CN106196689B - Fountain refrigerating plant and control method - Google Patents
Fountain refrigerating plant and control method Download PDFInfo
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- CN106196689B CN106196689B CN201510285568.7A CN201510285568A CN106196689B CN 106196689 B CN106196689 B CN 106196689B CN 201510285568 A CN201510285568 A CN 201510285568A CN 106196689 B CN106196689 B CN 106196689B
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Abstract
A kind of fountain refrigerating plant of present invention offer and control method.Fountain refrigerating plant includes:Cooling cycle system, fluid circulation system and babinet;The cooling cycle system includes the compressor to link together, condenser, capillary and evaporator;The fluid circulation system includes liquid pump, nozzle and fluid reservoir, and the liquid pump is connected through the evaporator with the nozzle, and the liquid pump is connected with the fluid reservoir, and the fluid reservoir is connected to the inner cavity of the babinet;Drying fan is additionally provided in the babinet.The ejecting liquid in fluid circulation system is cooled down by cooling cycle system, the coefficient of performance of refrigeration equipment is improved, improves energy utilization efficiency, realize the function of quickly cooling;Simultaneously as cooling rate is very fast, but also the start-stop time of compressor significantly reduces, the service life of fountain refrigerating plant is extended.
Description
Technical field
The present invention relates to refrigerating plant more particularly to a kind of fountain refrigerating plant and control methods.
Background technology
The cold transmittance process of refrigeration equipment at present (heat transfer process is in contrast):Refrigerant in evaporator steams
Hair heat absorption, produced cold reduce the liner of refrigeration equipment temperature for being close to evaporator by way of " heat conduction ", the system of low temperature
Cool equipment liner makes system by free convection, radiation (if internal have the heat exchange mode of forced convection device for forced convertion)
Confining gas cooling inside cool equipment, cryogenic gas is by free convection (if the internal heat exchange mode for having forced convection device
For forced convertion) it exchanges heat with storing, the heat of storing is taken away.Refrigeration equipment inner wall is with storing also by radiation heat transfer
Mode the heat of storing is taken away.
There are two main problems for above-mentioned cold transmittance process:First, exchanged heat to be main with air inside refrigeration equipment
Medium, since the density (1.164kg/m3,20 DEG C) and thermal coefficient (2.524 × 10-2W/ (m DEG C)) of air are relatively low,
Cause heat transfer coefficient low;Two kinds of (refrigeration equipment internal face in storing temperature range) changes second is that free convection and radiation heat transfer
Hot mode coefficient of heat transfer itself is relatively low, in 10~100W/ (m2 DEG C) range.On the one hand, according to heat exchange amount=heat exchange system
The thermal conduction study fundamental formular of number × heat transfer temperature difference × heat exchange area needs higher heat exchange heat when refrigeration equipment storing is more
Amount, refrigeration equipment generally realized by reducing evaporating temperature (increase heat transfer temperature difference), and according to thermodynamics Carnot's theorem,
Refrigeration equipment evaporating temperature is lower, and coefficient of performance of refrigerating (COP) is lower, and cooling rate is slower;On the other hand, freeze at present
The temperature sensing package of equipment temperature controller is placed on the pipeline of refrigeration system and (is typically placed at evaporator pipeline exit), passes through evaporation
The temperature in device exit come judge refrigerate indoor air temperature whether be reduced to setting value, the air themperature inside refrigeration equipment
Compressor is shut down when being reduced to set temperature lower limit, until the air themperature inside refrigeration equipment rises to temperature controller setting
Compressor just turns back on work when temperature upper limit.Since there are the larger temperature difference with storing temperature for air themperature, so when compression
When machine is shut down, storing temperature is not reduced to set temperature, therefore storing heat quickly heats refrigeration equipment inner air,
Temperature is increased to compressor and turns back on work, directly results in the frequent start-stop of compressor.Cooling rate makes the section of refrigerator-freezer slowly
Energy property is in urgent need to be improved, and the start and stop of compressor frequently so that the functional reliability of refrigerator-freezer declines, and greatly shorten the use of compressor
Service life.
Currently, being changed by the forced convertion of water and storing instead of air as the water refrigeration equipment of heat exchange refrigerant using water
Heat, for heat transfer coefficient range at 1000~10000W/ (m2 DEG C), this increases the heat transfer system of refrigeration equipment to a certain extent
Number, but the inside of water refrigeration equipment must determine the utilization journey of refrigeration equipment volume with the presence of a large amount of water, the liquid level of water
Degree, while the presence of a large amount of water also increases the requirement of refrigeration equipment intensity.In addition the evaporator of refrigeration system is positioned over refrigeration
Inside equipment, the dischargeable capacity of refrigeration equipment is occupied.
Invention content
In view of this, a kind of fountain refrigerating plant of present invention offer and control method, it is intended to reduce fountain refrigeration dress
The start-stop time for the compressor set realizes the function of quickly cooling.
Technical solution provided by the invention is a kind of fountain refrigerating plant, which is characterized in that including:Refrigeration cycle system
System, fluid circulation system and babinet;The cooling cycle system include the compressor to link together, condenser, capillary and
Evaporator;The fluid circulation system includes liquid pump, nozzle and fluid reservoir, and the liquid pump is through the evaporator and the spray
Mouth is connected, and the liquid pump is connected with the fluid reservoir, and the fluid reservoir is connected to the inner cavity of the babinet;The babinet
In be additionally provided with drying fan.
Further, the babinet is formed with air duct, and the air inlet in the air duct is located at the bottom of the inner cavity of the babinet,
The air outlet in the air duct is located at the top of the inner cavity of the babinet and towards the bottom of the inner cavity of the babinet, the drying wind
Fan is located in the air duct.
Further, the air duct is provided with multiple air outlets and multiple air inlets, each air outlet direction
Corresponding air inlet direction outlet air.
Further, the cooling cycle system further includes that four-way reversing valve and switching switch, the four-way reversing valve
Common inlet and public outlet are connect with the exhaust pipe of the compressor and air intake duct respectively, and other the two of the four-way reversing valve
The reduction of fractions to a common denominator is not connected with the condenser and the evaporator, the capillary be set to the condenser and the evaporator it
Between;The switching switch controls the four-way reversing valve commutation for triggering.
Further, further include control system, the control system includes temperature controller, temperature sensor, differential pressure pickup
And position switch, the temperature sensor are set between the fluid reservoir and the liquid collection opening of the bottom of box, the temperature controller
It is respectively connected with the temperature sensor, the liquid pump, the compressor, the differential pressure pickup is set to the liquid pump
Import and export between, the differential pressure pickup is connected to the compressor, and the position switch is set to the door body of the babinet
Place.
Further, the evaporator is plate heat exchanger or double pipe heat exchanger, and the liquid pump passes through the evaporation
Device is connected with the nozzle;Alternatively, being connected by pipeline between the liquid pump and nozzle, the pipeline and the evaporator
Heat conduction connects.
The present invention also provides a kind of control method of fountain refrigerating plant, the fountain refrigerating plant includes:Refrigeration
The circulatory system, fluid circulation system and babinet;The cooling cycle system includes the compressor, condenser, hair to link together
Tubule and evaporator;The fluid circulation system includes liquid pump, nozzle and fluid reservoir, the liquid pump through the evaporator with
The nozzle is connected, and the liquid pump is connected with the fluid reservoir, and the fluid reservoir is connected to the inner cavity of the babinet;Institute
It states and is additionally provided with drying fan in babinet;
Control method is:It is exchanged heat by the evaporator and the ejecting liquid in the fluid circulation system, it is described
Ejecting liquid in fluid circulation system is exchanged heat in a manner of spraying with the storing of cabinets cavity by the nozzle.
Further, the fountain refrigerating plant further includes control system, and the control system includes temperature controller, temperature
Sensor, differential pressure pickup and position switch, the temperature sensor are set to the liquid collecting of the fluid reservoir and the bottom of box
Between mouthful, the temperature controller is respectively connected with the temperature sensor, the liquid pump, the compressor, and the pressure difference passes
Sensor is set between the import and export of the liquid pump, and the differential pressure pickup is connected to the compressor, and the position switch is set
At the door body of the babinet;
Control method specifically includes:
S1:After fountain refrigerating plant is powered, the position switch judges whether door body is opened, if opening, the liquid
Systemic circulatory system and the cooling cycle system do not start;If being not turned on, it is transferred to S2;
S2:The temperature and setting value that the temperature controller temperature sensor is passed back are set if the temperature passed back is higher than
Definite value then starts the liquid pump;If the temperature passed back is higher than setting value, while the pressure difference between the inlet and outlet of the liquid pump
Sensor shows pressure difference, then starts the cooling cycle system, and fountain refrigerating plant enters working condition;
S3:When the temperature that the temperature sensor is passed back reaches setting value, the temperature controller sends out stopping signal, the system
SAPMAC method system and the fluid circulation system are cut off in succession, are stopped.
Further, control method further includes:S4:It is described when the temperature that the temperature sensor is passed back reaches setting value
Temperature controller sends out starting fan signal, and processing is blowed to storing surface in the drying starting fan.
Further, the cooling cycle system further includes that four-way reversing valve and switching switch, the four-way reversing valve
Common inlet and public outlet are connect with the exhaust pipe of the compressor and air intake duct respectively, and other the two of the four-way reversing valve
The reduction of fractions to a common denominator is not connected with the condenser and the evaporator, the capillary be set to the condenser and the evaporator it
Between;The switching switch controls the four-way reversing valve commutation for triggering;Control method further includes:By switching switching
Four-way reversing valve changes the flow direction of refrigerant, realizes the evaporator of cooling cycle system and the exchange function of condenser, will make
Cold control is switched to heating control.
Fountain refrigerating plant provided by the invention and control method, by cooling cycle system in fluid circulation system
Ejecting liquid cooled down, ejecting liquid will be directly injected to by nozzle on the storing that cabinets cavity is held, the spray of low temperature
Heat exchange will directly be carried out with storing by drenching liquid, and since the heat transfer coefficient of liquid is replaced, the ejecting liquid on storing can be fast
Speed carries out heat exchange with storing, improves the coefficient of performance of refrigeration equipment, improves energy utilization efficiency, realizes the work(of quickly cooling
Energy;Simultaneously as cooling rate is very fast, but also the start-stop time of compressor significantly reduces, fountain refrigerating plant is extended
Service life;Likewise, the state by changing four-way reversing valve, can also realize refrigeration control being switched to heating control
System, realizes the multi-functional of quickly cooling/speed heat, becomes full season electric appliance, reduce cost.
Description of the drawings
In order to more clearly explain the embodiment of the invention or the technical proposal in the existing technology, to embodiment or will show below
There is attached drawing needed in technology description to be briefly described, it should be apparent that, the accompanying drawings in the following description is this hair
Some bright embodiments for those of ordinary skill in the art without having to pay creative labor, can be with
Obtain other attached drawings according to these attached drawings.
Fig. 1 is the schematic diagram one of fountain refrigerating plant embodiment of the present invention;
Fig. 2 is the schematic diagram two of fountain refrigerating plant embodiment of the present invention;
Fig. 3 is the structural schematic diagram of the babinet in fountain refrigerating plant embodiment of the present invention.
Specific implementation mode
In order to make the object, technical scheme and advantages of the embodiment of the invention clearer, below in conjunction with the embodiment of the present invention
In attached drawing, technical scheme in the embodiment of the invention is clearly and completely described, it is clear that described embodiment is
A part of the embodiment of the present invention, instead of all the embodiments.Based on the embodiments of the present invention, those of ordinary skill in the art
The every other embodiment obtained without making creative work, shall fall within the protection scope of the present invention.
As shown in figures 1 and 3, the present embodiment fountain refrigerating plant includes mainly compressor 1, condenser 3, capillary
4, evaporator 5, liquid pump 6, nozzle 7, fluid reservoir 8, regulating valve 9, filter 10, temperature controller 11, temperature sensor 12, pressure difference pass
Sensor 13, position switch 14 and babinet 15.Wherein, compressor 1, condenser 3, capillary 4 and evaporator 5 form refrigeration cycle
System;Liquid pump 6, filter 10, nozzle 7, fluid reservoir 8 and regulating valve 9 form fluid circulation system;Temperature controller 11, temperature pass
14 forming control system of sensor 12, differential pressure pickup 13 and position switch.
The structure of cooling cycle system is specially:Compressor 1, condenser 3, capillary 4 and evaporator 5 are connected by circulation successively
The refrigerating circuit flowed for refrigerant is formed together.
The structure of fluid circulation system is specially:The ejecting liquid that liquid pump 6 exports conveys after evaporator 5 is freezed
To nozzle 7, nozzle 7 stretches into the inner cavity of babinet 15, and liquid pump 6 is connected through filter 10, regulating valve 9 with fluid reservoir 8 successively, storage
Flow container 8 is connected to the inner cavity of babinet 15.Wherein, the intracavity bottom of babinet 15 could be formed with liquid collection opening, fluid reservoir 8 and the liquid collecting
Ejecting liquid in mouth connection collection tank 15;In addition, the knots such as plate heat exchanger or double pipe heat exchanger may be used in evaporator 5
Structure has two flow paths in evaporator 5, wherein a flow path is flowed for refrigerant, another flow path is flowed for spray liquid, liquid pump
6 are connect by evaporator 5 with nozzle 7, alternatively, directly being connected by pipeline between liquid pump 6 and nozzle 7, which is attached to steaming
To flow through the spray liquid in the pipeline by the refrigeration of evaporator 5 on hair device 5.
The structure of control system is specially:Temperature sensor 12 is set between the liquid collection opening of 15 bottom of fluid reservoir 8 and babinet,
Temperature controller 11 is separately connected with temperature sensor 12, liquid pump 6, compressor 1, differential pressure pickup 13 be set to liquid pump 6 into and out of
Between mouthful, differential pressure pickup 13 is additionally coupled to compressor 1, and position switch 14 is set at the door body of babinet 15, for judging babinet
Door body on 15(It is not shown)Whether open.
Wherein, configured with drying fan 151 in the babinet 15 in the present embodiment, by drying up fan 151 to storing surface
Ejecting liquid carry out drying processing, and dry up the top that fan 151 can be arranged directly on 15 inner cavity of babinet, it is preferred that case
Body 15 is provided with air duct 152, and the air inlet 1522 in air duct 152 is located at the bottom of the inner cavity of babinet 15, the air outlet in air duct 152
1521 are located at the top of the inner cavity of babinet 15 and towards the bottom of the inner cavity of babinet 15, dry up fan 151 and be located in air duct 152,
Specifically, under the action of drying up fan 151, air duct 152 will be from 1522 air draught of air inlet of bottom and from the air outlet at top
1521 blowouts, air outlet 1521 are dried downward, and so as to blow the ejecting liquid on storing surface off, and air inlet 1522 is located at
Lower section air draught, the ejecting liquid being more advantageous on storing flow downward.Air duct 152 can be provided with multiple air outlets 1521 and more
A air inlet 1522, each air outlet 1521 is towards the 1522 direction outlet air of corresponding air inlet.
The course of work and control method of the present embodiment fountain refrigerating plant are illustrated below in conjunction with the accompanying drawings, with case
The storing refrigerated in body 15 is for beverage.
The working condition of the present embodiment fountain refrigerating plant is broadly divided into startup, operation, shutdown and door body and opens four kinds
Operating mode, beverage are deposited in a manner of vertical angles as possible in the inner cavity of babinet 15, set the spray droplet size of nozzle 7 in
Etc. sizes, the particle size values of the spray droplet of median be 1-3mm, close door body, 11 set temperature value of temperature controller is 10 DEG C, is connected
Power supply, the present embodiment fountain refrigerating plant enter the start operating performance stage.
Cooling cycle system is exchanged heat by the ejecting liquid in evaporator 5 and fluid circulation system, and fluid circulation system is logical
It crosses nozzle 7 ejecting liquid after refrigeration is ejected on storing and exchange heat;Control system control simultaneously cooling cycle system and
Fluid circulation system;The step of fluid circulation system controls cooling cycle system simultaneously, cooling cycle system be specially:
Judge whether door body is opened according to the position switch 14 of unexpected winner body first(It is turned off at this time);Then temperature sensor
12 temperature signals for passing to temperature controller 11 are room temperature(Because beverage is just put into), and set temperature value has deviation, temperature controller
11 control 6 power supply of liquid pump connections immediately, fluid circulation system start-up operation are also turned on 1 power supply of compressor;
But after 1 power supply of compressor is connected, whether compressor 1 starts the control of also compression gap sensor 13, passes through pressure difference
Sensor 13 judges whether the inlet and outlet of liquid pump 6 are successfully established pressure difference, if being successfully established pressure difference, liquid circulation system
System normal work, compressor 1 start, and cooling cycle system is started to work.
The transmittance process of cold is:Refrigerant evaporation endothermic in the evaporator 5 of cooling cycle system generates cold, liquid
The circulatory system(By taking water as an example, ejecting liquid is that the ethyl alcohol of pure water, ethylene glycol, one or more of glycerine or phenol is water-soluble
The soluble-salt of liquid or alkali and alkaline earth metal ions(Such as sodium chloride, calcium chloride)Aqueous solution, according to the refrigeration of storing, freezing
The applicable ejecting liquid of temperature selection)Water evaporator 5 be pumped to by liquid pump 6 freeze, absorb the cold of refrigerant
Become cold water, cold water is high speed droplet by the atomization of nozzle 7, and droplet is directly injected to beverage packaging surface, is changed with beverage
Heat, simultaneously because droplet has very high flow velocity, getting on beverage can be such that beverage shakes, and cold is made quickly to be passed from beverage packaging
It is delivered to beverage inside, while reducing beverage periphery and the internal temperature difference, beverage is made to be fully cooled;Liquid after exchanging heat with beverage
Drip temperature to increase, and come together in 15 bottom of babinet, be discharged into the fluid reservoir 8 of fluid circulation system from liquid collection opening by gravity, then according to
Secondary valve after the adjustment 9, filter 10 are pumped by liquid pump 6 at evaporator 5, are recycled into next round.
Water can flow through temperature sensor 12 when entering fluid reservoir 8 from the liquid collection opening of babinet 15, and the temperature signal of water is transmitted
To temperature controller 11.Due to the continuous transmission of cold, the temperature of beverage continuously decreases, and the temperature of return water is gradually lowered.Work as temperature
When reaching 10 DEG C of setting, temperature controller 11 simultaneously switches off the power supply of liquid pump 6 and compressor 1, and fluid circulation system and refrigeration are followed
Loop system is simultaneously stopped work, into shutdown operating mode.It is continuous incoming due to external heat, make internal beverage temperature it is gradual on
It rises, when the upper limit value for reaching the startup of temperature controller 11, the restarting of fountain refrigerating plant.
Likewise, when the temperature that temperature sensor 12 is passed back reaches setting value, temperature controller 11 sends out starting fan signal, blows
Dry-air blast fan 151 starts is blowed processing to storing surface, and the ejecting liquid on storing surface is disposed, user is facilitated to take
It uses, and the run time for drying up fan 151 can have manufacturer's setting that can also be set by user oneself according to actual needs.
Fountain refrigerating plant is in normal operation, if door body is opened in midway, the liquid to prevent nozzle 7 from spraying flies out case
Body 15, position switch 14 control liquid pump 6 and compressor 1 and power off simultaneously, fluid circulation system and cooling cycle system while quilt
Cut-out, fountain refrigerating plant are stopped.After door body is closed, liquid pump 6 and compressor 1 are restarted.
Analysis finds, cold and storing heat exchange in weakest link just inside fountain refrigerating plant, thus this hair
The bright spray heat transfer technology that the coefficient of heat transfer can reach to 100000W/ (m2 DEG C) is introduced into fountain refrigerating plant refrigerating field,
Meanwhile proposing that spray mode is adjustable and spray droplet size is by babinet 15 according to the philosophy of hydrodynamics, thermal conduction study
Portion storing type determines, for refrigerating function, fountain refrigerating plant of the present invention refrigerates soft bottle beverage in addition to selling, can be with
It realizes to the quick-frozen of fruit or packaged food.
Such as:
For bottled drink, selection sprays liquid to storing surface close to columnar spray droplet size, and right
Larger spray droplet size is selected in glass, metal bottled drink(The median grain size of drop is 2-5.5mm), plastic bottle
Liquid beverage is secondly(The ranging from 1-3mm of the median diameter value of drop), fruit then select smaller spray droplet size(Drop
Median diameter value ranging from 0.5-2mm).This is because larger size droplet diameter has relatively high kinetic energy, it can be with
So that beverage bottle and internal liquid is shaken, also internal heat is strengthened while strengthening storing external heat-exchanging, it is further real
Quickly cooling/speed heat function of existing refrigeration equipment.
And for the storing of such as fruits, because of its surface rapid wear and internal heat conduction is the bottleneck entirely to conduct heat, excessively
It is little to overall contribution to strengthen external heat-exchanging, therefore uniform low temperature environment need to be only provided, so the close atomization of selection
Spray droplet size.
The raising of 15 internal heat coefficient of babinet makes the coefficient of heat transfer from refrigerant to storing improve, and transmits identical heat
The required temperature difference will reduce, and technical solution using the present invention is freezed, evaporating temperature and the temperature of cooling cycle system
The temperature difference≤5 DEG C between the temperature sensing package temperature of device 11 are controlled, the temperature difference≤10 DEG C between the target temperature of storing greatly optimize system
The performance of SAPMAC method system.
Conventional refrigeration equipment is under heavy load there are two the basic reasons of high frequent start and stop:First, temperature controller temperature sensing package
Position;Second is that there is the larger temperature difference between evaporating temperature and storing.Wherein, as before, the introducing of spraying technique reduces evaporation temperature
The temperature difference between degree and storing, on the other hand, temperature sensor 12 is installed on the collection of 15 bottom of refrigeration equipment babinet by the present invention
Between liquid mouth and fluid reservoir 8.Under the premise of being packed into 80 bottles of 500ml bottled waters inside 128L refrigeration equipments, by Experimental comparison,
In for 24 hours, conventional refrigeration equipment start-stop 100 times, and the quickly cooling energy-saving cabinet only start and stop of the present invention 2 times.
As shown in Fig. 2, in addition to realizing above-mentioned quickly cooling function, the present embodiment fountain refrigerating plant is based on above-mentioned technical side
Case, difference lies in can be opened with the storing in heating compartment 15 specifically, refrigeration cycle further includes four-way reversing valve 2 and switching
It closes(It is not shown);The structure of cooling cycle system is specially:The common inlet of four-way reversing valve 2 and public outlet respectively with compression
The exhaust pipe of machine 1 is connected with air intake duct, and other two reduction of fractions to a common denominator of four-way reversing valve 2 is not connected with condenser 3 and evaporator 5, hair
Tubule 4 is set between condenser 3 and evaporator 5;Switching switch is connected by controlling power supply with four-way reversing valve 2.
In particular, it is desirable to when being switched to heating state by refrigerating state, switching switch is pulled, control power supply is changed to four-way
To 2 one high level pulses of valve, realize that four-way reversing valve 2 commutates, the flow direction of refrigerant changes, evaporator 5 and condenser 3
Exchange function, then realize speed heat function, the present embodiment fountain refrigerating plant can be made in winter or other desired
Occasion is used as " hot drink " heater, improves energy utilization efficiency, reduces vacancy rate, has given full play to the present embodiment fountain
The frequency of use of refrigerating plant becomes the multifunctional electric appliance in full season.
Finally it should be noted that:The above embodiments are merely illustrative of the technical solutions of the present invention, rather than its limitations;Although
Present invention has been described in detail with reference to the aforementioned embodiments, it will be understood by those of ordinary skill in the art that:It still may be used
With technical scheme described in the above embodiments is modified or equivalent replacement of some of the technical features;
And these modifications or replacements, various embodiments of the present invention technical solution that it does not separate the essence of the corresponding technical solution spirit and
Range.
Claims (3)
1. a kind of control method of fountain refrigerating plant, which is characterized in that the fountain refrigerating plant includes:Refrigeration cycle
System, fluid circulation system and babinet;The cooling cycle system includes the compressor, condenser, capillary to link together
And evaporator;The fluid circulation system includes liquid pump, nozzle and fluid reservoir, the liquid pump through the evaporator with it is described
Nozzle is connected, and the liquid pump is connected with the fluid reservoir, and the fluid reservoir is connected to the inner cavity of the babinet;The case
Drying fan is additionally provided in body;
Control method is:It is exchanged heat by the evaporator and the ejecting liquid in the fluid circulation system, the liquid
Ejecting liquid in the circulatory system is exchanged heat in a manner of spraying with the storing of cabinets cavity by the nozzle;
The fountain refrigerating plant further includes control system, and the control system includes temperature controller, temperature sensor, pressure difference biography
Sensor and position switch, the temperature sensor are set between the fluid reservoir and the liquid collection opening of the bottom of box, the temperature
Control device is respectively connected with the temperature sensor, the liquid pump, the compressor, and the differential pressure pickup is set to the liquid
Between the import and export of body pump, the differential pressure pickup is connected to the compressor, and the position switch is set to the door of the babinet
At body;
Control method specifically includes:
S1:After fountain refrigerating plant is powered, the position switch judges whether door body is opened, if opening, the liquid follows
Loop system and the cooling cycle system do not start;If being not turned on, it is transferred to S2;
S2:The temperature and setting value that the temperature controller temperature sensor is passed back, if the temperature passed back is higher than setting value,
Then start the liquid pump;If the temperature passed back is higher than setting value, while the pressure difference sensing between the inlet and outlet of the liquid pump
Device shows pressure difference, then starts the cooling cycle system, and fountain refrigerating plant enters working condition;
S3:When the temperature that the temperature sensor is passed back reaches setting value, the temperature controller sends out stopping signal, and the refrigeration is followed
Loop system and the fluid circulation system are cut off in succession, are stopped.
2. the control method of fountain refrigerating plant according to claim 1, which is characterized in that control method further includes:
S4:When the temperature that the temperature sensor is passed back reaches setting value, the temperature controller sends out starting fan signal, the drying wind
Fan starts is blowed processing to storing surface.
3. the control method of fountain refrigerating plant according to claim 1, which is characterized in that the cooling cycle system
Further include that four-way reversing valve and switching switch, the common inlet of the four-way reversing valve and public outlet respectively with the compressor
Exhaust pipe connected with air intake duct, other two reduction of fractions to a common denominator of the four-way reversing valve is not connected with the condenser and the evaporator
It connects, the capillary is set between the condenser and the evaporator;The switching switch controls the four-way for triggering
Reversal valve commutates;Control method further includes:Change the flow direction of refrigerant by switching switching four-way reversing valve, realizes system
Refrigeration control is switched to heating control by the evaporator of SAPMAC method system and the exchange function of condenser.
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201420515218 | 2014-09-09 | ||
CN201410455996.5A CN104180553A (en) | 2014-09-09 | 2014-09-09 | Spraying type energy-saving fast refrigerator and control method thereof |
CN2014104559965 | 2014-09-09 | ||
CN2014205152186 | 2014-09-09 |
Publications (2)
Publication Number | Publication Date |
---|---|
CN106196689A CN106196689A (en) | 2016-12-07 |
CN106196689B true CN106196689B (en) | 2018-10-09 |
Family
ID=54527425
Family Applications (23)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201520263828.6U Active CN204787452U (en) | 2014-09-09 | 2015-04-28 | Fountain refrigerating plant |
CN201520263717.5U Active CN204787389U (en) | 2014-09-09 | 2015-04-28 | Fountain storing equipment |
CN201510207066.2A Active CN106152589B (en) | 2014-09-09 | 2015-04-28 | Fountain heating-cooling equipment and control method |
CN201520263825.2U Active CN204787390U (en) | 2014-09-09 | 2015-04-28 | Fountain equipment of heating |
CN201510207273.8A Active CN106152591B (en) | 2014-09-09 | 2015-04-28 | Fountain storage equipment and control method |
CN201510207235.2A Active CN106152701B (en) | 2014-09-09 | 2015-04-28 | Fountain refrigeration equipment and control method |
CN201510207304.XA Active CN106152630B (en) | 2014-09-09 | 2015-04-28 | Fountain refrigerating plant and control method |
CN201520263937.8U Active CN204787391U (en) | 2014-09-09 | 2015-04-28 | Fountain refrigeration plant |
CN201510219907.1A Active CN106196687B (en) | 2014-09-09 | 2015-05-04 | Spray refrigeration equipment and control method |
CN201510219890.XA Active CN106196830B (en) | 2014-09-09 | 2015-05-04 | Water cooled refrigeration equipment and control method |
CN201520279178.4U Active CN204787392U (en) | 2014-09-09 | 2015-05-04 | Refrigerating plant sprays |
CN201510220152.7A Active CN106196688B (en) | 2014-09-09 | 2015-05-04 | Spray refrigerating plant and control method |
CN201520279359.7U Active CN204787393U (en) | 2014-09-09 | 2015-05-04 | Refrigeration plant sprays |
CN201520279360.XU Active CN204787513U (en) | 2014-09-09 | 2015-05-04 | Water -cooled refrigeration plant |
CN201520360057.2U Active CN204787395U (en) | 2014-09-09 | 2015-05-29 | Fountain refrigeration plant |
CN201510285448.7A Active CN106196708B (en) | 2014-09-09 | 2015-05-29 | Adjustable spraying refrigeration equipment and control method |
CN201510285568.7A Active CN106196689B (en) | 2014-09-09 | 2015-05-29 | Fountain refrigerating plant and control method |
CN201510285611.XA Active CN106196690B (en) | 2014-09-09 | 2015-05-29 | Fountain refrigeration equipment and control method |
CN201520360018.2U Active CN204787403U (en) | 2014-09-09 | 2015-05-29 | Refrigeration plant sprays with adjustable |
CN201520359889.2U Active CN204787394U (en) | 2014-09-09 | 2015-05-29 | Fountain refrigerating plant |
CN201510370432.6A Active CN106196691B (en) | 2014-09-09 | 2015-06-30 | Fountain refrigerating plant and control method |
CN201510370460.8A Active CN106196692B (en) | 2014-09-09 | 2015-06-30 | Spray refrigeration equipment and control method |
CN201510370431.1A Active CN105444460B (en) | 2014-09-09 | 2015-06-30 | Fountain refrigeration equipment and control method |
Family Applications Before (16)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201520263828.6U Active CN204787452U (en) | 2014-09-09 | 2015-04-28 | Fountain refrigerating plant |
CN201520263717.5U Active CN204787389U (en) | 2014-09-09 | 2015-04-28 | Fountain storing equipment |
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CN204787452U (en) * | 2014-09-09 | 2015-11-18 | 青岛海尔特种电冰柜有限公司 | Fountain refrigerating plant |
CN106594914A (en) * | 2016-12-20 | 2017-04-26 | 苏州美高图环境技术有限公司 | Air treatment system |
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CN109632636A (en) * | 2019-01-09 | 2019-04-16 | 南京航空航天大学 | The refrigerating plant and method of high throughput test fiber and resin micro interface performance |
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CN114719466B (en) * | 2022-03-23 | 2024-02-13 | 山西新源谷能源科技有限公司 | Auxiliary heat dissipation device for ground source heat pump |
CN115097878B (en) * | 2022-06-23 | 2023-11-17 | 北京京仪自动化装备技术股份有限公司 | Control method and control system of temperature control system and temperature control system |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2314311Y (en) * | 1997-12-31 | 1999-04-14 | 徐新琦 | Dual-path multi-circulation icefree water cooling preserving apparatus on fishing boat |
CN204787394U (en) * | 2014-09-09 | 2015-11-18 | 青岛海尔特种电冰柜有限公司 | Fountain refrigerating plant |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1537821A (en) * | 1975-01-09 | 1979-01-10 | Mk Refrigeration Ltd | Cooling apparatus |
JP2004257609A (en) * | 2003-02-25 | 2004-09-16 | Sanei Kogyo Kk | Spray type auxiliary cooling device of cooler |
JP2008533426A (en) * | 2005-03-18 | 2008-08-21 | キャリア・コマーシャル・リフリージレーション・インコーポレーテッド | Heat transfer by condensate in a transcritical carbon dioxide refrigeration system |
US8096138B2 (en) * | 2005-10-07 | 2012-01-17 | Stokely-Van Camp, Inc. | Bottle pasteurizer and method |
CN101806528A (en) * | 2009-02-13 | 2010-08-18 | 林崇实 | Small packaged beer and beverage rapid cooling device |
KR20110032611A (en) * | 2009-09-23 | 2011-03-30 | 엘지전자 주식회사 | Refrigerator |
DE102010021742A1 (en) * | 2010-05-20 | 2011-11-24 | Ralf Schneider Holding Gmbh | Device for drying bulk material in at least one storage container |
CN202630498U (en) * | 2012-04-18 | 2012-12-26 | 广东志高空调有限公司 | Air-conditioner with functions of ultrasonic defrosting and cleaning |
-
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Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2314311Y (en) * | 1997-12-31 | 1999-04-14 | 徐新琦 | Dual-path multi-circulation icefree water cooling preserving apparatus on fishing boat |
CN204787394U (en) * | 2014-09-09 | 2015-11-18 | 青岛海尔特种电冰柜有限公司 | Fountain refrigerating plant |
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