CN105445046B - A kind of refrigeration and pressure charging system for pipeline structure environmental simulation - Google Patents
A kind of refrigeration and pressure charging system for pipeline structure environmental simulation Download PDFInfo
- Publication number
- CN105445046B CN105445046B CN201410382817.XA CN201410382817A CN105445046B CN 105445046 B CN105445046 B CN 105445046B CN 201410382817 A CN201410382817 A CN 201410382817A CN 105445046 B CN105445046 B CN 105445046B
- Authority
- CN
- China
- Prior art keywords
- helium
- heat exchanger
- level
- liquid
- entrance
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
The present invention is a kind of refrigeration and pressure charging system for pipeline structure environmental simulation.Including：High-pressure helium entrance (16), level-one Recuperative heat exchanger (7), two level Recuperative heat exchanger (10), liquid nitrogen heat exchanger (8), liquid helium heat exchanger (9)；Wherein, high-pressure helium entrance (16) inputs normal temperature high voltage helium, is exported after level-one Recuperative heat exchanger (7), liquid nitrogen heat exchanger (8), two level Recuperative heat exchanger (10), liquid helium heat exchanger (9) to test object successively；Test object return-air is recycled again after two level Recuperative heat exchanger (10), level-one Recuperative heat exchanger (7) successively；Liquid nitrogen recycles after liquid nitrogen heat exchanger (8), and liquid helium is recycled after liquid helium heat exchanger (9), two level Recuperative heat exchanger (10), level-one Recuperative heat exchanger (7) successively.Can simulated pressure and low temperature integrated environment, can also simulated high-pressure, low temperature, cooling, heating actual environment.
Description
Technical field
The invention belongs to utilize liquid nitrogen and liquid helium multi-stage refrigerating and its control method, available for structures such as pipeline, housing, cabins
Pressure and low temperature environment simulation, belong to refrigerant system design and control technical field.
Background technology
Pipe-line system be pipe, pipe connections, valve and pipeline support etc. connect into for conveying gas, liquid or with solid
The device of the fluid of body particle.With the rapid development of China's industry, pipe-line system be applied to more and more widely plumbing,
In the various commercial plants such as heat supply, gas supply, long distance delivery, agricultural irrigation, hydraulic engineering.In aerospace field, engine
Pipeline is mainly used for the conveying of the media such as hydraulic oil, fuel, lubricating oil and air, is the important composition portion of engine accessory power rating device
Point.The cryogenic liquid of condition (certain temperature, pressure, flow etc.) needed for cryogenic pipe to outlet offer, in LNG ship oceangoing ship, liquid
Propellant rocket and its ground loading system, spacecraft space environmental simulation equipment etc. are widely used in fields.
Due to the use of the influence of the external environments acute variation such as the vibration of environment and temperature, pressure, these integrated environments
Often cause pipe-line system that various vibration faults or even the destruction for causing pipeline often occurs and causes serious thing
Therefore.Therefore, it first has to consider comprehensively the characteristic of pipe-line system in the design phase of pipe-line system, and verifies the hand of design rationality
Section is exactly to simulate true working environment, and carry out environmental test.Result of the test will directly expose design defect, will be more effective
Design, therefore pipeline environment simulation system implementation have very big theory value and practical meaning in engineering.
The present invention provides a kind of refrigeration and pressure charging system for pipeline structure environmental simulation, with cycle helium to testpieces
It is cooled down and is pressurized, refrigeration can meet low-temperature space more than liquid nitrogen temperature and the profound hypothermia area below liquid nitrogen temperature, press
Power is adjusted.For profound hypothermia area, the present invention makes full use of the cold that liquid helium exports and test object exports, uses the technology of rising again
Liquid helium usage amount is reduced, and improves refrigerating efficiency.
Invention content
The object of the present invention is to provide a kind of refrigeration and pressure charging system for pipeline structure environmental simulation, with cycle helium
Testpieces is cooled down and is pressurized, refrigeration can meet low-temperature space more than liquid nitrogen temperature and the depth below liquid nitrogen temperature
Low-temperature space, pressure adjustable section.In addition, a kind of refrigeration and pressure charging system for pipeline structure environmental simulation provided by the invention is also
Available for cavity, storage tank, the isostructural working environment simulation in cabin.
The present invention is a kind of refrigeration and pressure charging system for pipeline structure environmental simulation, wherein, including：High-pressure helium enters
Mouth, level-one Recuperative heat exchanger, two level Recuperative heat exchanger, liquid nitrogen heat exchanger, liquid helium heat exchanger；Wherein, high-pressure helium entrance inputs
Normal temperature high voltage helium, successively after level-one Recuperative heat exchanger, liquid nitrogen heat exchanger, two level Recuperative heat exchanger, liquid helium heat exchanger
It exports to test object；Test object return-air carries out again after two level Recuperative heat exchanger, level-one Recuperative heat exchanger successively
Cycle；Liquid nitrogen recycles after liquid nitrogen heat exchanger, and liquid helium is successively by liquid helium heat exchanger, two level Recuperative heat exchanger, level-one backheat
It is recycled after heat exchanger；
Wherein, level-one Recuperative heat exchanger is tentatively pre- by normal temperature circulation helium using the cold of liquid helium and test object return-air
Cold, two level Recuperative heat exchanger utilizes liquid helium outlet and the further cooling cycle helium of test object return-air cold；Liquid nitrogen heat exchanger
For recycling the heat exchange of helium and liquid nitrogen, liquid helium heat exchanger is used to recycle the heat exchange of helium and liquid helium.
A kind of refrigeration and pressure charging system for pipeline structure environmental simulation as described above, wherein, it further includes：Helium follows
Ring pumps；Surge tank shut-off valve；Surge tank；By-passing valve；Room temperature intake valve；Room temperature return-air valve；Main road flowmeter；Bypass flow meter；
Helium air bleeding valve；
Low temperature air inlet valve；Low temperature return-air valve；Inlet temperature；Inlet pressure；Outlet temperature；Air bleeding valve；High-pressure helium entrance；
High pressure helium air valve；Liquid nitrogen valve；Liquid nitrogen entrance；Liquid nitrogen exports；Liquid helium valve；Liquid helium entrance；Liquid helium exports；Helium recovery unit；
Also, level-one Recuperative heat exchanger includes：Level-one Recuperative heat exchanger liquid helium entrance；Level-one Recuperative heat exchanger liquid helium goes out
Mouthful；Level-one Recuperative heat exchanger room temperature helium entrance；Level-one Recuperative heat exchanger room temperature helium exports；Level-one Recuperative heat exchanger recycles helium
Gas return air inlet；Level-one Recuperative heat exchanger recycles helium return air outlet；
Liquid nitrogen heat exchanger includes：Liquid nitrogen heat exchanger helium entrance；Liquid nitrogen heat exchanger helium exports；Liquid nitrogen heat exchanger liquid nitrogen enters
Mouthful；Liquid nitrogen heat exchanger liquid nitrogen exports；
Liquid helium heat exchanger includes：Liquid helium heat exchanger liquid helium entrance；Liquid helium heat exchanger liquid helium exports；Liquid helium heat exchanger helium enters
Mouthful；Liquid helium heat exchanger helium exports；
Two level Recuperative heat exchanger includes：Two level Recuperative heat exchanger liquid helium entrance；Two level Recuperative heat exchanger liquid helium exports；Two level
Recuperative heat exchanger helium entrance；Two level Recuperative heat exchanger helium exports；Two level Recuperative heat exchanger recycles helium return air inlet；Two level
Recuperative heat exchanger recycles helium return air outlet；
Wherein, circulated helium pump is power source；Helium is recycled through liquid nitrogen heat exchanger and liquid helium heat exchanger by liquid nitrogen and liquid helium
The cold of generation is brought to test object；Circulated helium pumps helium to be driven to recycle in pipeline and test object, and exchange liquid
The cold of nitrogen and liquid helium cools down test object；
Surge tank stablizes the flow of circulated helium pump generation and the pulsation of pressure；The upper end of surge tank is provided with high-pressure helium
Valve and high-pressure helium entrance, for the input of high-pressure helium；The lower end of surge tank is provided with surge tank shut-off valve；
The level-one Recuperative heat exchanger, liquid nitrogen heat exchanger, liquid helium heat exchanger, two level Recuperative heat exchanger are integrated in Dewar
It is interior；
Circulated helium pump discharge is connected with surge tank shut-off valve, room temperature intake valve, bypass flow meter, surge tank shut-off valve
The other end is connected with surge tank, and high pressure helium air valve is connected to surge tank and high-pressure helium entrance；
Room temperature intake valve is connected to circulated helium pump and main road flowmeter, and one in the other end and Dewar of main road flowmeter
Level-one Recuperative heat exchanger room temperature helium entrance on grade Recuperative heat exchanger is connected, the outlet of level-one Recuperative heat exchanger room temperature helium and liquid
Nitrogen heat exchanger helium entrance connects, and the outlet of liquid nitrogen heat exchanger helium is connected with two level Recuperative heat exchanger helium entrance, two level backheat
The outlet of heat exchanger helium is connected with liquid helium heat exchanger helium entrance；Low temperature air inlet valve both ends are connected to liquid helium heat exchanger helium respectively
Outlet and inlet temperature and inlet pressure test point；Low temperature return-air valve is connected to test object exhaust outlet and two level Recuperative heat exchanger
Recycle helium return air inlet；Two level Recuperative heat exchanger recycles helium return air outlet and enters with level-one Recuperative heat exchanger cycle helium return-air
Mouth is connected, and level-one Recuperative heat exchanger cycle helium return air outlet is connected with room temperature return-air valve and air bleeding valve；Recycle returning for helium pump
Gas port is connected with by-passing valve and by-passing valve；The by-passing valve other end is connected to bypass flow meter；
For liquid helium circuit, liquid helium valve both ends connection liquid helium entrance and liquid helium heat exchanger liquid helium entrance, liquid helium heat exchanger liquid
Helium out connects two level Recuperative heat exchanger liquid helium entrance, and the outlet of two level Recuperative heat exchanger liquid helium enters with level-one Recuperative heat exchanger liquid helium
Mouth is connected, and helium air bleeding valve is connected to the outlet of level-one Recuperative heat exchanger liquid helium and liquid helium outlet, and liquid helium outlet is arranged on helium time
On receiving apparatus；
Cycle helium in system is provided with two branches, monitors helium using main road flowmeter and bypass flow meter respectively
Flow；Helium is used to carry the cold cooling test object of liquid nitrogen and liquid helium in main road, and main road total flow can be other by adjusting
Port valve is adjusted；
The cycle helium of main road is expressed as follows：The high-pressure helium generated by circulated helium pump is adjusted through room temperature intake valve presses
Power, and flow is shown by main road flowmeter, enter level-one Recuperative heat exchanger from level-one Recuperative heat exchanger room temperature helium entrance, from one
Enter liquid nitrogen heat exchanger through liquid nitrogen heat exchanger helium entrance after the outlet discharge of grade Recuperative heat exchanger room temperature helium fully to change with liquid nitrogen
Heat；Cycle helium enters the heat exchange of two level backheat after liquid nitrogen heat exchanger helium outlet discharge through two level Recuperative heat exchanger helium entrance
Device, and enter liquid helium heat exchanger through liquid helium heat exchanger helium entrance by two level Recuperative heat exchanger helium outlet discharge；It is changed from liquid helium
The cycle helium of hot device helium outlet discharge enters test object, and monitor inlet temperature and entrance after the adjustment of low temperature air inlet valve
Pressure；The cycle helium of test object discharge recycles helium return air inlet after the adjustment of low temperature return-air valve through two level Recuperative heat exchanger
Into two level Recuperative heat exchanger and by the cycle helium return air outlet discharge of two level Recuperative heat exchanger；Hereafter, cycle helium is through level-one
Recuperative heat exchanger cycle helium return air inlet enters level-one Recuperative heat exchanger and exchanges heat with initial cycle helium；It is changed from level-one backheat
Circulated helium pump is back to through room temperature return-air valve complete cycle after hot device cycle helium return air outlet discharge；
The circulated helium of bypass is expressed as follows：The high-pressure helium part generated by circulated helium pump is after by-passing valve adjusts
Circulated helium pump is directly back to, this road flow is monitored by bypass flow meter.
The present invention proposes a kind of refrigeration and pressure charging system for pipeline structure environmental simulation, the advantage is that, system makes
It is pressurized with liquid nitrogen and liquid helium two-stage refrigeration, and by high-pressure helium, plays pressure stabilization function using surge tank in system, pressure can be simulated
The integrated environment of power and low temperature, can also simulated high-pressure, low temperature, cooling, the actual environment to heat up.System is provided with main road and branch
Road can adjust main road flow by by-passing valve, realize the purpose for adjusting the test object temperature difference.There is provided level-one backheats to change for system
Hot device, two level Recuperative heat exchanger make full use of the cold of rising again of cycle helium in liquid helium and test specimen, and cycle helium is tentatively made
It is cold, it realizes and reduces liquid helium dosage, and improve the purpose of refrigerating efficiency.
Description of the drawings
Fig. 1 is used for the refrigeration of pipeline structure environmental simulation and pressure charging system principle；
Fig. 2 low-temperature space environmental simulation flows；
Fig. 3 profound hypothermias area's environmental simulation flow.
1 circulated helium pumps；2 surge tank shut-off valves；3 surge tanks；4 by-passing valves；4a room temperature intake valves；4b room temperature return-air valves；
5a main road flowmeters；5b bypass flow meters；6 helium air bleeding valves；7 level-one Recuperative heat exchangers；7a level-one Recuperative heat exchanger liquid heliums enter
Mouthful；7b level-one Recuperative heat exchangers liquid helium exports；7c level-one Recuperative heat exchanger room temperature helium entrances；7d level-one Recuperative heat exchanger room temperature
Helium exports；7e level-ones Recuperative heat exchanger recycles helium return air inlet；7f level-ones Recuperative heat exchanger recycles helium return air outlet；8
Liquid nitrogen heat exchanger；8a liquid nitrogen heat exchanger helium entrances；8b liquid nitrogen heat exchangers helium exports；8c liquid nitrogen heat exchanger liquid nitrogen entrances；8d
Liquid nitrogen heat exchanger liquid nitrogen exports；9 liquid helium heat exchangers；9a liquid helium heat exchanger liquid helium entrances；9b liquid helium heat exchangers liquid helium exports；9c liquid
Helium heat exchanger helium entrance；9d liquid helium heat exchangers helium exports；10 two level Recuperative heat exchangers；10a two level Recuperative heat exchanger liquid heliums
Entrance；10b two level Recuperative heat exchangers liquid helium exports；10c two level Recuperative heat exchanger helium entrances；10d two level Recuperative heat exchanger helium
Gas exports；10e two levels Recuperative heat exchanger recycles helium return air inlet；10f two levels Recuperative heat exchanger recycles helium return air outlet；
11a low temperature air inlet valves；11b low temperature return-air valves；12 inlet temperatures；13 inlet pressures；14 outlet temperatures；15 air bleeding valves；16 high pressures
Helium entrance；16a high pressure helium air valves；17 liquid nitrogen valves；18a liquid nitrogen entrances；18b liquid nitrogen exports；19 liquid helium valves；20a liquid helium entrances；
20b liquid heliums export；21 helium recovery units.
Specific embodiment
The present invention is described further with reference to the accompanying drawings and examples.
As shown in Figure 1, a kind of refrigeration and pressure charging system for pipeline structure environmental simulation, using cycle helium to experiment
Part is cooled down and is pressurized, and can realize that the depth more than following liquid helium region of low-temperature space and liquid nitrogen temperature more than liquid nitrogen temperature is low
Warm area, and realize the accurate adjusting of pressure.
Including circulated helium pump 1；Surge tank shut-off valve 2；Surge tank 3；By-passing valve 4；Room temperature intake valve 4a；Room temperature return-air valve
4b；Main road flowmeter 5a；Bypass flow meter 5b；Helium air bleeding valve 6；Level-one Recuperative heat exchanger 7；Level-one Recuperative heat exchanger liquid helium enters
Mouth 7a；Level-one Recuperative heat exchanger liquid helium exports 7b；Level-one Recuperative heat exchanger room temperature helium entrance 7c；Level-one Recuperative heat exchanger room temperature
Helium exports 7d；Level-one Recuperative heat exchanger cycle helium return air inlet 7e；Level-one Recuperative heat exchanger cycle helium return air outlet 7f；
Liquid nitrogen heat exchanger 8；Liquid nitrogen heat exchanger helium entrance 8a；Liquid nitrogen heat exchanger helium exports 8b；Liquid nitrogen heat exchanger liquid nitrogen entrance 8c；Liquid
Nitrogen heat exchanger liquid nitrogen exports 8d；Liquid helium heat exchanger 9；Liquid helium heat exchanger liquid helium entrance 9a；Liquid helium heat exchanger liquid helium exports 9b；Liquid helium
Heat exchanger helium entrance 9c；Liquid helium heat exchanger helium exports 9d；Two level Recuperative heat exchanger 10；Two level Recuperative heat exchanger liquid helium entrance
10a；Two level Recuperative heat exchanger liquid helium exports 10b；Two level Recuperative heat exchanger helium entrance 10c；Two level Recuperative heat exchanger helium goes out
Mouth 10d；Two level Recuperative heat exchanger cycle helium return air inlet 10e；Two level Recuperative heat exchanger cycle helium return air outlet 10f；It is low
Warm intake valve 11a；Low temperature return-air valve 11b；Inlet temperature 12；Inlet pressure 13；Outlet temperature 14；Air bleeding valve 15；High-pressure helium
Entrance 16；High pressure helium air valve 16a；Liquid nitrogen valve 17；Liquid nitrogen entrance 18a；Liquid nitrogen exports 18b；Liquid helium valve 19；Liquid helium entrance 20a；Liquid
Helium out 20b；Helium recovery unit 21.
Wherein, circulated helium pump 1 is power source, makes helium that fluid resistance be overcome to be recycled in pipeline, and realize requirement
Flow.Cycle helium brings the cold that liquid nitrogen and liquid helium generate to test object through liquid nitrogen heat exchanger 8 and liquid helium heat exchanger 9.Helium
Gas circulating pump 1 exchanges the cold cooling test pair of liquid nitrogen and liquid helium for helium to be driven to be recycled in pipeline and test object
As.
Surge tank 3 be used for stablize circulated helium pump 1 generate flow and pressure pulsation, also to system boost, be depressured
Journey plays cushioning effect, and pressure and flow is made not to generate mutation.The upper end of surge tank 3 is provided with high pressure helium air valve 16a and high pressure
Helium entrance 16 for the input of high-pressure helium, realizes the purpose of supercharging.The lower end of surge tank 3 is provided with surge tank shut-off valve
2, when closing surge tank shut-off valve 2 after the test, the helium in surge tank 3 can be stored, in case next time, experiment used, it is main
Syllabus is the usage amount for saving helium, and shorten the time of gas displacement in pipeline.Surge tank 3 is compressible and swollen using gas
Swollen characteristic, alternate storage or release, achieve the purpose that reduce flow and pressure fluctuation in pipeline.
To reduce system leakage heat, the level-one Recuperative heat exchanger 7, liquid nitrogen heat exchanger 8, liquid helium heat exchanger 9, two level backheat
Heat exchanger 10 is integrated in Dewar.
Normal temperature circulation helium is tentatively pre-chilled using the cold of liquid helium and test object return-air for level-one Recuperative heat exchanger 7, and two
Grade Recuperative heat exchanger 10 utilizes liquid helium outlet and the further cooling cycle helium of test object return-air cold.Liquid nitrogen heat exchanger is used for
The heat exchange of helium and liquid nitrogen is recycled, liquid helium heat exchanger is used to recycle the heat exchange of helium and liquid helium.
Level-one Recuperative heat exchanger 7 is provided with level-one Recuperative heat exchanger liquid helium entrance 7a, level-one Recuperative heat exchanger liquid helium exports
7b, level-one Recuperative heat exchanger room temperature helium entrance 7c, level-one Recuperative heat exchanger room temperature helium outlet 7d, level-one Recuperative heat exchanger follow
Ring helium return air inlet 7e, level-one Recuperative heat exchanger cycle helium return air outlet 7f；
Liquid nitrogen heat exchanger 8 is provided with liquid nitrogen heat exchanger helium entrance 8a, liquid nitrogen heat exchanger helium outlet 8b, liquid nitrogen heat exchanger
Liquid nitrogen entrance 8c, liquid nitrogen heat exchanger liquid nitrogen outlet 8d；
Liquid helium heat exchanger 9 is provided with liquid helium heat exchanger liquid helium entrance 9a, liquid helium heat exchanger liquid helium outlet 9b, liquid helium heat exchanger
Helium entrance 9c, liquid helium heat exchanger helium outlet 9d；
Two level Recuperative heat exchanger 10 is provided with two level Recuperative heat exchanger liquid helium entrance 10a, two level Recuperative heat exchanger liquid helium goes out
Mouth 10b, two level Recuperative heat exchanger helium entrance 10c, two level Recuperative heat exchanger helium outlet 10d, two level Recuperative heat exchanger cycle
Helium return air inlet 10e, two level Recuperative heat exchanger cycle helium return air outlet 10f.
1 outlet of circulated helium pump is connected with surge tank shut-off valve 2, room temperature intake valve 4a, bypass flow meter 5b, and surge tank is cut
Only the other end of valve 2 is connected with surge tank 3, and high pressure helium air valve 16a is connected to surge tank 3 and high-pressure helium entrance 16.
Room temperature intake valve 4a is connected to circulated helium pump 1 and main road flowmeter 5a, the other end of main road flowmeter 5a and Du
Level-one Recuperative heat exchanger room temperature helium entrance 7c on level-one Recuperative heat exchanger 7 in watt is connected, level-one Recuperative heat exchanger room temperature
Helium outlet 7d is connected with liquid nitrogen heat exchanger helium entrance 8a, liquid nitrogen heat exchanger helium outlet 8b and two level Recuperative heat exchanger helium
Entrance 10c is connected, and two level Recuperative heat exchanger helium outlet 10d is connected with liquid helium heat exchanger helium entrance 9c.Low temperature air inlet valve 11a
Both ends are connected to liquid helium heat exchanger helium outlet 9d and 13 test point of inlet temperature 12 and inlet pressure respectively.Low temperature return-air valve
11b is connected to test object exhaust outlet and two level Recuperative heat exchanger cycle helium return air inlet 10e.Two level Recuperative heat exchanger recycles
Helium return air outlet 10f is connected with level-one Recuperative heat exchanger cycle helium return air inlet 7e, level-one Recuperative heat exchanger cycle helium
Return air outlet 7f is connected with room temperature return-air valve 4b and air bleeding valve 15.Recycle the gas returning port of helium pump 1 and by-passing valve 4 and by-passing valve 4
It is connected.4 other end of by-passing valve is connected to bypass flow meter 5b.
For liquid helium circuit, 19 both ends of liquid helium valve connection liquid helium entrance 20a and liquid helium heat exchanger liquid helium entrance 9a, liquid helium change
Hot device liquid helium exports 9b connection two level Recuperative heat exchanger liquid helium entrance 10a, and two level Recuperative heat exchanger liquid helium outlet 10b is returned with level-one
Heat exchanger liquid helium entrance 7a is connected, and helium air bleeding valve 6 is connected to level-one Recuperative heat exchanger liquid helium outlet 7b and liquid helium outlet
20b, liquid helium outlet 20b are arranged on helium recovery unit 21.
Cycle helium in system is provided with two branches, is monitored respectively using main road flowmeter 5a and bypass flow meter 5b
Helium gas flow.Helium is used to carry the cold cooling test object of liquid nitrogen and liquid helium in main road, and main road total flow can pass through tune
Section by-passing valve 4 is adjusted.
The cycle helium of main road is expressed as follows：The high-pressure helium generated by circulated helium pump 1 is adjusted through room temperature intake valve 4a
Pressure, and flow is shown by main road flowmeter 5a, enter the heat exchange of level-one backheat from level-one Recuperative heat exchanger room temperature helium entrance 7c
Device 7 enters liquid nitrogen heat exchanger 8 after level-one Recuperative heat exchanger room temperature helium outlet 7d discharges through liquid nitrogen heat exchanger helium entrance 8a
It fully exchanges heat with liquid nitrogen.Helium is recycled after liquid nitrogen heat exchanger helium outlet 8b discharges through two level Recuperative heat exchanger helium entrance
10c enters two level Recuperative heat exchanger 10, and by two level Recuperative heat exchanger helium outlet 10d discharges through liquid helium heat exchanger helium entrance
9c enters liquid helium heat exchanger 9.It is laggard in low temperature air inlet valve 11a adjustment from the cycle helium of liquid helium heat exchanger helium outlet 9d discharges
Enter test object, and monitor inlet temperature 12 and inlet pressure 13.The cycle helium of test object discharge is through low temperature return-air valve 11b
Enter two level Recuperative heat exchanger 10 through two level Recuperative heat exchanger cycle helium return air inlet 10e after adjustment and exchanged heat by two level backheat
Device cycle helium return air outlet 10f discharges.Hereafter, cycle helium enters through level-one Recuperative heat exchanger cycle helium return air inlet 7e
Level-one Recuperative heat exchanger 7 exchanges heat with initial cycle helium.After the cycle helium return air outlet 7f discharges of level-one Recuperative heat exchanger
Circulated helium pump 1, which is back to, through room temperature return-air valve 4b completes cycle.
The circulated helium of bypass is expressed as follows：The high-pressure helium part generated by circulated helium pump 1 is adjusted through by-passing valve 4
It is directly back to circulated helium pump 1 afterwards, this road flow is monitored by bypass flow meter 5b.
Liquid nitrogen injection embodiment is as follows：Liquid nitrogen is entered by liquid nitrogen entrance 18a, and adjusts flow through liquid nitrogen valve 17, is passed through
Liquid nitrogen heat exchanger liquid nitrogen entrance 8c enters liquid nitrogen heat exchanger 8, and in liquid nitrogen heat exchanger 8, liquid nitrogen fully exchanges heat with cycle helium.Liquid
Nitrogen endothermic gasification exports 8d through liquid nitrogen heat exchanger liquid nitrogen and exports 18b discharges by liquid nitrogen.
Liquid helium injection embodiment is as follows：Liquid helium enters pipeline by liquid helium entrance 20a, and flow is adjusted through liquid helium valve 19, by
Liquid helium heat exchanger liquid helium entrance 9a enters liquid helium heat exchanger 9.In liquid helium heat exchanger 9, liquid helium and cycle helium sufficient heat exchange.
Helium is recycled by liquid helium heat exchanger liquid helium outlet 9b discharges, enters two level backheat by two level Recuperative heat exchanger liquid helium entrance 10a
Heat exchanger 10, in two level Recuperative heat exchanger 10, recycle the return-air of helium with the discharge gas of liquid helium with cycle helium
Air inlet heat exchange.It recycles after helium is discharged by two level Recuperative heat exchanger liquid helium outlet 10b through level-one Recuperative heat exchanger liquid helium entrance
7a enters level-one Recuperative heat exchanger 7, by being adjusted after level-one Recuperative heat exchanger liquid helium outlet 7b discharges through helium air bleeding valve 6, and by
Liquid helium outlet 20b enters helium recovery unit 21.The flow of liquid helium can be adjusted by liquid helium valve 19 and helium air bleeding valve 6.
The pressure of pressure namely cycle helium inside test object can jointly be adjusted by high-pressure helium and air bleeding valve,
When cycle helium pressure is relatively low, high-pressure helium enters through high-pressure helium entrance, and enters after high-pressure helium pressure regulating valve
Surge tank enters cycle helium pipeline after voltage stabilizing through surge tank shut-off valve.When cycle helium pressure is higher, air bleeding valve row is opened
Gas, and the inlet pressure of monitoring and test object after reaching desired value, close air bleeding valve.Because of the pressure stabilization function of surge tank, entirely
Adjustment process, pressure and flow change more steady.
Temperature inside test object, the low-temperature space and the following liquid helium temperature of liquid nitrogen temperature being divided into more than liquid nitrogen temperature
Above profound hypothermia area.When needing the temperature environment simulated for low-temperature space environment, then close liquid helium valve and stop liquid helium supply, it is only necessary to
Liquid nitrogen provides cold.Then liquid helium is needed to supply for profound hypothermia area environment when needing the temperature environment simulated.
The process simulated is summarized as follows first：
(1) gas displacement in pipeline：It is pressurized after the experiment preparation stage by high-pressure helium entrance until increasing to displacement
Pressure, voltage stabilizing detect whether vacuum degree reaches requirement for a period of time afterwards by being vented valve exhaust, after exhaust, if not up to
Then pressurising and being vented is repeated the above process until reach vacuum level requirements again.
(2) system boost：It is pressurized by helium entrance until increasing to the goal pressure of test requirements document, and pass through inlet pressure
Monitoring, then continues pressurising if the goal pressure for reaching test requirements document, passes through air bleeding valve exhaust decompression if being more than goal pressure.
(3) system cools down：Liquid nitrogen is added in by liquid nitrogen entrance, starts cycle helium pump, cycle helium is in liquid nitrogen heat exchanger
Interior and liquid nitrogen heat exchange, cycle helium bring cold into test object.
When experiment is the simulation of profound hypothermia area, after above-mentioned temperature is down to liquid nitrogen temperature, liquid helium is entered by liquid helium entrance
Pipeline, cycle helium exchange heat with liquid helium in liquid helium heat exchanger, and cycle helium brings the cold of liquid helium into test object.When experiment is
When low-temperature space is simulated, then the operation of above-mentioned liquid helium supply is not needed to.
Because in the process cycle helium be cooled volume reduction, pressure reduction, when inlet pressure detects pressure reduction, lead to
The supercharging of high-pressure helium entrance is crossed until inlet temperature and inlet pressure reach test requirements document.
(4) the entrance temperature difference adjusts：By inlet pressure and the entrance temperature difference of outlet pressure monitoring and test object, work as temperature
When degree difference is larger, adjusts by-passing valve and monitor main road flowmeter, with the entrance temperature difference of the increase test object of main road flow
Reduce, until reaching test requirements document.
(5) after experiment reaches and want seeking time, surge tank shut-off valve is closed, stops circulated helium and pumps, by being vented valve exhaust
Decompression, test object are risen again naturally, off-test.
The present invention proposes a kind of refrigeration and pressure charging system for pipeline structure environmental simulation, the advantage is that, system makes
It is pressurized with liquid nitrogen and liquid helium two-stage refrigeration, and by high-pressure helium, plays pressure stabilization function using surge tank in system, pressure can be simulated
The integrated environment of power and low temperature, can also simulated high-pressure, low temperature, cooling, the actual environment to heat up.System is provided with main road and branch
Road can adjust main road flow by by-passing valve, realize the purpose for adjusting the test object temperature difference.There is provided level-one backheats to change for system
Hot device, two level Recuperative heat exchanger make full use of the cold of rising again of cycle helium in liquid helium and test specimen, and cycle helium is tentatively made
It is cold, it realizes and reduces liquid helium dosage, and improve the purpose of refrigerating efficiency.
Detailed process is described as follows：
Low-temperature space environmental simulation flow is with reference to Fig. 2：
(1) it tests the preparation stage, at the external air source, liquid nitrogen entrance 18a at connecting test object, high-pressure helium entrance 16
Liquid nitrogen source, liquid helium entrance 20a liquid helium, confirm main road flowmeter 5a, bypass flow meter 5b, 12 sensor of inlet temperature, enter
13 sensor of mouth pressure, 14 normal operation of sensor of outlet temperature.
(2) high-pressure helium is injected by high-pressure helium entrance 16, and enters surge tank after passing through high pressure helium air valve 16a adjustment
3, circulation line is entered by surge tank shut-off valve 2, realizes the supercharging of replacement process.Pass through inlet pressure 13 during being somebody's turn to do and monitor pressure
Power when pressure is more than goal pressure, is opened air bleeding valve 15 and is vented.After pressure increases to displacement pressure, high pressure helium air valve is closed
16a, steady pressure for a period of time, after no pressure variation, are opened air bleeding valve 15 and are vented.Vacuum degree is detected after pressure release, such as not up to
Vacuum level requirements are then pressurized and are vented again, until reaching vacuum level requirements.
(3) high-pressure helium is injected by high-pressure helium entrance 16, realizes the supercharging of process of refrigerastion.It is supervised by inlet pressure 13
Measuring pressure when pressure is more than goal pressure, is opened air bleeding valve 15 and is vented.Liquid nitrogen is entered by liquid nitrogen entrance 18a, and through liquid nitrogen valve
17 adjustment flows, enter liquid nitrogen heat exchanger 8 by liquid nitrogen heat exchanger liquid nitrogen entrance 8c, are exported after gasification by liquid nitrogen heat exchanger liquid nitrogen
8d is simultaneously discharged through liquid nitrogen outlet 18b.
(4) start circulated helium pump 1, cycle helium fully exchanges heat, and it is cold to carry cold in liquid nitrogen heat exchanger 8 with liquid nitrogen
But liquid helium heat exchanger 9, test object, two level Recuperative heat exchanger 10 and level-one Recuperative heat exchanger 7.Since temperature reduces, helium is recycled
The pressure of gas will decrease, and be monitored according to inlet pressure 13, when pressure decreases, inject high pressure by high-pressure helium entrance 16
Helium steady pressure.According to 12 monitoring temperature of inlet temperature until temperature is down to desired value.When inlet temperature 12 is higher than target temperature
When spending, the aperture of liquid nitrogen valve 17 is increased, increases liquid nitrogen flow；When inlet temperature 12 is less than target temperature, reduce liquid nitrogen valve 17
Aperture, reduce liquid nitrogen flow.
According to the entrance temperature difference requirement of test object, the temperature difference is tested by inlet temperature 12 and outlet temperature 14.Work as survey
When trying the temperature difference more than target temperature difference, reduce the aperture of by-passing valve 4, increase main road flow (can be monitored by main road flowmeter 5a),
Until the test temperature difference reaches target temperature difference.When testing the temperature difference less than target temperature difference, increase the aperture of by-passing valve 4, reduce main road
Flow (can be monitored) by main road flowmeter 5a, increase bypass flow (can be monitored by bypass flow meter 5b), until test temperature
Difference reaches target temperature difference.According to test requirements document, the requirement of temperature, pressure, the temperature difference is maintained, completes test period, until experiment knot
Beam.
(5) after the test, 15 exhaust decompression of air bleeding valve is opened, test object is risen again, supervised by inlet temperature 12 naturally
It surveys, until test object rises to natural temperature.
Environmental simulation flow in profound hypothermia area is with reference to Fig. 3：
(1) it tests the preparation stage, at the external air source, liquid nitrogen entrance 18a at connecting test object, high-pressure helium entrance 16
Liquid nitrogen source, liquid helium entrance 20a liquid helium, confirm main road flowmeter 5a, bypass flow meter 5b, 12 sensor of inlet temperature, enter
13 sensor of mouth pressure, 14 normal operation of sensor of outlet temperature.
(2) high-pressure helium is injected by high-pressure helium entrance 16, and enters surge tank after passing through high pressure helium air valve 16a adjustment
3, circulation line is entered by surge tank shut-off valve 2, realizes the supercharging of replacement process.Pass through inlet pressure 13 during being somebody's turn to do and monitor pressure
Power when pressure is more than goal pressure, is opened air bleeding valve 15 and is vented.After pressure increases to displacement pressure, high pressure helium air valve is closed
16a, steady pressure for a period of time, after no pressure variation, are opened air bleeding valve 15 and are vented.Vacuum degree is detected after pressure release, such as not up to
Vacuum level requirements are then pressurized and are vented again, until reaching vacuum level requirements.
(3) high-pressure helium is injected by high-pressure helium entrance 16, realizes the supercharging of process of refrigerastion.It is supervised by inlet pressure 13
Measuring pressure when pressure is more than goal pressure, is opened air bleeding valve 15 and is vented.Liquid nitrogen is entered by liquid nitrogen entrance 18a, and through liquid nitrogen valve
17 adjustment flows, enter liquid nitrogen heat exchanger 8 by liquid nitrogen heat exchanger liquid nitrogen entrance 8c, are exported after gasification by liquid nitrogen heat exchanger liquid nitrogen
8d is simultaneously discharged through liquid nitrogen outlet 18b.
(4) start circulated helium pump 1, cycle helium fully exchanges heat, and it is cold to carry cold in liquid nitrogen heat exchanger 8 with liquid nitrogen
But liquid helium heat exchanger 9, test object, two level Recuperative heat exchanger 10 and level-one Recuperative heat exchanger 7.Since temperature reduces, helium is recycled
The pressure of gas will decrease, and be monitored according to inlet pressure 13, when pressure decreases, inject high pressure by high-pressure helium entrance 16
Helium steady pressure.According to 12 monitoring temperature of inlet temperature until the temperature of test object is down to liquid nitrogen temperature.Work as inlet temperature
12 when being higher than liquid nitrogen temperature, increases the aperture of liquid nitrogen valve 17, increases liquid nitrogen flow；When inlet temperature 12 is less than liquid nitrogen temperature,
Reduce the aperture of liquid nitrogen valve 17, reduce liquid nitrogen flow.
(5) liquid helium is injected into pipeline by liquid helium entrance 20a, flow is adjusted through liquid helium valve 19, by liquid helium heat exchanger liquid
Helium entrance 9a enters liquid helium heat exchanger 9.In liquid helium heat exchanger 9, the heat of liquid helium absorption cycle helium, heating gasification, cycle
Helium brings the cold of liquid helium to test object.
According to 12 monitoring and test object temperature of inlet temperature until temperature is down to desired value.When inlet temperature 12 is higher than target
During temperature, the aperture of liquid helium valve 19 is increased, increases liquid helium flow；When inlet temperature 12 is less than target temperature, reduce liquid helium valve
19 aperture reduces liquid helium flow.
According to the entrance temperature difference requirement of test object, the temperature difference is tested by inlet temperature 12 and outlet temperature 14.Work as survey
When trying the temperature difference more than target temperature difference, reduce the aperture of by-passing valve 4, increase main road flow (can be monitored by main road flowmeter 5a),
Until the test temperature difference reaches target temperature difference.When testing the temperature difference less than target temperature difference, increase the aperture of by-passing valve 4, reduce main road
Flow (can be monitored) by main road flowmeter 5a, increase bypass flow (can be monitored by bypass flow meter 5b), until test temperature
Difference reaches target temperature difference.According to test requirements document, the requirement of temperature, pressure, the temperature difference is maintained, completes test period, until experiment knot
Beam.
(6) after the test, 15 exhaust decompression of air bleeding valve is opened, test object is risen again naturally, is closed liquid helium valve 19 and is stopped
Liquid helium is supplied.It is monitored by inlet temperature 12, until test object rises to natural temperature.
The embodiment of the present invention is explained in detail above, the above embodiment is only most highly preferred embodiment of the invention,
It, within the knowledge of a person skilled in the art, can also be but the present invention is not limited to above-described embodiment
It is made a variety of changes under the premise of not departing from present inventive concept.
Claims (2)
1. a kind of refrigeration and pressure charging system for pipeline structure environmental simulation, which is characterized in that including：High-pressure helium entrance
(16), level-one Recuperative heat exchanger (7), two level Recuperative heat exchanger (10), liquid nitrogen heat exchanger (8), liquid helium heat exchanger (9)；Wherein, it is high
Helium entrance (16) is pressed to input normal temperature high voltage helium, is returned successively by level-one Recuperative heat exchanger (7), liquid nitrogen heat exchanger (8), two level
It is exported after heat exchanger (10), liquid helium heat exchanger (9) to test object；Test object return-air exchanges heat successively by two level backheat
It is recycled again after device (10), level-one Recuperative heat exchanger (7)；Liquid nitrogen recycles after liquid nitrogen heat exchanger (8), and liquid helium is successively
It is recycled after liquid helium heat exchanger (9), two level Recuperative heat exchanger (10), level-one Recuperative heat exchanger (7)；
Wherein, normal temperature circulation helium is tentatively pre-chilled using the cold of liquid helium and test object return-air for level-one Recuperative heat exchanger (7),
Two level Recuperative heat exchanger (10) utilizes liquid helium outlet and the further cooling cycle helium of test object return-air cold；Liquid nitrogen heat exchanger
(8) for recycling the heat exchange of helium and liquid nitrogen, liquid helium heat exchanger (9) is for recycling the heat exchange of helium and liquid helium.
2. a kind of refrigeration and pressure charging system for pipeline structure environmental simulation as described in claim 1, which is characterized in that also
Including：Circulated helium pumps (1)；Surge tank shut-off valve (2)；Surge tank (3)；By-passing valve (4)；Room temperature intake valve (4a)；Room temperature returns
Air valve (4b)；Main road flowmeter (5a)；Bypass flow meter (5b)；Helium air bleeding valve (6)；
Low temperature air inlet valve (11a)；Low temperature return-air valve (11b)；Inlet temperature (12)；Inlet pressure (13)；Outlet temperature (14)；Row
Air valve (15)；High-pressure helium entrance (16)；High pressure helium air valve (16a)；Liquid nitrogen valve (17)；Liquid nitrogen entrance (18a)；Liquid nitrogen exports
(18b)；Liquid helium valve (19)；Liquid helium entrance (20a)；Liquid helium exports (20b)；Helium recovery unit (21)；
Also, level-one Recuperative heat exchanger (7) includes：Level-one Recuperative heat exchanger liquid helium entrance (7a)；Level-one Recuperative heat exchanger liquid helium
It exports (7b)；Level-one Recuperative heat exchanger room temperature helium entrance (7c)；Level-one Recuperative heat exchanger room temperature helium exports (7d)；Level-one is returned
Heat exchanger cycle helium return air inlet (7e)；Level-one Recuperative heat exchanger cycle helium return air outlet (7f)；
Liquid nitrogen heat exchanger (8) includes：Liquid nitrogen heat exchanger helium entrance (8a)；Liquid nitrogen heat exchanger helium exports (8b)；Liquid nitrogen exchanges heat
Device liquid nitrogen entrance (8c)；Liquid nitrogen heat exchanger liquid nitrogen exports (8d)；
Liquid helium heat exchanger (9) includes：Liquid helium heat exchanger liquid helium entrance (9a)；Liquid helium heat exchanger liquid helium exports (9b)；Liquid helium exchanges heat
Device helium entrance (9c)；Liquid helium heat exchanger helium exports (9d)；
Two level Recuperative heat exchanger (10) includes：Two level Recuperative heat exchanger liquid helium entrance (10a)；Two level Recuperative heat exchanger liquid helium exports
(10b)；Two level Recuperative heat exchanger helium entrance (10c)；Two level Recuperative heat exchanger helium exports (10d)；Two level Recuperative heat exchanger
Recycle helium return air inlet (10e)；Two level Recuperative heat exchanger cycle helium return air outlet (10f)；
Wherein, circulated helium pump (1) is power source；Recycle helium through liquid nitrogen heat exchanger (8) and liquid helium heat exchanger (9) by liquid nitrogen and
The cold that liquid helium generates is brought to test object；Circulated helium pumps (1) for helium to be driven to be recycled in pipeline and test object, and
Exchange the cold cooling test object of liquid nitrogen and liquid helium；
Surge tank (3) stablizes the flow of circulated helium pump (1) generation and the pulsation of pressure；The upper end of surge tank (3) is provided with height
Helium valve (16a) and high-pressure helium entrance (16) are pressed, for the input of high-pressure helium；The lower end of surge tank (3) is provided with buffering
Tank shut-off valve (2)；
The level-one Recuperative heat exchanger (7), liquid nitrogen heat exchanger (8), liquid helium heat exchanger (9), two level Recuperative heat exchanger (10) collection
Into in Dewar；
Circulated helium pump (1) outlet is connected with surge tank shut-off valve (2), room temperature intake valve (4a), bypass flow meter (5b), is buffered
The other end of tank shut-off valve (2) is connected with surge tank (3), and high pressure helium air valve (16a) is connected to surge tank (3) and high-pressure helium enters
Mouth (16)；
Room temperature intake valve (4a) is connected to circulated helium pump (1) and main road flowmeter (5a), the other end of main road flowmeter (5a)
It is connected with the level-one Recuperative heat exchanger room temperature helium entrance (7c) on the level-one Recuperative heat exchanger (7) in Dewar, level-one backheat is changed
Hot device room temperature helium outlet (7d) connects with liquid nitrogen heat exchanger helium entrance (8a), liquid nitrogen heat exchanger helium outlet (8b) and two level
Recuperative heat exchanger helium entrance (10c) is connected, two level Recuperative heat exchanger helium outlet (10d) and liquid helium heat exchanger helium entrance
(9c) is connected；Low temperature air inlet valve (11a) both ends be connected to respectively liquid helium heat exchanger helium outlet (9d) and inlet temperature (12) and
Inlet pressure (13) test point；Low temperature return-air valve (11b) is connected to test object exhaust outlet and recycles helium with two level Recuperative heat exchanger
Gas return air inlet (10e)；Two level Recuperative heat exchanger cycle helium return air outlet (10f) is returned with level-one Recuperative heat exchanger cycle helium
Gas entrance (7e) is connected, level-one Recuperative heat exchanger cycle helium return air outlet (7f) and room temperature return-air valve (4b) and air bleeding valve (15)
It is connected；The gas returning port of cycle helium pump (1) is connected with by-passing valve (4) and by-passing valve (4)；By-passing valve (4) other end is connected to side
Through-flow gauge (5b)；
For liquid helium circuit, liquid helium valve (19) both ends connection liquid helium entrance (20a) and liquid helium heat exchanger liquid helium entrance (9a), liquid helium
Heat exchanger liquid helium outlet (9b) connection two level Recuperative heat exchanger liquid helium entrance (10a), two level Recuperative heat exchanger liquid helium outlet (10b)
It is connected with level-one Recuperative heat exchanger liquid helium entrance (7a), helium air bleeding valve (6) is connected to the outlet of level-one Recuperative heat exchanger liquid helium
(7b) and liquid helium export (20b), and liquid helium outlet (20b) is arranged on helium recovery unit (21)；
Cycle helium in system is provided with two branches, is monitored respectively using main road flowmeter (5a) and bypass flow meter (5b)
Helium gas flow；Helium is used to carry the cold cooling test object of liquid nitrogen and liquid helium in main road, and main road total flow can pass through tune
By-passing valve (4) is saved to adjust；
The circulated helium of main road is expressed as follows：The high-pressure helium that (1) generation is pumped by circulated helium is adjusted through room temperature intake valve (4a)
Pressure, and flow is shown by main road flowmeter (5a), from level-one Recuperative heat exchanger room temperature helium entrance (7c) into level-one backheat
Heat exchanger (7) enters after level-one Recuperative heat exchanger room temperature helium outlet (7d) discharge through liquid nitrogen heat exchanger helium entrance (8a)
Liquid nitrogen heat exchanger (8) fully exchanges heat with liquid nitrogen；Helium is recycled after liquid nitrogen heat exchanger helium outlet (8b) discharge through two level backheat
Heat exchanger helium entrance (10c) is discharged into two level Recuperative heat exchanger (10), and by two level Recuperative heat exchanger helium outlet (10d)
Through liquid helium heat exchanger helium entrance (9c) into liquid helium heat exchanger (9)；From the cycle of liquid helium heat exchanger helium outlet (9d) discharge
Helium enters test object, and monitor inlet temperature (12) and inlet pressure (13) after low temperature air inlet valve (11a) adjustment；Test
The cycle helium of object discharge recycles helium return air inlet after low temperature return-air valve (11b) adjustment through two level Recuperative heat exchanger
(10e) is discharged into two level Recuperative heat exchanger (10) and by two level Recuperative heat exchanger cycle helium return air outlet (10f)；Hereafter,
It recycles helium and recycles helium return air inlet (7e) into level-one Recuperative heat exchanger (7) and initial cycle through level-one Recuperative heat exchanger
Helium exchanges heat；Helium is back to after discharging from level-one Recuperative heat exchanger cycle helium return air outlet (7f) through room temperature return-air valve (4b) to follow
Ring pump (1) completes cycle；
The circulated helium of bypass is expressed as follows：The high-pressure helium part that (1) generation is pumped by circulated helium is adjusted through by-passing valve (4)
It is directly back to circulated helium pump (1) afterwards, this road flow is monitored by bypass flow meter (5b).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410382817.XA CN105445046B (en) | 2014-08-06 | 2014-08-06 | A kind of refrigeration and pressure charging system for pipeline structure environmental simulation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410382817.XA CN105445046B (en) | 2014-08-06 | 2014-08-06 | A kind of refrigeration and pressure charging system for pipeline structure environmental simulation |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105445046A CN105445046A (en) | 2016-03-30 |
| CN105445046B true CN105445046B (en) | 2018-06-26 |
Family
ID=55555506
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410382817.XA Active CN105445046B (en) | 2014-08-06 | 2014-08-06 | A kind of refrigeration and pressure charging system for pipeline structure environmental simulation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105445046B (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107238450A (en) * | 2017-06-05 | 2017-10-10 | 安徽万瑞冷电科技有限公司 | A kind of cryogenic fluid transfer pipeline leakage heat test device and method |
| CN107525660B (en) * | 2017-08-07 | 2019-03-12 | 裴渐强 | A kind of low-temperature safety valve calibration equipment |
| CN108458888B (en) * | 2018-02-07 | 2020-01-31 | 中国科学院理化技术研究所 | Performance testing device for low-temperature heat exchanger with temperature range below K |
| CN110792923A (en) * | 2018-08-01 | 2020-02-14 | 乔治洛德方法研究和开发液化空气有限公司 | Device and method for filling a container with a pressurized gas |
| CN115307918B (en) * | 2022-10-12 | 2023-03-24 | 天津航天瑞莱科技有限公司 | Test run test system of pulse type engine |
| CN117214224B (en) * | 2023-11-09 | 2024-02-09 | 西安聚能超导磁体科技有限公司 | Closed circulation sample testing temperature changing system |
| CN117723327B (en) * | 2023-12-07 | 2024-06-18 | 中国科学院近代物理研究所 | 2K negative pressure visual heat exchanger test platform, system and use method |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5402647A (en) * | 1994-03-25 | 1995-04-04 | Praxair Technology, Inc. | Cryogenic rectification system for producing elevated pressure nitrogen |
| CN102200356B (en) * | 2001-02-23 | 2014-03-26 | 布鲁克斯自动化公司 | Ultra-low temperature closed-loop recirculating gas chilling system |
| CN203010996U (en) * | 2012-12-21 | 2013-06-19 | 山东大学 | Rapid refrigeration system utilizing liquid nitrogen |
| CN203298519U (en) * | 2013-04-18 | 2013-11-20 | 南京瑞柯徕姆环保科技有限公司 | Overlaid cold capacity circulating and refrigerating device |
| CN204008175U (en) * | 2014-08-06 | 2014-12-10 | 天津航天瑞莱科技有限公司 | A kind of refrigeration for pipeline structure environmental simulation and pressure charging system |
-
2014
- 2014-08-06 CN CN201410382817.XA patent/CN105445046B/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| CN105445046A (en) | 2016-03-30 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105445046B (en) | A kind of refrigeration and pressure charging system for pipeline structure environmental simulation | |
| WO2018227976A1 (en) | Helium gas experiment loop device for fusion reactor | |
| CN106896134B (en) | A kind of overcritical low temperature thermal technology Testing Platform of double media | |
| CN204008175U (en) | A kind of refrigeration for pipeline structure environmental simulation and pressure charging system | |
| CN106151865B (en) | One kind being used for pipeline low-temperature cyclic loading test system | |
| CN209800101U (en) | Performance testing device for engine fuel regulator | |
| CN108036538B (en) | Superfluid helium low-temperature circulating system | |
| CN109556984A (en) | Fast aeration chilldown system and its application method | |
| CN204592847U (en) | A kind of for pipeline low-temperature cyclic loading test system | |
| CN110985367A (en) | High-speed hydraulic pump performance test device | |
| CN115419829B (en) | High-pressure liquid hydrogen conveying system and method for liquid hydrogen engine test | |
| CN107905992B (en) | Ultralow temperature cold compressor performance test system | |
| CN107421764A (en) | A kind of liquid-cooling heat radiation equipment performance test system | |
| CN216524275U (en) | Mass method liquid hydrogen flow standard device driven by liquid hydrogen pump | |
| CN111610090A (en) | Pressure cycle test system and method for gas container | |
| CN114753996A (en) | Water pump test bench and test method | |
| CN205203423U (en) | Refrigerating system suitable for aircraft fuel oil system icing tests | |
| CN215492487U (en) | Test platform of supercritical carbon dioxide printed circuit board type heat exchanger | |
| RU2403547C1 (en) | Test stand | |
| CN207133059U (en) | A kind of liquid-cooling heat radiation equipment performance test system | |
| CN215764594U (en) | Gas pressure stabilizing and adjusting system | |
| CN110630588A (en) | Hydraulic test bed for testing low-temperature static performance of hydraulic valve | |
| CN210829976U (en) | Hydraulic test bed for testing low-temperature static performance of hydraulic valve | |
| CN204390751U (en) | A kind of nuclear power plant reactor coolant system injector testing system | |
| CN107816431B (en) | Nuclear second-level high-pressure safety injection pump environment simulation test system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| CB02 | Change of applicant information | ||
| CB02 | Change of applicant information |
Address after: No. 9, central North Third Street, west area of Tanggu District Development Zone, Tianjin Applicant after: Tianjin Aerospace Ruilai Technology Co., Ltd. Applicant after: BEIJING AEROSTANDARD TECHNOLOGY CO., LTD. Applicant after: Beijing Institute of Structure and Environment Engineering Applicant after: China Academy of Launch Vehicle Technology Address before: No. 9, central North Third Street, west area of Tanggu District Development Zone, Tianjin Applicant before: Tianjin Aerospace Ruilai Technology Co., Ltd. Applicant before: Beijing Space Star Technology Equipment Company Applicant before: Beijing Institute of Structure and Environment Engineering Applicant before: China Academy of Launch Vehicle Technology |
|
| GR01 | Patent grant | ||
| GR01 | Patent grant |