CN203533948U - Compound type evaporative type cooling device having natural cooling function and used for large-scale device - Google Patents
Compound type evaporative type cooling device having natural cooling function and used for large-scale device Download PDFInfo
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- CN203533948U CN203533948U CN201320667454.5U CN201320667454U CN203533948U CN 203533948 U CN203533948 U CN 203533948U CN 201320667454 U CN201320667454 U CN 201320667454U CN 203533948 U CN203533948 U CN 203533948U
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Abstract
The utility model discloses a compound type evaporative type cooling device having a natural cooling function and used for a large-scale device. The cooling device comprises a refrigeration compressor (1), a condenser (2), a dry filter (3), a refrigerant fluid pipeline electromagnetic valve (4), an expansion valve (5), a gas-liquid separation and recooling device (7), a refrigerant circulating pump (8) and a three-way control valve (12). The gas-liquid separation and recooling device (7) can be communicated with the refrigeration compressor (1) and the condenser (2) and can also be communicated with an outside natural cold source. According to the compound type evaporative type cooling device having the natural cooling function and used for the large-scale device, Freon is used as liquid refrigerants, the state of the refrigerants is converted through steam compression refrigeration cycle or natural cooling cycle, the working efficiency of a refrigeration device is improved, energy is saved, consumption is reduced, and the operation range of natural cooling refrigeration is expanded. The compound type evaporative type cooling device is simple in structure, convenient to use and capable of improving the safety of the large device and saving power consumption by more than 20%.
Description
Technical field
The utility model relates to the cooling of main equipment in the industrial circles such as computer equipment, data center and petrochemical industry and food pharmaceutical, specifically a kind of compound cooling evaporative cooler with natural cooling function for main equipment that adopts liquid cools.
Background technology
Modern large-scale computer center and data center, because electric energy in data handling procedure finally can be converted into heat energy, if this part heat energy can not be managed in time by its elimination, will cause computer equipment excess Temperature, thereby cause computer run Speed Reduction, fault rate increases, and even delays machine fault and loses critical data.Therefore, all mainframe computer center and data center, all need a kind of special refrigerating plant to be used for for computer equipment provides continual cooling service in long-term 24 hours, to guarantee that computer equipment moves reliably.
The cooling of active computer equipment is generally divided into two types: (1) Luftgekuhlte rotierende, and refrigerating plant reduces air themperature, and the air of low temperature is transported to the computer equipment of heating by blower fan, take away heat, keeps the temperature of computer.And the air that has absorbed the rising of computer craze amount temperature is got back to refrigerating plant by cooling again; (2) liquid cools type, refrigerating plant reduces a kind of temperature of liquid, and the liquid of low temperature is transported to the computer equipment of heating by pump, take away heat, keeps the temperature of computer.And the liquid that has absorbed the rising of computer craze amount temperature is got back to refrigerating plant by cooling again.Because the disposal ability of computer is more and more stronger, the power of processor is increasing, and the volume of electronic devices and components is more and more less, that is to say, under same volume, the power density of computer is more and more higher.In this case, because the thermal capacity of air is lower, it is the air of same volume flow, the heat that its heat that can carry can carry far below liquid, and therefore the capacity of heat transmission of air is also far below liquid,, computer equipment for high power density, the computer cooling device of above-mentioned the first Luftgekuhlte rotierende, can not be well for computer equipment provides cooling service, and large-scale computer equipment more and more adopts the device of liquid cools type.
In the computer equipment of liquid cools type, conventionally surface-mounted integrated circuit is arranged on a cooling base above, in the inside of cooling base, have the complicated microchannel for cooling liquid flow.The cooling liquid that temperature is lower flows into from the entrance of cooling base, from outlet, flows out.Cooling liquid in microchannel in mobile process, the heat that on surface-mounted integrated circuit, electronic device distributes, heat by cooling base passes to cooling liquid mobile in microchannel, therefore the heat that cooling liquid distributes surface-mounted integrated circuit is taken computer out of, and this part heat is eliminated by the mode of refrigeration by the refrigeration plant of computer outside again.Each large-scale computer equipment can be comprised of a lot of surface-mounted integrated circuits, therefore, in computer equipment, has accordingly each cooling base that is assigned to of cooling liquid, and the device that the cooling liquid being flowed out by each cooling base is pooled together.
At present to adopt the typical way of liquid cools type be the system of water cooling type to mass computing machine equipment, it is a kind of refrigeration plant that is called handpiece Water Chilling Units, the temperature of water is reduced, become the chilled water that temperature is lower, chilled water is transported to by delivery pump in the cooling base of computer equipment, to computer equipment, carries out cooling.After water absorbs heat, temperature rising is got back in handpiece Water Chilling Units, again, by handpiece Water Chilling Units equipment refrigeration cool-down, becomes the chilled water that temperature is lower.Use freezing water-cooled process for computing equipment, bring following deficiency or even potential danger: (1) water circulation time in computer equipment, the possibility of exist leaking all the time, once and water leaks, electric short circuit will cause catastrophic consequence.This is all unaffordable disasters of any one large-scale computer center or data center.And no matter take which kind of precautionary measures, this hidden danger all exists all the time.(2) water is only the medium that a kind of heat transmits between refrigerating plant and computer equipment, and refrigerating plant first will reduce the temperature of water by the circulation of cold-producing medium, then allows water be recycled in computer equipment, to absorb heat.Therefore,, in refrigerating plant, there is the cold-producing medium of refrigerating efficiency and the secondary heat exchange process of water of reducing in so cooling transfer process, for the efficiency that improves computer equipment and data center, is not a good approach.
According to the law of thermodynamics, heat circulating refrigerator always needs to input the process that certain energy could drive refrigeration, for example, the refrigeration system of steam compression cycle, it has comprised refrigeration compressor, evaporimeter, condenser, heating power expansion valve etc.No matter be summer or winter, refrigeration compressor all needs to consume electric energy, just can complete to cold-producing medium compress, the process of condensation, expansion and evaporation.In the high latitude area of the earth, the environment temperature in winter is lower, even lower than the running temperature of computer equipment.In this lower area of class winter environment temperature, in fact exist and can make full use of the chance that low temperature environment resource is freezed, be i.e. the said free cooling refrigeration technology of the utility model.If under low temperature environment, reduce and even do not use conventional thermodynamic cycle refrigeration in the winter time, will greatly reduce the electric power of the required consumption of year round cooling.
Summary of the invention
The purpose of this utility model is the problem existing for prior art, and it is liquid refrigerant the compound cooling evaporative cooler with natural cooling function for main equipment that can utilize natural environment that a kind of freon that adopts is provided.
The purpose of this utility model solves by the following technical programs:
A kind of compound cooling evaporative cooler with natural cooling function for main equipment, comprise refrigeration compressor, condenser, device for drying and filtering, refrigerant liquid pipeline electromagnetic valve, expansion valve, gas-liquid separation and recooler, refrigerant circulation pump and three-way control valve, it is characterized in that described gas-liquid separation is connected with the air entry on refrigeration compressor by pipeline with the gas refrigerant outlet on recooler, exhaust outlet on refrigeration compressor is connected with the refrigerant inlet on condenser by pipeline, refrigerant outlet on condenser by pipeline successively with device for drying and filtering, refrigerant liquid pipeline electromagnetic valve, expansion valve is connected, the outlet of expansion valve is connected with the gas-liquid mixed refrigerant import on recooler with gas-liquid separation by pipeline, gas-liquid separation is connected with refrigerant circulation pump by pipeline with the liquid refrigerant outlet on recooler, refrigerant circulation delivery side of pump end is connected with the entrance of liquid refrigerant collector by pipeline, the outlet of liquid refrigerant collector is connected with the entrance of cooling base, the outlet of cooling base is connected with the entrance of gas refrigerant collector, the outlet of gas refrigerant collector is connected with the gas refrigerant import on recooler with gas-liquid separation, cooling medium inlet place on described condenser is provided with cooling medium pipe, cooling medium pipe is provided with three-way control valve and temperature-detecting device, temperature-detecting device is positioned on the cooling medium pipe at entry port place of three-way control valve, the discharge port of three-way control valve is connected with the cooling medium inlet on recooler with gas-liquid separation by cooling medium pipe, gas-liquid separation and cooling medium outlet on recooler by cooling medium pipe, be connected with cooling medium inlet on condenser and condenser on cooling medium inlet by cooling medium pipe, be connected with the bypass port of three-way control valve.
Coolant interface on described refrigeration compressor is connected with the pipeline between the port of export of device for drying and filtering and the entrance point of refrigerant liquid pipeline electromagnetic valve by pipeline, and the pipeline at the coolant interface place of refrigeration compressor is provided with cooling electric magnet valve.
Described gas-liquid separation and recooler comprise the first end cap, the first tube end sheet, condensing heat-exchanging pipe, housing, liquid barrier, the second tube end sheet, the second end cap and cold heat exchanger tube again, the two ends of housing are respectively equipped with the first tube end sheet and the second tube end sheet, the outside of the first tube end sheet and the second tube end sheet is respectively equipped with the first end cap and the second end cap for sealing, the two ends of condensing heat-exchanging pipe and colder heat exchanger tube are separately positioned in the first tube end sheet and the second tube end sheet and condensing heat-exchanging pipe is positioned at the top of cold heat exchanger tube again, and liquid barrier is positioned at the top of condensing heat-exchanging pipe.
The first described end cap and the second end cap form cooling medium chamber with the first tube end sheet and the second tube end sheet respectively, this cooling medium chamber all with condensing heat-exchanging pipe and colder heat exchanger tube be connected and the first end cap or the second end cap are provided with the cooling medium being connected with cooling medium chamber and export and cooling medium inlet; Described gas refrigerant outlet, gas-liquid mixed refrigerant import, liquid refrigerant outlet and gas refrigerant import are all arranged on housing, and gas refrigerant outlet, gas-liquid mixed refrigerant import, liquid refrigerant outlet and gas refrigerant import are all connected with the annular seal space that housing and the first tube end sheet, the second tube end sheet form.
In described cooling medium chamber, be provided with dividing plate, cooling medium outlet and cooling medium inlet are separately positioned on first end cap or the second end cap of dividing plate upside and downside.
In described gas-liquid separation and recooler, be provided with spray thrower, top and spray thrower that spray thrower is arranged on liquid barrier are connected with shower by the spray interface on housing, the other end of shower is connected with the pipeline in liquid refrigerant exit and shower is provided with spray pump and spray control valve, and spray control valve is on the shower between spray pump and spray interface.
Described gas-liquid separation and recooler place are provided with pressure sensor, and pressure sensor is arranged on gas-liquid separation with on recooler or be communicated with on the pipeline of gas-liquid separation and recooler and refrigeration compressor.
Described gas-liquid separation and recooler are provided with liquid level sensor.
Described refrigeration compressor adopts magnetic suspension without oily centrifugal compressor, and described refrigeration compressor place is provided with load balance valve, and balanced valve is connected with exhaust outlet and the air entry of refrigeration compressor respectively.
Described liquid refrigerant outlet and the pipeline between refrigerant circulation pump are provided with liquid refrigerant current-sharing pipe, pipeline between refrigerant circulation pump and liquid refrigerant collector is provided with liquid refrigerant distributing manifold, and the pipeline between gas refrigerant collector and gas refrigerant import is provided with gas refrigerant return-air manifold trunk; The import department of described cooling medium pipe is provided with cooling medium upstream end manifold trunk, and the pipeline in the cooling medium exit on condenser is connected with cooling medium outlet side manifold trunk.
Utility model has the following advantages compared to existing technology:
The utility model passes through refrigeration compressor, condenser, device for drying and filtering, refrigerant liquid pipeline electromagnetic valve, expansion valve, gas-liquid separation and recooler, refrigerant circulation pump and three-way control valve form the foundation structure of a compound cooling evaporative cooler, adopt freon as liquid refrigerant, liquid refrigerant is transported in the middle of the cooling base of main equipment, in the microchannel of cooling base, liquid refrigerant absorbs the heat that main equipment distributes, evaporation becomes gaseous state, the cold-producing medium of gaseous state is got back in refrigerating plant, by vapor-compression refrigerant cycle or natural cool cycles, again become liquid refrigerant, be transported to again in main equipment, because freon refrigerant is that nonconducting medium and the boiling point under an atmospheric pressure are far below normal temperature, therefore as the leakage that freon occurs freon can flash to rapidly gas, and can not cause the electric short circuit of main equipment, can not there is the loss of catastrophic accident and critical data, cold-producing medium is the working media of vapor-compression refrigerant cycle in addition, also be the medium of Cooling calculation machine equipment simultaneously, therefore in whole cool cycles process, do not need as the type of cooling of chilled water, secondary heat exchange to be between cooling device and computer equipment, carried out, thereby the operating efficiency of refrigerating plant can be improved.
Compound cooling evaporative cooler of the present utility model can utilize the natural cold source of the Nature to freeze, thereby greatly reduces a large amount of energy that traditional thermodynamic cycle refrigeration modes consumes, and reaches energy-saving and cost-reducing object; This compound cooling evaporative cooler not only can utilize air dry-bulb temperature to change the natural cooling source having in addition, can also utilize the natural cooling source of air ' s wet bulb temperature variation, has greatly expanded the range of operation of free cooling refrigeration.
Compound cooling evaporative cooler of the present utility model is on the basis of said structure, application by magnetic suspension without oily centrifugal refigerating compressor, with respect to traditional handpiece Water Chilling Units, computer equipment is carried out to cooling mode, not only greatly improve the security of mainframe computer center and data center, and can save power consumption the whole year more than 20%.
Accompanying drawing explanation
Accompanying drawing 1 is compound cooling evaporative cooler basic functional principle figure of the present utility model;
Accompanying drawing 2 is gas-liquid separation of the present utility model and recooler structural representation;
Accompanying drawing 3 is gas-liquid separation and the recooler cross section structure schematic diagram of accompanying drawing 2;
Accompanying drawing 4 is the compound cooling evaporative cooler basic functional principle figure with spraying cooling function of the present utility model;
Accompanying drawing 5 is the gas-liquid separation with spraying cooling function of the present utility model and recooler structural representation;
Accompanying drawing 6 is the gas-liquid separation with spraying cooling function of accompanying drawing 5 and recooler cross section structure schematic diagram;
Accompanying drawing 7 is compound cooling evaporative cooler modular unit basic functional principle figure of the present utility model;
Accompanying drawing 8 is the compound cooling evaporative cooler modular unit basic functional principle figure with spraying cooling function of the present utility model;
Accompanying drawing 9 is the combining structure schematic diagram of compound cooling evaporative cooler modular unit of the present utility model.
Wherein: 1-refrigeration compressor; 1-1-exhaust outlet; 1-2-air entry; 1-3-coolant interface; 2-condenser; 2-1-refrigerant inlet; 2-2-refrigerant outlet; The outlet of 2-3-cooling medium; 2-4-cooling medium inlet; 3-device for drying and filtering; 4-refrigerant liquid pipeline electromagnetic valve; 5-expansion valve; 6-compressor cooling electric magnet valve; 7-gas-liquid separation and recooler; The outlet of 7-1-gas refrigerant; The import of 7-2-gas-liquid mixed refrigerant; The outlet of 7-3-liquid refrigerant; The import of 7-4-gas refrigerant; The outlet of 7-5-cooling medium; 7-6-cooling medium inlet; 7-7-cooling medium chamber; 7-8-dividing plate; 7-9-the first end cap; 7-10-the first tube end sheet; 7-11-condensing heat-exchanging pipe; 7-12-housing; 7-13-liquid barrier; 7-14-the second tube end sheet; 7-15-the second end cap; The cold heat exchanger tube of 7-16-again; 7-17-spray interface; 7-18-spray thrower; 8-refrigerant circulation pump; 9-cooling base; 10-liquid refrigerant collector; 11-gas refrigerant collector; 12-three-way control valve; 12-1-entry port; 12-2-discharge port; 12-3-bypass port; 13-liquid level sensor; 14-liquid refrigerant current-sharing pipe; 15-liquid refrigerant distributing manifold; 16-gas refrigerant return-air manifold trunk; 17-cooling medium upstream end manifold trunk; 18-cooling medium outlet side manifold trunk; 19-spray pump; 20-spray control valve; 21-load balance valve; 22-pressure sensor; 23-pipe jointer; 24-temperature-detecting device; 25-cooling medium pipe; 26-computer controller; 27-connection; 28-shower.
The specific embodiment
Below in conjunction with accompanying drawing and embodiment, the utility model is further described.
As shown in Fig. 1-6: a kind of compound cooling evaporative cooler with natural cooling function for main equipment, comprises refrigeration compressor 1, condenser 2, device for drying and filtering 3, refrigerant liquid pipeline electromagnetic valve 4, expansion valve 5, gas-liquid separation and recooler 7, refrigerant circulation pump 8 and three-way control valve 12, wherein gas-liquid separation and recooler 7 comprise the first end cap 7-9, the first tube end sheet 7-10, condensing heat-exchanging pipe 7-11, housing 7-12, liquid barrier 7-13, the second tube end sheet 7-14, the second end cap 7-15 and colder heat exchanger tube 7-16, the two ends of housing 7-12 are respectively equipped with the first tube end sheet 7-10 and the second tube end sheet 7-14, the outside of the first tube end sheet 7-10 and the second tube end sheet 7-14 is respectively equipped with the first end cap 7-9 and the second end cap 7-15 for sealing, condensing heat-exchanging pipe 7-11 and the two ends of colder heat exchanger tube 7-16 are separately positioned on the top that the upper and condensing heat-exchanging pipe 7-11 of the first tube end sheet 7-10 and the second tube end sheet 7-14 is positioned at cold heat exchanger tube 7-16 again, and liquid barrier 7-13 is positioned at the top of condensing heat-exchanging pipe 7-11, the first end cap 7-9 and the second end cap 7-15 form cooling medium chamber 7-7 with the first tube end sheet 7-10 and the second tube end sheet 7-14 respectively, this cooling medium chamber 7-7 all with condensing heat-exchanging pipe 7-11 and colder heat exchanger tube 7-16 be connected and the first end cap 7-9 or the second end cap 7-15 are provided with cooling medium outlet 7-5 and the cooling medium inlet 7-6 being connected with cooling medium chamber 7-7, in the 7-7 of cooling medium chamber, be provided with dividing plate 7-8 in addition, cooling medium outlet 7-5 and cooling medium inlet 7-6 are separately positioned on the first end cap 7-9 or the second end cap 7-15 of dividing plate 7-8 upside and downside, housing 7-12 and the first tube end sheet 7-10, the second tube end sheet 7-14 form annular seal space and sealing chamber is connected with upper gas refrigerant outlet 7-1, gas-liquid mixed refrigerant import 7-2, liquid refrigerant outlet 7-3 and the gas refrigerant import 7-4 arranging of housing 7-12 respectively.Gas-liquid separation is connected with the air entry 1-2 on refrigeration compressor 1 by pipeline with the gas refrigerant outlet 7-1 on recooler 7, exhaust outlet 1-1 on refrigeration compressor 1 is connected with the refrigerant inlet 2-1 on condenser 2 by pipeline, refrigerant outlet 2-2 on condenser 2 by pipeline successively with device for drying and filtering 3, refrigerant liquid pipeline electromagnetic valve 4, expansion valve 5 is connected, the outlet of expansion valve 5 is connected with the gas-liquid mixed refrigerant import 7-2 on recooler 7 with gas-liquid separation by pipeline, gas-liquid separation is connected with refrigerant circulation pump 8 by pipeline with the liquid refrigerant outlet 7-3 on recooler 7, the port of export of refrigerant circulation pump 8 is connected with the entrance of liquid refrigerant collector 10 by pipeline, the outlet of liquid refrigerant collector 10 is connected with the entrance of cooling base 9, the outlet of cooling base 9 is connected with the entrance of gas refrigerant collector 11, the outlet of gas refrigerant collector 11 is connected with the gas refrigerant import 7-4 on recooler 7 with gas-liquid separation, cooling medium inlet 2-4 place on condenser 2 is provided with cooling medium pipe 25, cooling medium pipe 25 is provided with three-way control valve 12 and temperature-detecting device 24, temperature-detecting device 24 is positioned on the cooling medium pipe 25 at entry port 12-1 place of three-way control valve 12, the discharge port 12-2 of three-way control valve 12 is connected with the cooling medium inlet 7-6 on recooler 7 with gas-liquid separation by cooling medium pipe 25, gas-liquid separation and cooling medium outlet 7-5 on recooler 7 by cooling medium pipe 25, be connected with cooling medium inlet 2-4 on condenser 2 and condenser 2 on cooling medium inlet 2-4 by cooling medium pipe 25, be connected with the bypass port 12-3 of three-way control valve 12.Coolant interface 1-3 on refrigeration compressor 1 is connected with the pipeline between the port of export of device for drying and filtering 3 and the entrance point of refrigerant liquid pipeline electromagnetic valve 4 by pipeline in addition, and the pipeline at the coolant interface 1-3 place of refrigeration compressor 1 is provided with cooling electric magnet valve 6; The cold having in order to obtain more expeditiously nature environment, in gas-liquid separation and recooler 7, be provided with spray thrower 7-18, top and spray thrower 7-18 that spray thrower 7-18 is arranged on liquid barrier 7-13 are connected with shower 28 by the spray interface 7-17 on housing 7-12, the other end of shower 28 is connected with the pipeline at liquid refrigerant outlet 7-3 place and shower 28 is provided with spray pump 19 and spray control valve 20, and spray control valve 20 is on the shower 28 between spray pump 19 and spray interface 7-17.In addition for this cooling device of effective monitoring, on gas-liquid separation and recooler 7, be provided with liquid level sensor 13, liquid level sensor 13, for detection of the liquid level of gas-liquid separation and recooler 7 interior liquid refrigerants, according to testing result, is controlled the aperture of expansion valve 5, when liquid level is lower, the aperture that increases expansion valve 5, allows more cold-producing medium enter in gas-liquid separation and recooler 7, when liquid level is higher, reduce the aperture of expansion valve 5, reduce entering of cold-producing medium; In gas-liquid separation and recooler 7 places, be also provided with pressure sensor 22, pressure sensor 22 is arranged on gas-liquid separation with on recooler 7 or be communicated with on the pipeline of gas-liquid separation and recooler 7 and refrigeration compressor 1, pressure-detecting device 22 is according to pressure detecting result, regulate the output refrigerating capacity of refrigeration compressor 1, when pressure is higher, improve the output refrigerating capacity of refrigeration compressor 1, and when pressure decreased, reduce the output refrigerating capacity of refrigeration compressor 1, or close the operation of refrigeration compressor 1.
As Figure 7-9, the structural form of compound cooling evaporative cooler of the present utility model can be unit group mode, also can be modular combination mode, modular combination mode, that each modular unit is except having comprised above-described all parts, also comprised between module for interconnected parts, for interconnected parts, comprise liquid refrigerant current-sharing pipe 14, liquid refrigerant distributing manifold 15, gas refrigerant return-air manifold trunk 16, cooling medium upstream end manifold trunk 17 and cooling medium outlet side manifold trunk 18, liquid refrigerant current-sharing pipe 14 is arranged on the pipeline between liquid refrigerant outlet 7-3 and refrigerant circulation pump 8, liquid refrigerant distributing manifold 15 is arranged on the pipeline between refrigerant circulation pump 8 and liquid refrigerant collector 10, gas refrigerant return-air manifold trunk 16 is arranged on the pipeline between gas refrigerant collector 11 and gas refrigerant import 7-4, cooling medium upstream end manifold trunk 17 is arranged on the import department of cooling medium pipe 25, cooling medium outlet side manifold trunk 18 is arranged on the cooling medium outlet 2-3 place on condenser 2, add the compound cooling evaporative cooler of the syndetons such as liquid refrigerant current-sharing pipe 14, liquid refrigerant distributing manifold 15, gas refrigerant return-air manifold trunk 16, cooling medium upstream end manifold trunk 17 and cooling medium outlet side manifold trunk 18 to form a compound cooling evaporative cooler modular unit that can mutually combine.This compound cooling evaporative cooler modular unit both can independently be used, also more than one compound cooling evaporative cooler modular unit can be interconnected by pipe jointer 23, become a modularization unit being formed by compound cooling evaporative cooler modular unit and use, thus become refrigerating capacity larger and be standby and extendible assembly each other.The system that this assembly is comprised of computer controller 26 and communication line 27 is controlled, according to the load variations of computer equipment, automatically regulates, and redundancy marginal capacity while thering is fault.As Figure 7-8, Fig. 9 is the combining structure schematic diagram of compound cooling evaporative cooler modular unit to the basic functional principle figure of compound cooling evaporative cooler modular unit.
The refrigeration compressor 1 that the utility model adopts adopts magnetic suspension without oily centrifugal compressor, because magnetic suspension does not need oil lubrication without oily centrifugal refigerating compressor, therefore, pure cold-producing medium can be transported in computer equipment, whether and needn't can pollute computer equipment by worried lubricating oil, and whether lubricating oil can be got back in compressor.In addition, magnetic suspension has the function of variable speed drives without oily centrifugal compressor, can, expeditiously according to the variation of load and the variation of external environmental condition, change the rotating speed of compressor.And the change of compressor rotary speed means that the output refrigerating capacity of compressor keeps the consistent of height with operating condition and the variation of physical condition, thereby greatly improve the efficiency of year round cooling operation.At refrigeration compressor 1 place, be provided with load balance valve 21 in addition, balanced valve 21 is connected with exhaust outlet 1-1 and the air entry 1-2 of refrigeration compressor 1 respectively, when the output loading of refrigeration compressor 1 is lower, load balance valve 21 is opened, the part exhaust of refrigeration compressor 1 is entered by the import of load balance valve 21, adjusting through load balance valve 21 is controlled, then is flowed out by the outlet of load balance valve 21, enters the air entry 1-2 of refrigeration compressor 1.
As Figure 1-3, when compound cooling evaporative cooler of the present utility model is used, from the air entry 1-2 of refrigeration compressor 1, enter the gas refrigerant of refrigeration compressor 1, cooled compressor 1 is collapsed into the high-pressure gas refrigerant that temperature is higher, high-pressure gas refrigerant is discharged by the exhaust outlet 1-1 of refrigeration compressor 1, refrigerant inlet 2-1 by condenser 2 enters in the coolant channel of condenser 2, cooling medium enters from the entry port 12-1 of three-way control valve 12 by cooling medium pipe 25, by the distribution of three-way control valve 12, cooling medium inlet 2-4 by condenser 2 enters in the coolant guiding channel of condenser 2, in condenser 2, after the cold-producing medium release heat of high pressure, condensation becomes the liquid refrigerant of high pressure, the liquid refrigerant of high pressure is discharged by the cold-producing medium outlet 2-2 of condenser 2, and cooling medium absorbed the heat that cold-producing medium discharges after temperature be enhanced, cooling medium outlet 2-3 by condenser 2 discharges, the high pressure liquid refrigerant of being discharged by condenser 2 enters device for drying and filtering 3 from the import of device for drying and filtering 3, in device for drying and filtering 3, dry filter is to eliminate micro-moisture, by the outlet of device for drying and filtering 3, discharged again, the liquid refrigerant of discharging is divided into two parts, a part is through compressor cooling electric magnet valve 6, coolant interface 1-3 by refrigeration compressor 1 enters into refrigeration compressor 1, the heat producing when this partially liq cold-producing medium absorption refrigeration compressor 1 built-in motor and electrical equipment work, after evaporation becomes gas refrigerant, cooled compressor 1 compresses again, other a part of liquid refrigerant that device for drying and filtering 3 is discharged enters expansion valve 5 by magnetic valve 4, and in the interior expansion throttling of expansion valve 5, the gas and the liquid admixture that present low-temp low-pressure, from the outlet of expansion valve 5, discharge again, the cold-producing medium of being discharged by expansion valve 5 enters in gas-liquid separation and recooler 7 by the gas-liquid mixed refrigerant import 7-2 on gas-liquid separation and recooler 7, the cold-producing medium that enters gas-liquid separation and gas-liquid mixed state in recooler 7 from expansion valve 5 is separated the interior generation gas of gas-liquid separation and recooler 7 and liquid, wherein the refrigerant flow direction gas-liquid separation of liquid condition and the sap cavity of recooler 7, the cold-producing medium of gaseous state flows to the air cavity of gas-liquid separation and recooler 7, in gas-liquid separation and recooler 7, liquid refrigerant is flowed out by liquid refrigerant outlet 7-3, after the pressure that promotes liquid refrigerant through refrigerant circulation pump 8, be transported in main equipment, first this liquid refrigerant is transported in the liquid refrigerant collector 10 of main equipment, via liquid refrigerant collector, within 10 minutes, be clipped in different cooling base 9, in the inside of cooling base 9, be useful on the mobile microchannel of liquid refrigerant, the heat that surface-mounted integrated circuit on cooling base 9 produces when work is by the heat conduction of cooling base 9, pass to flowing liquid cold-producing medium in microchannel, after liquid refrigerant absorbs heat, evaporation becomes gas refrigerant, enter the gas refrigerant collector 11 of main equipment, by the outlet of gas collectors 11, flow out main equipment again, flow out the gas refrigerant of computer equipment, again by the gas refrigerant import 7-4 of gas-liquid separation and recooler 7, get back to above-mentioned compound cooling evaporative cooler, by the gas refrigerant import 7-4 of gas-liquid separation and recooler 7, entered the gas refrigerant of gas-liquid separation and recooler 7, the liquid refrigerant evaporating that partly may not be gasified totally is separated, enter the sap cavity of gas-liquid separation and recooler 7, again add the circulation of carrying toward computer equipment, the gas refrigerant being separated be present in gas-liquid separation with together with other gas refrigerants in recooler 7, by gas refrigerant outlet, 7-1 discharges, air entry 1-2 through refrigeration compressor 1 enters in refrigeration compressor 1, cooled compressor 1 compression again, thereby complete primary coolant to the transpiration-cooled circulation of equipment.Heat transfer process in gas-liquid separation and recooler 7 can be summarized as: gas refrigerant enters respectively coolant channel by the cold-producing medium of gas refrigerant entrance 7-4, gas and liquid admixture by gas-liquid mixed refrigerant entrance 7-2, in coolant channel, gas refrigerant and liquid refrigerant are separated, gas refrigerant is cooling by the lower cooling medium of the temperature in condensing heat-exchanging pipe 7-11, by gaseous state condensation, become liquid condition, condenser heat discharges to cooling medium by the heat conduction of condensing heat-exchanging pipe 7-11; And the liquid refrigerant being separated the gas-liquid mixed refrigerant entering from gas-liquid mixed refrigerant entrance 7-2, and the above cold-producing medium that is become liquid by condensation of gas, by cooling at the liquid refrigerant cooling medium that temperature is lower in cold heat exchanger tube 7-16 again, the temperature of liquid refrigerant reduces, then is discharged by liquid refrigerant outlet 7-3.
When temperature-detecting device 24 detects the temperature of the cooling medium of the entry port 12-1 entering on three-way control valve 12, while exporting the liquid refrigerant temperature of 7-3 discharge higher than the liquid refrigerant by gas-liquid separation and recooler 7, the entry port 12-1 of three-way control valve 12 and the passage between bypass port 12-3 are by conducting, and entry port 12-1 and the passage of discharging between port 12-2 will be closed, now cooling medium will not enter gas-liquid separation and recooler 7, but directly by the cooling medium inlet 2-4 on condenser 2, enter in condenser 2, after the interior absorption heat of condenser 2, by the cooling medium on condenser 2, export 2-3 eductor condenser 2, when temperature-detecting device 24 detects the temperature of the cooling medium of the entry port 12-1 entering on three-way control valve 12, while exporting the liquid refrigerant temperature of 7-3 discharge lower than the liquid refrigerant by gas-liquid separation and recooler 7, the entry port 12-1 of three-way control valve 12 and the passage between bypass port 12-3 will be closed, and entry port 12-1 and discharge passage between port 12-2 by conducting, now, first cooling medium is entered in cold heat exchanger tube 7-16 and condensing heat-exchanging pipe 7-11 by the cooling medium inlet 7-6 on gas-liquid separation and recooler 7 again, by heat, conduct the heat of absorption refrigeration agent passage inner refrigerant, cooling medium from gas-liquid separation and recooler 7 outlet 7-5 discharges gas-liquid separation and recooler 7 again, then by the cooling medium inlet 2-4 on condenser 2, enter in condenser 2, in the interior continuation of condenser 2, absorb after heat, by the cooling medium outlet 2-3 eductor condenser 2 on condenser 2.
For further promoting the performance of this compound cooling evaporative cooler, in gas-liquid separation and recooler 7, be provided with spray thrower 7-18.During use, when temperature-detecting device 24 detects the temperature of the cooling medium of the entry port 12-1 entering on three-way control valve 12, while exporting the liquid refrigerant temperature of 7-3 discharge lower than the liquid refrigerant by gas-liquid separation and recooler 7, close the operation of refrigeration compressor 1, open spray control valve 20 and start spray pump 19 operations, the liquid refrigerant that the liquid refrigerant outlet 7-3 of a part in gas-liquid separation and recooler 7 discharges, by entering in spray thrower 7-18 from the spray interface 7-17 of gas-liquid separation and recooler 7 after spray pump 19 and spray control valve 20, the liquid refrigerant of the supercooled state in gas-liquid separation and recooler 7, by the even cloth of spray thrower 7-18, spilt and become the drop of whereabouts state, make the cold-producing medium of liquid refrigerant and gaseous state have larger contact area, due to the saturation temperature of excessively cold liquid refrigerant temperature lower than gas refrigerant, therefore liquid refrigerant is in the process falling, can absorb the heat of a part of gas refrigerant being in contact with it, and its condensation is become to liquid, so not only the condensing heat-exchanging pipe 7-11 in gas-liquid separation and recooler 7 can become liquid by gas refrigerant condensation, the liquid refrigerant that spray thrower 7-18 sprays has also added the condensation process to gas refrigerant, thereby improved the temperature that enters that can utilize the needed cooling medium of natural environment cold completely.
When this compound cooling evaporative cooler need to be used in combination, between the liquid refrigerant current-sharing pipe 14 on each compound cooling evaporative cooler modular unit, liquid refrigerant distributing manifold 15, gas refrigerant return-air manifold trunk 16, cooling medium upstream end manifold trunk 17 and cooling medium outlet side manifold trunk 18, by pipe jointer 23, be connected and can form cold-producing medium and the mobile passage of cooling medium.For example: the connector on the connector on the cooling medium arrival end manifold trunk 17 of first modular unit and the cooling medium arrival end collector 17 of second modular unit is connected by pipe jointer 23, connector on the cooling medium arrival end collector 17 of second modular unit and the 3rd modular unit cooling medium arrival end collector 17 on connector by pipe jointer 23, be connected, remaining modular unit all connects successively with identical method, these are connected cooling medium arrival end collector 17 successively, become the public passage that cooling medium enters compound cooling evaporative cooler in assembly, connector on connector on the cooling medium outlet side manifold trunk 18 of first modular unit and the cooling medium outlet side manifold trunk 18 of second modular unit is connected by pipe jointer 23, connector on the cooling medium outlet side manifold trunk 18 of second modular unit and the 3rd modular unit cooling medium outlet side manifold trunk 18 on connector by pipe jointer 23, be connected, remaining modular unit all connects successively with identical method, these are connected cooling medium outlet side manifold trunk 18 successively, become the public passage that cooling medium leaves compound cooling evaporative cooler in assembly, connector on connector on the liquid refrigerant current-sharing pipe 14 of first modular unit and the liquid refrigerant current-sharing pipe 14 of second modular unit is connected by pipe jointer 23, connector on the liquid refrigerant current-sharing pipe 14 of second modular unit and the 3rd modular unit liquid refrigerant current-sharing pipe 14 on connector by pipe jointer 23, be connected, remaining modular unit all connects successively with identical method, these are connected liquid refrigerant current-sharing pipe 14 successively, the passage of balanced system cryogen between each compound cooling evaporative cooler, connector on the liquid refrigerant distributing manifold 15 of first modular unit is connected by pipe jointer 23 with the connector on the liquid refrigerant distributing manifold 15 of second modular unit, connector on the liquid refrigerant distributing manifold 15 of second modular unit and the 3rd modular unit liquid refrigerant distributing manifold 15 on connector by pipe jointer 23, be connected, remaining modular unit all connects successively with identical method, these are connected liquid refrigerant distributing manifold 15 successively, become the public passage that liquid refrigerant flows out each compound cooling evaporative cooler, connector on connector on the gas refrigerant return-air manifold trunk 16 of first modular unit and the gas refrigerant return-air manifold trunk 16 of second modular unit is connected by pipe jointer 23, connector on the gas refrigerant return-air manifold trunk 16 of second modular unit and the 3rd modular unit gas refrigerant return-air manifold trunk 16 on connector by pipe jointer 23, be connected, remaining modular unit all connects successively with identical method, these are connected gas refrigerant return-air manifold trunk 16 successively, become the public passage that gas refrigerant flows back to each compound cooling evaporative cooler.In above-mentioned assembly, in each compound cooling evaporative cooler, be provided with a computer controller 26, when a plurality of compound cooling evaporative cooler modular units are combined, computer controller 26 on each modular unit is connected to each other by connection 27, form one and controlled network, in all compound cooling evaporative cooler modular units, computer controller 26 on any one modular unit can become the master controller of controlling in network, master controller can be according to the caloric value of main equipment, there is the situation of fault in compound cooling evaporative cooler modular unit, allow each compound cooling evaporative cooler modular unit drop into, exit or rotation operation.
Compound cooling evaporative cooler of the present utility model is by refrigeration compressor 1 inhaling air cryogen and it is compressed, become the high-pressure gas refrigerant that temperature is higher, this part high-pressure gas refrigerant enters condenser 2, condensation becomes the cold-producing medium of liquid condition, again by expansion valve 5 throttlings, becoming the gas-liquid mixed refrigerant that temperature is lower enters in gas-liquid separation and recooler 7, 7 pairs of gas refrigerants of gas-liquid separation and recooler carry out separated with liquid refrigerant, wherein liquid refrigerant is transported in main equipment to be cooled by refrigerant circulation pump 8, by the distributor in main equipment to be cooled, liquid refrigerant is assigned in each cooling base that combines surface-mounted integrated circuit 9 again, and the heat that the liquid refrigerant absorption integrated circuit plate that enters cooling base 9 distributes, evaporation becomes gas refrigerant and flows out cooling base 9, and after collecting, again get back in the gas-liquid separation and recooler 7 of compound cooling evaporative cooler, in gas-liquid separation and recooler 7, part cold-producing medium that may not be evaporated completely or liquid condition is separated, converge with other liquid refrigerants in gas-liquid separation and recooler 7, continue to add the cooling circulation of supply main equipment, and the gas refrigerant being separated, the cooled compressor 1 of cold-producing medium together with other gaseous states in gas-liquid separation and recooler 7 sucks, and has started next circulation, in condenser 2, the higher high-pressure gas refrigerant of temperature of conventionally by other cooling medium (such as water or air), refrigeration compressor 1 being discharged carries out condensation, cooling medium has carried by transmitting heat out in main equipment, by another device, is rejected to other places.The water of take is example as cooling medium, from condenser 2 cooling medium water out, can be transported in cooling tower or similar equipment, by cooling tower, heat is diffused in atmospheric environment.
For winter of the high latitude area of the earth or spring and autumn transition season, because environment temperature is lower, even lower than carrying toward the temperature of the liquid refrigerant of main equipment to be cooled, the low-temperature receiver that in this case, can utilize naturally to exist completely carries out cooling to main equipment to be cooled.Therefore, in the utility model device, temperature-detecting device 24 is used for detecting entering temperature and carrying toward the temperature difference between the liquid refrigerant in main equipment to be cooled of cooling medium, if the temperature that enters of cooling medium is low to moderate certain degree than the liquid refrigerant temperature of the past main equipment to be cooled of conveying, now, will open entry port 12-1 on three-way control valve 12 to the passage of discharging port 12-2, close entry port 12-1 to the passage of bypass port 12-3 simultaneously, therefore cooling medium is introduced in gas-liquid separation and recooler 7, to the cold-producing medium in gas-liquid separation and recooler 7, carry out cooling, in this process, the cold-producing medium of liquid condition is by excessively cold, the cold-producing medium of gaseous state is condensed into as liquid.Owing to there being this part to derive from the adding of cold of natural environment, therefore refrigeration compressor 1 can reduce output refrigerating capacity, when the temperature of cooling medium is enough low, by natural environment cold, substitutes compressor 1 refrigeration even completely, thereby greatly save the power consumption of refrigeration.In this course, gas-liquid separation and recooler 7 not only have the effect of gas-liquid separation, utilize in addition natural environment low-temperature receiver, cold-producing medium are carried out to the effect of free cooling refrigeration.The use of spray thrower 7-18, spray pump 19 and spray control valve 20 has further improved the efficiency of obtaining the cold that nature environment has.
The utility model passes through refrigeration compressor 1, condenser 2, device for drying and filtering 3, refrigerant liquid pipeline electromagnetic valve 4, expansion valve 5, gas-liquid separation and recooler 7, refrigerant circulation pump 8 and three-way control valve 12 form the foundation structure of a compound cooling evaporative cooler, adopt freon as liquid refrigerant, liquid refrigerant is transported in the middle of the cooling base 9 of main equipment, in the microchannel of cooling base 9, liquid refrigerant absorbs the heat that main equipment distributes, evaporation becomes gaseous state, the cold-producing medium of gaseous state is got back in refrigerating plant, by vapor-compression refrigerant cycle or natural cool cycles, again become liquid refrigerant, be transported to again in main equipment, because freon refrigerant is that nonconducting medium and the boiling point under an atmospheric pressure are far below normal temperature, therefore as the leakage that freon occurs freon can flash to rapidly gas, and can not cause the electric short circuit of main equipment, can not there is the loss of catastrophic accident and critical data, cold-producing medium is the working media of vapor-compression refrigerant cycle in addition, also be the medium of Cooling calculation machine equipment simultaneously, therefore in whole cool cycles process, do not need as the type of cooling of chilled water, secondary heat exchange to be between cooling device and computer equipment, carried out, thereby the operating efficiency of refrigerating plant can be improved.If for example the needed cooling medium inlet temperature of computer equipment is 10 ℃, for adopting freezing water-cooled mode, the leaving water temperature that handpiece Water Chilling Units must offer the chilled water of computer equipment is 10 ℃.And in order to obtain the chilled water of 10 ℃, in the evaporimeter in handpiece Water Chilling Units, the evaporating temperature of vapor-compression refrigerant cycle will be 5 ℃ of left and right, to keep certain heat transfer temperature difference, now the efficiency of refrigeration system is exactly the efficiency when evaporating temperature is 5 ℃; And for compound cooling evaporative cooler of the present utility model, the cold-producing medium that is directly 10 ℃ by saturation temperature is sent in the cooling base 9 of computer equipment, the interior absorption heat of cooling base 9 at computer directly evaporates and becomes gas, that is to say that the evaporating temperature of kind of refrigeration cycle is than adopting the mode of handpiece Water Chilling Units to improve 5 ℃ of left and right, for vapor-compression refrigerant cycle, evaporating temperature is higher, and refrigerating efficiency is also just higher.What cold-producing medium carried that the ability of heat relies in addition is that cold-producing medium is become the latent heat of vaporization of steam by liquid evaporation.Take R134A cold-producing medium as example, and the cold-producing medium of every conveying 1kg, can take away the heat of 190kJ, and this is equivalent to carry the chilled water of 45kg, and allows its temperature raise 5 ℃ time, the heat that can take away.Therefore, the carry-on heat energy of gasification latent heat mode is the decades of times of the carry-on heat energy of sensible heat mode, cooling same caloric value, the flow of the needed cold-producing medium of vapor cooling system is far smaller than the flow of the required water of chilled water mode, thereby greatly reduce the transmission power of pump, improve the efficiency of system.
Compound cooling evaporative cooler of the present utility model is on the basis of said structure, application by magnetic suspension without oily centrifugal refigerating compressor, with respect to traditional handpiece Water Chilling Units, computer equipment is carried out to cooling mode, not only greatly improve the security of mainframe computer center and data center, and can save power consumption the whole year more than 20%; This compound cooling evaporative cooler can utilize the natural cold source of the Nature to freeze in addition, thereby greatly reduces a large amount of energy that traditional thermodynamic cycle refrigeration modes consumes, and reaches energy-saving and cost-reducing object; And this compound cooling evaporative cooler not only can utilize air dry-bulb temperature to change the natural cooling source having, and can also utilize the natural cooling source of air ' s wet bulb temperature variation, has greatly expanded the range of operation of free cooling refrigeration.
Above embodiment is only explanation technological thought of the present utility model, can not limit protection domain of the present utility model with this, every technological thought according to the utility model proposes, any change of doing on technical scheme basis, within all falling into the utility model protection domain; The technology that the utility model does not relate to all can be realized by prior art.
Claims (10)
1. the compound cooling evaporative cooler with natural cooling function for main equipment, comprise refrigeration compressor (1), condenser (2), device for drying and filtering (3), refrigerant liquid pipeline electromagnetic valve (4), expansion valve (5), gas-liquid separation and recooler (7), refrigerant circulation pump (8) and three-way control valve (12), it is characterized in that described gas-liquid separation is connected with the air entry (1-2) on refrigeration compressor (1) by pipeline with the gas refrigerant outlet (7-1) on recooler (7), exhaust outlet (1-1) on refrigeration compressor (1) is connected with the refrigerant inlet (2-1) on condenser (2) by pipeline, refrigerant outlet (2-2) on condenser (2) by pipeline successively with device for drying and filtering (3), refrigerant liquid pipeline electromagnetic valve (4), expansion valve (5) is connected, the outlet of expansion valve (5) is connected with the gas-liquid mixed refrigerant import (7-2) on recooler (7) with gas-liquid separation by pipeline, gas-liquid separation is connected with refrigerant circulation pump (8) by pipeline with the liquid refrigerant outlet (7-3) on recooler (7), the port of export of refrigerant circulation pump (8) is connected with the entrance of liquid refrigerant collector (10) by pipeline, the outlet of liquid refrigerant collector (10) is connected with the entrance of cooling base (9), the outlet of cooling base (9) is connected with the entrance of gas refrigerant collector (11), the outlet of gas refrigerant collector (11) is connected with the gas refrigerant import (7-4) on recooler (7) with gas-liquid separation, cooling medium inlet (2-4) on described condenser (2) locates to be provided with cooling medium pipe (25), cooling medium pipe (25) is provided with three-way control valve (12) and temperature-detecting device (24), temperature-detecting device (24) is positioned on the cooling medium pipe (25) that the entry port (12-1) of three-way control valve (12) locates, the discharge port (12-2) of three-way control valve (12) is connected with the cooling medium inlet (7-6) on recooler (7) with gas-liquid separation by cooling medium pipe (25), gas-liquid separation and cooling medium outlet (7-5) on recooler (7) by cooling medium pipe (25), be connected with cooling medium inlet (2-4) on condenser (2) and condenser (2) on cooling medium inlet (2-4) by cooling medium pipe (25), be connected with the bypass port (12-3) of three-way control valve (12).
2. the compound cooling evaporative cooler with natural cooling function for main equipment according to claim 1, it is characterized in that the coolant interface (1-3) on described refrigeration compressor (1) is connected with the pipeline between the port of export of device for drying and filtering (3) and the entrance point of refrigerant liquid pipeline electromagnetic valve (4) by pipeline, the pipeline that the coolant interface (1-3) of refrigeration compressor (1) is located is provided with cooling electric magnet valve (6).
3. the compound cooling evaporative cooler with natural cooling function for main equipment according to claim 1, it is characterized in that described gas-liquid separation and recooler (7) comprise the first end cap (7-9), the first tube end sheet (7-10), condensing heat-exchanging pipe (7-11), housing (7-12), liquid barrier (7-13), the second tube end sheet (7-14), the second end cap (7-15) and colder heat exchanger tube (7-16), the two ends of housing (7-12) are respectively equipped with the first tube end sheet (7-10) and the second tube end sheet (7-14), the outside of the first tube end sheet (7-10) and the second tube end sheet (7-14) is respectively equipped with the first end cap (7-9) and the second end cap (7-15) for sealing, condensing heat-exchanging pipe (7-11) and the again two ends of cold heat exchanger tube (7-16) are separately positioned on the top that the upper and condensing heat-exchanging pipe (7-11) of the first tube end sheet (7-10) and the second tube end sheet (7-14) is positioned at cold heat exchanger tube (7-16) again, liquid barrier (7-13) is positioned at the top of condensing heat-exchanging pipe (7-11).
4. the compound cooling evaporative cooler with natural cooling function for main equipment according to claim 3, it is characterized in that described the first end cap (7-9) and the second end cap (7-15) form cooling medium chamber (7-7) with the first tube end sheet (7-10) and the second tube end sheet (7-14) respectively, this cooling medium chamber (7-7) all with condensing heat-exchanging pipe (7-11) and colder heat exchanger tube (7-16) be connected and the first end cap (7-9) or the second end cap (7-15) are provided with cooling medium outlet (7-5) and the cooling medium inlet (7-6) being connected with cooling medium chamber (7-7), it is upper that described gas refrigerant outlet (7-1), gas-liquid mixed refrigerant import (7-2), liquid refrigerant outlet (7-3) and gas refrigerant import (7-4) is all arranged on housing (7-12), and gas refrigerant outlet (7-1), gas-liquid mixed refrigerant import (7-2), liquid refrigerant outlet (7-3) and gas refrigerant import (7-4) are all connected with the annular seal space that housing (7-12) and the first tube end sheet (7-10), the second tube end sheet (7-14) form.
5. the compound cooling evaporative cooler with natural cooling function for main equipment according to claim 4, it is characterized in that being provided with dividing plate (7-8) in described cooling medium chamber (7-7), cooling medium outlet (7-5) and cooling medium inlet (7-6) are separately positioned on first end cap (7-9) or the second end cap (7-15) of dividing plate (7-8) upside and downside.
6. the compound cooling evaporative cooler with natural cooling function for main equipment according to claim 3, it is characterized in that being provided with spray thrower (7-18) in described gas-liquid separation and recooler (7), top and spray thrower (7-18) that spray thrower (7-18) is arranged on liquid barrier (7-13) are connected with shower (28) by the spray interface (7-17) on housing (7-12), the pipeline that the other end of shower (28) is located with liquid refrigerant outlet (7-3) is connected and shower (28) is provided with spray pump (19) and spray control valve (20), spray control valve (20) is positioned on the shower (28) between spray pump (19) and spray interface (7-17).
7. according to the compound cooling evaporative cooler with natural cooling function for main equipment described in claim 1 or 3, gas-liquid separation and recooler (7) described in it is characterized in that locate to be provided with pressure sensor (22), and pressure sensor (22) is arranged on gas-liquid separation and goes up or be communicated with on the pipeline of gas-liquid separation and recooler (7) and refrigeration compressor (1) with recooler (7).
8. according to the compound cooling evaporative cooler with natural cooling function for main equipment described in claim 1 or 3, it is characterized in that described gas-liquid separation and recooler (7) are provided with liquid level sensor (13).
9. the compound cooling evaporative cooler with natural cooling function for main equipment according to claim 1, it is characterized in that described refrigeration compressor (1) adopts magnetic suspension without oily centrifugal compressor, and described refrigeration compressor (1) locates to be provided with load balance valve (21), balanced valve (21) is connected with exhaust outlet (1-1) and the air entry (1-2) of refrigeration compressor (1) respectively.
10. the compound cooling evaporative cooler with natural cooling function for main equipment according to claim 1, it is characterized in that described liquid refrigerant outlet (7-3) and the pipeline between refrigerant circulation pump (8) are provided with liquid refrigerant current-sharing pipe (14), pipeline between refrigerant circulation pump (8) and liquid refrigerant collector (10) is provided with liquid refrigerant distributing manifold (15), and the pipeline between gas refrigerant collector (11) and gas refrigerant import (7-4) is provided with gas refrigerant return-air manifold trunk (16); The import department of described cooling medium pipe (25) is provided with cooling medium upstream end manifold trunk (17), and the pipeline that the cooling medium outlet (2-3) on condenser (2) is located is connected with cooling medium outlet side manifold trunk (18).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320667454.5U CN203533948U (en) | 2013-10-28 | 2013-10-28 | Compound type evaporative type cooling device having natural cooling function and used for large-scale device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320667454.5U CN203533948U (en) | 2013-10-28 | 2013-10-28 | Compound type evaporative type cooling device having natural cooling function and used for large-scale device |
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| CN203533948U true CN203533948U (en) | 2014-04-09 |
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| CN201320667454.5U Withdrawn - After Issue CN203533948U (en) | 2013-10-28 | 2013-10-28 | Compound type evaporative type cooling device having natural cooling function and used for large-scale device |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103528256A (en) * | 2013-10-28 | 2014-01-22 | 周伟 | Composite evaporative cooling device with natural cooling function for large-scale equipment |
| CN104390803A (en) * | 2014-12-11 | 2015-03-04 | 青岛大学 | Refrigerant supply device for refrigerator heat exchanger performance test system and test method |
| CN109405318A (en) * | 2018-10-17 | 2019-03-01 | 苏州必信空调有限公司 | It is a kind of with the refrigeration system and its control method that freely cool down |
-
2013
- 2013-10-28 CN CN201320667454.5U patent/CN203533948U/en not_active Withdrawn - After Issue
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103528256A (en) * | 2013-10-28 | 2014-01-22 | 周伟 | Composite evaporative cooling device with natural cooling function for large-scale equipment |
| CN104390803A (en) * | 2014-12-11 | 2015-03-04 | 青岛大学 | Refrigerant supply device for refrigerator heat exchanger performance test system and test method |
| CN104390803B (en) * | 2014-12-11 | 2017-01-11 | 青岛大学 | Refrigerant supply device for refrigerator heat exchanger performance test system and test method |
| CN109405318A (en) * | 2018-10-17 | 2019-03-01 | 苏州必信空调有限公司 | It is a kind of with the refrigeration system and its control method that freely cool down |
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