CN109701670A - Program-controlled formula precision growth cabinet - Google Patents

Program-controlled formula precision growth cabinet Download PDF

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Publication number
CN109701670A
CN109701670A CN201910103286.9A CN201910103286A CN109701670A CN 109701670 A CN109701670 A CN 109701670A CN 201910103286 A CN201910103286 A CN 201910103286A CN 109701670 A CN109701670 A CN 109701670A
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CN
China
Prior art keywords
gas
sink
filter
program
growth cabinet
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CN201910103286.9A
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Chinese (zh)
Inventor
杨雁梅
柯钢
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BEIJING KOOLAND SCIENCE AND TECHNOLOGY Co Ltd
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BEIJING KOOLAND SCIENCE AND TECHNOLOGY Co Ltd
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Priority to CN201910103286.9A priority Critical patent/CN109701670A/en
Publication of CN109701670A publication Critical patent/CN109701670A/en
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Abstract

The present invention relates to artificial environment analogue technique fields, more particularly to a kind of program-controlled formula precision growth cabinet, it include: cabinet, the cabinet is multilayered structure, it from top to bottom successively include experiment layer, interlayer and mechanical floor, partition is equipped between the experiment layer and the interlayer, the interlayer is channel structure, includes first passage and second channel;Simulation system, the simulation system is arranged in the interlayer and the mechanical floor, for adjusting the internal environment of growth cabinet;Stored program controlled, the stored program controlled are arranged in the mechanical floor, for detecting the environmental data in growth cabinet and controlling the simulation system.The present invention uses channel structure, when efficiently solving the low dew point continuous operation of low temperature caused by temperature and humidity fluctuation problem, effectively improve climate box Temperature and Humidity Control precision, cooperate stored program controlled, have the advantages that energy saving, economical and practical, wide scope, height are accurate.

Description

Program-controlled formula precision growth cabinet
Technical field
The present invention relates to artificial environment analogue technique fields, and in particular to a kind of program-controlled formula precision growth cabinet.
Background technique
Artificial environment simulator is not depend on outdoor weather variation, can manual control illumination, temperature, humidity, air pressure, wind Artificial climate environment in the confined space of the factors such as speed, gas componant can simulate different natural climate environment, and can contract The period of short research, it has also become a kind of critical facility of scientific research, teaching and production is led in botany, zoology, electromechanical instrument etc. There is extensive purposes in domain.With the continuous development of science and technology, environment simulator is led in industry, agricultural, aerospace etc. Domain is all widely used.Especially sustainable agriculture strategy is developed using green agriculture as this country in countries in the world Today, even more the promotion and popularization to artificial environment simulator bring unprecedented opportunities.
The one kind of growth cabinet as manual simulation's device can satisfy all kinds of property tests, simultaneously because body Product is small, also has the characteristics that convenient transportation, with short production cycle, operating cost is low.
Temperature and humidity is the important indicator of climatic simulation, and existing growth cabinet generallys use compression refrigeration and freeze drying side Formula certainly will lead to the frosting of system heat exchanger surface, longtime running, which will lead to, is if carrying out low temperature/low dew point operating condition operation for a long time Temperature control/control wet performance decline of uniting is even out of control.Existing high temperature (>5 DEG C) climate box does not provide the simulation of low dew point (<5 DEG C) generally Function, to guarantee the continuous operation of system.And low temperature (< 0 DEG C) climate box refrigeration system is generally equipped with defrosting system, but system The big ups and downs in the temperature inside the box and humidity short time are often led to during defrosting.
In addition, climate box currently on the market does not have low CO generally2Concentration of analog function is unable to satisfy low CO2Concentration examination Test demand.
Simultaneously as space is smaller in case, it is unable to satisfy the installation of certain examination measuring instruments, and existing climate box is logical Frequently with insulating plate structure, even if being furnished with observation window, but visibility is not able to satisfy experimental observation testing requirement still.
Therefore, need to develop a kind of multifunctional accurate climate box, fully consider climate box economy and various environment moulds The coupling of quasi- parameter is controlled to meet wide scope environmental simulation demand, while improving climate box visibility.
Summary of the invention
The purpose of the present invention is to provide a kind of program-controlled formula precision growth cabinets, using channel structure, effectively Temperature and humidity fluctuation problem caused by when solving the low dew point continuous operation of low temperature, effectively improves climate box Temperature and Humidity Control precision, matches Stored program controlled is closed, has the advantages that energy saving, economical and practical, wide scope, height are accurate.
To achieve the goals above, the invention provides the following technical scheme:
The present invention provides a kind of program-controlled formula precision growth cabinet, and the program-controlled formula precision growth cabinet includes:
Cabinet, the cabinet are multilayered structure, from top to bottom successively include experiment layer, interlayer and mechanical floor, the experiment Partition is equipped between layer and the interlayer, the interlayer is channel structure, includes first passage and second channel;
Simulation system, the simulation system is arranged in the interlayer and the mechanical floor, for adjusting growth cabinet Internal environment;
Stored program controlled, the stored program controlled are arranged in the mechanical floor, for detecting the environmental data in growth cabinet And the simulation system is controlled.
In above-mentioned program-controlled formula precision growth cabinet, preferably, the simulation system includes refrigeration Dehumidification system, the refrigerant dehumidification system include:
Compressor unit, the compressor unit includes one or more compressors in parallel, for exporting high pressure gas State refrigerant;
Oil eliminator, the input terminal of the oil eliminator is connect with the output end of the compressor, for separating high pressure gas Oil in state refrigerant;
Condenser, the input terminal of the condenser are connect with the output end of the oil eliminator, are used for high-pressure gaseous system Cryogen is condensed into high pressure liquid refrigerant;
Liquid storage device, the output end of the condenser is arranged in the liquid storage device, for storing high pressure liquid refrigerant;
Device for drying and filtering, the output end of the liquid storage device is arranged in the device for drying and filtering, for removing high-pressure liquid system Moisture in cryogen;
First high-pressure ball valve, the output end of the device for drying and filtering is arranged in first high-pressure ball valve, for controlling height Press the flow of liquid refrigerant;
Vaporising device, the vaporising device include the first evaporation element and the second evaporation element, first evaporation element With second evaporation element and be connected in the first high-pressure ball valve outlet end, the vaporising device is used for high pressure liquid refrigerant Evaporation;
The output end of the vaporising device is arranged in gas-liquid separator, the gas-liquid separator, is used for liquid refrigerant It is separated with gaseous refrigerant;
Suction filter, the input terminal and output end of the suction filter are respectively connected to the gas-liquid separator and institute Compressor unit is stated, circulation loop is formed, the suction filter is used to remove the impurity in gaseous refrigerant;
Preferably, liquid-sighting glass is additionally provided between the device for drying and filtering and first high-pressure ball valve, the liquid-sighting glass is used In the circulation status of observation high pressure liquid refrigerant;
More preferably, it is additionally provided with the second high-pressure ball valve between the vaporising device and the gas-liquid separator, described second High-pressure ball valve is used to control the flow of gaseous refrigerant.
In above-mentioned program-controlled formula precision growth cabinet, preferably, first evaporation element and described Second evaporation element is separately positioned in the first passage and the second channel, and first evaporation element includes successively phase First filter, first throttle valve and the first evaporator even, second evaporation element include the second filtering being sequentially connected The output end of device, second throttle and the second evaporator, first evaporator and second evaporator is connected to described Second high-pressure ball valve.
In above-mentioned program-controlled formula precision growth cabinet, preferably, first evaporation element further includes First circulation blower, second evaporation element further include second circulation blower, and the first circulation blower and described second follows Ring blower is respectively used to the first evaporator and the second evaporator conveying wind;
Preferably, the first passage is equipped with the first return air inlet, and the second channel is equipped with the second return air inlet.
In above-mentioned program-controlled formula precision growth cabinet, preferably, the simulation system further includes humidification System, the humidification system include:
Water tank, the water tank is interior to be equipped with third filter, and the third filter was used for the impurity in drainage;
Water supply pump, the water supply pump are arranged in water tank, for the water in water tank to be conveyed to atomization dress by liquid supply pipe It sets;
Atomising device, the atomising device are arranged above water tank, the water atomization for carrying out water supply pump conveying;
Water container, the water container are arranged below vaporising device, for collecting since the vaporising device absorbs heat And the condensed water generated, condensed water collected by the water container convey feed-tank by pipeline and the third filter;
Preferably, liquidometer, water supplement port and drain valve are additionally provided in the water tank;
More preferably, the water container includes the first drip tray and the second drip tray, and the first drip tray setting exists Below first evaporator, second drip tray is arranged below the second evaporator, and first drip tray and described second connects Condensed water collected by water pond passes through pipeline and third filter conveying feed-tank.
In above-mentioned program-controlled formula precision growth cabinet, preferably, the atomising device includes the first water Slot, the first atomising head, the second sink, the second atomising head and balance pipe, first sink and second sink are arranged at Above the water tank and it is in same level, first sink and second sink lower part are connected by the balance pipe Logical, the first sink setting is in the first passage, and the second sink setting is in the second channel, first atomization Head is arranged in first sink, and second atomising head is arranged in second sink;
Preferably, first sink top is equipped with overflow pipe, and the overflow pipe other end is connected to the third filtering Device, the liquid supply pipe are connected to the top of first sink;
More preferably, the bottom of first sink and second sink passes through pipeline and the drain valve is connected to Third filter.
In above-mentioned program-controlled formula precision growth cabinet, preferably, the simulation system further includes CO2It is de- Except system, the CO2Removing system includes:
Air pump, the air pump are equipped with inlet end and exhaust end, for from inlet end sucking gas, from the exhaust end Gas is discharged;
Air inlet, the air inlet setting is in the experiment layer, for sucking gas from the experiment layer;
CO2Removing means, the CO2The input terminal of removing means is connected to by pipeline with the air inlet, output end passes through Pipeline connection is to the air pump inlet end, for removing CO2Gas;
Exhaust outlet, in the experiment layer, the exhaust outlet passes through pipeline connection to air pump exhaust end for the exhaust outlet setting;
Preferably, the CO2Pipeline between removing means and the air pump inlet end is equipped with the 4th filter and the One muffler, the pipeline between the exhaust outlet and the air pump exhaust end are equipped with the second muffler, the 4th filter For filtering the impurity from the gas that it passes through.
In above-mentioned program-controlled formula precision growth cabinet, preferably, the simulation system further includes CO2It mends Gas system, the CO2Air compensating system includes:
Gas source, the gas source is for providing CO2Gas;
Pressure reducing valve, the pressure reducing valve setting is in the source output end, for reducing the CO of gas source output2The gas of gas Pressure;
5th filter, the 5th filter are arranged in the pressure reducing valve output end, for filtering CO2It is miscellaneous in gas Matter;
Solenoid valve, the solenoid valve are arranged in the 5th filter output end, for controlling CO2Gas transfer pipeline On-off;
Current limiter, the current limiter are arranged in the solenoid valve output end, for controlling CO2The feed flow of gas;
Gas supplementing opening, the gas supplementing opening are arranged in the experiment layer, pass through pipeline connection to the current limiter output end, be used for CO is conveyed to the experiment layer2Gas.
In above-mentioned program-controlled formula precision growth cabinet, preferably, the simulation system further includes heating System, the heating system include primary heater and secondary heater, and the primary heater is arranged in the first passage, The secondary heater is arranged in the second channel;
Preferably, the program-controlled formula precision growth cabinet further includes having light filling equipment and supervision equipment, the experiment Layer is transparent hood configuration, and the light filling equipment and supervision equipment setting are outside experiment layer.
In above-mentioned program-controlled formula precision growth cabinet, preferably, the stored program controlled includes:
Controller, the controller export control signal for carrying out processing analysis to the signal of acquisition;
Signal pickup assembly, the signal pickup assembly are connected to the signal input part of the controller, including temperature and humidity Sensor, gas concentration sensor, refrigerant dehumidification system detect signal, heating system detects signal, air compensating system detects signal, Degassing system detection signal matches power detection signal;
Signal control device, the signal control device are connected to the signal output end of the controller, including refrigeration is removed Wet system controller, circulating fan driver, heater controller, humidification system controller, electromagnetic valve driver, air pump driving Device;
More preferably, the stored program controlled further includes touch screen, and the touch screen is connect with controller.
Compared with the immediate prior art, technical solution provided by the invention has following excellent effect:
The present invention provides a kind of program-controlled formula precision growth cabinet, by the way that channel structure form, corollary system is arranged Design, can be realized low temperature/low dew point continuous operation, is precisely controlled;Refrigerant dehumidification system base of evaporator configures water-collecting tray and receives Collect condensed water, retain header tank storage under the effect of gravity, after filtering by filter, reduces system and humidify water consumption, subtract simultaneously Demand is discharged in few condensed water, facilitates climate box is mobile to use;Humidification system be equipped with draining and water supply structure, low humidity operating condition can Effectively moisture is avoided to enter in climate box, can quickly supplement air moisture in high wet cooling condition;System configuration CO2Removing system, It can be realized low concentration CO2Regulatory function meets more experimental study demands;Climate box matched with vacuum cloche, light filling equipment It is external, it can be effectively reduced efficiency and improve trial zone utilization rate;The present invention is a kind of environmentally friendly, economical and practical, high accurately may be used Program control type precision growth cabinet.
Detailed description of the invention
The accompanying drawings constituting a part of this application is used to provide further understanding of the present invention, and of the invention shows Examples and descriptions thereof are used to explain the present invention for meaning property, does not constitute improper limitations of the present invention.Wherein:
Fig. 1 is the program-controlled formula precision growth cabinet structural schematic diagram of the embodiment of the present invention;
Fig. 2 is the interlayer overlooking structure diagram of the program-controlled formula precision growth cabinet of the embodiment of the present invention;
Fig. 3 is the refrigerant dehumidification system connection relationship signal of the program-controlled formula precision growth cabinet of the embodiment of the present invention Figure;
Fig. 4 is the humidification system connection relationship diagram of the program-controlled formula precision growth cabinet of the embodiment of the present invention;
Fig. 5 is the CO of the program-controlled formula precision growth cabinet of the embodiment of the present invention2Removing system connection relationship diagram;
Fig. 6 is the CO of the program-controlled formula precision growth cabinet of the embodiment of the present invention2Air compensating system connection relationship diagram;
Fig. 7 is that the interlayer of the program-controlled formula precision growth cabinet of the embodiment of the present invention is laid out structural schematic diagram;
Fig. 8 is the stored program controlled connection relationship diagram of the program-controlled formula precision growth cabinet of the embodiment of the present invention;
Fig. 9 is the light filling equipment and audiomonitor layout signal of the program-controlled formula precision growth cabinet of the embodiment of the present invention Figure.
Description of symbols:
101- cabinet;102- tests layer;103- partition;104- interlayer;105- mechanical floor;106- first passage;107- Two channels;
1- compressor;2- oil eliminator;3- condenser;4- liquid storage device;5- device for drying and filtering;
6- liquid-sighting glass;The first high-pressure ball valve of 7-;8- first filter;The second filter of 9-;10- first throttle valve;
11- second throttle;The first evaporator of 12-;The second evaporator of 13-;The second high-pressure ball valve of 14-;15- gas-liquid separation Device;
16- suction filter;171- first circulation blower;172- second circulation blower;18- water tank;19- water supply pump;20- Liquid supply pipe;
21- overflow pipe;The first sink of 22-;The second sink of 23-;The first atomizer of 24-;The second atomizer of 25-;
26- balance pipe;27- drain valve;The first drip tray of 28-;The second drip tray of 29-;30- third filter;
31- air pump;The first muffler of 32-;The 4th filter of 33-;34-CO2Removing means;35- air inlet;
36- exhaust outlet;The second muffler of 37-;38- gas source;39- pressure reducing valve;The 5th filter of 40-;
41- solenoid valve;42- current limiter;43- gas supplementing opening;44- primary heater;45- secondary heater;
The first return air inlet of 46-;The second return air inlet of 47-;48- Temperature Humidity Sensor;49- gas concentration sensor;50- refrigeration Dehumidification system detects signal;
51- heating system detects signal;52- air compensating system detects signal;53- degassing system detection signal;54- matches electric-examination Survey signal;55- refrigerant dehumidification system controller;
56- circulating fan driver;57- heater controller;58- humidification system controller;59- electromagnetic valve driver; 60- air pump driver;
61- touch screen;62- controller;63- light filling equipment;64- supervision equipment.
Specific embodiment
The present invention will be described in detail below with reference to the accompanying drawings and embodiments.It should be noted that in the feelings not conflicted Under condition, the features in the embodiments and the embodiments of the present application be can be combined with each other.
In the description of the present invention, term " longitudinal direction ", " transverse direction ", "upper", "lower", "front", "rear", "left", "right", " perpendicular Directly ", the orientation or positional relationship of the instructions such as "horizontal", "top", "bottom" is to be based on the orientation or positional relationship shown in the drawings, and is only For ease of description the present invention rather than require the present invention that must be constructed and operated in a specific orientation, therefore should not be understood as pair Limitation of the invention.Term used in the present invention " connected ", " connection " shall be understood in a broad sense, for example, it may be fixedly connected, It may be a detachable connection;It can be directly connected, can also be indirectly connected by intermediate member, for the common of this field For technical staff, the concrete meaning of above-mentioned term can be understood as the case may be.
As shown in Figure 1 and Figure 2, according to an embodiment of the invention, providing a kind of program-controlled formula precision growth cabinet, packet Include: cabinet 101, cabinet 101 are multilayered structure, from top to bottom successively include testing layer 102, interlayer 104 and mechanical floor 105, real It tests and is equipped with partition 103 between layer 102 and interlayer 104, interlayer 104 is channel structure, includes that first passage 106 and second are logical Road 107;Simulation system, simulation system is arranged in interlayer 104 and mechanical floor 105, for adjusting the inner loop of growth cabinet Border;Stored program controlled, stored program controlled setting is in mechanical floor 105, for detecting the environmental data in growth cabinet and being to simulation System is controlled.The various environment of growth cabinet are simulated in experiment layer 102, binary channels, simulation system institute are set in interlayer 104 The equipment setting needed realizes the rotation defrost of low temperature, low dew point operating condition by twin-channel switching, it is ensured that be in mechanical floor 105 Temperature and humidity stability during system defrost.Refrigerated dehumidification is arranged in each channel, heating, heating, circulated air end are set It is standby.Interlayer overlooking structure diagram as shown in Figure 2, first passage 106 and second channel 107 be in interlayer 104 it is horizontal simultaneously Row arrangement.
As shown in figure 3, preferably, simulation system includes in above-mentioned program-controlled formula precision growth cabinet There is refrigerant dehumidification system, refrigerant dehumidification system includes: compressor Unit 1, and compressor Unit 1 includes one or more in parallel Compressor 1, for exporting high-pressure gaseous refrigerant;Oil eliminator 2, the input terminal of oil eliminator 2 and the output end of compressor 1 connect It connects, for separating the oil in high-pressure gaseous refrigerant;Condenser 3, the input terminal of condenser 3 and the output end of oil eliminator 2 connect It connects, for high-pressure gaseous refrigerant to be condensed into high pressure liquid refrigerant;The defeated of condenser 3 is arranged in liquid storage device 4, liquid storage device 4 Outlet, for storing high pressure liquid refrigerant;Device for drying and filtering 5, device for drying and filtering 5 are arranged in the output end of liquid storage device 4, are used for Remove the moisture in high pressure liquid refrigerant;The output of device for drying and filtering 5 is arranged in first high-pressure ball valve 7, the first high-pressure ball valve 7 End, for controlling the flow of high pressure liquid refrigerant;Vaporising device, vaporising device include that the first evaporation element and the second evaporation are single Member, the first evaporation element and the second evaporation element are simultaneously connected in 7 outlet end of the first high-pressure ball valve, and vaporising device is used for high pressure liquid The evaporation of state refrigerant;The output end of vaporising device is arranged in gas-liquid separator 15, gas-liquid separator 15, is used for liquid refrigerant It is separated with gaseous refrigerant;Suction filter 16, the input terminal and output end of suction filter 16 are respectively connected to gas-liquid separation Device 15 and compressor Unit 1, form circulation loop, and suction filter 16 is used to remove the impurity in gaseous refrigerant;It is dried Liquid-sighting glass 6 is additionally provided between filter 5 and the first high-pressure ball valve 7, liquid-sighting glass 6 is used to observe the circulation shape of high pressure liquid refrigerant State;The second high-pressure ball valve 14 is additionally provided between vaporising device and gas-liquid separator 15, the second high-pressure ball valve 14 is for controlling gaseous state The flow of refrigerant.
In above-mentioned program-controlled formula precision growth cabinet, preferably, the first evaporation element and the second evaporation Unit is separately positioned in first passage 106 and second channel 107, and the first evaporation element includes the first filter being sequentially connected 8, first throttle valve 10 and the first evaporator 12, the second evaporation element include the second filter 9 being sequentially connected, second throttle 11 and second evaporator 13, the output end of the first evaporator 12 and the second evaporator 13 is connected to the second high-pressure ball valve 14.
In above-mentioned program-controlled formula precision growth cabinet, preferably, the first evaporation element further includes first Circulating fan 171, the second evaporation element further include second circulation blower 172, first circulation blower 171 and second circulation blower 172 are respectively used to the first evaporator 12 and the second evaporator 13 conveying wind.First passage 106 is equipped with the first return air inlet 46, the Two channels 107 are equipped with the second return air inlet 47.
After one or more 1 parallel connections of compressor successively with oil eliminator 2, condenser 3, liquid storage device 4, device for drying and filtering 5, view Liquid border is connected with the first high-pressure ball valve 7.First filter 8 and 9 parallel connection of the second filter and pipeline phase after the first high-pressure ball valve 7 Even.First filter 8, first throttle valve 10,12 pipeline of the first evaporator are sequentially connected as 106 refrigeration system of first passage end End;Second filter 9, second throttle 11,13 pipeline of the second evaporator are sequentially connected as 107 refrigeration system of second channel end End;First evaporator 12 is connected with after 13 parallel connection of the second evaporator with the second high-pressure ball valve 14;Second high-pressure ball valve 14 successively with Gas-liquid separator 15, suction filter 16, compressor 1 are connected;2 oil pipe of oil eliminator is connected with 1 muffler of compressor.First is logical Road 106 configures first circulation blower 171, second channel 107 configures second circulation blower 172.
End and second channel 107 end of freezing of freezing of first passage 106 can be run or independent operating simultaneously.The When one channel 106 is run, first circulation blower 171 is run by air quantity is determined;When second channel 107 is run, second circulation blower 172 It is run by specified air quantity.First circulation blower 171 and second circulation blower 172 have independent air quantity regulating power.
When 106 cooling condition of first passage, first throttle valve 10 and first circulation blower 171 are program-controlled by cooling condition receiving System control;When second channel 107 removes wet cooling condition, second throttle 11 and second circulation blower 172 receive journey by except wet cooling condition The control of control system.
When 106 defrost of first passage, the refrigeration of first passage 106 end stops working, and first circulation blower 171 stops work Make, nature defrost is used for worst hot case.It, can also mating hot gas defrosting or electrochemical cream if climate box is chronically at worst cold case System is evaporated device wheel and changes defrost.
As shown in figure 4, preferably, simulation system is also wrapped in above-mentioned program-controlled formula precision growth cabinet Humidification system is included, humidification system includes: water tank 18, third filter 30 is equipped in water tank 18, third filter 30 is for filtering Impurity in water;Water supply pump 19, water supply pump 19 are arranged in water tank 18, for conveying the water in water tank 18 by liquid supply pipe 20 To atomising device;Atomising device, atomising device are arranged above water tank 18, the water atomization for carrying out the conveying of water supply pump 19;It connects Water installations, water container are arranged below vaporising device, for collecting due to the condensed water that vaporising device absorbs heat and generates, water receiving Condensed water collected by device conveys feed-tank 18 by pipeline and third filter 30;It is additionally provided with liquidometer in water tank 18, mends The mouth of a river and drain valve 27;Water container includes the first drip tray 28 and the second drip tray 29, and the first drip tray 28 is arranged first 12 lower section of evaporator, the second drip tray 29 are arranged below the second evaporator 13,29 institute of the first drip tray 28 and the second drip tray The condensed water of collection passes through pipeline and third filter 30 conveys feed-tank 18.
In above-mentioned program-controlled formula precision growth cabinet, preferably, atomising device include the first sink 22, First atomising head, the second sink 23, the second atomising head and balance pipe 26, the first sink 22 and the second sink 23 are arranged at water tank Above 18 and it is in same level, the first sink 22 and 23 lower part of the second sink pass through balance pipe 26 and be connected to, the first sink 22 Setting is arranged in the first sink 22 in first passage 106, the setting of the second sink 23 in second channel 107, the first atomising head, and second Atomising head is arranged in the second sink 23;First sink, 22 top is equipped with overflow pipe 21, and 21 other end of overflow pipe is connected to third mistake Filter 30, liquid supply pipe 20 are connected to the top of the first sink 22;The bottom of first sink 22 and the second sink 23 passes through pipeline Third filter 30 is connected to drain valve 27.
Water tank 18 contains liquidometer, water supplement port, drain valve 27 etc., and is equipped with third filter device, and water supply pump 19 is mounted on In water tank 18, water supply pump 19 is connected by liquid supply pipe 20 with the first sink 22;First sink 22 passes through overflow pipe 21 and third mistake Device is filtered to be connected;First sink 22 is connected by balance pipe 26 with the second sink 23, and linker is formed.First sink 22 and second The discharge outlet of sink 23 after pipeline parallel connection with drain valve 27 by being connected.First atomising head is mounted in the first sink 22, and second Atomising head is mounted in the second sink 23;First sink 22 and the first atomising head are that first passage 106 humidifies end;Second sink 23 and second atomising head be second channel 107 humidify end.
First drip tray 28 and the second drip tray 29 are connected by discharge pipe line with third filter device, can be to system Condensed water is recycled.First drip tray 28 is the condensate drain pan of the first evaporator 12, is located in first passage 106;The Two drip trays 29 are the condensate drain pan of the second evaporator 13, are located in second channel 107.
As shown in figure 5, preferably, simulation system is also wrapped in above-mentioned program-controlled formula precision growth cabinet Include CO2Removing system, CO2Removing system includes: air pump 31, and air pump 31 is equipped with inlet end and exhaust end, for sucking from inlet end Gas is discharged from exhaust end in gas;Air inlet 35, the setting of air inlet 35 is in experiment layer 102, for sucking gas from experiment layer 102 Body;CO2 removing means 34, the input terminal of CO2 removing means 34 is connected to by pipeline with air inlet 35, output end is connected by pipeline 31 inlet end of air pump is passed to, for removing CO2Gas;Exhaust outlet 36, for the setting of exhaust outlet 36 in experiment layer 102, exhaust outlet 36 is logical Pipeline connection is crossed to 31 exhaust end of air pump;Pipeline between 31 inlet end of CO2 removing means 34 and air pump is equipped with the 4th filtering Device 33 and the first muffler 32, the pipeline between 31 exhaust end of exhaust outlet 36 and air pump are equipped with the second muffler 37, the 4th mistake Filter 33 is for filtering the impurity from the gas that it passes through.31 exhaust end of air pump is connected with the second muffler 37, and second disappears Sound device 37 is connected by pipeline with exhaust outlet 36.31 inlet end of air pump successively with the first muffler 32, the 4th filter 33, CO2 Removing means 34, air inlet 35 are connected.Exhaust outlet 36 and air inlet 35 are located on partition 103, communicate with experiment layer 102.At this In embodiment, CO2 removing means 34 will handle the CO in air2Absorption is captured, to realize removing, can be inhaled using known The chemical reaction for receiving carbon dioxide absorbs the carbon dioxide in gas by CO2 removing means 34, such as some bases Substance.
As shown in fig. 6, preferably, simulation system is also wrapped in above-mentioned program-controlled formula precision growth cabinet CO2 air compensating system is included, CO2 air compensating system includes: gas source 38, and gas source 38 is for providing CO2 gas;Pressure reducing valve 39, pressure reducing valve 39 Setting is in 38 output end of gas source, for reducing the air pressure for the CO2 gas that gas source 38 exports;5th filter 40, the 5th filter 40 are arranged in 39 output end of pressure reducing valve, for filtering CO2Impurity in gas;Solenoid valve 41, solenoid valve 41 are arranged in the 5th mistake 40 output end of filter, for controlling CO2The on-off of gas transfer pipeline;Current limiter 42, the setting of current limiter 42 are defeated in solenoid valve 41 Outlet, for controlling CO2The feed flow of gas;Gas supplementing opening 43, the setting of gas supplementing opening 43 are testing layer 102, are passing through pipeline connection To 42 output end of current limiter, for conveying CO to experiment layer 1022Gas.Gas source 38 by pipeline successively with pressure reducing valve 39, filtering Device, solenoid valve 41, current limiter 42, gas supplementing opening 43 are connected.Gas supplementing opening 43 is located on partition 103, communicates with experiment layer 102;Gas Source 38 may be selected to be CO2Gas cylinder.
As shown in fig. 7, preferably, simulation system is also wrapped in above-mentioned program-controlled formula precision growth cabinet Heating system is included, heating system includes primary heater 44 and secondary heater 45, and primary heater 44 is arranged in first passage 106, secondary heater 45 is arranged in second channel 107.In first passage 106 and second channel 107: in first passage 106 It is sequentially installed with first circulation blower 171, the first sink 22, primary heater 44, the first evaporator 12 and the first return air inlet 46; Second circulation blower 172, the second sink 23, secondary heater 45,13 and of the second evaporator are sequentially installed in second channel 107 Second return air inlet 47;First atomising head is mounted in the first sink 22, and the second atomising head is mounted in the second sink 23;First connects Water pond 28 is arranged below the first evaporator 12, and the second drip tray 29 is arranged below the second evaporator 13.
As shown in figure 9, program-controlled formula precision growth cabinet further includes having light filling equipment 63 and supervision equipment 64, layer is tested 102 be transparent hood configuration, and light filling equipment 63 and the setting of supervision equipment 64 are outside experiment layer 102.Cabinet 101 tests layer 102 It is made of vacuum glass cover, cabinet 101 can exterior light filling equipment 63 and supervision equipment 64 except remaining unexpected side of door side.Case Body 101 tests layer 102 and uses vacuum glass cover, can reduce leakage heat by with translucency.Light filling equipment 63 can be according to test Part demand selects different light sources, at the same be not take up experiment layer 102 in the useful space, reduce experiment layer 102 in load and Space requirement amount.The installation site of supervision equipment 64 is determined that backlight is not arranged as far as possible with light filling equipment 63 by test demand.
As shown in figure 8, stored program controlled includes controller, the controller 61 is used to carry out the signal of acquisition processing point Analysis, and export control signal;Signal pickup assembly, the signal pickup assembly are connected to the signal input of the controller 61 End, including Temperature Humidity Sensor 48, gas concentration sensor 49, refrigerant dehumidification system detection signal 50, heating system detection letter Numbers 51, air compensating system detection signal 52, degassing system detection signal 53, match power detection signal 54;Signal control device, the letter Number control device is connected to the signal output end of the controller 61, including refrigerant dehumidification system controller 55, circulating fan drive Dynamic device 56, heater controller 57, humidification system controller 58, electromagnetic valve driver 59, air pump driver 60.
In signal input part: Temperature Humidity Sensor 48 and gas concentration sensor 49, which are arranged in growth cabinet, is suitable for Position monitors the temperature and humidity of its local environment and the concentration of some gases;The refrigerant dehumidification system detection characterization refrigeration of signal 50 is removed The state of wet system, the operating status including each equipment of refrigerant dehumidification system (lead to by shutdown, refrigeration, dehumidifying, refrigerated dehumidification, defrosting Road selects situation etc., and these are generated by 61 algorithm of controller), further include whether the faulty signal (related transducer that system carries Device or detector generate), opening of device situation (61 algorithm of equipment feedback signal or controller) etc.;Heating system detects signal 51 Characterize the operating status, including channel selecting (61 algorithm of controller), temperature protection signal (overheat protector) etc. of heater); Air compensating system detects the vapour source supply state (pressure sensor) that signal 52 characterizes air compensating system;Deaerate 53 table of system detection signal Sign degassing pump 31 operating status feedback signals (whether system normally starts), system start and stop state (61 algorithm of controller);Distribution Detect signal 54 by phase sequence relay detection, can also mating electric current, voltage sensor, be mainly used for judging distribution whether just Often.
In signal control terminal: refrigerant dehumidification system controller 55 controls the equipment of refrigerant dehumidification system, and control is set Standby includes compressor 1, throttle valve (control of mechanical or analog output), condenser fan start and stop or PWM output.System carries phase The signals such as the feedback transducer, including pressure, temperature of control are closed, such as condenser fan passes through condensation pressure regulation loading capacity;It follows The control of ring fan driver 56 exports circulating fan voltage Power Regulation;Heater controller 57 carries out PWM duty cycle to heater Output control;Humidification system controller 58 controls the equipment of humidification system, control equipment include drain solenoid valve 41 after Electric appliance, 19 relay of water supply pump, atomising head relay etc..Specific control method:
Humidify operating condition: humidification system process is as shown in Figure 4.When controller 61 determines that simulation system needs to provide humidification, System starts humidification function.Drain valve 27 is closed, and water supply pump 19 works, and the water in water tank 18 is pumped into the first sink through water supplying pipe 22, the water in the first sink 22 enters the second sink 23 through balance pipe 26, when hypervolia, returns to water tank through overflow pipe 21 18。
Humidification function starts simultaneously, when controller 61 determines that first passage 106 works, the work of the first atomizer 24, when When determining that second channel 107 works, humidification purpose is realized in the work of the second atomizer 25.First passage 106 and second channel 107 Can run simultaneously can also be subject to the judgement of controller 61 with isolated operation.
When controller 61 determines humidification function revocation, water supply pump 19 stops working, and drain valve 27 is opened, and empties the first sink 22 and the second water in sink 23.
Water tank 18 is equipped with third filter 30, the condensed water of recycling and unused humidification water, returns to water after filtering Case 18 is spare.Water tank 18 is equipped with water supplement port, is when recycle-water is not able to satisfy test demand, carries out artificial recharge.It is set in water tank 18 There is water level switch, when water shortage in water tank 18, issues alarm signal to controller 61, controller 61 issues the protection of water supply pump 19 and stops It only instructs, and the display alarm information on touch screen 61.
Preferably, the stored program controlled further includes touch screen 61, and the touch screen 61 is connect with controller 61, is used Human-computer interaction is carried out between operator and controller 61.
At work, the processing wind in climate box is in first circulation blower for program-controlled formula precision growth cabinet of the invention 171 or second circulation blower 172 swabbing action under respectively successively pass through the first return air inlet 46 or the second return air inlet 47, through first 13 refrigeration/dehumidification of evaporator 12 or the second evaporator is heated through primary heater 44 or secondary heater 45, through the first sink 22 Or second sink 23 humidification be sent into test block.
First passage 106 and second channel 107 can run simultaneously with independent operating or rotation run.Controller 61 according to testing results, by the procedure selection channel load condition of setting, and each system of coordinated control, it is ensured that tank test area Temperature and humidity is precisely controlled.
Target component can be arranged in operator on touch screen 61, and starts/halt system operation.User can choose temperature The independent regulation of degree or temperature and humidity combined regulating.
Controller 61 by signal wire or communication line to Temperature and Humidity signal, refrigerant dehumidification system detect signal 50, Heating system detects signal 51, carries out sampling and analysis of signal with power detection signal 54.Starting or limitation needed for decision-making system Function, by signal wire or communication line to refrigerant dehumidification system, circulating fan driver 56, heater controller 57, humidification system System etc. carries out Collaborative Control.
When work, it generally will appear following several operating conditions:
Refrigeration/dehumidification operating condition: when controller 61 determines that simulation system needs to provide refrigeration but do not need dehumidification function, it is System starting cooling condition;When controller 61 determines that simulation system needs to provide dehumidification function, stored program controlled starts desiccant cooling Operating condition.
Refrigeration system process is as shown in figure 3, refrigeration system compressor 1 and condenser 3 receive stored program controlled control.
When 106 cooling condition of first passage, first throttle valve 10 and first circulation blower 171 are program-controlled by cooling condition receiving System control;When first passage 106 removes wet cooling condition, first throttle valve 10 and first circulation blower 171 receive journey by except wet cooling condition The control of control system.When 106 defrost of first passage, the refrigeration of first passage 106 end stops working, and first circulation blower 171 stops Work uses nature defrost for worst hot case.It, can also mating hot gas defrosting or electrification if climate box is chronically at worst cold case Defrosting system is evaporated device wheel and changes defrost.
107 operating mode of second channel is similar to first passage 106, and controller 61 coordinates 106 He of first passage when defrosting Second channel 107, which enters, forces rotation defrost pattern, reduces the temperature and humidity fluctuation in trial zone, improves control precision.Defrost After, refrigeration system enters preset operational mode.
During refrigeration/dehumidification and defrosting, the first drip tray 28 of 13 bottom of the first evaporator 12 or the second evaporator or Second drip tray 29 carries out the condensed water of collection by discharge pipe line after the filtering of third filter 30 to system condensing water Recycling.
Heating condition: when controller 61 determines that simulation system needs to provide heating, stored program controlled starts heating condition.
When 106 heating condition of first passage, if not removing wet cooling condition parallel, first circulation blower 171 is connect by heating condition It is controlled by stored program controlled;If having parallel except wet cooling condition, first circulation blower 171 receives stored program controlled control by except wet cooling condition.The One heater 44 receives stored program controlled control by heating condition.
Humidify operating condition: humidification system process is as shown in Figure 4.When controller 61 determines that simulation system needs to provide humidification, System starts humidification function.Drain valve 27 is closed, and water supply pump 19 works, and the water in water tank 18 is pumped into the first water through liquid supply pipe 20 Slot 22, the water in the first sink 22 enters the second sink 23 through balance pipe 26, when hypervolia, through overflow pipe 21 through third mistake Filter 30 returns to water tank 18 after filtering.
Humidification function starts simultaneously, when controller 61 determines that first passage 106 works, the first atomising head work, when sentencing When determining the work of second channel 107, humidification purpose is realized in the work of the second atomising head.First passage 106 and second channel 107 can be with Operation simultaneously can also be subject to the judgement of controller 61 with isolated operation.
When controller 61 determines humidification function revocation, water supply pump 19 stops working, and drain solenoid valve 41 is opened, emptying first Water in sink 22 and the second sink 23.
Water tank 18 is equipped with third filter 30, the condensed water of recycling and unused humidification water, returns to water after filtering Case 18 is spare.Water tank 18 is equipped with water supplement port, is when recycle-water is not able to satisfy test demand, carries out artificial recharge.It is set in water tank 18 There is water level switch, when water shortage in water tank 18, issues alarm signal to controller 61, controller 61 issues the protection of water supply pump 19 and stops It only instructs, and the display alarm information on touch screen 61.
Program-controlled formula precision growth cabinet of the invention also adds CO2Concentration adjusting function, increases CO2Tonifying Qi system System and removing system.
Target component can be arranged in operator on touch screen 61, and starts/halt system operation.Operator can select It selects and carries out CO2Concentration independently regulate and control or with temperature, humidity index combined regulating.
Controller 61 by signal wire or communication line to Temperature and Humidity signal, refrigerant dehumidification system detect signal 50, Heating system detection signal 51, air compensating system detect signal 52, degassing system detection signal 53, carry out letter with power detection signal 54 Number acquisition and analysis.The function of starting or limitation needed for decision-making system, by signal wire or communication line to refrigerant dehumidification system, follow Ring fan driver 56, heater controller 57, humidification system, electromagnetic valve driver 59, air pump driver 60 etc. are cooperateed with Control.
When controller 61 determines that simulation system needs to provide gas compensation function, stored program controlled enters CO2Tonifying Qi operating condition, when sentencing When determining simulation system and needing to provide remove, stored program controlled carries out CO2Remove operating condition.
CO2Tonifying Qi operating condition:
CO2Air compensating system process is as shown in Figure 6.CO in gas source 382Gas passes through the 39 pressure-reduced and-regulated standby of pipeline pressure reducing valve With.Solenoid valve 41 receives the load instruction of controller 61, adjusts air compensation, CO2Gas is filtered, current limiter 42, mends Port 43 is quantitatively sent into experiment layer 102, CO in stability test layer2Concentration.
CO2 removes operating condition:
CO2It is as shown in Figure 5 to remove system flow.Air pump 31 receives the load instruction of controller 61, adjusts amount of gas evolved, test Partial air in layer removes CO under 31 swabbing action of air pump, into CO2 removing means 342Gas component.Through the 4th filtering Device 33, the first muffler 32, air pump 31, the second muffler 37, exhaust outlet 36 enter test layer.First muffler 32 and second disappears Sound device 37 can reduce system noise.
The above description is only a preferred embodiment of the present invention, is not intended to restrict the invention, for those skilled in the art For member, the invention may be variously modified and varied.All within the spirits and principles of the present invention, it is made it is any modification, Equivalent replacement, improvement etc., should all be included in the protection scope of the present invention.

Claims (10)

1. a kind of program-controlled formula precision growth cabinet, which is characterized in that the program-controlled formula precision growth cabinet includes:
Cabinet, the cabinet are multilayered structure, from top to bottom successively include experiment layer, interlayer and mechanical floor, the experiment layer and Partition is equipped between the interlayer, the interlayer is channel structure, includes first passage and second channel;
Simulation system, the simulation system is arranged in the interlayer and the mechanical floor, for adjusting in growth cabinet Portion's environment;
Stored program controlled, stored program controlled setting is in the mechanical floor, for detecting the environmental data in growth cabinet and right The simulation system is controlled.
2. program-controlled formula precision growth cabinet as described in claim 1, which is characterized in that the simulation system includes system Cold dehumidification system, the refrigerant dehumidification system include:
Compressor unit, the compressor unit includes one or more compressors in parallel, for exporting high-pressure gaseous system Cryogen;
Oil eliminator, the input terminal of the oil eliminator is connect with the output end of the compressor, for separating high-pressure gaseous system Oil in cryogen;
Condenser, the input terminal of the condenser are connect with the output end of the oil eliminator, are used for high-pressure gaseous refrigerant It is condensed into high pressure liquid refrigerant;
Liquid storage device, the output end of the condenser is arranged in the liquid storage device, for storing high pressure liquid refrigerant;
Device for drying and filtering, the output end of the liquid storage device is arranged in the device for drying and filtering, for removing high pressure liquid refrigerant In moisture;
First high-pressure ball valve, the output end of the device for drying and filtering is arranged in first high-pressure ball valve, for controlling high pressure liquid The flow of state refrigerant;
Vaporising device, the vaporising device include the first evaporation element and the second evaporation element, first evaporation element and institute It states the second evaporation element and is connected in the first high-pressure ball valve outlet end, the vaporising device is for steaming high pressure liquid refrigerant Hair;
The output end of the vaporising device is arranged in gas-liquid separator, the gas-liquid separator, for liquid refrigerant is gentle The separation of state refrigerant;
Suction filter, the input terminal and output end of the suction filter are respectively connected to the gas-liquid separator and the pressure Contracting machine unit, forms circulation loop, and the suction filter is used to remove the impurity in gaseous refrigerant;
Preferably, liquid-sighting glass is additionally provided between the device for drying and filtering and first high-pressure ball valve, the liquid-sighting glass is for seeing Examine the circulation status of high pressure liquid refrigerant;
More preferably, the second high-pressure ball valve, second high pressure are additionally provided between the vaporising device and the gas-liquid separator Ball valve is used to control the flow of gaseous refrigerant.
3. program-controlled formula precision growth cabinet as claimed in claim 2, which is characterized in that first evaporation element and institute It states the second evaporation element to be separately positioned in the first passage and the second channel, first evaporation element includes successively Connected first filter, first throttle valve and the first evaporator, second evaporation element include the second mistake being sequentially connected The output end of filter, second throttle and the second evaporator, first evaporator and second evaporator is connected to institute State the second high-pressure ball valve.
4. program-controlled formula precision growth cabinet as claimed in claim 3, which is characterized in that first evaporation element also wraps First circulation blower is included, second evaporation element further includes second circulation blower, the first circulation blower and described second Circulating fan is respectively used to the first evaporator and the second evaporator conveying wind;
Preferably, the first passage is equipped with the first return air inlet, and the second channel is equipped with the second return air inlet.
5. program-controlled formula precision growth cabinet as claimed in claim 4, which is characterized in that the simulation system further includes adding Wet system, the humidification system include:
Water tank, the water tank is interior to be equipped with third filter, and the third filter was used for the impurity in drainage;
Water supply pump, the water supply pump is arranged in water tank, for the water in water tank to be conveyed to atomising device by liquid supply pipe;
Atomising device, the atomising device are arranged above water tank, the water atomization for carrying out water supply pump conveying;
Water container, the water container are arranged below vaporising device, produce for collecting since the vaporising device absorbs heat Raw condensed water, condensed water collected by the water container convey feed-tank by pipeline and the third filter;
Preferably, liquidometer, water supplement port and drain valve are additionally provided in the water tank;
More preferably, the water container includes the first drip tray and the second drip tray, and first drip tray is arranged first Below evaporator, second drip tray is arranged below the second evaporator, first drip tray and second drip tray Collected condensed water passes through pipeline and third filter conveying feed-tank.
6. program-controlled formula precision growth cabinet as claimed in claim 5, which is characterized in that the atomising device includes first Sink, the first atomising head, the second sink, the second atomising head and balance pipe, first sink and second sink are respectively provided with Above the water tank and it is in same level, first sink and second sink lower part pass through the balance pipe Connection, in the first passage, second sink is arranged in the second channel, first mist for the first sink setting Change head to be arranged in first sink, second atomising head is arranged in second sink;
Preferably, first sink top is equipped with overflow pipe, and the overflow pipe other end is connected to the third filter, institute State the top that liquid supply pipe is connected to first sink;
More preferably, the bottom of first sink and second sink passes through pipeline and the drain valve is connected to third Filter.
7. program-controlled formula precision growth cabinet as claimed in claim 6, which is characterized in that the simulation system further includes CO2 Removing system, the CO2Removing system includes:
Air pump, the air pump are equipped with inlet end and exhaust end, for being discharged from inlet end sucking gas, from the exhaust end Gas;
Air inlet, the air inlet setting is in the experiment layer, for sucking gas from the experiment layer;
CO2Removing means, the CO2The input terminal of removing means is connected to by pipeline with the air inlet, output end passes through pipeline It is connected to the air pump inlet end, for removing CO2Gas;
Exhaust outlet, in the experiment layer, the exhaust outlet passes through pipeline connection to air pump exhaust end for the exhaust outlet setting;
Preferably, the CO2Pipeline between removing means and the air pump inlet end is equipped with the 4th filter and the first noise reduction Device, the pipeline between the exhaust outlet and the air pump exhaust end are equipped with the second muffler, and the 4th filter was used for Filter the impurity from the gas that it passes through.
8. program-controlled formula precision growth cabinet as claimed in claim 7, which is characterized in that the simulation system further includes CO2 Air compensating system, the CO2Air compensating system includes:
Gas source, the gas source is for providing CO2Gas;
Pressure reducing valve, the pressure reducing valve setting is in the source output end, for reducing the CO of gas source output2The air pressure of gas;
5th filter, the 5th filter are arranged in the pressure reducing valve output end, for filtering CO2Impurity in gas;
Solenoid valve, the solenoid valve are arranged in the 5th filter output end, for controlling CO2The on-off of gas transfer pipeline;
Current limiter, the current limiter are arranged in the solenoid valve output end, for controlling CO2The feed flow of gas;
Gas supplementing opening, the gas supplementing opening are arranged in the experiment layer, by pipeline connection to the current limiter output end, are used for institute State experiment layer conveying CO2Gas.
9. program-controlled formula precision growth cabinet as claimed in claim 8, which is characterized in that the simulation system further includes adding Hot systems, the heating system include primary heater and secondary heater, and the primary heater setting is logical described first Road, the secondary heater are arranged in the second channel;
Preferably, the program-controlled formula precision growth cabinet further includes having light filling equipment and supervision equipment, and the experiment layer is Transparent hood configuration, the light filling equipment and supervision equipment setting are outside experiment layer.
10. program-controlled formula precision growth cabinet as claimed in claim 9, which is characterized in that the stored program controlled includes:
Controller, the controller export control signal for carrying out processing analysis to the signal of acquisition;
Signal pickup assembly, the signal pickup assembly are connected to the signal input part of the controller, including temperature and humidity sensing Device, gas concentration sensor, refrigerant dehumidification system detection signal, heating system detection signal, air compensating system detection signal, degassing System detection signal matches power detection signal;
Signal control device, the signal control device are connected to the signal output end of the controller, including refrigerated dehumidification system System controller, circulating fan driver, heater controller, humidification system controller, electromagnetic valve driver, air pump driver;
More preferably, the stored program controlled further includes touch screen, and the touch screen is connect with controller.
CN201910103286.9A 2019-02-01 2019-02-01 Program-controlled formula precision growth cabinet Pending CN109701670A (en)

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CN113835454A (en) * 2021-11-29 2021-12-24 中国飞机强度研究所 Method for adjusting and controlling environmental temperature of airplane climate environment test
CN113835453A (en) * 2021-11-29 2021-12-24 中国飞机强度研究所 Multi-working-condition airplane climate environment test temperature regulation control system

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CN106642779A (en) * 2016-09-28 2017-05-10 东南大学 High-precision temperature and humidity control refrigerating system and method for laboratory
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CN101181091A (en) * 2007-11-23 2008-05-21 广州大学 Test table for simulating refrigerated transport condition of perishable food
CN204952922U (en) * 2015-04-28 2016-01-13 上海航天设备制造总厂 High low temperature test box that can dehumidify in succession under low temperature working condition
CN205216859U (en) * 2015-11-18 2016-05-11 广东三木科技有限公司 Energy -saving constant temperature and moisture test case
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CN113835454A (en) * 2021-11-29 2021-12-24 中国飞机强度研究所 Method for adjusting and controlling environmental temperature of airplane climate environment test
CN113835453A (en) * 2021-11-29 2021-12-24 中国飞机强度研究所 Multi-working-condition airplane climate environment test temperature regulation control system
CN113835454B (en) * 2021-11-29 2022-02-08 中国飞机强度研究所 Method for adjusting and controlling environmental temperature of airplane climate environment test
CN113835453B (en) * 2021-11-29 2022-02-08 中国飞机强度研究所 Multi-working-condition airplane climate environment test temperature regulation control system

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