CN105699413B - Work in the simulation system for thermodynamics exhaust system research of room temperature warm area - Google Patents

Work in the simulation system for thermodynamics exhaust system research of room temperature warm area Download PDF

Info

Publication number
CN105699413B
CN105699413B CN201610104049.0A CN201610104049A CN105699413B CN 105699413 B CN105699413 B CN 105699413B CN 201610104049 A CN201610104049 A CN 201610104049A CN 105699413 B CN105699413 B CN 105699413B
Authority
CN
China
Prior art keywords
storage tank
sensor
tube
room temperature
warm area
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
Application number
CN201610104049.0A
Other languages
Chinese (zh)
Other versions
CN105699413A (en
Inventor
黄永华
陈忠灿
李鹏
孙培杰
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shanghai Jiaotong University
Shanghai Aerospace System Engineering Institute
Original Assignee
Shanghai Jiaotong University
Shanghai Aerospace System Engineering Institute
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Shanghai Jiaotong University, Shanghai Aerospace System Engineering Institute filed Critical Shanghai Jiaotong University
Priority to CN201610104049.0A priority Critical patent/CN105699413B/en
Publication of CN105699413A publication Critical patent/CN105699413A/en
Application granted granted Critical
Publication of CN105699413B publication Critical patent/CN105699413B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N25/00Investigating or analyzing materials by the use of thermal means
    • G01N25/02Investigating or analyzing materials by the use of thermal means by investigating changes of state or changes of phase; by investigating sintering
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/10Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/06Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
    • F28F13/12Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media by creating turbulence, e.g. by stirring, by increasing the force of circulation
    • GPHYSICS
    • G05CONTROLLING; REGULATING
    • G05DSYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
    • G05D16/00Control of fluid pressure
    • G05D16/20Control of fluid pressure characterised by the use of electric means

Abstract

The present invention relates to a kind of simulation systems for thermodynamics exhaust system research for working in room temperature warm area, wherein storage tank is used to hold propellant, it is provided with propellant intake line and gas exhaust piping, heat exchange injection apparatus is located inside storage tank, heat exchange and injection dual function are coupled, heater is arranged on the outside of storage tank, for simulating storage tank leakage heat, tonifying Qi pressure piping is used to be pressurized into storage tank, sensor is provided on the pipeline set on storage tank and storage tank, data collecting instrument is connect with sensor, it acquires the data of sensor and is transferred to computer, the data of computer receiving sensor, and after making logic judgment, the keying of valve and circulating pump on order control piper is sent by logic controller, realize the automation control for meeting thermodynamics exhaust disciplinarian request.The present invention is operated in room temperature warm area, and system structure simply, securely and reliably, can be effectively used for realizing certainly supercharging and exhaust pressure control process simulation of the fluid in closed container after heated generation gas-liquid phase transition.

Description

Work in the simulation system for thermodynamics exhaust system research of room temperature warm area
Technical field
The present invention relates to a kind of for studying the simulation system of thermodynamics exhaust system, room is worked in more particularly, to one kind The simulation system for thermodynamics exhaust system research of warm area.
Background technology
Cryogenic propellant (such as liquid hydrogen LH2, liquid oxygen LO2, liquid methane LCH4Deng) in long-term in-orbit storage process, due to sky Between environment leakage heat so that cryogenic propellant is vaporized so as to cause pressure rise in storage tank, when reaching tank designs pressure allowable value When, it is necessary to it gives and discharges.Since gas-liquid unobvious detach under microgravity, according to the method being periodically directly vented, then will cause Outside big quantity of fluid discharge case, propellant mass is caused to lose.Seek a kind of not only can effectively control storage tank pressure but also can be in phase By the new technical means of cryogenic propellant minimization of loss under the conditions of, the long-term in-orbit storage of cryogenic propellant is actually weighed It will.It is proposed in the United States Patent (USP) of Publication No. US5398515 by Rockwell Internationnal Corporation Thermodynamics exhaust system (Thermodynamic Vent System, TVS) is the effective solution party that disclosure satisfy that this requirement One of case, it can realize only exhaust not drain under ground 1g gravity and space 0g gravity environments, can also eliminate in storage tank The thermally stratified layer of liquid controls storage tank pressure under double action.But the patent is for LO2、LH2Etc. cryogens storage tanks, it is real Existing technical difficulty is big, safety requirements is high, involves great expense, and is not suitable for the general character regular basis research of thermodynamics exhaust technique.It is stored up Case is obturator, can not either be inconvenient to replace internal heat assembly of elements or the configuration of component is operated;In case not Relate to reflect in real time that the temperature measurement system of fluid thermally stratified layer level and reflection liquid fill/remaining liquid level are surveyed in storage tank Amount system;Also lack the enabled condition that visual observation is carried out to gas-liquid two-phase fluid thermodynamic state in storage tank.Due to low temperature There are huge thermal fields, the tank system thermal insulation control of the patent between fluid and atmospheric environment to be not easy to realize;It works under low temperature Low-power consumption circulating pump technical difficulty it is big.
Find do not have provided on ground by the use of boiling temperature higher refrigerant as working medium is simulated both at home and abroad through retrieval Thermodynamics is vented the device or system of common technology research.This device or system requirements can facilitate, are real at low cost The measurement observation of medium heat mechanical change process in existing storage tank and the assessment of each composition cell operation performance of thermodynamics exhaust, permit Perhaps babinet frequently open and replace, be configured inside device.
Invention content
It is an object of the present invention to overcome the above-mentioned drawbacks of the prior art and provide a kind of simple in structure, safety Reliably, the simulation system for thermodynamics exhaust system research for working in room temperature warm area that is at low cost, being easy to disassembling, assembling and replacing.This The simulation system of invention can be effectively used for realizing fluid heated supercharging certainly and exhaust occurred after gas-liquid phase transition in closed container Pressure control process simulation.
The purpose of the present invention can be achieved through the following technical solutions:
A kind of simulation system for thermodynamics exhaust system research for working in room temperature warm area, including:
Storage tank:Both ends carry the cylinder of ellipse head, for holding propellant, are provided with propellant intake line With gas exhaust piping, valve is set on propellant intake line and gas exhaust piping;
Exchange heat injection apparatus:Inside storage tank, the inside of lower end and storage tank is connected as circulation loop by pipeline, is following Loop back path is equipped with solenoid valve and circulating pump, and upper end setting outlet, outlet is with stretching out the propellant efferent duct outside storage tank Road connects, and solenoid valve is set on propellant output pipe;
Heater:It is arranged on the outside of storage tank, for simulating storage tank leakage heat;
Tonifying Qi pressure piping:It is communicated with inside storage tank, for being pressurized into storage tank;
Sensor:Including being pressed inside monitoring storage tank, on propellant intake line, propellant output pipe and gas exhaust piping Power, flow, liquid level, the pressure sensor of temperature, flow sensor, differential pressure liquid level sensor and temperature sensor;
Data collecting instrument:It is connect with sensor, acquire the data of sensor and is transferred to computer;
Computer:The data of receiving sensor, and after making logic judgment, pass through logic controller and send order control electromagnetism The automation control for meeting thermodynamics exhaust disciplinarian request is realized in the open and close of valve and circulating pump.
The heat exchange injection apparatus include three double pipe heat exchangers, dispenser, mounting flange and injector, described three Double pipe heat exchanger includes the inner tube, intermediate tube and the outer tube that are arranged concentrically, between the inner tube, the intermediate tube and outer tube Interlayer simultaneously connect with the dispenser, composition three double pipe heat exchangers a round trip heat exchanger channels, the inner tube Interlayer between intermediate tube is another heat exchanger channels of three double pipe heat exchangers, and between the inner tube and intermediate tube Interlayer connects inlet tube and outlet, the mounting flange are welded to connect, and Method for Installation simultaneously with inner tube, intermediate tube and outer tube Blue center opens up the opening connected with internal tube, and the injector is mounted on outer tube outer wall, and with intermediate tube and outer tube Between interlayer communicate.The interlayer silk of spiral winding disturbance in an axial direction between the inner tube and intermediate tube, and the disturbance silk is tight Outer wall of inner tube, interlayer between the intermediate tube and outer tube silk of spiral winding disturbance in an axial direction are pasted, and during the disturbance silk is close to Between pipe outer wall.The disturbance silk is copper wire.Silk is disturbed by setting, enhances flow disturbance, improves heat exchanger efficiency.
The dispenser is the cavity body structure being made of top surface and bottom surface, the bottom surface of the dispenser simultaneously with it is interior Pipe, intermediate tube and outer tube connect, and the circular hole communicated with inner tube are offered among the bottom surface of the dispenser, around circular hole Weld access hole is offered, the interlayer between the weld access hole and intermediate tube and outer tube communicates.The top surface of the dispenser For the curve form of evagination, curve form reduce fluid via the dispenser enter the three double pipe heat exchangers outer tube with The energy loss generated during interlayer between intermediate tube.
The injector shares several groups, and every group of injector is located in a plane of outer tube outer wall, difference group injection It is arranged in parallel between device, every group of injector shares 4, and along outer tube outer wall into quadrant week tangential distribution, the injector is The L-shaped playpipe to smoothly transit, for arrival end vertical connection on outer tube wall, the port of export is parallel to outer tube circumference tangential direction. The injector is separated by 90 degree of tangentially fired fluids in outer tube circumferencial direction, and injector realizes cryogenic propellant in storage tank Interior disturbance enhances the effect for eliminating thermally stratified layer.Offer screw thread on the inside of the port of export of the injector, can by Whether the port of export of injector is threaded into plug to realize on-demand non-homogeneous injection, to adapt to practical in-orbit cryogenic propellant The storage tank sun is to the situation of unlucky nonuniform heat flux.Similarly, screw thread can also be opened up on the outside of the port of export of injector, twisted Enter the nut of closing to block injector.
The heat exchange injection apparatus realizes two fluids heat exchange and wherein stream of fluid injection will return to storage tank coupling The dual function being integrated..
The storage tank both ends are respectively upper end head and lower end head, and upper end head passes through connecting flange and storage tank main body Be connected, realize storage tank open wide and it is closed, can be by opening connection method when needing to install, replacing storage tank inside unit under test Orchid simultaneously removes upper end head realization;The mounting flange is fixed on the inside bottom of storage tank lower end head, and outside storage tank Equipped with circulation line, which is connected in lower end head, and with being connected inside storage tank, which leads to The opening crossed on mounting flange is connected with internal tube.
By circulation line head end caudad direction, solenoid valve, valve, filter, stream are sequentially set on circulation line Quantity sensor, circulating pump, flow sensor and solenoid valve draw throttling pipeline between circulating pump and flow sensor, and The throttling pipeline is connected with inlet tube, on throttle pipe road be equipped with solenoid valve and throttle valve, filter for prevent impurity into It becomes a mandarin in gauge.
Valve, flow sensor and valve, the propellant output pipe are sequentially set on the gas exhaust piping Solenoid valve is equipped with, the tonifying Qi pressure piping is equipped with valve, and the tonifying Qi pressure piping is connect with nitrogen cylinder, described Propellant intake line be equipped with valve, the pressure sensor by pipeline directly with storage tank inside connect.
The storage tank outer wall is symmetrically opened up there are two observation window, for observing gas-liquid two inside storage tank by high speed camera Phase flowing law.
The storage tank bottom is set there are three the supporting leg with idler wheel so that storage tank can be moved easily, three branch midlegs There is epoxy plate interlayer to reduce leakage heat of the storage tank by supporting leg.
The differential pressure liquid level sensor is arranged in storage tank outer bottom, for measuring the liquid level of storage tank, is passed with differential pressure liquid level The gas phase pressure guiding pipe that sensor is connected is arranged with liquid phase pressure guiding pipe along storage tank internal face, not only reduces the shadow of external environment leakage heat It rings, decreases the influence for fluid flow fields in storage tank and thermal field.One plumbing bar is set in storage tank, the equidistant cloth on plumbing bar It is equipped with temperature sensor.Plumbing bar is thin epoxy bar, reduces influence of plumbing bar itself heat conduction for thermal field in storage tank.
The heater is made of the semi-open type heating watt for being close to four power adjustables of storage tank outside wall surface, both can be with mould Intend storage tank and uniformly leak heat, the non-homogeneous leakage heat of storage tank can also be simulated.
Compared with prior art, the present invention has the following advantages and beneficial effects:
1st, new heat exchange injection apparatus is employed in the present invention, by two fluids heat exchange and the stream of wherein one return storage tank Body injection dual function coupling is integrated, and the injection apparatus that exchanges heat is independent device, using flanged joint, facilitate installation, Dismounting and replacement., the heat exchanger used in injection apparatus that exchanges heat is three double pipe heat exchangers, and heat exchange is improved by increasing heat exchange area Efficiency.By retaining fluid in storage tank and discharging the wall-type heat exchange between fluid, the equalizing temperature for retaining fluid is realized;It changes Runner spiral cloth has disturbance silk in thermal spray equipment heat exchanger so that simple in structure, compact, heat exchange efficiency is high;Heat exchange injection dress It puts and is sprayed using several groups of injectors of quadrant week tangential distribution, stirring effect is apparent, can also easily vary injection The effective quantity of head and distribution, to realize on-demand non-homogeneous injection, with adapt to the practical in-orbit cryogenic propellant storage tank sun to The situation of unlucky nonuniform heat flux.Exchanging heat, injection apparatus is simple in structure, heat exchange efficiency is high, jeting effect is apparent, can be effective The thermally stratified layer in cryogenic propellant storage tank is eliminated, achievees the purpose that auxiliary control cryogenic propellant storage tank pressure, helps to realize The long-term storage of cryogenic propellant.
2nd, in present system, all components for thermodynamics exhaust system research all work under room temperature warm area, drop Low technology and cost requirement to equipment such as circulating pump, liquid level gauge, flowmeters, present system experiment is safe, very It is suitable under safe and reliable and inexpensive prerequisite, gropes and be disclosed for the thermodynamics exhaust of gas-liquid phase transition fluid The basic general character rule of technology.
3rd, in present system, be provided with it is multiple including monitoring storage tank inside, propellant intake line, propellant efferent duct Road and pressure, flow, liquid level, the pressure sensor of temperature, flow sensor, differential pressure liquid level sensor and temperature on gas exhaust piping Sensor, and data collecting instrument is connect with sensor, is acquired the data of sensor and is transferred to computer, and computer, which receives, to be passed The data of sensor, and after making logic judgment, pass through unlatching and pass that logic controller sends order control solenoid valve and circulating pump It closes, realizes the automation control for meeting thermodynamics exhaust disciplinarian request.Therefore, it adopts in present system and carries out in an automated fashion Thermodynamics exhaust system research.
Description of the drawings
Fig. 1 is the structure diagram of simulation system of the present invention;
Fig. 2 is the specific three dimensional structure diagram in dotted line frame I in Fig. 1;
Fig. 3 is broken section structure diagram in dotted line frame II in Fig. 2;
Fig. 4 is the dimensional structure diagram of heat exchange injection apparatus;
Fig. 5 is the schematic cross-sectional view of heat exchange injection apparatus;
Fig. 6 is A-A faces schematic cross-sectional view in Fig. 4;
Fig. 7 is B-B faces schematic cross-sectional view in Fig. 4;
Fig. 8 is enlarged structure schematic diagram at C in Fig. 5.
Figure label:1 is storage tank, and 2 be plumbing bar, and 3 be heat exchange injection apparatus, and 4 be differential pressure liquid level sensor, 5,10,13,19 For solenoid valve, 6,16,18,21 it is shut-off valve, 29 is valve, 7 be filter, and 8,11,17 be flow sensor, and 9 be circulating pump, 12 be throttle valve, and 14 be heater, and 15 be pressure sensor, and 20 be tonifying Qi pressure piping, and 22 be computer, and 23 be logic control Device, 24 be data collecting instrument, and 25 be interlayer, and 26 be observation window, and 27 be connecting flange, and 28 be upper end head, and 30 be mounting flange, 31 be three double pipe heat exchangers, and 32 be dispenser, and 33 be injector, and 34 be weld access hole, and 35 be inner tube, and 36 be intermediate tube, 37 It is outlet for outer tube, 38,39 be disturbance silk, and 40 be inlet tube.
Specific embodiment
The present invention is described in detail with specific embodiment below in conjunction with the accompanying drawings.
Embodiment
A kind of simulation system for thermodynamics exhaust system research for working in room temperature warm area, as shown in FIG. 1 to 3, Including storage tank 1, heat exchange injection apparatus 3, heater 14, tonifying Qi pressure piping 20, data collecting instrument 24 and computer 22, wherein, 1 both ends of storage tank carry the cylinder of ellipse head, for holding propellant, are provided with propellant intake line and exhaust pipe Road sets valve on propellant intake line and gas exhaust piping;Heat exchange injection apparatus 3 is located inside storage tank 1, lower end and storage tank 1 inside is connected as circulation loop by pipeline, and solenoid valve and circulating pump 9, upper end setting outlet are equipped on circulation loop 38, outlet 38 is connected with stretching out the propellant output pipe outside storage tank 1, and solenoid valve is set on propellant output pipe; Heater 14 is arranged on 1 outside of storage tank, leaks heat for simulating storage tank 1;It communicates, is used for inside tonifying Qi pressure piping 20 and storage tank 1 It is pressurized into storage tank 1;Sensor is included inside monitoring storage tank 1, propellant intake line, propellant output pipe and gas exhaust piping Upper pressure, flow, liquid level, the pressure sensor 15 of temperature, flow sensor 8,11,17, differential pressure liquid level sensor 4 and temperature pass Sensor;Data collecting instrument 24 is connect with sensor, is acquired the data of sensor and is transferred to computer 22;Computer 22, which receives, to be passed The data of sensor, and after making logic judgment, pass through logic controller 23 and send order control solenoid valve, valve and circulating pump 9 It opens and closes, realizes the automation control for meeting thermodynamics exhaust disciplinarian request.
The storage tank 1 of the present embodiment is diameter 450mm, high 790mm, wall thickness 3mm, and both ends carry major and minor axis 2:1 ellipse head Cylinder, 1 both ends of storage tank are respectively upper end head 28 and lower end head, and upper end head 28 passes through connecting flange 27 and storage tank master Body is connected, realize storage tank 1 open wide and it is closed, when needing to install, replacing unit under test inside storage tank, can pass through and open connection Flange 27 simultaneously removes upper end head realization;Mounting flange 30 is fixed on the inside bottom of 1 lower end head of storage tank, and outside storage tank 1 Portion is equipped with circulation line, which is connected in lower end head, and is connected with 1 inside of storage tank, the circulation line tail End is connected by the opening on mounting flange 30 with 35 inside of inner tube.
By circulation line head end caudad direction, solenoid valve 5, shut-off valve 6, filter are sequentially set on circulation line 7th, flow sensor 8, circulating pump 9, flow sensor 11 and solenoid valve 13 are drawn between circulating pump 9 and flow sensor 11 Throttle pipeline, and the throttling pipeline is connected with inlet tube 40, and solenoid valve 10 and throttle valve 12 are equipped on throttle pipe road.
Shut-off valve 16, flow sensor 17 and shut-off valve 18 are sequentially set on gas exhaust piping, on propellant output pipe Equipped with solenoid valve 19, tonifying Qi pressure piping 20 is equipped with shut-off valve 21, and tonifying Qi pressure piping 20 is connect with nitrogen cylinder, and propellant is defeated Enter pipeline equipped with valve 29, pressure sensor 15 is directly connected by pipeline with 1 inside of storage tank.What flow sensor 17 measured It is the flow rate of refrigerant gas being evaporated from storage tank, which is only measuring the hot stage use of the practical leakage of storage tank, making in TVS With the stage, the flowmeter does not use, and storage tank refrigerant gas is discharged by 19 place pipeline of solenoid valve at this time.
1 outer wall of storage tank is symmetrically opened up there are two observation window 26, for observing gas-liquid two-phase inside storage tank by high speed camera Flowing law.1 bottom of storage tank is set there are three the supporting leg with idler wheel so that storage tank 1 can be moved easily, and three branch midlegs have Thickness is the epoxy plate interlayer 25 of 50mm to reduce leakage heat of the storage tank 1 by supporting leg.
Differential pressure liquid level sensor 4 is arranged in 1 outer bottom of storage tank, for measuring the liquid level of storage tank 1, with differential pressure liquid level sensor 4 connected gas phase pressure guiding pipes are arranged with liquid phase pressure guiding pipe along 1 internal face of storage tank, not only reduce the shadow of external environment leakage heat It rings, decreases the influence for fluid flow fields and thermal field in storage tank 1.
One plumbing bar 2 of setting, temperature sensor is arranged in equal spacing on plumbing bar 2 in storage tank 1.Plumbing bar 2 is diameter 5mm's Thin epoxy bar, one end is threadedly secured to storage tank upper end head inside top, hangs on inside storage tank vertically, detachably more It changes, reduces influence of plumbing bar itself heat conduction for thermal field in storage tank 1.
Heater 14 is made of the semi-open type heating watt for being close to four power adjustables of 1 outside wall surface of storage tank, in the present embodiment, Semi-open type heating watt peak power is 220W, can both simulate storage tank and uniformly leak heat, can also simulate the non-homogeneous leakage heat of storage tank.
As Figure 4-8, heat exchange injection apparatus 3 includes three double pipe heat exchangers 31, dispenser 32, mounting flange 30 and spray Emitter 33, three double pipe heat exchangers 31 include the inner tube 35 that the outer diameter that is arranged concentrically is respectively φ 14mm, φ 19mm and φ 24mm, Intermediate tube 36 and outer tube 37, the interlayer between inner tube 35, intermediate tube 36 and outer tube 37 connect simultaneously with dispenser 32, form three sets One round trip heat exchanger channels of pipe heat exchanger 31, the interlayer between inner tube 35 and intermediate tube 36 are three double pipe heat exchangers 31 Another heat exchanger channels, and the interlayer between inner tube 35 and intermediate tube 36 connects inlet tube 40 and outlet 38, mounting flange 30 It is welded to connect simultaneously with inner tube 35, intermediate tube 36 and outer tube 37, and 30 center of mounting flange opens up what is connected with 35 inside of inner tube Opening, injector 33 is mounted on 37 outer wall of outer tube, and the interlayer between intermediate tube 36 and outer tube 37 communicates.Inner tube 35 is in Between the interlayer silk 39 of spiral winding disturbance in an axial direction between pipe 36, and the disturbance silk 39 is close to 35 outer wall of inner tube, intermediate tube 36 with The interlayer silk 39 of spiral winding disturbance in an axial direction between outer tube 37, and the disturbance silk 39 is close to 36 outer wall of intermediate tube.Disturb silk 39 Copper wire for a diameter of 1.5mm.Silk 39 is disturbed by setting, enhances flow disturbance, improves heat exchanger efficiency.
Dispenser 32 is the cavity body structure being made of top surface and bottom surface, the bottom surface of dispenser 32 simultaneously with inner tube 35, intermediate Pipe 36 and outer tube 37 connect, and the circular hole communicated with inner tube 35 is offered among the bottom surface of dispenser 32, is opened up around circular hole There is weld access hole 34, the interlayer between weld access hole 34 and intermediate tube 36 and outer tube 37 communicates.The top surface of dispenser 32 is evagination Curve form, curve form reduce fluid via the dispenser enter the three double pipe heat exchangers outer tube and intermediate tube Between interlayer when the energy loss that generates.
Injector 33 shares several groups, and every group of injector 33 is located in a plane of 37 outer wall of outer tube, difference group injection It is arranged in parallel between device 33, axial distance 24mm, every group of injector 33 shares 4, along 37 outer wall of outer tube into cutting in quadrant week To distribution, injector 33 is the L-shaped playpipe to smoothly transit, and for arrival end vertical connection on 37 side wall of outer tube, the port of export is parallel In 37 circumference tangential direction of outer tube.Injector is separated by 90 degree of tangentially fired fluids in outer tube circumferencial direction, and injector realizes Disturbance of the cryogenic propellant in storage tank enhances the effect for eliminating thermally stratified layer.The port of export internal diameter of injector be 2mm, inside Offer screw thread, can by realizing on-demand non-homogeneous injection whether the port of export of injector is threaded into plug, with Adapt to situation of the practical in-orbit cryogenic propellant storage tank sun to unlucky nonuniform heat flux.It similarly, can also be in injector The port of export on the outside of open up screw thread, be screwed into the nut of closing to block injector.
Heat exchange injection apparatus 3 realizes two fluids heat exchange and wherein stream of fluid injection return storage tank 1 is coupled as one The dual function of body.
The operation when simulation system of the present invention uses is as follows:
It is initially turned off valve 6,16,18,21,29 to be in closing, solenoid valve 5,10,13,19 is in closed state, first It opens valve 29 and is added in R141b refrigerants working medium in storage tank 1 by charging mouth, pass through differential pressure liquid level sensor in filling process 4 read real-time level in storage tank, and until storage tank liquid level reaches predetermined value, valve 29 is closed in stopping filling.Heater 14 is transferred to Predetermined power, opening stop valve 16,18 after 17 stable reading of flow sensor, record the reading of flow sensor 17 respectively V, the reading T of the thermometer before the reading P of pressure sensor 15 and pressure sensor 17.It is actually entered by formula (1) calculating The heat of storage tank
Q=v. ρ Δs h (1)
ρ is density of the working medium under pressure P, temperature T-shaped state in formula, and △ h are the latent heat of vaporization of the working medium under pressure P.
After obtaining the heat for actually entering storage tank, shut-off valve 16,18 is closed, thermodynamics exhaust system (TVS) is carried out and acts on Under pressure control procedure:As heat constantly enters storage tank, the pressure in case gradually rises, and is measured when by pressure sensor 15 Pneumatic die cushion pressure PPneumatic die cushionReach the upper limit P of predetermined pressure control bandmaxWhen, the opens solenoid valve 5,13 under the effect of logic controller 23 And circulating pump 9, injector 33 is run, circulating pump 9 extracts the liquid or biphase gas and liquid flow in storage tank, it is pressed directly into injector It is sprayed after 33 and returns to storage tank, the liquid in storage tank is stirred with this, eliminate thermally stratified layer, the pressure of storage tank is reduced, until the pressure of storage tank Power is reduced to pressure lower limit Pmin.In 33 course of work of injector, when the corresponding saturation pressure of storage tank liquid medium temperature PsatWhen reaching the lower limit of press belt, by 23 opens solenoid valve 10,19 of logic controller, run throttle valve 12 and bushing type is changed Hot device 31, the partially liq that circulating pump 9 is sent out obtained cold fluid by the cooling of throttle valve 12, and entered double pipe heat exchanger 31 Cold end and the liquid of heat exchanger hot junction flowing carry out heat exchange, and own temperature is increased and completely vaporized after absorbing heat, discharge storage Case;And the fluid in heat exchanger hot junction is returned in storage tank after being then cooled and is mixed with remaining liquid storage, solenoid valve 10,19 is with electricity later The closing of magnet valve 5,13 and circulating pump 9 and close.After the pressure controlling cycle under completing an above-mentioned TVS effect, storage tank pressure Power restarts to increase, until reaching press belt upper limit P againmax, the pressure controlling cycle under being acted on into next TVS.Such as This continuous operation can realize the simulation of the lower storage tank lengthy pressure continuous cycles variation of TVS effects.Pass through during experiment Differential pressure liquid level sensor 4, pressure sensor 15, flow sensor 8,11 can obtain liquid level in storage tank, Gas Gap Pressure, pump in real time Flow, throttling take out than etc. physical quantitys, by before and after being arranged in storage tank internal face, flow sensor, before and after throttle valve, exhaust ports And the temperature sensor on plumbing bar can obtain the thermally stratified layer situation in the temperature and storage tank of corresponding position.In addition, experiment process In can also using high speed camera pass through observation window 26 carry out storage tank in gas-liquid phase transition rule visual research.After the completion of experiment Open valve 6 can discharge storage tank residue working medium.
The above description of the embodiments is intended to facilitate ordinary skill in the art to understand and use the invention. Person skilled in the art obviously can easily make these embodiments various modifications, and described herein general Principle is applied in other embodiment without having to go through creative labor.Therefore, the present invention is not limited to above-described embodiment, abilities Field technique personnel announcement according to the present invention, improvement and modification made without departing from the scope of the present invention all should be the present invention's Within protection domain.

Claims (10)

1. a kind of simulation system for thermodynamics exhaust system research for working in room temperature warm area, which is characterized in that including:
Storage tank (1):Both ends carry the cylinder of ellipse head, for holding propellant, are provided with propellant intake line With gas exhaust piping, valve is set on propellant intake line and gas exhaust piping;
Exchange heat injection apparatus (3):Internal positioned at storage tank (1), the inside of lower end and storage tank (1) is connected as being recycled back to by pipeline Road is equipped with solenoid valve and circulating pump (9) on circulation loop, and upper end setting outlet (38), outlet (38) is with stretching out storage tank (1) external propellant output pipe connection, solenoid valve is set on propellant output pipe;
Heater (14):It is arranged on the outside of storage tank (1), for simulating storage tank (1) leakage heat;
Tonifying Qi pressure piping (20):With being communicated inside storage tank (1), for being pressurized into storage tank (1);
Sensor:Including pressure on monitoring storage tank (1) inside, propellant intake line, propellant output pipe and gas exhaust piping, Flow, liquid level, the pressure sensor (15) of temperature, flow sensor (8,11,17), differential pressure liquid level sensor (4) and temperature pass Sensor;
Data collecting instrument (24):It is connect with sensor, acquire the data of sensor and is transferred to computer (22);
Computer (22):The data of receiving sensor, and after making logic judgment, pass through logic controller (23) and send order control The automation control for meeting thermodynamics exhaust disciplinarian request is realized in the open and close of solenoid valve and circulating pump (9).
2. a kind of simulation system for thermodynamics exhaust system research for working in room temperature warm area according to claim 1 System, which is characterized in that the heat exchange injection apparatus (3) includes three double pipe heat exchangers (31), dispenser (32), mounting flange (30) and injector (33),
Three double pipe heat exchangers (31) include the inner tube (35), intermediate tube (36) and the outer tube (37) that are arranged concentrically,
Interlayer between the inner tube (35), the intermediate tube (36) and outer tube (37) simultaneously with the dispenser (32) Connection forms a round trip heat exchanger channels of three double pipe heat exchangers (31),
Interlayer between the inner tube (35) and intermediate tube (36) is another heat exchanger channels of three double pipe heat exchangers (31), And the interlayer between the inner tube (35) and intermediate tube (36) connects inlet tube (40) and outlet (38),
It the mounting flange (30) while is welded to connect, and mounting flange with inner tube (35), intermediate tube (36) and outer tube (37) (30) center opens up the opening with being connected inside inner tube (35),
The injector (33) is on outer tube (37) outer wall, and the interlayer phase between intermediate tube (36) and outer tube (37) It is logical.
3. a kind of simulation system for thermodynamics exhaust system research for working in room temperature warm area according to claim 2 System, which is characterized in that the dispenser (32) is the cavity body structure being made of top surface and bottom surface, the dispenser (32) Bottom surface is connect simultaneously with inner tube (35), intermediate tube (36) and outer tube (37), is offered among the bottom surface of the dispenser (32) The circular hole communicated with inner tube (35) offers weld access hole (34), the weld access hole (34) and centre around circular hole Pipe (36) is communicated with the interlayer between outer tube (37).
4. a kind of simulation system for thermodynamics exhaust system research for working in room temperature warm area according to claim 2 System, which is characterized in that the injector (33) is several groups shared, and every group of injector (33) is positioned at one of outer tube (37) outer wall It in plane, is arranged in parallel between difference group injectors (33), every group of injector (33) shares 4, along outer tube (37) outer wall into four Cyclotomy week tangential distribution, the injector (33) is the L-shaped playpipe to smoothly transit, and arrival end vertical connection is in outer tube (37) On side wall, the port of export is parallel to outer tube (37) circumference tangential direction.
5. a kind of simulation system for thermodynamics exhaust system research for working in room temperature warm area according to claim 2 System, which is characterized in that described storage tank (1) both ends are respectively upper end head (28) and lower end head, and upper end head (28) passes through Connecting flange (27) is connected with storage tank main body, realizes the unlimited and closed of storage tank (1), the mounting flange (30) is fixed on storage The inside bottom of case (1) lower end head, and circulation line is equipped with outside storage tank (1), which is connected to lower end On end socket, and with being connected inside storage tank (1), which passes through in the opening on mounting flange (30) and inner tube (35) Portion connects.
6. a kind of simulation system for thermodynamics exhaust system research for working in room temperature warm area according to claim 5 System, which is characterized in that by circulation line head end caudad direction, solenoid valve (5), valve are sequentially set on circulation line (6), filter (7), flow sensor (8), circulating pump (9), flow sensor (11) and solenoid valve (13), in circulating pump (9) Throttling pipeline is drawn between flow sensor (11), and the throttling pipeline is connected with inlet tube (40), in throttling pipeline It is equipped with solenoid valve (10) and throttle valve (12).
7. a kind of simulation system for thermodynamics exhaust system research for working in room temperature warm area according to claim 1 System, which is characterized in that shut-off valve (16), flow sensor (17) and shut-off valve are sequentially set on the gas exhaust piping (18), the propellant output pipe is equipped with solenoid valve (19), and the tonifying Qi pressure piping (20) is equipped with shut-off valve (21), the tonifying Qi pressure piping (20) is connect with nitrogen cylinder, and the propellant intake line is equipped with valve (29), institute The pressure sensor (15) stated is by pipeline directly with being connected inside storage tank (1).
8. a kind of simulation system for thermodynamics exhaust system research for working in room temperature warm area according to claim 1 System, which is characterized in that described storage tank (1) outer wall offers observation window (26).
9. a kind of simulation system for thermodynamics exhaust system research for working in room temperature warm area according to claim 1 System, which is characterized in that the differential pressure liquid level sensor (4) is arranged in storage tank (1) outer bottom, for measuring the liquid of storage tank (1) Position, the gas phase pressure guiding pipe being connected with differential pressure liquid level sensor (4) are arranged with liquid phase pressure guiding pipe along storage tank (1) internal face;It is storing up One plumbing bar of setting (2), temperature sensor is arranged in equal spacing on plumbing bar (2) in case (1).
10. a kind of simulation system for thermodynamics exhaust system research for working in room temperature warm area according to claim 1 System, which is characterized in that the heater (14) is by being close to the semi-open type heating watts of four power adjustables of storage tank (1) outside wall surface Composition.
CN201610104049.0A 2016-02-25 2016-02-25 Work in the simulation system for thermodynamics exhaust system research of room temperature warm area Active CN105699413B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610104049.0A CN105699413B (en) 2016-02-25 2016-02-25 Work in the simulation system for thermodynamics exhaust system research of room temperature warm area

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610104049.0A CN105699413B (en) 2016-02-25 2016-02-25 Work in the simulation system for thermodynamics exhaust system research of room temperature warm area

Publications (2)

Publication Number Publication Date
CN105699413A CN105699413A (en) 2016-06-22
CN105699413B true CN105699413B (en) 2018-06-29

Family

ID=56222394

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610104049.0A Active CN105699413B (en) 2016-02-25 2016-02-25 Work in the simulation system for thermodynamics exhaust system research of room temperature warm area

Country Status (1)

Country Link
CN (1) CN105699413B (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108386708B (en) * 2018-01-12 2020-09-25 中国矿业大学 Pressure-control low-temperature storage tank with injection device
CN108150822A (en) * 2018-01-12 2018-06-12 中国矿业大学 A kind of low temperature liquid hydrogen storage tank with exhaust cold energy use
CN108163398B (en) * 2018-01-12 2019-09-13 中国矿业大学 A kind of efficiently controlling pressure cryogenic propellant storage tank with induction apparatus
CN109723962A (en) * 2019-02-26 2019-05-07 重庆零壹空间航天科技有限公司 Cryogenic propellant tank, long-term in-orbit integrated low temperature storage are for system and method
CN110282157A (en) * 2019-06-29 2019-09-27 西安交通大学 A kind of thermodynamics exhaust system using tangential centrifugal atomization
CN112550779B (en) * 2020-11-27 2022-04-12 中国运载火箭技术研究院 Ground integration test device and method for low-temperature propellant thermodynamic exhaust system
CN113963618B (en) * 2021-09-09 2024-02-02 西北工业大学 Working process simulation device of extrusion type liquid rocket engine
CN113984826B (en) * 2021-10-22 2022-10-28 西安交通大学 Visual experimental device for observing fluid phase state in low-temperature bare-wall storage tank
CN114384197B (en) * 2022-01-13 2022-12-02 西安交通大学 Experimental apparatus is observed to no pump drive's thermodynamics exhaust system flow state

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5398515A (en) * 1993-05-19 1995-03-21 Rockwell International Corporation Fluid management system for a zero gravity cryogenic storage system
CN1616884A (en) * 2003-11-14 2005-05-18 气体产品与化学公司 Fuel staging process for low NOx operations

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5398515A (en) * 1993-05-19 1995-03-21 Rockwell International Corporation Fluid management system for a zero gravity cryogenic storage system
CN1616884A (en) * 2003-11-14 2005-05-18 气体产品与化学公司 Fuel staging process for low NOx operations

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
Thermodynamic vent system performance testing with subcooled liquid methane and gaseous helium pressurant;R.H. Flachbart等;《Cryogenics》;20081231;217-222 *
工作于室温温区的热力学排气模拟与增压测试;陈忠灿等;《上海交通大学学报》;20170831;第51卷(第8期);946-953 *

Also Published As

Publication number Publication date
CN105699413A (en) 2016-06-22

Similar Documents

Publication Publication Date Title
CN105699413B (en) Work in the simulation system for thermodynamics exhaust system research of room temperature warm area
WO2018227976A1 (en) Helium gas experiment loop device for fusion reactor
CN201289435Y (en) Test stand for heat dispersion of radiator
CN101666704B (en) Quick test device and method for performances of trough type solar thermal collector
CN102564167B (en) Single-flow low-temperature spiral winding tube type heat exchanger with vacuum heat-insulation effect
CN107196012B (en) A kind of cold and hot fluid circulation for power battery bench test
CN112213355A (en) Supercritical carbon dioxide visual flow heat transfer experiment system
CN108717029A (en) Low-temperature control system and control method for vacuum QCM
CN105444591B (en) A kind of heat exchange injection apparatus for eliminating thermally stratified layer in cryogenic propellant storage tank
CN213600620U (en) Supercritical carbon dioxide visual flow heat transfer experiment system
CN104347125A (en) Double-channel natural circulation system device
CN206387180U (en) Many temperature electric heaters
CN103017814A (en) Hydrogen eliminating test system with safety protection function
CN109738486A (en) H2 heat management experimental rig and test method are put in a kind of suction of hydrogenation magnesium fuel cell
CN109030557A (en) A kind of electric automobile power battery temperature control plate testing device for heat transferring performance and method
CN203869557U (en) Liquid-nitrogen evaporator for X-ray single-crystal diffractometer
CN205981498U (en) Cryogenic insulation pipeline heat leakage measures on - line measuring device
CN104409118B (en) Thermal hydraulic experimental system and method for study on corrosion product deposit of fusion reactor
CN109974320A (en) A kind of high temperature deionized water cooling device
CN203173206U (en) Storage tank with heat tracing coil
CN205861586U (en) A kind of heat stability testing device of solid-liquid phase change material
CN110849205B (en) Water-cooling constant-pressure liquid supplementing water tank system and application method thereof
CN204494075U (en) There is the LNG filling measuring apparatus keeping function from pre-cold-peace low temperature
CN103983129A (en) Liquid nitrogen evaporator used for X-ray single-crystal diffractometer
CN103335411A (en) Centralized hot water supplying device with leakage alarm

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant