CN203190706U - 1-2K combined-type multilevel vessel refrigerating machine utilizing abundant cooling capacity - Google Patents
1-2K combined-type multilevel vessel refrigerating machine utilizing abundant cooling capacity Download PDFInfo
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- CN203190706U CN203190706U CN 201320026672 CN201320026672U CN203190706U CN 203190706 U CN203190706 U CN 203190706U CN 201320026672 CN201320026672 CN 201320026672 CN 201320026672 U CN201320026672 U CN 201320026672U CN 203190706 U CN203190706 U CN 203190706U
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Abstract
The utility model discloses a 1-2K combined-type multilevel vessel refrigerating machine utilizing abundant cooling capacity. The 1-2K combined-type multilevel vessel refrigerating machine comprises a precooling level low-frequency vessel refrigerating machine using a helium-4 working medium and a low-temperature level high-frequency vessel refrigerating machine using a helium-3 working medium. Due to the fact that the precooling level low-frequency vessel refrigerating machine is coupled with the precooling level low-frequency vessel refrigerating machine, 1-2K refrigerating temperature can be obtained under the condition that few helium-3 working medium is used. The abundant cooling capacity is extracted in the middle of a regenerator of the precooling level low-frequency vessel refrigerating machine, and the rate of using the cooling capacity of the precooling level vessel refrigerating machine is improved. Compared with a traditional two-level low-frequency vessel refrigerating machine using helium-3 as a working medium, the 1-2K combined-type multilevel vessel refrigerating machine utilizing the abundant cooling capacity has the advantages of being low in cost and convenient to obtain, and meanwhile the advantages of being compact in structure, long in service life and high in reliability of the traditional vessel refrigerating machine are remained.
Description
Technical field
The utility model relates to a kind of compound multistage vascular refrigerator, relates in particular to a kind of the utilization when having more than needed cold and uses helium-4 and helium-3 to be the compound multistage vascular refrigerator of the 1-2K low-and high-frequency of working medium.
Background technology
Low-temperature refrigeration technology has extensive and irreplaceable application in fields such as basic scientific research, low-temperature physics, commercial Application, medical biotechnology, national defense and military and space explorations, the scientific domain relevant with low temperature become core or high-tech representative at present, as large-scale science devices such as European hadron colliders.Arrange according to the world, low-temperature refrigeration technology is contained the following temperature province of 120K, the refrigeration modes of current whole low temperature warm area is ripe relatively, 1K and above warm area can adopt superfluid helium, liquid helium or other cryogenic liquid Dewar technology and mechanical type Refrigeration Technique to obtain, and 1K has technology such as adiabatic demagnetization refrigeration and dilution refrigeration with next.
In the low temperature warm area, 1-2K is a very crucial and special warm area, have a large amount of detector (mixing the gallium detector as germanium) and superconducting apparatus to be operated in this warm area on the one hand, the efficient acquisition of lower mK level warm area must be cooled off in advance at this warm area on the other hand.The refrigeration modes of current acquisition 1-2K warm area mainly contains superfluid helium find time technology and mechanical type Refrigeration Technique.
The superfluid helium a large amount of liquid helium of Technology Need of finding time, for guaranteeing the thermal insulation of system, system structure design is complicated unusually, simultaneously for guaranteeing the efficient utilization of helium, need to be equipped with complicated helium recovery and purification system, these all cause the superfluid helium technical costs height of finding time, and system architecture complexity and reliability are low.
The mechanical type Refrigeration Technique adopts the enclosed kind of refrigeration cycle to realize refrigeration effect, and refrigeration working medium (low temperature is generally helium) circulates in closed system, and it is few to have a helium consumption, compact conformation, long and reliability advantages of higher of life-span.Because the maximum helium exported country U.S. in the whole world exports restriction with helium as strategic materials, current global liquid helium supply day is becoming tight, and cost increases day by day, so the mechanical type refrigeration modes has obtained fast development and extensive use.
The mechanical type Refrigeration Technique mainly contains regenerative refrigerating technology and dividing wall type Refrigeration Technique, wherein the regenerative refrigerating technology is owing to adopted the efficient regenerator that is filled with high volumetric specific heat capacity backheat filler, have compact conformation efficient advantages of higher, obtained in fields such as low-temperature physics, military and national defense, Aero-Space using widely.Vascular refrigerator, GM refrigeration machine and sterlin refrigerator are three kinds of typical philip refrigerators, wherein vascular refrigerator does not have moving component at cold junction, has potential high reliability, and show according to existing open source literature data, only be the cryogenic temperature of the low frequency vascular refrigerator acquisition 1-2K of working medium with helium-3 in the current regenerative refrigerating technology, but it needs a large amount of helium-3, (Jiang N such as Jiang Ning, et al.Cryogenics, 2004,44:809.) adopt two-stage low frequency vascular refrigerator to obtain the lowest refrigerating temperature of 1.27K, but use the helium-3228 liter under the standard state altogether.
Helium-the 3rd, a kind of in the helium isotope, its content at occurring in nature is few, and only containing volume fraction in the normal helium is 1.3 * 10
-6The helium of %-3, be a kind of gas of rare costliness, the leading exporter U.S. of helium-3 has put into effect the relevant policies of restriction helium outlet in addition simultaneously, cause the substantial appreciation of prices of helium-3 in recent years, helium-3 rises from about 200 dollars/mark in 2007, rise to 2000 dollars/mark liter in 2009, the price of current helium-3 is about 10000 dollars/mark and rises, and expensive source simultaneously is difficult for acquisition.The Science magazine was delivered and is entitled as " Helium-3Shortage Could Put Freeze On Low-Temperature Research; helium-3 shortage makes the matter worse the low temperature correlative study " (A.Cho.Science in 2009,2009, Vol.306:778-779.) comment, article have been analyzed current helium-3 meeting in short supply and have been brought significantly and seriously influence to fields such as low-temperature physics.
Based on above-mentioned analysis as can be known, excavate novel not using helium-3 or use the 1-2K warm area Refrigeration Technique of helium-3 to the fast development of propelling low temperature related science research as far as possible less, it is most important to the influence of global association area to alleviate helium-3 shortage, provides a kind of compound multistage vascular refrigerator of 1-2K that can significantly reduce helium-3 consumption extremely urgent for this reason.
The utility model content
The utility model provides a kind of compound multistage vascular refrigerator of 1-2K that utilizes cold more than needed, by the coupling of different refrigeration modes and the extraction and application of cold more than needed, can under the prerequisite of using very a small amount of helium-3, efficiently obtain the cryogenic temperature of 1-2K, while compact conformation, reliability height.
Theory analysis and experimental study all find not only have refrigerating capacity at the regenerator cold junction in the low temperature pulse tubes refrigeration machine, also can export refrigerating capacity at regenerator near the part of cold junction, and in certain refrigerating capacity scope, cold that should extra output is very little to the influence of the lowest refrigerating temperature of vascular refrigerator and refrigerating capacity, generally be called cold more than needed, this part cold can be used for cooling off the more application of high-temperature region, and perhaps being used for provides precooling for multistage vascular refrigerator high temperature section regenerator.
And the correlation theory of vascular refrigerator points out to improve the volume that running frequency can significantly reduce refrigeration system, so improve the consumption that running frequency can significantly reduce helium-3, but because improving, frequency make gas and the heat exchange between the filler in the regenerator become insufficient, cause that THERMAL REGENERATOR EFFICIENCIES sharply descends, cause high-frequency vascular extremely low and can't obtain the cryogenic temperature of 1-2K in the efficient of low temperature warm area, it only is 3K that current high-frequency vascular refrigerator adopts the lowest refrigerating temperature of helium-3 working medium, for obtaining the cryogenic temperature of 1-2K, the precooling temperature that the more sum of series of high-frequency vascular refrigerator needs is lower (＜15K), refrigerator system also can become complicated unusually when lower precooling temperature was difficult to obtain, if with high-frequency vascular refrigerator with can lower temperature (＜15K) provide the low frequency vascular refrigerator of big pre-cold to be coupled together, utilize simultaneously that the cold more than needed in the regenerator comes to provide precooling for the higher warm area of high-frequency vascular refrigerator in the low temperature pulse tubes refrigeration machine, the compound multistage vascular refrigerator of this utilization cold more than needed will become a kind of compound vascular refrigerator of novel obtained 1-2K refrigeration warm area, because it is refrigeration working medium that the low frequency vascular refrigerator can adopt helium-4, so this compound vascular refrigerator only needs partly to adopt helium-3 at the high-frequency vascular refrigerator with smaller size smaller, namely adopt a spot of helium-3 gas just can obtain the cryogenic temperature of 1-2K, simultaneously owing to the cold more than needed that has utilized in the low frequency vascular refrigerator, so complete machine will have higher efficient, only just can obtain simultaneously the temperature of 1-2K with the precooling of single-stage low frequency vascular refrigerator, has compact conformation, advantages such as long-life.
In the compound multistage vascular refrigerator of 1-2K of the utilization that the utility model proposes cold more than needed, it is working medium that precooling level low frequency vascular refrigerator adopts traditional helium-4, can provide bigger pre-cold at 10K and above warm area, the cold more than needed at its regenerator middle part can be used to provide precooling at higher warm area simultaneously.High-frequency vascular refrigerator partly adopts helium-3 to be working medium, as previously mentioned, because this part running frequency is higher, structure is very compact, compare with the low frequency vascular refrigerator, its required helium-3 will rise less than 10 marks, thereby can realize using a small amount of helium-3 just can obtain the target of 1-2K warm area; Because the pre-cold of precooling level is enough big, obtains bigger phase modulation angle thereby can make low temperature inertia tube and air reservoir be cooled to lower temperature, and then provide more excellent phase angle (phase angle between mass flow and the pressure) for high-frequency vascular refrigerator; For increasing the cold junction pressure ratio of high-frequency vascular refrigerator, can between the regenerator of low temperature high-frequency vascular refrigerator different temperatures section, arrange the acoustic pressure amplifier that can increase pressure ratio; For reducing the consumption of helium-3, can select to use merely the low temperature inertia tube as pm mode, finally make complete machine obtain the cryogenic temperature of 1-2K efficiently.
Based on above-mentioned analysis and discussion, the utility model provides several pre-cold mould technical schemes, and following several compound multistage vascular refrigerator structures all can efficiently obtain the cryogenic temperature of 1-2K under the prerequisite of using less helium-3 working medium.
First kind of scheme is basic scheme of the present utility model, and be specific as follows:
A kind of compound multistage vascular refrigerator of 1-2K that utilizes cold more than needed, comprise precooling level low frequency vascular refrigerator unit and low temperature level high-frequency vascular refrigerator unit, described precooling level low frequency vascular refrigerator unit is single-stage low frequency vascular refrigerator, and its working medium of using is helium-4;
Described low temperature level high-frequency vascular refrigerator unit comprises the low temperature stage compressor, and the low temperature level regenerator hot end heat exchanger that is communicated with low temperature stage compressor outlet successively by pipeline, the low temperature level first precooling zone regenerator, the low temperature level first precooling zone regenerator cool end heat exchanger, the low temperature level second precooling zone regenerator, the low temperature level second precooling zone regenerator cool end heat exchanger, low temperature grade low-temp section regenerator, low temperature level cool end heat exchanger, low temperature level vascular, low temperature level vascular hot-side heat exchanger and low temperature level phase modulating mechanism; The refrigeration working medium that described low temperature level high-frequency vascular refrigerator unit adopts is helium-3;
Described precooling level low frequency vascular refrigerator unit and low temperature level high-frequency vascular refrigerator unit carry out a thermal coupling by the regenerator that is connected the low temperature level first precooling zone regenerator cool end heat exchanger and precooling level low frequency vascular refrigerator unit near cold junction first order heat bridge partly; Carry out the secondary thermal coupling by the second level heat bridge between the cool end heat exchanger that is connected the low temperature level second precooling zone regenerator cool end heat exchanger and precooling level low frequency vascular refrigerator unit.
In the technique scheme, concrete installation site between the regenerator of first order heat bridge and precooling level low frequency vascular refrigerator unit, need obtain by analog computation, i.e. the requirement of temperature and the more than needed refrigerating capacity of first order heat bridge in the installation site of the regenerator of the precooling level low frequency vascular refrigerator unit precooling temperature that need satisfy the low temperature level first precooling zone regenerator cool end heat exchanger and pre-cold.
Described low temperature level phase modulating mechanism can be selected multiple phase modulation parts for use, for example can adopt a kind of in little ports valve, inertia tube and the air reservoir or both combinations, for satisfying the needs of different occasions, mainly contain following two kinds of optimized technical scheme: wherein first kind of optimized technical scheme is: described low temperature level phase modulating mechanism is inertia tube, and this inertia tube is connected with described second level heat bridge with low temperature level vascular hot-side heat exchanger simultaneously, low temperature level phase modulating mechanism is inertia tube, the use amount of helium-3 gas is lower, and cost is lower.Second kind of optimized technical scheme is: described low temperature level phase modulating mechanism is inertia tube and the air reservoir that is communicated with inertia tube, and described inertia tube, air reservoir and low temperature level vascular hot-side heat exchanger are connected with described second level heat bridge simultaneously, select for use inertia tube and air reservoir as the phase modulation parts, further improve refrigeration performance, be suitable for the occasion that refrigeration performance is had relatively high expectations.
For further increasing the cold junction pressure ratio of low temperature level high-frequency vascular refrigerator unit, and then make low temperature level high-frequency vascular refrigeration unit obtain the cryogenic temperature of 1-2K efficiently, preferred as to first kind of basic scheme, be provided with between described low temperature level first precooling zone regenerator cool end heat exchanger outlet and the low temperature level second precooling zone regenerator entrance and be provided with first order acoustic pressure amplifier, this first order acoustic pressure amplifier is the major diameter pipe, the length of major diameter pipe be under its place temperature and pressure helium-3 gas corresponding wavelength 1/4.First order acoustic pressure amplifier can be realized the further amplification to low temperature level first precooling zone regenerator cool end heat exchanger outlet working medium acoustic pressure, has further improved the refrigeration performance of the utility model refrigeration machine.
For technique scheme, for reducing the use amount of helium-3 gas, described low temperature level phase modulating mechanism is inertia tube, and this inertia tube is connected with described second level heat bridge with low temperature level vascular hot-side heat exchanger simultaneously.Perhaps for obtaining the refrigeration machine of higher phase modulation performance, described low temperature level phase modulating mechanism is inertia tube and the air reservoir that is communicated with inertia tube, and described inertia tube, air reservoir and low temperature level vascular hot-side heat exchanger while are connected with described second level heat bridge.
For further improving the acoustic pressure of low temperature level second precooling zone regenerator cool end heat exchanger outlet working medium, preferred as to first kind of basic scheme, be provided with between described low temperature level second precooling zone regenerator cool end heat exchanger outlet and low temperature level the 3rd precooling zone regenerator entrance and be provided with second level acoustic pressure amplifier, this second level acoustic pressure amplifier is the major diameter pipe, the length of major diameter pipe be under its place temperature and pressure helium-3 gas corresponding wavelength 1/4.First order acoustic pressure amplifier and second level acoustic pressure amplifier can arrange simultaneously, and also desirable one setting can be determined according to actual needs.
In the technique scheme, described low temperature level phase modulating mechanism can be inertia tube, and this inertia tube is connected with described second level heat bridge with low temperature level vascular hot-side heat exchanger simultaneously.Perhaps, described low temperature level phase modulating mechanism is inertia tube and the air reservoir that is communicated with inertia tube, and described inertia tube, air reservoir and low temperature level vascular hot-side heat exchanger are connected with described second level heat bridge simultaneously.
Compared with prior art, the beneficial effects of the utility model are embodied in:
Compare as the 1-2K two-stage low frequency vascular refrigerator of working medium with existing employing helium-3, the single-stage high-frequency vascular refrigerator that working medium of single-stage low frequency vascular refrigerator precooling that the compound multistage vascular refrigerator structure employing working medium that the utility model proposes is helium-4 is helium-3, because the raising of frequency can reduce the volume of vascular refrigerator cold head and compressor significantly, so this structure can reduce the consumption of helium-3 significantly, according to preresearch estimates, the required volume of helium-3 under standard state of the composite structured acquisition 1-2K cryogenic temperature that the utility model proposes is less than 10 liters, much smaller than 228 liters of this specification background technology partial volume, so that the structure that the utility model proposes has a cost is low, be easy to advantages such as acquisition.
Simultaneously, owing to utilized the cold more than needed of the close low-temperature zone of regenerator in the single-stage low frequency vascular refrigerator to come to provide precooling for the high temperature section regenerator of low temperature level high-frequency vascular refrigeration unit, so this compound multistage vascular refrigerator has also kept vascular refrigerator compact conformation, efficient height, the life-span is long and the reliability advantages of higher, is a kind of novel 1-2K warm area mechanical type refrigeration structure with huge potential application foreground.
Description of drawings
Fig. 1 is a kind of structural representation of embodiment of the compound multistage vascular refrigerator of 1-2K of utilization of the present utility model cold more than needed.
Fig. 2 is the structural representation of the another kind of embodiment of utilization of the present utility model cold more than needed-compound multistage vascular refrigerator of 2K.
Fig. 3 is the structural representation of the third embodiment of the compound multistage vascular refrigerator of 1-2K of utilization of the present utility model cold more than needed.
Fig. 4 is the structural representation of the 4th kind of embodiment of the compound multistage vascular refrigerator of 1-2K of utilization of the present utility model cold more than needed.
Fig. 5 is the structural representation of the 5th kind of embodiment of the compound multistage vascular refrigerator of 1-2K of utilization of the present utility model cold more than needed.
Fig. 6 is the structural representation of the 6th kind of embodiment of the compound multistage vascular refrigerator of 1-2K of utilization of the present utility model cold more than needed.
In the above-mentioned accompanying drawing:
C1 is first order compressor, AC1 is first order level aftercooler, LV1 is first order compressor low-pressure control valve, HV1 is first order compressor high pressure control valve, RG1 is first order regenerator, HX2 is first order cool end heat exchanger, PT1 is first order vascular, HX3 is first order vascular hot-side heat exchanger, DO1 is first order bidirection air intake valve, O1 is the little ports valve of the first order, R1 is first order gas, C2 is the low temperature stage compressor, HX4 is low temperature level regenerator hot end heat exchanger, RG21 is the low temperature level first precooling zone regenerator, HX5 is the low temperature level first precooling zone regenerator cool end heat exchanger, PA1 is first order acoustic pressure amplifier, RG22 is the low temperature level second precooling zone regenerator, HX6 is the low temperature level second precooling zone regenerator cool end heat exchanger, PA2 is second level acoustic pressure amplifier, RG23 is low temperature grade low-temp section regenerator, HX7 is low temperature level cool end heat exchanger, PT2 is low temperature level vascular, HX8 is low temperature level vascular hot-side heat exchanger, I is low temperature level inertia tube, TB1 is first order heat bridge, TB2 is second level heat bridge, R is low temperature level air reservoir.
The specific embodiment
As shown in Figure 1, a kind of compound multistage vascular refrigerator of 1-2K of cold more than needed that utilizes comprises: precooling level low frequency vascular refrigerator, first order heat bridge TB1, second level heat bridge TB2 and low temperature level high-frequency vascular refrigerator.
Wherein:
Precooling level low frequency vascular refrigerator is made up of precooling stage compressor C1, precooling level level aftercooler AC1, precooling stage compressor low-pressure control valve LV1, precooling stage compressor high pressure control valve HV1, precooling level regenerator RG1, precooling level cool end heat exchanger HX2, precooling level vascular PT1, precooling level vascular hot-side heat exchanger HX3, precooling level bidirection air intake valve DO1, precooling level aperture valve O1, precooling level air reservoir R1.
Low temperature level high-frequency vascular refrigerator comprises low temperature stage compressor C2, low temperature level regenerator hot end heat exchanger HX4, the low temperature level first precooling zone regenerator RG21, the low temperature level first precooling zone regenerator cool end heat exchanger HX5, the low temperature level second precooling zone regenerator RG22, the low temperature level second precooling zone regenerator cool end heat exchanger HX6, low temperature grade low-temp section regenerator RG23, low temperature level cool end heat exchanger HX7, low temperature level vascular PT2, low temperature level vascular hot-side heat exchanger HX8 and low temperature level inertia tube I.
The annexation of above-mentioned each parts is as follows:
Precooling stage compressor C1, precooling level level aftercooler AC1, precooling stage compressor high pressure control valve HV1 and precooling stage compressor low-pressure control valve LV1 contact successively and form the closed circuit of precooling level low frequency compressor bank; Pipeline connection between the entrance of precooling level regenerator RG1 and precooling stage compressor high pressure control valve HV1 and the precooling stage compressor low-pressure control valve LV1; The outlet of precooling level regenerator RG1 is communicated with precooling level cool end heat exchanger HX2, precooling level vascular PT1, precooling level vascular hot-side heat exchanger HX3, precooling level aperture valve O1 and precooling level air reservoir R1 import by pipeline successively; Pipeline connection between precooling level bidirection air intake valve DO1 one end and precooling level regenerator RG1 and the precooling level low frequency compressor bank, the pipeline connection between the precooling level bidirection air intake valve DO1 other end and precooling level aperture valve O1 and the precooling level vascular hot-side heat exchanger HX3.
The outlet of low temperature stage compressor C2 is communicated with low temperature level regenerator hot end heat exchanger HX4, the low temperature level first precooling zone regenerator RG21, the low temperature level first precooling zone regenerator cool end heat exchanger HX5, the low temperature level second precooling zone regenerator RG22, the low temperature level second precooling zone regenerator cool end heat exchanger HX6, low temperature grade low-temp section regenerator RG23, low temperature level cool end heat exchanger HX7, low temperature level vascular PT2, low temperature level vascular hot-side heat exchanger HX8, low temperature level inertia tube I successively by pipeline.
Precooling level vascular refrigerator regenerator RG1 middle part is connected with first order heat bridge TB1 respectively with the low temperature level first precooling zone regenerator cool end heat exchanger HX5; The low temperature level second precooling zone regenerator cool end heat exchanger HX6, precooling level cool end heat exchanger of pulse tube refrigerator HX2, low temperature level vascular hot-side heat exchanger HX8 are connected with second level heat bridge TB2 respectively with low temperature level inertia tube I.
Precooling level low frequency vascular refrigerator unit and low temperature level high-frequency vascular refrigerator unit carry out a thermal coupling by the regenerator that is connected the low temperature level first precooling zone regenerator cool end heat exchanger HX5 and precooling level low frequency vascular refrigerator unit near cold junction first order heat bridge TB1 partly; Carry out the secondary thermal coupling by the second level heat bridge TB2 between the cool end heat exchanger that is connected the low temperature level second precooling zone regenerator cool end heat exchanger HX6 and precooling level low frequency vascular refrigerator unit.
The running of the compound multistage vascular refrigerator of 1-2K of the utilization of present embodiment cold more than needed is:
Starting stage, precooling stage compressor low pressure modulating valve LV1, precooling stage compressor septum valve HV1 all is in closed condition, gas becomes high temperature and high pressure gas after compressing through precooling stage compressor C1, high temperature and high pressure gas is flowed through and is cooled to room temperature behind the precooling level level aftercooler AC1, when gas pressure is higher than setting value, precooling stage compressor septum valve HV1 opens, the high pressure room temperature air is from precooling stage compressor high pressure valve HV1 outflow and be divided into two strands, one is by precooling level regenerator RG1 and carry out the heat exchange temperature with wherein filler and reduce and enter in the follow-up associated components, another strand enters in the follow-up associated components by precooling level bidirection air intake valve DO1, make whole system all be in high pressure conditions, precooling stage compressor septum valve HV1 closes then, precooling stage compressor low pressure modulating valve LV1 opens, gas is divided into two strands from precooling level air reservoir R1 through precooling level aperture valve O1, one gets back to precooling stage compressor C1 from precooling level bidirection air intake valve DO1 by precooling stage compressor low pressure modulating valve LV1, another stock-traders' know-how is crossed precooling level vascular PT1, precooling level regenerator RG1 finally gets back to precooling stage compressor C1 by precooling stage compressor low pressure modulating valve LV1, finishes a circulation thus.In cyclic process, precooling level regenerator RG1 takes out the gas that enters the low temperature level high-frequency vascular refrigerator second precooling zone regenerator RG22 in order to precooling near the cold more than needed of cold junction part by first order heat bridge TB1; There is the temperature difference in the gas of turnover precooling level cool end heat exchanger HX2, produces refrigeration effect thus, and this precooling level cold takes out the gas that enters low temperature grade low-temp section regenerator RG23 in order to precooling by second level heat bridge TB2 from precooling level cool end heat exchanger HX2.
At high pressure phase, flow through through the high temperature and high pressure gas of low temperature stage compressor C2 compression and to be cooled to room temperature behind the low temperature level regenerator hot end heat exchanger HX4, then with the low temperature grade low-temp high-frequency vascular first precooling zone regenerator RG21 in the backheat filler carry out heat exchange, temperature reduces, be cooled to the regenerator RG1 of first order vascular refrigerator at the low temperature level first precooling zone regenerator cool end heat exchanger HX5 place near the temperature of cold junction part, gas enters the low temperature level second precooling zone regenerator RG22 and carries out heat exchange with wherein backheat filler then, temperature reduces, be cooled to the cold junction temperature of precooling level vascular refrigerator at the low temperature level second precooling zone regenerator cool end heat exchanger HX6 place, the low temperature grade low-temp section of flowing through successively then regenerator RG23, low temperature level cool end heat exchanger HX7, low temperature level vascular PT2, low temperature level vascular hot-side heat exchanger HX8 enters low temperature level inertia tube I; Enter low pressure cycle then, gas passes through low temperature level vascular hot-side heat exchanger HX8 successively from low temperature level inertia tube I, low temperature level vascular PT2, low temperature level cool end heat exchanger HX7, low temperature grade low-temp section regenerator RG23, the low temperature level second precooling zone regenerator cool end heat exchanger HX6, the low temperature level second precooling zone regenerator RG22, the low temperature level first precooling zone regenerator cool end heat exchanger HX5, the low temperature level first precooling zone regenerator RG21, low temperature level regenerator hot end heat exchanger HX4 gets back to and finishes a circulation among the low temperature stage compressor C3, there is the temperature difference in the gas of turnover low temperature level cool end heat exchanger HX7 in cyclic process, thereby at the cryogenic temperature of low temperature level cool end heat exchanger HX7 place acquisition 1-2K and produce refrigeration effect.
Embodiment 2:
As shown in Figure 2, a kind of compound multistage vascular refrigerator that utilizes the 1-2K of cold more than needed, be with the difference of embodiment 1: the pm mode of its low temperature level high-frequency vascular refrigerator is the combination of low temperature level inertia tube I and low temperature level air reservoir R, and low temperature level air reservoir R is arranged on the heat bridge TB2 of the second level, by using low temperature level air reservoir R, can obtain more excellent phase modulation angle in low temperature level high-frequency vascular refrigerator, the final low temperature level high-frequency vascular refrigerator that further improves is at the refrigerating efficiency of 2K.
Embodiment 3:
As shown in Figure 3, a kind of compound multistage vascular refrigerator that utilizes the 1-2K of cold more than needed, and the difference of embodiment 1 is: arranged a second level acoustic pressure amplifier PA2 who is used for amplifying the low temperature level second precooling zone regenerator cold junction pressure ratio between the low temperature level second precooling zone regenerator cool end heat exchanger HX6 and the low temperature grade low-temp section regenerator RG23, second level acoustic pressure amplifier PA2 can make the cold junction pressure ratio of low temperature level high-frequency vascular refrigerator further amplify, thereby makes it have higher efficient at the 1-2K warm area.
In the present embodiment, second level acoustic pressure amplifier PA2 is the major diameter pipe, the length of major diameter pipe be under its place temperature and pressure helium-3 gas corresponding wavelength 1/4, the major diameter pipe can process voluntarily, perhaps selects commercially available metal tube etc. for use.
Embodiment 4:
As shown in Figure 4, a kind of compound multistage vascular refrigerator that utilizes the 1-2K of cold more than needed, be with the difference of embodiment 3: the pm mode of its low temperature level high-frequency vascular refrigerator is the combination of low temperature level inertia tube I and low temperature level air reservoir R, and low temperature level air reservoir R is arranged on the heat bridge TB2 of the second level, by using low temperature level air reservoir R, can obtain more excellent phase modulation angle in low temperature level high-frequency vascular refrigerator, the final low temperature level high-frequency vascular refrigerator that further improves is at the refrigerating efficiency of 2K.
Embodiment 5:
As shown in Figure 5, a kind of compound multistage vascular refrigerator that utilizes the 1-2K of cold more than needed, and the difference of embodiment 3 is: arranged a first order acoustic pressure amplifier PA1 who is used for amplifying the low temperature level first precooling zone regenerator cold junction pressure ratio between the low temperature level first precooling zone regenerator cool end heat exchanger HX5 and the low temperature level second precooling zone regenerator RG22, first order acoustic pressure amplifier PA1 can make the cold junction pressure ratio of low temperature level high-frequency vascular refrigerator further amplify, thereby makes it have higher efficient at the 1-2K warm area.
In the present embodiment, first order acoustic pressure amplifier PA1 is the major diameter pipe, the length of major diameter pipe be under its place temperature and pressure helium-3 gas corresponding wavelength 1/4, the major diameter pipe can process voluntarily, perhaps selects commercially available metal tube etc. for use.
Embodiment 6:
As shown in Figure 6, a kind of compound multistage vascular refrigerator that utilizes the 1-2K of cold more than needed, be with the difference of embodiment 5: the pm mode of its low temperature level high-frequency vascular refrigerator is the combination of low temperature level inertia tube I and low temperature level air reservoir R, and low temperature level air reservoir R is arranged on the heat bridge TB2 of the second level, by using low temperature level air reservoir R, can obtain more excellent phase modulation angle in low temperature level high-frequency vascular refrigerator, the final low temperature level high-frequency vascular refrigerator that further improves is at the refrigerating efficiency of 2K.
Claims (9)
1. compound multistage vascular refrigerator of 1-2K that utilizes cold more than needed, comprise precooling level low frequency vascular refrigerator unit and low temperature level high-frequency vascular refrigerator unit, described precooling level low frequency vascular refrigerator unit is single-stage low frequency vascular refrigerator, and its working medium of using is helium-4; It is characterized in that,
Described low temperature level high-frequency vascular refrigerator unit comprises low temperature stage compressor (C2), and the low temperature level regenerator hot end heat exchanger (HX4) that is communicated with low temperature stage compressor (C2) outlet successively by pipeline, the low temperature level first precooling zone regenerator (RG21), the low temperature level first precooling zone regenerator cool end heat exchanger (HX5), the low temperature level second precooling zone regenerator (RG22), the low temperature level second precooling zone regenerator cool end heat exchanger (HX6), low temperature grade low-temp section regenerator (RG23), low temperature level cool end heat exchanger (HX7), low temperature level vascular (PT2), low temperature level vascular hot-side heat exchanger (HX8) and low temperature level phase modulating mechanism; The refrigeration working medium that described low temperature level high-frequency vascular refrigerator unit adopts is helium-3;
Described precooling level low frequency vascular refrigerator unit and low temperature level high-frequency vascular refrigerator unit carry out a thermal coupling by the regenerator that is connected the low temperature level first precooling zone regenerator cool end heat exchanger (HX5) and precooling level low frequency vascular refrigerator unit near cold junction first order heat bridge (TB1) partly; Carry out the secondary thermal coupling by the second level heat bridge (TB2) between the cool end heat exchanger that is connected the low temperature level second precooling zone regenerator cool end heat exchanger (HX6) and precooling level low frequency vascular refrigerator unit.
2. the compound multistage vascular refrigerator of 1-2K of utilization according to claim 1 cold more than needed, it is characterized in that, described low temperature level phase modulating mechanism is inertia tube, and this inertia tube is connected with described second level heat bridge (TB2) with low temperature level vascular hot-side heat exchanger (HX8) simultaneously.
3. the compound multistage vascular refrigerator of 1-2K of utilization according to claim 1 cold more than needed, it is characterized in that, described low temperature level phase modulating mechanism is inertia tube and the air reservoir that is communicated with inertia tube, and described inertia tube, air reservoir and low temperature level vascular hot-side heat exchanger (HX8) are connected with described second level heat bridge (TB2) simultaneously.
4. the compound multistage vascular refrigerator of 1-2K of utilization according to claim 1 cold more than needed, it is characterized in that, be provided with first order acoustic pressure amplifier (PA1) between the described low temperature level first precooling zone regenerator cool end heat exchanger (HX5) outlet and low temperature level second precooling zone regenerator (RG22) entrance, this first order acoustic pressure amplifier is the major diameter pipe, the length of major diameter pipe be under its place temperature and pressure helium-3 gas corresponding wavelength 1/4.
5. the compound multistage vascular refrigerator of 1-2K of utilization according to claim 4 cold more than needed, it is characterized in that, described low temperature level phase modulating mechanism is inertia tube, and this inertia tube is connected with described second level heat bridge (TB2) with low temperature level vascular hot-side heat exchanger (HX8) simultaneously.
6. the compound multistage vascular refrigerator of 1-2K of utilization according to claim 4 cold more than needed, it is characterized in that, described low temperature level phase modulating mechanism is inertia tube and the air reservoir that is communicated with inertia tube, and described inertia tube, air reservoir and low temperature level vascular hot-side heat exchanger (HX8) are connected with described second level heat bridge (TB2) simultaneously.
7. according to the compound multistage vascular refrigerator of 1-2K of claim 1 or 4 described utilizations cold more than needed, it is characterized in that, be provided with second level acoustic pressure amplifier (PA2) between the described low temperature level second precooling zone regenerator cool end heat exchanger (HX6) outlet and low temperature level the 3rd precooling zone regenerator (RG23) entrance, this second level acoustic pressure amplifier is the major diameter pipe, the length of major diameter pipe be under its place temperature and pressure helium-3 gas corresponding wavelength 1/4.
8. the compound multistage vascular refrigerator of 1-2K of utilization according to claim 7 cold more than needed, it is characterized in that, described low temperature level phase modulating mechanism is inertia tube, and this inertia tube is connected with described second level heat bridge (TB2) with low temperature level vascular hot-side heat exchanger (HX8) simultaneously.
9. the compound multistage vascular refrigerator of 1-2K of utilization according to claim 7 cold more than needed, it is characterized in that, described low temperature level phase modulating mechanism is inertia tube and the air reservoir that is communicated with inertia tube, and described inertia tube, air reservoir and low temperature level vascular hot-side heat exchanger (HX8) are connected with described second level heat bridge (TB2) simultaneously.
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|---|---|---|---|
| CN 201320026672 CN203190706U (en) | 2013-01-17 | 2013-01-17 | 1-2K combined-type multilevel vessel refrigerating machine utilizing abundant cooling capacity |
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| CN 201320026672 CN203190706U (en) | 2013-01-17 | 2013-01-17 | 1-2K combined-type multilevel vessel refrigerating machine utilizing abundant cooling capacity |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103075834A (en) * | 2013-01-17 | 2013-05-01 | 浙江大学 | 1-2K composite multistage pulse pipe refrigerating machine for utilizing redundant cold quantity |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103075834A (en) * | 2013-01-17 | 2013-05-01 | 浙江大学 | 1-2K composite multistage pulse pipe refrigerating machine for utilizing redundant cold quantity |
| CN103075834B (en) * | 2013-01-17 | 2015-02-25 | 浙江大学 | 1-2K composite multistage pulse pipe refrigerating machine for utilizing redundant cold quantity |
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