode and a mechanical refrigeration recooling mode, when t W3S -Δt 2 <t WB <t W3S -Δt 1 At Deltat 1 At a temperature of-3 to 9 ℃, preferably 3 ℃, Δt 2 The compressor 1 is operated at 4-16 ℃, preferably 8 ℃, the first control valve 10 is powered off, the second control valve 14 is powered on, and the cooling water pump 17 and the fan of the cooling tower 18 are in an operating state; the low-temperature cooling water cooled by the cooling tower 18 is conveyed to the third control valve 16 by the cooling water pump 17 and is split into two paths, wherein one path enters the water-cooling condenser 2 to absorb the condensation heat of the high-temperature high-pressure gas refrigerant, and the other path enters the natural cooling heat exchanger module 13 to precool the chilled water with relatively high temperature; the chilled water entering the unit is conveyed to a second control valve 14 by a chilled water pump 9 after passing through a chilled water filter 8, then enters a natural cooling heat exchanger module 13 through a chilled water pipe 6, exchanges heat with low-temperature cooling water flowing from a cooling tower and having relatively low temperature in the natural cooling heat exchanger module 13, releases heat to the low-temperature cooling water, the temperature of the chilled water is reduced after the low-temperature cooling water is precooled by the low-temperature cooling water, the chilled water continuously flows to an evaporator 4 through the chilled water pipe 6, and after the heat temperature of the chilled water absorbed by the low-temperature cooling water in the natural cooling heat exchanger module 13 is increased, the low-temperature cooling water continuously flows to a water inlet of a cooling tower 18 through a cooling water pipe 7; the low-temperature low-pressure gas refrigerant from the evaporator 4 enters the compressor 1, is compressed into high-temperature high-pressure gas and then enters the water-cooled condenser 2, and is condensed The released large amount of heat is discharged to low-temperature cooling water to heat the low-temperature cooling water, and the low-temperature cooling water is condensed into high-pressure liquid; then, the high-pressure liquid refrigerant enters a throttling device 3, is throttled and depressurized into low-temperature low-pressure refrigerant, then enters an evaporator 4, absorbs the heat of the chilled water precooled by low-temperature cooling water, cools the chilled water again, evaporates into low-pressure gas, and then returns to the compressor 1 again to be compressed into high-temperature high-pressure gas, and thus the circulation is repeated; the temperature of the chilled water cooled again by the low-temperature low-pressure refrigerant is reduced to the target value t W3S E is 0.3-3 c, preferably 0.5 c, after which it leaves the unit from the refrigerated water outlet of the evaporator 4; cooling water heated by high-temperature high-pressure refrigerant in the water-cooled condenser 2 and cooling water heated by chilled water in the natural cooling heat exchanger module 13 are collected by the cooling water pipe 7 and then led to a water inlet of the cooling tower 18, heat is discharged to outdoor air in the cooling tower 18, the cooling water temperature is reduced, and then the cooling water is respectively conveyed to the water-cooled condenser 2 and the natural cooling heat exchanger module 13 by the cooling water pump 17 through the third control valve 16; when the unit operates in the natural cooling precooling and mechanical refrigeration recooling modes, all fans of the cooling tower 18 and the cooling water pump 17 are at the highest frequency, and the air inlet wet bulb temperature t of the cooling tower WB The lower the natural cooling heat exchanger module 13 cools the incoming water temperature t W4 The lower the corresponding, the larger the heat exchange temperature difference and the heat exchange amount between the low-temperature cooling water and the chilled water in the natural cooling heat exchanger module 13, i.e. the larger the precooling amount of the low-temperature cooling water to the chilled water, the higher the chilled water inlet temperature t of the evaporator 4 W2 The lower it is, the lower it is from the frozen total outlet water temperature target value t W3S The smaller the deviation is, the smaller the refrigeration load of the water-cooling water chilling unit module 5 and the running power consumption of the compressor 1 are, and the higher the refrigerating energy efficiency of the unit is; the unit centralized controller module 15 is used for controlling the total water outlet temperature t according to the freezing W3 With a target value t W3S To control the operating capacity of the compressor 1, when t W3 <t W3S -e, unloading the compressor 1; when t W3 >t W3S At +e, loading the compressor 1; when t W3S -e≤t W3 ≤t W3S At +e, the operating capacity of the compressor 1 remains unchanged; unit setThe centralized controller module 15 cools the water outlet temperature t according to the water-cooled condenser 2 W6 The flow distribution proportion of the cooling water is controlled by a third control valve 16, and the inlet air wet bulb temperature t of the cooling tower WB The lower the water outlet temperature of the cooling tower 18, i.e. the lower the water inlet temperature t of the natural cooling heat exchanger module 13 W4 The lower the water cooled condenser 2 cools the water outlet temperature t W6 The lower the same; when t W6 <t W6S Gradually decreasing the flow of cooling water into the water-cooled condenser 2, i.e. gradually increasing the flow of cooling water into the free-cooling heat exchanger module 13, until t W6 ≥t W6S . At this time, as the flow rate of the cooling water entering the natural cooling heat exchanger module 13 increases, the heat exchange amount between the low-temperature cooling water and the chilled water in the natural cooling heat exchanger module 13 increases, i.e. the precooling capacity of the low-temperature cooling water to the chilled water increases, thereby reducing the chilled water inlet temperature t of the evaporator 4 W2 And finally, the refrigeration load of the water-cooling chiller module 5 and the operation power consumption of the compressor 1 are reduced, and the refrigeration energy efficiency of the unit is improved.
In particular, the natural cooling precooling mode, when t WB ≤t W3S -Δt 2 At Deltat 2 The compressor 1 stops running at 4-16 ℃, preferably 8 ℃, the first control valve 10 is powered off, the second control valve 14 is powered on, the cooling water pump 17 and the cooling tower 18 are in a running state, the low-temperature cooling water cooled by the cooling tower 18 is conveyed to the third control valve 16 by the cooling water pump 17, and then all or part of the cooling water flow enters the natural cooling heat exchanger module 13 through the third control valve 16 to cool the chilled water with relatively high temperature; chilled water entering the unit is conveyed to a second control valve 14 by a chilled water pump 9 after passing through a chilled water filter 8, then enters a natural cooling heat exchanger module 13 through a chilled water pipe 6, exchanges heat with low-temperature cooling water flowing from a cooling tower and having relatively low temperature in the natural cooling heat exchanger module 13, and the temperature of the chilled water cooled by the low-temperature cooling water is directly reduced to a target value t of the total chilled water temperature W3S E is 0.3 to 3 ℃, preferably 0.5 ℃; at the same time, the low-temperature cooling water absorbs the heat of the chilled water in the natural cooling heat exchanger module 13The temperature is increased after the measurement, then the heat is flowed to a water inlet of a cooling tower 18 through a cooling water pipe 7, the temperature of cooling water is reduced after the heat is discharged to outdoor low-temperature air in the cooling tower 18, and then the cooling water is conveyed to a natural cooling heat exchanger module 13 again through a third control valve 16 by a cooling water pump 17, and the circulation is repeated; the unit centralized controller module 15 is used for controlling the total water outlet temperature t according to the freezing W3 With a target value t W3S The running number and the running frequency of the cooling tower fans are controlled by the deviation of the cooling tower fans, and the total freezing water outlet temperature t is obtained W3 With the water inlet temperature t of the evaporator W2 Equal; when t W3 <t W3S E, gradually reducing the operation number and the operation frequency of each fan of the cooling tower 18 so as to reduce the cooling capacity of the outdoor air in the cooling tower 18 to the cooling water and improve the cooling water inlet temperature t of the natural cooling heat exchanger module 13 W4 Thereby reducing the heat exchange temperature difference and the heat exchange amount between the low-temperature cooling water and the chilled water in the natural cooling heat exchanger module 13, and improving the total chilled water outlet temperature t W3 The method comprises the steps of carrying out a first treatment on the surface of the Only 1 fan is operated at the lowest frequency and still satisfies t W3 <t W3S In condition-e, part of the low-temperature cooling water is bypassed to the water-cooled condenser 2 so as to reduce the flow rate of the low-temperature cooling water entering the natural cooling heat exchanger module 13, reduce the heat exchange amount between the low-temperature cooling water and the chilled water in the natural cooling heat exchanger module 13, namely reduce the cooling capacity of the low-temperature cooling water to the chilled water, thereby improving the total freezing water outlet temperature t W3 To make it and target value t W3S The deviation of (2) is controlled within the allowable deviation e; when t W3 >t W3S At +e, the flow rate of the low-temperature cooling water entering the natural cooling heat exchanger module 13 is gradually increased to improve the heat exchange amount between the low-temperature cooling water and the chilled water in the natural cooling heat exchanger module 13, namely the cooling capacity of the low-temperature cooling water to the chilled water is improved, thereby reducing the total freezing water outlet temperature t W3 To make it and target value t W3S The deviation of (2) is controlled within the allowable deviation e; after all the low-temperature cooling water conveyed by the cooling water pump 17 flows to the natural cooling heat exchanger module 13, if t is still satisfied W3 >t W3S In the +e condition, the number and frequency of the fans of the cooling tower 18 are gradually increased to increase the outdoor low temperature air pair in the cooling tower 18The cooling capacity of the cooling water reduces the cooling inlet water temperature t of the natural cooling heat exchanger module 13 W4 Thereby improving the heat exchange temperature difference and the heat exchange quantity between the low-temperature cooling water and the chilled water in the natural cooling heat exchanger module 13, and reducing the total chilled water outlet temperature t W3 The method comprises the steps of carrying out a first treatment on the surface of the To make it and target value t W3S The deviation of (2) is controlled within the allowable deviation e; when t W3S -e≤t W3 ≤t W3S +e, the number of fans of the cooling tower 18 and the operating frequency are kept unchanged, and simultaneously, the opening degrees from the interface a of the third control valve 16 to the interfaces b and c are kept unchanged.
On the basis of the common sense in the art, the above preferred conditions can be arbitrarily combined to obtain the preferred examples of the application.
The technical scheme has the following advantages or beneficial effects: the water cooling integrated water chilling unit integrates the water chilling unit, the cooling tower, the cooling water pump, the hydraulic module, the centralized control system and other equipment, the distance between the condenser of the water chilling unit and the cooling tower as well as between the condenser of the water chilling unit and the cooling water pump is short, the resistance of the cooling water system is small, and the power consumption of the cooling water pump can be saved by about 33%. Meanwhile, according to the energy-saving optimization control strategy, the on-off states, the running capacities and the running frequencies of compressors, chilled water pumps, cooling tower fans, and the on-off states and the running parameters of each electric two-way valve and each electric three-way valve under different outdoor air temperatures, chilled water temperature running working conditions and different air conditioner loading conditions can be intelligently controlled, the annual refrigerating energy efficiency of the unit is improved to the maximum extent, the system integration level is high, the system is functionally equivalent to an integral air conditioner cold collecting station, the installation, the running and the maintenance are convenient, and a special air conditioner room is not needed. In winter, the unit can directly utilize the low-temperature characteristic of the outdoor air to realize cooling of chilled water, and the compressor is not required to be started, so that the operation energy consumption can be greatly reduced, and the refrigeration energy efficiency of the unit is obviously improved. The water-cooling integrated water chilling unit is directly arranged outdoors, a special air conditioner room is omitted, and the construction cost can be further reduced. Of course, not all of the advantages described above are necessarily achieved at the same time by any one of the solutions of the application.
Drawings
In order to more clearly illustrate the embodiments of the present application or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below. It will be obvious to a person skilled in the art that other figures can be obtained from the figures provided without the inventive effort.
Fig. 1 is a schematic structural diagram of a water-cooling integrated chiller with a natural cooling function according to an embodiment of the present application.
Fig. 2 is a schematic diagram illustrating connection control of a centralized controller of a water-cooling integrated chiller with a natural cooling function according to an embodiment of the present application.
Wherein, 1-compressor; 2-a water-cooled condenser; 3-a throttle device; 4-an evaporator; 5-a water-cooling chiller module; 6-freezing water pipe; 7-cooling water pipes; 8-chilled water filter; 9-a chilled water pump; 10-a first control valve; 11-an expansion tank; 12-a freezing hydraulic module; 13-naturally cooling the heat exchanger module; 14-a second control valve; 15-a centralized controller module; 16-a third control valve; 17-a cooling water pump; 18-a cooling tower; 19-cooling the heat rejection module.
Detailed Description
The technical solutions in the embodiments of the present application are clearly and completely described below with reference to the accompanying drawings. It is obvious that the described embodiments are only some of the embodiments of the present application and are intended to explain the inventive concept. All other embodiments, which can be made by those skilled in the art based on the embodiments of the application without making any inventive effort, are intended to fall within the scope of the application.
The terms "first," "second," and the like, as used in the description, are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defining "a first" or "a second" may explicitly or implicitly include one or more such feature. The term "plurality" means two or more, unless specifically defined otherwise.
The terms "coupled," "connected," and the like as used in the description herein are to be construed broadly and may be, for example, fixedly coupled, detachably coupled, or integrally formed, unless otherwise specifically defined and limited; may be a mechanical connection, an electrical connection; can be directly connected and indirectly connected through an intermediate medium; may be a communication between two elements or an interaction between two elements. The specific meaning of the terms in the embodiments can be understood by those of ordinary skill in the art according to the specific circumstances.
The terms "one particular embodiment" and "one particular embodiment" as used in this description mean that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the application. In this specification, schematic representations of the above terms are not necessarily directed to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples. Furthermore, the different embodiments or examples described in this specification and the features of the different embodiments or examples may be combined and combined by those skilled in the art without contradiction.
Referring to fig. 1, a water-cooling integrated chiller with a natural cooling function is provided in an embodiment of the present application, which includes a water-cooling chiller module 5, a cooling heat rejection module 19, a freezing hydraulic module 12, a natural cooling heat exchanger module 13, and a centralized controller module 15 for sending control instructions to the above modules, where the water-cooling integrated chiller integrates the above modules into a whole, and the system integration is high, and is functionally completely equivalent to an integral air-conditioning cold-collecting station, so as to facilitate installation and maintenance. The water-cooling integrated water chilling unit is directly installed outdoors, thereby saving a special air conditioner room and further reducing the construction cost. The low temperature characteristic of the outdoor air can be directly utilized to cool the chilled water in winter, a compressor is not required to be started, the operation energy consumption can be greatly reduced, and the refrigeration energy efficiency of the unit is obviously improved.
The water-cooling chiller module 5 comprises a compressor 1, a water-cooling condenser 2, a throttling device 3 and an evaporator 4 which are sequentially connected and form a circulation loop. The compressor 1 may be a screw compressor, a scroll compressor or a centrifugal compressor, or other types of compressors. The throttling device 3 can adopt a thermal expansion valve, an electronic expansion valve or an electric butterfly valve, and other types of throttling valves. The chilled water power module 12 includes a chilled water filter 8, an expansion tank 11, a chilled water pump 9, a first control valve 10, and a second control valve 14. The outlet of the chilled water pump 9 is respectively connected with the chilled water inlets of the first control valve 10 and the second control valve 14 through the chilled water pipe 6; the freezing water outlet of the first control valve 10 is respectively connected with the freezing water inlet of the evaporator 4 and the freezing water outlet of the natural cooling heat exchanger module 13 through the freezing water pipe 6, and the freezing water outlet of the second control valve 14 is connected with the freezing water inlet of the natural cooling heat exchanger module 13 through the freezing water pipe 6. The first control valve 10 and the second control valve 14 can adopt a switch type electric two-way valve or a proportional type electric two-way valve, so that chilled water output by the chilled water pump 9 in different operation modes directly enters the evaporator 4 or enters the natural cooling heat exchanger module 13 first and then enters the evaporator 4.
The cooling heat rejection module 19 comprises a third control valve 16, a cooling water pump 17, a cooling tower 18. The third control valve 16 may be an electric three-way valve or two electric two-way valves leading to the water-cooled condenser 2 and the natural cooling heat exchanger module 13, respectively, to control the flow distribution ratio of the cooling water delivered by the cooling water pump 17 between the natural cooling heat exchanger module 13 and the water-cooled condenser 2. The cooling tower 18 may be an open cooling tower, a closed cooling tower, or other types of cooling towers.
Taking the electric three-way valve as an example of the third control valve 16, the inlet of the cooling water pump 17 is connected with the cooling water outlet at the bottom of the cooling tower 18 through the cooling water pipe 7, the interface a of the third control valve 16 is connected with the outlet of the cooling water pump 17 through the cooling water pipe 7, the interface c of the third control valve 16 is connected with the cooling water inlet of the water-cooled condenser 2 through the cooling water pipe 7, and the interface b of the third control valve 16 is connected with the cooling water inlet of the natural cooling heat exchanger module 13 through the cooling water pipe 7. The cooling water outlet of the water-cooled condenser 2 and the cooling water outlet of the natural cooling heat exchanger module 13 are connected to the top water inlet of the cooling tower 18 through the cooling water pipe 7.
The freezing water outlet of the freezing water pump 9 is provided with a temperature sensor, and the detected temperature is the total freezing water inlet temperature t W1 . The freezing water inlet and the freezing water outlet of the evaporator 4 are respectively provided with a temperature sensor, and the detected temperatures are the freezing water inlet temperature t of the evaporator 4 W2 Total water temperature t of freezing W3 . The cooling water inlet and the cooling water outlet of the natural cooling heat exchanger module 13 are respectively provided with a temperature sensor, and the detected temperatures are respectively the cooling water inlet temperature t of the natural cooling heat exchanger module 13 W4 Temperature t of cooling water W5 . The cooling water outlet of the water-cooled condenser 2 is provided with a temperature sensor, and the detected temperature is the cooling water outlet temperature t of the condenser 2 W6 . The air inlet side of the cooling tower 18 is provided with a dry bulb temperature sensor and a wet bulb temperature sensor, and the detected temperatures are respectively the air inlet dry bulb temperature t of the cooling tower 18 DB Wet bulb temperature of air intake t WB 。
When the total water outlet temperature t is frozen W3 With a target value t W3S When the deviation of (a) is less than or equal to e, e is 0.3-3 ℃, preferably 0.5 ℃, and the unit centralized controller module 15 is used for controlling the total water inlet temperature t according to the freezing W1 And total frozen water outlet temperature t W3 The temperature difference between the two controls the flow rate of the chilled water and the operating frequency of the chilled water pump. When the load of the tail end of the air conditioner is low, the total freezing water inlet temperature t W1 And total frozen water outlet temperature t W3 When the temperature difference between the two water flows is smaller than the set value a, the temperature a is 3-10 ℃, preferably 7 ℃, and the unit centralized controller module 15 controls the running frequency of the chilled water pump 9 to be reduced so as to reduce the chilled water flow and improve the total chilled water inlet temperature t W1 And total frozen water outlet temperature t W3 The temperature difference between the two, thereby reducing the operation power consumption of the chilled water pump 9. Conversely, when the end load of the air conditioner is higher, the total freezing water inlet temperature t W1 And total frozen water outlet temperature t W3 When the temperature difference between the two water flows is larger than the set value a, the unit centralized controller module 15 controls the operation frequency of the chilled water pump 9 to be increased so as to increase the chilled water flow and reduce the total chilled water inflowTemperature t W1 And total frozen water outlet temperature t W3 The temperature difference between the two components is suitable for the increase of the load of the air conditioner.
The unit centralized controller module 15 is used for controlling the temperature t of the wet bulb of the air inlet of the cooling tower WB And a target value t of the total water temperature of freezing W3S The running mode of the unit is controlled by the difference of the two types of the unit, and the unit has three running modes of mechanical refrigeration, natural cooling precooling, mechanical refrigeration recooling and natural cooling.
The first mode, mechanical refrigeration mode. When t WB ≥t W3S -Δt 1 At Deltat 1 At-3 to 9 ℃, preferably 3 ℃, the compressor 1 is operated, the first control valve 10 is electrified, the second control valve 14 is powered off, and the cooling water pump 17 and the cooling tower 18 are in an operating state. Chilled water entering the unit passes through a chilled water filter 8 and is then sequentially delivered by a chilled water pump 9 to a first control valve 10 and an evaporator 4, where the evaporator 4 exchanges heat with a relatively low temperature, low pressure refrigerant flowing from a restriction 3.
The low-temperature low-pressure gas refrigerant coming out of the evaporator 4 enters the compressor 1, is compressed into high-temperature high-pressure gas, then enters the water-cooled condenser 2, discharges a large amount of heat released in the condensation process to the cooling water to heat the cooling water, and is condensed into high-pressure liquid; then, the high-pressure liquid refrigerant enters the throttling device 3, throttled and depressurized into low-temperature low-pressure refrigerant, then enters the evaporator 4, absorbs the relatively high-temperature chilled water heat to cool the low-pressure refrigerant, evaporates into low-pressure gas, and then returns to the compressor 1 again to be compressed into high-temperature high-pressure gas, and thus the high-pressure refrigerant is repeatedly circulated.
The cooling water absorbs the condensation heat discharged by the high-temperature high-pressure refrigerant in the water-cooled condenser 2, then the temperature of the cooling water rises, the cooling water is led to the cooling tower 18 from the cooling water outlet of the water-cooled condenser 2 through the cooling water pipe 7, the cooling water temperature is reduced after the heat is discharged to the outdoor air in the cooling tower 18, and then the cooling water is conveyed to the third control valve 16 by the cooling water pump 17 and then enters the water-cooled condenser 2, and the circulation is repeated.
The unit centralized controller module 15 is used for controlling the temperature t of the cooling water outlet of the water-cooled condenser 2 W6 To control the cooling by the height of the water heaterThe number of fan operations and the frequency of operation of the tower 18. When t W6 <t W6S ,t W6S The fan operation number and operation frequency of the cooling tower 18 are gradually reduced for the lowest cooling water outlet temperature, the range is 20-30 ℃, and the preferable range is 25 ℃; if only 1 fan is operated at the lowest frequency, t is still satisfied W6 <t W6S Under the condition, the flow distribution proportion of the cooling water is controlled by the third control valve 16, the opening degree of the interface a to the interface c of the third control valve 16 is gradually reduced, and the opening degree of the interface a to the interface b is increased to reduce the flow rate of the cooling water entering the water-cooled condenser 2 until t W6 ≥t W6S During this process the flow of cooling water from the interface a of the third control valve 16 to the free cooling heat exchanger module 13 will gradually increase.
And in the second mode, the natural cooling precooling and mechanical refrigeration recooling modes are adopted. When t W3S -Δt 2 <t WB <t W3S -Δt 1 At Deltat 2 At 4-16 c, preferably 8 c, the compressor 1 is operated, the first control valve 10 is de-energized, the second control valve 14 is energized, and the cooling water pump 17 and cooling tower 18 are in operation. The low-temperature cooling water cooled by the cooling tower 18 is delivered to the third control valve 16 by the cooling water pump 17, and is split into two paths, wherein one path enters the water-cooled condenser 2 from the interface c of the third control valve 16 to absorb the condensation heat of the high-temperature high-pressure gas refrigerant, and the other path enters the natural cooling heat exchanger module 13 from the interface b of the third control valve 16 to precool the chilled water with relatively high temperature.
Chilled water entering the unit is conveyed to a second control valve 14 by a chilled water pump 9 after passing through a chilled water filter 8, then enters a natural cooling heat exchanger module 13 through a chilled water pipe 6, exchanges heat with low-temperature cooling water flowing from a cooling tower and having relatively low temperature in the natural cooling heat exchanger module 13, releases heat to the low-temperature cooling water, and after the low-temperature cooling water is precooled, the temperature of the chilled water is reduced, and then the chilled water continuously flows to the evaporator 4 through the chilled water pipe 6. At the same time, after the temperature of the low-temperature cooling water is increased by absorbing the heat of the chilled water in the natural cooling heat exchanger module 13, the low-temperature cooling water continuously flows to the water inlet of the cooling tower 18 through the cooling water pipe 7.
The low-temperature low-pressure gas refrigerant from the evaporator 4 enters the compressor 1, is compressed into high-temperature high-pressure gas, enters the water-cooled condenser 2, discharges a large amount of heat released in the condensation process to low-temperature cooling water to heat the low-temperature cooling water, and is condensed into high-pressure liquid; then, the high-pressure liquid refrigerant enters the throttling device 3, throttled and depressurized into low-temperature low-pressure refrigerant, then enters the evaporator 4, absorbs the heat of the chilled water precooled by the low-temperature cooling water, cools the chilled water again, evaporates into low-pressure gas, and then returns to the compressor 1 again to be compressed into high-temperature high-pressure gas, and the cycle is repeated. The temperature of the chilled water cooled again by the low-temperature low-pressure refrigerant is reduced to the target value t W3S Within the allowable deviation e of (2) and then leaves the unit from the refrigerated water outlet of the evaporator 4. The cooling water heated by the high-temperature and high-pressure refrigerant in the water-cooled condenser 2 increases in temperature, and then passes from the cooling water outlet of the water-cooled condenser 2 to the water inlet of the cooling tower 18 via the cooling water pipe 7.
The cooling water heated by the high-pressure refrigerant in the water-cooled condenser 2 and the cooling water heated by the chilled water in the natural cooling heat exchanger module 13 are collected by the cooling water pipe 7 and led to the cooling tower 18, the cooling water temperature is reduced after the heat is discharged to the outdoor air in the cooling tower 18, and then the cooling water is respectively conveyed to the water-cooled condenser 2 and the natural cooling heat exchanger module 13 by the cooling water pump 17 through the third control valve 16.
When the unit is operated in the natural cooling precooling plus mechanical refrigeration recooling mode, all fans of the cooling tower 18 and the cooling water pump 17 are at the highest frequency. Air inlet wet bulb temperature t of cooling tower WB The lower the natural cooling heat exchanger module 13 cools the incoming water temperature t W4 The lower the corresponding, the larger the heat exchange temperature difference and the heat exchange amount between the low-temperature cooling water and the chilled water in the natural cooling heat exchanger module 13, i.e. the larger the precooling amount of the low-temperature cooling water to the chilled water, the higher the chilled water inlet temperature t of the evaporator 4 W2 The lower it is, the lower it is from the frozen total outlet water temperature target value t W3S The smaller the deviation, the smaller the refrigeration load of the water-cooled chiller module 5 and the operation power consumption of the compressor 1, and the higher the refrigeration energy efficiency of the unit.
Unit centralized controller module 15 according to the total water outlet temperature t W3 And target value t W3S To control the operating capacity of the compressor 1. When t W3 <t W3S -e, unloading the compressor 1; when t W3 >t W3S At +e, loading the compressor 1; when t W3S -e≤t W3 ≤t W3S At +e, the operating capacity of the compressor 1 remains unchanged. The unit centralized controller module 15 cools the outlet water temperature t according to the water-cooled condenser 2 W6 To control the flow distribution of the third control valve 16. Air inlet wet bulb temperature t of cooling tower WB The lower the cooling tower outlet water temperature is, i.e. the cooling inlet water temperature t of the natural cooling heat exchanger module 13 is W4 The temperature is the same as the cooling inlet water temperature of the water-cooled condenser 2, and the cooling outlet water temperature t of the water-cooled condenser 2 W6 The lower the same; when t W6 <t W6S The opening degree of the interfaces a to c of the third control valve 16 is gradually reduced, namely the opening degree of the interfaces a to b is increased, so as to reduce the flow rate of the cooling water entering the water-cooled condenser 2 until t W6 ≥t W6S . At this time, as the flow rate of the cooling water entering the natural cooling heat exchanger module 13 increases, the heat exchange amount between the low-temperature cooling water and the chilled water in the natural cooling heat exchanger module 13 increases, i.e. the precooling capacity of the low-temperature cooling water to the chilled water increases, thereby reducing the chilled water inlet temperature t of the evaporator 4 W2 And finally, the refrigeration load of the water-cooling chiller module 5 and the operation power consumption of the compressor 1 are reduced, and the refrigeration energy efficiency of the unit is improved.
Third mode, natural cooling mode. When t WB ≤t W3S -Δt 2 When the compressor 1 is stopped, the first control valve 10 is powered off, the second control valve 14 is powered on, and the cooling water pump 17 and the cooling tower 18 are in operation. The low-temperature cooling water cooled by the cooling tower 18 is delivered to the third control valve 16 by the cooling water pump 17, and then all or part of the cooling water enters the natural cooling heat exchanger module 13 through the interface b of the third control valve 16 to cool the chilled water with relatively high temperature.
Chilled water entering the unit is conveyed to a second control valve 14 by a chilled water pump 9 after passing through a chilled water filter 8 and then cooledThe frozen water pipe 6 enters a natural cooling heat exchanger module 13, heat exchange is carried out between the natural cooling heat exchanger module 13 and low-temperature cooling water flowing from a cooling tower and having relatively low temperature, and the temperature of the frozen water cooled by the low-temperature cooling water is directly reduced to a target value t of the frozen total outlet water temperature W3S Within the allowable deviation e of (2) and then continues to flow to the evaporator 4. Since the compressor 1 is stopped, the refrigerant in the evaporator 4 is in a stagnant state, and heat exchange between the refrigerant and chilled water does not occur.
At the same time, the low-temperature cooling water is increased in temperature after absorbing the heat of the chilled water in the natural cooling heat exchanger module 13, then flows to the water inlet of the cooling tower 18 through the cooling water pipe 7, is reduced in temperature after discharging the heat to the outdoor low-temperature air in the cooling tower 18, and is then re-conveyed to the natural cooling heat exchanger module 13 through the third control valve 16 by the cooling water pump, thus repeatedly circulating.
The unit centralized controller module 15 is used for controlling the total water outlet temperature t according to the freezing W3 With a target value t W3S The running number and the running frequency of the cooling tower fans are controlled by the deviation of the cooling tower fans, and the total freezing water outlet temperature t is obtained W3 With the water inlet temperature t of the evaporator W2 Equal.
a. When t W3 <t W3S E, gradually reducing the operation number and the operation frequency of fans of the cooling tower 18 to reduce the cooling capacity of the outdoor air in the cooling tower 18 to the cooling water and improve the cooling water inlet temperature t of the natural cooling heat exchanger module 13 W4 Thereby reducing the heat exchange temperature difference and the heat exchange amount between the low-temperature cooling water and the chilled water in the natural cooling heat exchanger module 13, and improving the total chilled water outlet temperature t W3 The method comprises the steps of carrying out a first treatment on the surface of the Only 1 fan is operated at the lowest frequency and still satisfies t W3 <t W3S In the condition of-e, the opening from the electric three-way valve interface a to the interface c is gradually increased so as to bypass part of the low-temperature cooling water to the water-cooled condenser 2, reduce the flow rate of the low-temperature cooling water entering the natural cooling heat exchanger module 13, reduce the heat exchange amount between the low-temperature cooling water and the chilled water in the natural cooling heat exchanger module 13, namely reduce the cooling capacity of the low-temperature cooling water to the chilled water, and further improve the total freezing outlet water temperature t W3 To make it and target value t W3S The deviation of (2) is controlled within the allowable deviation e.
b. When t W3 >t W3S In +e, the opening from the electric three-way valve interface a to the interface c is gradually reduced, i.e. the opening from the electric three-way valve interface a to the interface b is gradually increased, so as to increase the flow of the low-temperature cooling water entering the natural cooling heat exchanger module 13, improve the heat exchange amount between the low-temperature cooling water and the chilled water in the natural cooling heat exchanger module 13, i.e. improve the cooling capacity of the low-temperature cooling water to the chilled water, and further reduce the total freezing outlet water temperature t W3 To make it and target value t W3S The deviation of (2) is controlled within the allowable deviation e. When the opening of the electric three-way valve from the interface a to the interface c is completely closed, that is, after all the low-temperature cooling water conveyed by the cooling water pump 17 flows to the natural cooling heat exchanger module 13, if t is still satisfied W3 >t W3S In the +e condition, the number and frequency of fans of the cooling tower 18 are gradually increased to increase the cooling capacity of the outdoor low-temperature air in the cooling tower 18 to the cooling water and reduce the cooling water inlet temperature t of the natural cooling heat exchanger module 13 W4 Thereby improving the heat exchange temperature difference and the heat exchange quantity between the low-temperature cooling water and the chilled water in the natural cooling heat exchanger module 13, and reducing the total chilled water outlet temperature t W3 The method comprises the steps of carrying out a first treatment on the surface of the To make it and target value t W3S The deviation of (2) is controlled within the allowable deviation e.
c. When t W3S -e≤t W3 ≤t W3S +e, the number of fans of the cooling tower 18 and the operating frequency are kept unchanged, and simultaneously, the opening degrees from the interface a of the third control valve 16 to the interfaces b and c are kept unchanged.
While embodiments of the present application have been illustrated and described above, it will be appreciated that the above described embodiments are illustrative and should not be construed as limiting the application. The present application is subject to various changes and modifications without departing from the spirit and scope thereof, and such changes and modifications fall within the scope of the application as hereinafter claimed.
Claims (10)
1. The utility model provides a take water-cooling integral type cooling water set of natural cooling function which characterized in that: the system comprises a water cooling chiller module (5), a freezing hydraulic power module (12), a natural cooling heat exchanger module (13), a cooling heat rejection module (19) and a centralized controller module (15) for sending control instructions to the modules; the water-cooling chiller module (5) comprises a compressor (1), a water-cooling condenser (2), a throttling device (3) and an evaporator (4) which are sequentially connected and form a circulation loop; the freezing hydraulic power module (12) comprises a freezing water filter (8), a freezing water pump (9), a first control valve (10) and a second control valve (14), wherein an outlet of the freezing water pump (9) is respectively connected with a freezing water inlet of the first control valve (10) and a freezing water inlet of the second control valve (14) through a freezing water pipe (6), a freezing water outlet of the first control valve (10) is respectively connected with a freezing water inlet of the evaporator (4) and a freezing water outlet of the natural cooling heat exchanger module (13) through the freezing water pipe (6), and a freezing water outlet of the second control valve (14) is connected with a freezing water inlet of the natural cooling heat exchanger module (13) through the freezing water pipe (6); the cooling heat rejection module (19) comprises a third control valve (16), a cooling water pump (17) and a cooling tower (18), wherein an inlet of the cooling water pump (17) is connected with a cooling water outlet at the bottom of the cooling tower (18) through a cooling water pipe (7), the third control valve (16) controls cooling water at an outlet of the cooling water pump (17) to flow to the water-cooled condenser (2) and/or the natural cooling heat exchanger module (13), and a cooling water outlet of the water-cooled condenser (2) and a cooling water outlet of the natural cooling heat exchanger module (13) are connected to a top water inlet of the cooling tower (18) through the cooling water pipe (7); the freezing water outlet of the freezing water pump (9), the freezing water inlet and the freezing water outlet of the evaporator (4), the cooling water inlet and the cooling water outlet of the natural cooling heat exchanger module (13), the cooling water outlet of the water cooling condenser (2) and the air inlet side of the cooling tower (18) are all provided with sensors; the centralized controller module (15) controls each fan, the first control valve (10), the second control valve (14), the third control valve (16) and the throttling device (3) of the compressor (1), the chilled water pump (9), the cooling water pump (17) and the cooling tower (18) according to data acquired by the sensors.
2. The water cooling integrated chiller with natural cooling function according to claim 1 and characterized in that: the compressor (1) is selected from a screw compressor, a scroll compressor, a centrifugal compressor or other type of compressor.
3. The water cooling integrated chiller with natural cooling function according to claim 1 and characterized in that: the throttling device (3) is selected from a thermal expansion valve, an electronic expansion valve, an electric butterfly valve or other types of throttling elements.
4. The water cooling integrated chiller with natural cooling function according to claim 1 and characterized in that: the first control valve (10) and the second control valve (14) are selected from a switch type electric two-way valve or a proportion type electric two-way valve so as to realize that chilled water output by the chilled water pump (9) in different operation modes directly enters the evaporator (4) or enters the natural cooling heat exchanger module (13) before entering the evaporator (4); or the freezing hydraulic module (12) further comprises an expansion tank (11).
5. The water cooling integrated chiller with natural cooling function according to claim 1 and characterized in that: the third control valve (16) adopts an electric three-way valve or two electric two-way valves which are respectively communicated with the water-cooling condenser (2) and the natural cooling heat exchanger module (13) so as to control the flow distribution proportion of the cooling water conveyed by the cooling water pump (17) between the natural cooling heat exchanger module (13) and the water-cooling condenser (2).
6. The water cooling integrated chiller with natural cooling function according to claim 1 and characterized in that: the cooling tower (18) is selected from an open cooling tower, a closed cooling tower or other types of cooling towers.
7. A control method of a water-cooling integrated chiller with a natural cooling function, wherein the water-cooling integrated chiller is selected from any one of claims 1 to 6, and is characterized in that: the centralized controller module (15) is used for controlling the temperature t of the inlet air wet bulb of the cooling tower WB And a target value t of the total water temperature of freezing W3S The difference of the (2) is used for controlling the operation mode of the unit, wherein the unit comprises a mechanical refrigeration mode, natural cooling precooling and mechanical operationCooling sub-cooling mode, natural cooling mode.
8. The control method of the water-cooling integrated chiller with the natural cooling function according to claim 7, wherein the control method comprises the following steps: the mechanical refrigeration mode, when t WB ≥t W3S -Δt 1 At Deltat 1 The compressor (1) is operated at the temperature of-3 ℃ to 9 ℃, preferably 3 ℃, the first control valve (10) is electrified, the second control valve (14) is powered off, and the cooling water pump (17) and the cooling tower (18) are in an operating state; chilled water entering the unit passes through a chilled water filter (8) and is sequentially conveyed to a first control valve (10) and an evaporator (4) by a chilled water pump (9), and heat exchange is carried out between the chilled water and low-temperature low-pressure refrigerant which is relatively low in temperature and flows from a throttling device (3) in the evaporator (4);
The low-temperature low-pressure gas refrigerant coming out of the evaporator (4) enters the compressor (1), is compressed into high-temperature high-pressure gas, then enters the water-cooled condenser (2), discharges a large amount of heat released in the condensation process to the cooling water to heat the cooling water, and is condensed into high-pressure liquid; then, the high-pressure liquid refrigerant enters a throttling device (3), throttled and depressurized into low-temperature low-pressure refrigerant, then enters an evaporator (4), absorbs relatively high-temperature chilled water heat to cool the low-pressure refrigerant, evaporates into low-pressure gas, then returns to a compressor (1) again to be compressed into high-temperature high-pressure gas, and repeatedly circulates in this way;
the cooling water absorbs condensation heat discharged by the high-temperature high-pressure refrigerant in the water-cooling condenser (2) and then rises in temperature, then is led to the cooling tower (18) from a cooling water outlet of the water-cooling condenser (2) through the cooling water pipe (7), discharges heat to outdoor air in the cooling tower (18) and then reduces in cooling water temperature, and then is conveyed to the third control valve (16) by the cooling water pump (17) and then enters the water-cooling condenser (2), and the circulation is repeated;
the unit centralized controller module (15) cools the outlet water temperature t according to the water-cooled condenser (2) W6 To control the number and frequency of fan operations of the cooling tower (18), when t W6 <t W6S At time t W6S The minimum cooling water outlet temperature is 20-30 ℃, preferably 25 ℃,gradually reducing the number and frequency of fan operations of the cooling tower (18); if only 1 fan is operated at the lowest frequency, t is still satisfied W6 <t W6S If the conditions are that the flow distribution proportion of the cooling water is controlled by a third control valve (16), the flow of the cooling water entering the water-cooled condenser (2) is gradually reduced, namely the flow of the cooling water entering the natural cooling heat exchanger module (13) is gradually increased until t W6 ≥t W6S 。
9. The control method of the water-cooling integrated chiller with the natural cooling function according to claim 7, wherein the control method comprises the following steps: the unit is in a natural cooling precooling and mechanical refrigeration sub-cooling mode, when t W3S -Δt 2 <t WB <t W3S -Δt 1 At Deltat 1 At a temperature of-3 to 9 ℃, preferably 3 ℃, Δt 2 The compressor (1) is operated at 4-16 ℃, preferably 8 ℃, the first control valve (10) is powered off, the second control valve (14) is powered on, and the cooling water pump (17) and the cooling tower (18) are in an operating state; the low-temperature cooling water cooled by the cooling tower (18) is conveyed to a third control valve (16) by a cooling water pump (17), and then is split into two paths, wherein one path enters a water-cooling condenser (2) to absorb the condensation heat of high-temperature high-pressure gas refrigerant, and the other path enters a natural cooling heat exchanger module (13) to precool chilled water with relatively high temperature;
The chilled water entering the unit is conveyed to a second control valve (14) by a chilled water pump (9) after passing through a chilled water filter (8), then enters a natural cooling heat exchanger module (13) by a chilled water pipe (6), exchanges heat with low-temperature cooling water flowing from a cooling tower and having relatively low temperature in the natural cooling heat exchanger module (13), releases heat to the low-temperature cooling water, the temperature of the chilled water is reduced after the low-temperature cooling water is precooled by the low-temperature cooling water, the chilled water continuously flows to an evaporator (4) by the chilled water pipe (6), and the low-temperature cooling water continuously flows to a water inlet of a cooling tower (18) by a cooling water pipe (7) after the heat temperature of the chilled water absorbed by the low-temperature cooling water in the natural cooling heat exchanger module (13) is increased; the low-temperature low-pressure gas refrigerant coming out of the evaporator (4) enters the compressor (1), is compressed into high-temperature high-pressure gas, then enters the water-cooled condenser (2), discharges a large amount of heat released in the condensation process to low-temperature cooling water to heat the low-temperature cooling water, and is condensed into high-pressure liquid; then, the high-pressure liquid refrigerant enters a throttling device (3), is throttled and depressurized into low-temperature low-pressure refrigerant, then enters an evaporator (4), absorbs heat of chilled water precooled by low-temperature cooling water, cools the chilled water again, evaporates into low-pressure gas, and then returns to a compressor (1) again to be compressed into high-temperature high-pressure gas, and thus the circulation is repeated;
The chilled water temperature after being cooled again by the low-temperature low-pressure refrigerant is reduced to its target value t W3S E is 0.3-3 ℃, preferably 0.5 ℃, after which it leaves the unit from the refrigerated water outlet of the evaporator (4); cooling water heated by high-temperature high-pressure refrigerant in the water-cooled condenser (2) and cooling water heated by chilled water in the natural cooling heat exchanger module (13) are collected through the cooling water pipe (7) and then led to a water inlet of the cooling tower (18), heat is discharged to outdoor air in the cooling tower (18) and then the cooling water temperature is reduced, and then the cooling water is respectively conveyed to the water-cooled condenser (2) and the natural cooling heat exchanger module (13) through the third control valve (16) by the cooling water pump (17);
when the unit operates in a natural cooling precooling mode and a mechanical refrigeration recooling mode, all fans of a cooling tower (18) and a cooling water pump (17) are at the highest frequency, and the inlet air wet bulb temperature t of the cooling tower WB The lower the temperature t of the cooling water of the natural cooling heat exchanger module (13) W4 Correspondingly, the lower the temperature difference and the heat exchange amount between the low-temperature cooling water and the chilled water in the natural cooling heat exchanger module (13) are, namely the larger the precooling amount of the low-temperature cooling water to the chilled water is, the freezing water inlet temperature t of the evaporator (4) is W2 The lower the total water outlet temperature target value t W3S The smaller the deviation is, the smaller the refrigeration load of the water-cooling chiller module (5) and the running power consumption of the compressor (1) are, and the higher the refrigerating energy efficiency of the unit is;
the unit centralized controller module (15) is used for controlling the total water outlet temperature t according to the freezing W3 With a target value t W3S To control the operating capacity of the compressor (1), when t W3 <t W3S -e, unloading the compressor (1); when t W3 >t W3S When +e, loading the compressor (1); when t W3S -e≤t W3 ≤t W3S At +e, the operating capacity of the compressor (1) remains unchanged;
the unit centralized controller module (15) cools the outlet water temperature t according to the water-cooled condenser (2) W6 The flow distribution proportion of the cooling water is controlled by a third control valve (16), and the inlet air wet bulb temperature t of the cooling tower WB The lower the water outlet temperature of the cooling tower (18) is, namely the lower the water inlet temperature t of the natural cooling heat exchanger module (13) W4 The lower the water cooling condenser (2) cools the outlet water temperature t W6 The lower the same; when t W6 <t W6S Gradually reducing the flow of cooling water into the water-cooled condenser (2), i.e. gradually increasing the flow of cooling water into the natural cooling heat exchanger module (13) until t W6 ≥t W6S The method comprises the steps of carrying out a first treatment on the surface of the At the moment, with the increase of the flow of the cooling water entering the natural cooling heat exchanger module (13), the heat exchange amount between the low-temperature cooling water and the chilled water in the natural cooling heat exchanger module (13) is increased, namely the precooling capacity of the low-temperature cooling water to the chilled water is improved, thereby reducing the chilled water inlet temperature t of the evaporator (4) W2 And finally, the refrigeration load of the water-cooling chiller module (5) and the operation power consumption of the compressor (1) are reduced, and the refrigeration energy efficiency of the unit is improved.
10. The control method of the water-cooling integrated chiller with the natural cooling function according to claim 7, wherein the control method comprises the following steps: the natural cooling precooling mode is as t WB ≤t W3S -Δt 2 At Deltat 2 The compressor (1) stops running at 4-16 ℃, preferably 8 ℃, the first control valve (10) is powered off, the second control valve (14) is powered on, the cooling water pump (17) and the cooling tower (18) are in a running state, low-temperature cooling water cooled by the cooling tower (18) is conveyed to the third control valve (16) by the cooling water pump (17), and then all or part of the cooling water enters the natural cooling heat exchanger module (13) through the third control valve (16) to cool and cool relatively high-temperature chilled water;
chilled water entering the unit is filtered by a chilled water filter (8) and then is pumped by a chilled water pump (9)Is conveyed to a second control valve (14), then enters a natural cooling heat exchanger module (13) through a freezing water pipe (6), exchanges heat with low-temperature cooling water flowing from a cooling tower and having relatively low temperature in the natural cooling heat exchanger module (13), and the temperature of the freezing water cooled by the low-temperature cooling water is directly reduced to a target value t of the total freezing water outlet temperature W3S E is 0.3 to 3 ℃, preferably 0.5 ℃;
simultaneously, the temperature of the low-temperature cooling water is increased after the low-temperature cooling water absorbs the heat of the chilled water in the natural cooling heat exchanger module (13), then the low-temperature cooling water flows to the water inlet of the cooling tower (18) through the cooling water pipe (7), the temperature of the cooling water is reduced after the heat is discharged to the outdoor low-temperature air in the cooling tower (18), and then the cooling water is conveyed to the natural cooling heat exchanger module (13) again through the third control valve (16) by the cooling water pump (17), and the cooling water is repeatedly circulated in the same way;
the unit centralized controller module (15) is used for controlling the total water outlet temperature t according to the freezing W3 With a target value t W3S The running number and the running frequency of the cooling tower fans are controlled by the deviation of the cooling tower fans, and the total freezing water outlet temperature t is obtained W3 With the freezing water inlet temperature t of the evaporator (4) W2 Equal;
when t W3 <t W3S E, gradually reducing the operation number and the operation frequency of each fan of the cooling tower (18) so as to reduce the cooling capacity of outdoor air in the cooling tower (18) to cooling water and improve the cooling water inlet temperature t of the natural cooling heat exchanger module (13) W4 Thereby reducing the heat exchange temperature difference and the heat exchange quantity between the low-temperature cooling water and the chilled water in the natural cooling heat exchanger module (13) and further improving the total chilled water outlet temperature t W3 The method comprises the steps of carrying out a first treatment on the surface of the Only 1 fan is operated at the lowest frequency and still satisfies t W3 <t W3S In the condition of E, part of low-temperature cooling water is bypassed and flows to the water-cooling condenser (2) so as to reduce the flow rate of the low-temperature cooling water entering the natural cooling heat exchanger module (13), reduce the heat exchange amount between the low-temperature cooling water and the chilled water in the natural cooling heat exchanger module (13), namely reduce the cooling capacity of the low-temperature cooling water to the chilled water, thereby improving the total chilled water outlet temperature t W3 To make it and target value t W3S The deviation of (2) is controlled within the allowable deviation e;
when t W3 >t W3S In +e, the low-temperature cooling water flow entering the natural cooling heat exchanger module (13) is gradually increased, so that the heat exchange amount between the low-temperature cooling water and the chilled water in the natural cooling heat exchanger module (13) can be improved, namely the cooling capacity of the low-temperature cooling water to the chilled water is improved, and the total freezing water outlet temperature t is reduced W3 To make it and target value t W3S The deviation of (2) is controlled within the allowable deviation e; after all low-temperature cooling water conveyed by the cooling water pump (17) flows to the natural cooling heat exchanger module (13), if t is still satisfied W3 >t W3S In the +e condition, the operation number and the operation frequency of each fan of the cooling tower (18) are gradually increased so as to improve the cooling capacity of outdoor low-temperature air in the cooling tower (18) to cooling water and reduce the cooling water inlet temperature t of the natural cooling heat exchanger module (13) W4 Thereby improving the heat exchange temperature difference and the heat exchange quantity between the low-temperature cooling water and the chilled water in the natural cooling heat exchanger module (13) so as to reduce the total chilled water outlet temperature t W3 The method comprises the steps of carrying out a first treatment on the surface of the To make it and target value t W3S The deviation of (2) is controlled within the allowable deviation e; when t W3S -e≤t W3 ≤t W3S +e, the running number and the running frequency of fans of the cooling tower (18) are kept unchanged, and meanwhile, the opening degrees from an interface a to an interface b and an interface c of the third control valve (16) are respectively kept unchanged.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202311011731.1A CN117006560B (en) | 2023-08-11 | 2023-08-11 | Water-cooling integrated water chilling unit with natural cooling function and control method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202311011731.1A CN117006560B (en) | 2023-08-11 | 2023-08-11 | Water-cooling integrated water chilling unit with natural cooling function and control method |
Publications (2)
Publication Number | Publication Date |
---|---|
CN117006560A true CN117006560A (en) | 2023-11-07 |
CN117006560B CN117006560B (en) | 2024-06-07 |
Family
ID=88575955
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202311011731.1A Active CN117006560B (en) | 2023-08-11 | 2023-08-11 | Water-cooling integrated water chilling unit with natural cooling function and control method |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN117006560B (en) |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101650056A (en) * | 2009-09-09 | 2010-02-17 | 北京康孚环境控制有限公司 | Combined cold supply system of cooling towers and water cooling unit and control method thereof |
CN104776731A (en) * | 2015-03-31 | 2015-07-15 | 清华大学 | System and method for freezing resistance of cooling tower in winter by utilizing indirect evaporative cooling |
CN106032919A (en) * | 2015-03-13 | 2016-10-19 | 阿里巴巴集团控股有限公司 | Chilled-water cooling system |
CN206055810U (en) * | 2016-09-30 | 2017-03-29 | 安徽中烟工业有限责任公司 | A kind of United system of air-conditioning |
CN111565543A (en) * | 2020-05-11 | 2020-08-21 | 葛洲坝节能科技有限公司 | Water-cooling natural cooling refrigerant direct cooling refrigeration system |
CN112628899A (en) * | 2021-01-06 | 2021-04-09 | 山东通想智能科技有限公司 | Multi-cold source conversion device for data machine room and control method |
CN116007078A (en) * | 2021-10-21 | 2023-04-25 | 中国移动通信集团设计院有限公司 | Method, device and equipment for acquiring operation parameters of refrigeration system |
CN220601671U (en) * | 2023-08-11 | 2024-03-15 | 浙江国祥股份有限公司 | Water-cooling integrated water chilling unit with natural cooling function |
-
2023
- 2023-08-11 CN CN202311011731.1A patent/CN117006560B/en active Active
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101650056A (en) * | 2009-09-09 | 2010-02-17 | 北京康孚环境控制有限公司 | Combined cold supply system of cooling towers and water cooling unit and control method thereof |
CN106032919A (en) * | 2015-03-13 | 2016-10-19 | 阿里巴巴集团控股有限公司 | Chilled-water cooling system |
CN104776731A (en) * | 2015-03-31 | 2015-07-15 | 清华大学 | System and method for freezing resistance of cooling tower in winter by utilizing indirect evaporative cooling |
CN206055810U (en) * | 2016-09-30 | 2017-03-29 | 安徽中烟工业有限责任公司 | A kind of United system of air-conditioning |
CN111565543A (en) * | 2020-05-11 | 2020-08-21 | 葛洲坝节能科技有限公司 | Water-cooling natural cooling refrigerant direct cooling refrigeration system |
CN112628899A (en) * | 2021-01-06 | 2021-04-09 | 山东通想智能科技有限公司 | Multi-cold source conversion device for data machine room and control method |
CN116007078A (en) * | 2021-10-21 | 2023-04-25 | 中国移动通信集团设计院有限公司 | Method, device and equipment for acquiring operation parameters of refrigeration system |
CN220601671U (en) * | 2023-08-11 | 2024-03-15 | 浙江国祥股份有限公司 | Water-cooling integrated water chilling unit with natural cooling function |
Also Published As
Publication number | Publication date |
---|---|
CN117006560B (en) | 2024-06-07 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN107014016B (en) | Fluorine pump natural cooling evaporation type condensation water chiller and control method thereof | |
CN100552312C (en) | The air-conditioning unit device and the air-treatment method thereof of the wet segment processing of heat | |
CN107014014B (en) | Heat pipe natural cooling evaporation type condensation water chiller and control method thereof | |
CN103175276A (en) | Air-cooling direct-current frequency-conversion magnetic levitation nature cold source water chilling unit | |
CN107166582B (en) | air conditioner cooling water system, air conditioner system and air conditioner cooling water system control method | |
CN220601671U (en) | Water-cooling integrated water chilling unit with natural cooling function | |
CN107906785A (en) | A kind of low temperature natural coldness resource utilizing system and method | |
CN113446756A (en) | Four-pipe air source heat pump unit with variable-speed compressor | |
CN115289714A (en) | Evaporation condensation heat pump unit with hydraulic module and control method thereof | |
CN203323266U (en) | Air-cooling direct-current variable-frequency magnetic-levitation water chilling unit with natural cold source | |
CN117803997A (en) | Dehumidifier unit with low dew point exceeding zero depth intelligent cleaning and control method | |
CN217900220U (en) | Evaporation condensation heat pump unit with hydraulic module | |
CN115235052B (en) | Automatic adjusting control system of water chiller | |
CN217685941U (en) | Double-working-condition water chilling unit | |
CN207936542U (en) | A kind of low temperature natural coldness resource utilizing system | |
CN117006560B (en) | Water-cooling integrated water chilling unit with natural cooling function and control method | |
CN215529686U (en) | Cold water type cold station system | |
CN211854312U (en) | High-efficient evaporation cooling formula cooling water set | |
CN114198872B (en) | Machine room air conditioner, operation control method and device of machine room air conditioner | |
CN115143658A (en) | Double-working-condition water chilling unit and control method thereof | |
CN212109083U (en) | Air conditioning system | |
CN109210814B (en) | Multifunctional refrigerating system | |
CN112665053A (en) | Cooling system | |
CN221258977U (en) | Double-evaporation central air conditioner with natural cooling function | |
CN216048475U (en) | Four-pipe air source heat pump unit with variable-speed compressor |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant |