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CN105333694A - Multistage liquefaction device of gaseous of multistage thermoacoustic engine drive of loop - Google Patents

Multistage liquefaction device of gaseous of multistage thermoacoustic engine drive of loop Download PDF

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CN105333694A
CN105333694A CN201510792247.6A CN201510792247A CN105333694A CN 105333694 A CN105333694 A CN 105333694A CN 201510792247 A CN201510792247 A CN 201510792247A CN 105333694 A CN105333694 A CN 105333694A
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refrigeration
low
unit
temperature
gas
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CN105333694B (en
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罗二仓
徐静远
张丽敏
陈燕燕
戴巍
胡剑英
吴张华
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Technical Institute of Physics and Chemistry of CAS
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0225Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process using other external refrigeration means not provided before, e.g. heat driven absorption chillers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0203Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process using a single-component refrigerant [SCR] fluid in a closed vapor compression cycle
    • F25J1/0208Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process using a single-component refrigerant [SCR] fluid in a closed vapor compression cycle in combination with an internal quasi-closed refrigeration loop, e.g. with deep flash recycle loop
    • F25J1/0209Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process using a single-component refrigerant [SCR] fluid in a closed vapor compression cycle in combination with an internal quasi-closed refrigeration loop, e.g. with deep flash recycle loop as at least a three level refrigeration cascade
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B9/00Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
    • F25B9/14Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the cycle used, e.g. Stirling cycle
    • F25B9/145Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the cycle used, e.g. Stirling cycle pulse-tube cycle
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/0002Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the fluid to be liquefied
    • F25J1/0005Light or noble gases
    • F25J1/001Hydrogen
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/0002Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the fluid to be liquefied
    • F25J1/0012Primary atmospheric gases, e.g. air
    • F25J1/0015Nitrogen
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/0002Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the fluid to be liquefied
    • F25J1/0022Hydrocarbons, e.g. natural gas
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2309/00Gas cycle refrigeration machines
    • F25B2309/14Compression machines, plants or systems characterised by the cycle used 
    • F25B2309/1407Pulse-tube cycles with pulse tube having in-line geometrical arrangements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2309/00Gas cycle refrigeration machines
    • F25B2309/14Compression machines, plants or systems characterised by the cycle used 
    • F25B2309/1425Pulse tubes with basic schematic including several pulse tubes
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2309/00Gas cycle refrigeration machines
    • F25B2309/14Compression machines, plants or systems characterised by the cycle used 
    • F25B2309/1426Pulse tubes with basic schematic including at the pulse tube warm end a so called warm end expander
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2270/00Refrigeration techniques used
    • F25J2270/90External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration
    • F25J2270/908External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration by regenerative chillers, i.e. oscillating or dynamic systems, e.g. Stirling refrigerator, thermoelectric ("Peltier") or magnetic refrigeration
    • F25J2270/91External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration by regenerative chillers, i.e. oscillating or dynamic systems, e.g. Stirling refrigerator, thermoelectric ("Peltier") or magnetic refrigeration using pulse tube refrigeration

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  • Devices That Are Associated With Refrigeration Equipment (AREA)

Abstract

一种环路多级热声发动机驱动的气体多级液化装置,其由M个热声发动机单元及旁接其出口的脉管制冷机单元组成,M为3~6正整数;一制冷机回热器和一低温端换热器为一制冷单元,脉管制冷机单元具两个以上制冷单元;在制冷机回热器和脉冲管间设多路旁通管路,使两者相连形成至少一条旁通气流通道;热声发动机自激产生的声功在制冷机回热器中发生热声转换,多个低温端换热器维持在不同制冷温度下;待液化气体依次通过每一低温端换热器,温度梯级下降而被液化;具无运动部件,结构紧凑,功率密度高;环路结构使发动机单元处行波相位;多路旁通结构实现气体膨胀制冷可提高脉冲管制冷机效率;同时多级制冷单元梯级降低气体温度,有效减少不可逆传热损失。

A gas multi-stage liquefaction device driven by a loop multi-stage thermoacoustic engine, which is composed of M thermoacoustic engine units and pulse tube refrigerator units bypassing the outlets, where M is a positive integer of 3 to 6; The heat exchanger and a low-temperature end heat exchanger are a refrigeration unit, and the pulse tube refrigerator unit has more than two refrigeration units; multiple bypass pipes are set between the refrigerator regenerator and the pulse tube, so that the two are connected to form at least A bypass air flow channel; the sound work generated by the self-excitation of the thermoacoustic engine undergoes thermoacoustic conversion in the regenerator of the refrigerator, and multiple low-temperature end heat exchangers are maintained at different refrigeration temperatures; the gas to be liquefied passes through each low-temperature end in turn The heat exchanger is liquefied due to the temperature drop; it has no moving parts, compact structure, and high power density; the loop structure makes the engine unit in the traveling wave phase; the multi-path bypass structure realizes gas expansion and refrigeration, which can improve the efficiency of the pulse tube refrigerator ; At the same time, the multi-stage refrigeration unit lowers the gas temperature step by step, effectively reducing the irreversible heat transfer loss.

Description

一种环路多级热声发动机驱动的气体多级液化装置A multi-stage gas liquefaction device driven by a loop multi-stage thermoacoustic engine

技术领域technical field

本发明属于气体液化领域的气体液化装置,特别涉及一种环路多级热声发动机驱动的气体多级液化装置。The invention belongs to a gas liquefaction device in the field of gas liquefaction, in particular to a gas multistage liquefaction device driven by a loop multistage thermoacoustic engine.

背景技术Background technique

液化过程指物质由气态转变为液态的过程。由于气体液化后体积会变成原来的几千分之一,便于贮藏和运输,现实中通常对一些气体进行液化处理。实现液化有两种手段,一是降低温度,二是压缩体积。任何气体在温度降到足够低时都可以液化。因此,如何能制造可靠性高、寿命长、高效且能够梯级液化气体的低温制冷机成为了令人关注的问题。Liquefaction is the process by which a substance changes from a gaseous state to a liquid state. Since the volume of the gas after liquefaction will become one thousandth of its original volume, which is convenient for storage and transportation, some gases are usually liquefied in reality. There are two ways to achieve liquefaction, one is to lower the temperature, and the other is to compress the volume. Any gas can be liquefied when the temperature drops low enough. Therefore, how to manufacture a cryogenic refrigerator with high reliability, long life, high efficiency, and ability to cascade liquefy gas has become a concern.

热声发动机是一种利用管道和换热器在其内部获得合适的声场,并通过工作介质和回热器固体填料之间的相互作用将外部热能转化为声能的装置,具有无机械运动部件、可靠性高、寿命长和潜在热效率高等优点,受到人们的广泛关注。在目前广泛应用的低温制冷机中,脉冲管制冷机是利用压力周期性变化的气流在一根低导热率的管中振荡来完成制冷过程,它省去了低温端的运动部件,因此具有结构简单、振动小、可靠性高等优点。将热声发动机中自激振荡产生的声功来驱动脉管制冷机,便产生了一种从驱动源到冷端都没有任何运动部件的制冷机,具有可靠性高、寿命长和潜在热效率高等优点,受到人们的广泛关注。近几年,声学共振型热声制冷系统因具有结构紧凑、功率密度高、潜在热效率高等优点,引起了广泛关注,并进一步推动了热驱动脉管制冷机的发展。A thermoacoustic engine is a device that uses pipes and heat exchangers to obtain a suitable sound field inside it, and converts external heat energy into sound energy through the interaction between the working medium and the solid packing of the regenerator, with no mechanical moving parts , high reliability, long life and high potential thermal efficiency have attracted widespread attention. Among the low-temperature refrigerators widely used at present, the pulse tube refrigerator uses the airflow with periodically changing pressure to oscillate in a tube with low thermal conductivity to complete the refrigeration process. It eliminates the moving parts at the low-temperature end, so it has a simple structure. , small vibration, high reliability and so on. The acoustic work generated by the self-excited oscillation in the thermoacoustic engine is used to drive the pulse tube refrigerator, and a refrigerator without any moving parts from the driving source to the cold end is produced, which has high reliability, long life and high potential thermal efficiency. The advantages are widely concerned by people. In recent years, acoustic resonance thermoacoustic refrigeration systems have attracted extensive attention due to their compact structure, high power density, and high potential thermal efficiency, and further promoted the development of thermally driven pulse tube refrigerators.

图1为专利CN1035788提出的多路旁通脉冲管制冷机。它是由依次相通连接的制冷机主水冷器2、制冷机回热器3、低温端换热器4、连接管5、脉冲管7、制冷机次水冷器10、惯性管11和气库12组成,由压力波发生器驱动。在制冷机回热器和脉冲管中间部位的适当位置处,通过多路旁通管路13将两者相连通,每级制冷机回热器中形成至少一条旁通气流通路;同时,在脉冲管适当地设置阻力填料,能使气体均匀、顺利通过。这种脉冲管制冷机可以获得更大的制冷功率和更低的制冷温度,从而提高了制冷效率。Fig. 1 is the multiple bypass pulse tube refrigerator proposed by the patent CN1035788. It is composed of refrigerator main water cooler 2, refrigerator regenerator 3, low-temperature end heat exchanger 4, connecting pipe 5, pulse tube 7, refrigerator secondary water cooler 10, inertia tube 11 and gas storage 12, which are connected in sequence , driven by a pressure wave generator. At an appropriate position in the middle of the regenerator of the refrigerator and the pulse tube, the two are connected through a multi-channel bypass pipeline 13, and at least one bypass airflow path is formed in the regenerator of each stage of the refrigerator; at the same time, in the pulse tube Properly set the resistance packing in the tube to make the gas pass through evenly and smoothly. This pulse tube refrigerator can obtain greater refrigeration power and lower refrigeration temperature, thereby improving refrigeration efficiency.

图2为罗二仓等人提出的声学共振型热声制冷系统。该系统主要由多个热声发动机单元14和脉管制冷机单元1组成,每个脉冲制冷机单元只有一级低温端换热器。每一级热声发动机单元通过谐振管23首尾相连构成环路结构。该系统结构紧凑,能实现谐振管中声功回收,潜在热效率高,并且可根据冷量的需要串入任意数量的热声发动机单元及脉管制冷机单元。系统可被应用于液化气体流程的最后部分,即吸收液化温度下气体的潜热,使气体由气态变为液态。但是,若利用该系统完成将常温气体液化到低温液体的整体液化过程,则会由于无法实现气体梯级降温而产生很大的传热损失,效率非常低。Figure 2 shows the acoustic resonance thermoacoustic refrigeration system proposed by Luo Ercang et al. The system is mainly composed of a plurality of thermoacoustic engine units 14 and a pulse tube refrigerator unit 1, and each pulse refrigerator unit has only one low-temperature end heat exchanger. Each stage of the thermoacoustic engine unit is connected end to end through a resonant tube 23 to form a loop structure. The system has a compact structure, can realize the recovery of sound power in the resonance tube, has high potential thermal efficiency, and can be connected in series with any number of thermoacoustic engine units and pulse tube refrigerator units according to the cooling capacity requirements. The system can be applied in the final part of the liquefied gas process, that is, to absorb the latent heat of the gas at the liquefaction temperature to change the gas from gas to liquid. However, if this system is used to complete the overall liquefaction process of liquefying normal-temperature gas to low-temperature liquid, it will cause a large heat transfer loss due to the inability to realize gas cascade cooling, and the efficiency is very low.

为了解决以上存在的问题,本发明提出一种能够实现气体液化一体化的环路多级热声发动机驱动的气体多级液化装置;它完全没有运动部件,安全可靠,发动机核心部件均在行波相位中;具有多个不同温度的低温端换热器,可以梯级地降低气体温度,有效减小传热损失;利用多路旁通结构,使得脉冲管内压力波动变大,压力波和体积流率的相位更接近同相,可以获得更大的制冷功率和更低的制冷温度;系统结构简单,运动部件较少,安全可靠。In order to solve the above existing problems, the present invention proposes a gas multi-stage liquefaction device driven by a loop multi-stage thermoacoustic engine that can realize the integration of gas liquefaction; it has no moving parts at all, is safe and reliable, and the core components of the engine are all in the traveling wave In the middle phase; there are multiple low-temperature end heat exchangers with different temperatures, which can reduce the gas temperature in steps and effectively reduce heat transfer loss; the use of multiple bypass structures makes the pressure fluctuations in the pulse tube larger, and the pressure wave and volume flow rate The phase is closer to the same phase, which can obtain greater cooling power and lower cooling temperature; the system has a simple structure, fewer moving parts, and is safe and reliable.

发明内容Contents of the invention

本发明的目的在于提供一种环路多级热声发动机驱动的气体多级液化装置,其无运动部件,可靠性高,结构简单,且热声发动机单元工作在行波相位,工作效率高;多个低温端换热器的温度从室温依次降低到气体液化温度,能够梯级降低气体的温度,有效减小传热损失;多路旁通结构能够使脉冲管旁通点成为制冷部位,管中形成膨胀制冷过程,因此制冷机具有更优的制冷性能;在脉冲管旁通点处布置阻力填料,减小气流紊乱带来的混合损失;该装置可实现气体液化的整体流程,在气体液化方面具有广阔的发展和应用前景。The object of the present invention is to provide a gas multi-stage liquefaction device driven by a loop multi-stage thermoacoustic engine, which has no moving parts, high reliability and simple structure, and the thermoacoustic engine unit works in the traveling wave phase with high work efficiency; The temperature of multiple low-temperature end heat exchangers is lowered from room temperature to gas liquefaction temperature in turn, which can reduce the temperature of gas in steps and effectively reduce heat transfer loss; the multi-channel bypass structure can make the bypass point of the pulse tube a cooling part, and the The expansion refrigeration process is formed, so the refrigerator has better refrigeration performance; the resistance packing is arranged at the bypass point of the pulse tube to reduce the mixing loss caused by the turbulence of the air flow; the device can realize the overall process of gas liquefaction, and in terms of gas liquefaction It has broad development and application prospects.

本发明的技术方案如下:Technical scheme of the present invention is as follows:

本发明提供的环路多级热声发动机驱动的气体多级液化装置,其由M个热声发动机单元14通过谐振管23首尾相连构成的环路结构及M个脉管制冷机单元1组成,M=3~6正整数;所述热声发动机单元14由依次相连的直流抑制器15、发动机主冷却器16、发动机回热器17、加热器18、高温端层流化元件19、热缓冲管20、发动机室温端层流化元件21和发动机次冷却器22组成;每一热声发动机单元14的发动机次冷却器22出口处旁接一个脉管制冷机单元1;The gas multistage liquefaction device driven by a loop multistage thermoacoustic engine provided by the present invention is composed of a loop structure formed by connecting M thermoacoustic engine units 14 end to end through resonance tubes 23 and M pulse tube refrigerator units 1. M=3~6 positive integers; the thermoacoustic engine unit 14 is composed of a DC suppressor 15, an engine main cooler 16, an engine regenerator 17, a heater 18, a high-temperature end laminar fluidization element 19, and a thermal buffer that are connected in sequence. Tube 20, engine room temperature end laminar fluidization element 21 and engine sub-cooler 22; each thermoacoustic engine unit 14 is connected to a pulse tube refrigerator unit 1 at the outlet of the engine sub-cooler 22;

所述脉管制冷机单元1由依次相连的制冷机主水冷器2、第一至第N级制冷单元、连接管5、脉冲管7、制冷机次水冷器10、惯性管11和气库12组成,其中N=2~6的正整数;所述制冷单元由一个制冷机回热器3及与其串接的一个低温端换热器4组成;第1级制冷单元的制冷机回热器3与制冷机主水冷器2相连,第N级制冷单元的低温端换热器4通过连接管5与脉冲管7冷端相连接;脉冲管7两端分别装有低温端导流丝网6和制冷机室温端导流丝网9;The pulse tube refrigerator unit 1 is composed of the main water cooler 2 of the refrigerator, the first to Nth stage refrigeration units, the connecting pipe 5, the pulse tube 7, the secondary water cooler 10 of the refrigerator, the inertia tube 11 and the gas storage 12, which are connected in sequence. , wherein N=a positive integer of 2 to 6; the refrigeration unit is composed of a refrigerator regenerator 3 and a low-temperature end heat exchanger 4 connected in series; the refrigerator regenerator 3 of the first-stage refrigeration unit is connected to The main water cooler 2 of the refrigerator is connected, and the low-temperature end heat exchanger 4 of the Nth-stage refrigeration unit is connected with the cold end of the pulse tube 7 through the connecting pipe 5; Diversion wire mesh 9 at the room temperature end of the machine;

在每一脉管制冷机单元1中,制冷单元的制冷机回热器3通过旁通管路13与脉冲管7相连形成至少一条旁通气流通道;脉冲管7内装有阻力填料8,阻力填料8轴向层叠于气体工质进出脉冲管7的接口两侧,所述阻力填料8为丝网或者多孔介质材料;In each pulse tube refrigerator unit 1, the refrigerator regenerator 3 of the refrigeration unit is connected to the pulse tube 7 through a bypass line 13 to form at least one bypass air flow channel; the pulse tube 7 is equipped with resistance packing 8, and the resistance packing 8 are axially stacked on both sides of the interface where the gas working medium enters and exits the pulse tube 7, and the resistance packing 8 is a wire mesh or a porous medium material;

每一热声发动机单元14的加热器18与热源相连以吸收热源热量形成相同温度的高温端;发动机主冷却器16和发动机次冷却器22均通过水冷器冷却以维持在室温范围;因此,每一级热声发动机单元14的发动机回热器17上形成温度梯度;在该温度梯度下,发动机回热器17内部工作气体与其内的固体填料间产生热声效应,将输入到加热器18的热量转化成声功;声功沿着温度梯度的正方向传播并放大,一部分声功传递到脉管制冷机单元1中,另一部分通过谐振管23传递到下一级热声发动机单元中重复以上过程;在脉管制冷机单元1中,制冷机主水冷器2和制冷机次水冷器10通过冷却水冷却维持在室温范围;在第N级制冷单元中,从热声发动机中产生的声功传递到制冷机回热器3中发生热声转换,将第N级低温端换热器4的热量泵送到第N-1级的低温端换热器中,第N级低温端换热器4保持低温;如上所述,传递到第N-1级制冷单元中的声功经过热声转换,将第N-1级低温端换热器的热量泵送到第N-2级的低温端换热器中,第N-1级低温端换热器保持低温;最终,所有低温端换热器的热量均泵送到制冷机主水冷器2中,热量由冷却水带走,N级低温端换热器的制冷温度依次降低至气体液化温度;待液化气体按照制冷温度从高到低的顺序依次通过每一制冷单元的低温端换热器,气体热量被吸收,温度梯级降低,最终气体被液化;其中,通过从每级制冷机回热器3旁通到脉冲管7内一部分气体形成膨胀制冷。The heater 18 of each thermoacoustic engine unit 14 is connected with the heat source to absorb the heat of the heat source to form a high-temperature end of the same temperature; the engine main cooler 16 and the engine sub-cooler 22 are all cooled by the water cooler to maintain the room temperature range; therefore, each A temperature gradient is formed on the engine regenerator 17 of the first-stage thermoacoustic engine unit 14; under this temperature gradient, a thermoacoustic effect is generated between the working gas inside the engine regenerator 17 and the solid filler therein, and the input to the heater 18 The heat is converted into sound work; the sound work is propagated and amplified along the positive direction of the temperature gradient, part of the sound work is transferred to the pulse tube refrigerator unit 1, and the other part is transferred to the next-stage thermoacoustic engine unit through the resonant tube 23 to repeat the above Process; in the pulse tube refrigerator unit 1, the refrigerator main water cooler 2 and the refrigerator sub water cooler 10 are cooled by cooling water to maintain the room temperature range; in the Nth stage refrigeration unit, the sound work generated from the thermoacoustic engine Transfer to the refrigerator regenerator 3 for thermoacoustic conversion, and pump the heat of the N-th stage low-temperature end heat exchanger 4 to the N-1th stage low-temperature end heat exchanger, and the N-th stage low-temperature end heat exchanger 4 Keep the low temperature; as mentioned above, the sound work transferred to the N-1th refrigeration unit undergoes thermoacoustic conversion, and the heat of the N-1th low-temperature heat exchanger is pumped to the N-2th low-temperature end Among the heat exchangers, the heat exchanger at the low-temperature end of the N-1 stage keeps the low temperature; finally, the heat of all the heat exchangers at the low-temperature end is pumped to the main water cooler 2 of the refrigerator, and the heat is taken away by the cooling water. The refrigeration temperature of the end heat exchanger is lowered to the gas liquefaction temperature in turn; the liquefied gas passes through the low-temperature end heat exchanger of each refrigeration unit in sequence according to the refrigeration temperature from high to low, the heat of the gas is absorbed, and the temperature is lowered in steps, and the final gas Be liquefied; Wherein, by bypassing the regenerator 3 of each stage refrigerator to a part of the gas in the pulse tube 7 to form expansion refrigeration.

上述装置中,脉管制冷机单元1的脉冲管7与制冷单元的制冷机回热器3非同轴布置。In the above device, the pulse tube 7 of the pulse tube refrigerator unit 1 is arranged non-coaxially with the refrigerator regenerator 3 of the refrigeration unit.

本发明的环路多级热声发动机驱动的气体多级液化装置,其由M个热声发动机单元14通过谐振管23首尾相连构成的环路结构及M个脉管制冷机单元1组成,M=3~6正整数;所述热声发动机单元14由依次相连的直流抑制器15、发动机主冷却器16、发动机回热器17、加热器18、高温端层流化元件19、热缓冲管20、发动机室温端层流化元件21和发动机次冷却器22组成;每一热声发动机单元14的发动机次冷却器22出口处旁接一个脉管制冷机单元1;The gas multistage liquefaction device driven by a loop multistage thermoacoustic engine of the present invention is composed of a loop structure formed by connecting M thermoacoustic engine units 14 end-to-end through resonance tubes 23 and M pulse tube refrigerator units 1, M = 3 to 6 positive integers; the thermoacoustic engine unit 14 is composed of a DC suppressor 15, an engine main cooler 16, an engine regenerator 17, a heater 18, a high-temperature end laminar fluidization element 19, and a thermal buffer tube connected in sequence 20. The engine room temperature end laminar fluidization element 21 and the engine sub-cooler 22 are composed; the outlet of the engine sub-cooler 22 of each thermoacoustic engine unit 14 is connected with a pulse tube refrigerator unit 1;

所述脉管制冷机单元1由制冷机主水冷器2,与制冷机主水冷器2相连的第一级至第N级制冷单元,位于所述第一级至第N级制冷单元的制冷机回热器3之内的脉冲管7,制冷机次水冷器10、惯性管11和气库12组成,其中N=2~6的正整数;所述制冷单元由一个制冷机回热器3及与其串接的一个低温端换热器4组成;第1级制冷单元的制冷机回热器3及脉冲管7室温端与制冷机主水冷器2相连,第N级制冷单元的低温端换热器4与脉冲管7冷端相连接;脉冲管7两端分别装有低温端导流丝网6和制冷机室温端导流丝网9;The pulse tube refrigerator unit 1 is composed of a refrigerator main water cooler 2, a first stage to an Nth stage refrigeration unit connected to the refrigerator main water cooler 2, and a refrigerator located in the first stage to the Nth stage refrigeration unit The pulse tube 7 inside the regenerator 3, the refrigerator secondary water cooler 10, the inertia tube 11 and the gas storage 12 are composed, wherein N=a positive integer of 2 to 6; the refrigeration unit is composed of a refrigerator regenerator 3 and its A low-temperature end heat exchanger 4 connected in series; the refrigerator regenerator 3 of the first-stage refrigeration unit and the room temperature end of the pulse tube 7 are connected to the main water cooler 2 of the refrigerator, and the low-temperature end heat exchanger of the N-stage refrigeration unit 4 is connected to the cold end of the pulse tube 7; the two ends of the pulse tube 7 are respectively equipped with a low-temperature end guide wire mesh 6 and a refrigerator room temperature end guide wire mesh 9;

在每一脉管制冷机单元1中,制冷单元的制冷机回热器3与脉冲管7通过两者共同壁面上开的多个通孔或者直接制作的多孔介质壁面相连通;脉冲管7内装有阻力填料8,阻力填料8轴向层叠于气体工质进出脉冲管7的接口两侧,所述阻力填料8为丝网或者多孔介质材料;In each pulse tube refrigerator unit 1, the refrigerator regenerator 3 of the refrigeration unit communicates with the pulse tube 7 through a plurality of through holes opened on the common wall surface of the two or a porous medium wall surface made directly; There is a resistance packing 8, and the resistance packing 8 is axially stacked on both sides of the interface where the gas working medium enters and exits the pulse tube 7, and the resistance packing 8 is a wire mesh or a porous medium material;

每一热声发动机单元14的加热器18与热源相连以吸收热源热量形成相同温度的高温端;发动机主冷却器16和发动机次冷却器22均通过水冷器冷却以维持在室温范围;因此,每一级热声发动机单元14的发动机回热器17上形成温度梯度;在该温度梯度下,发动机回热器17内部工作气体与其内的固体填料间产生热声效应,将输入到加热器18的热量转化成声功;声功沿着温度梯度的正方向传播并放大,一部分声功传递到脉管制冷机单元1中,另一部分通过谐振管23传递到下一级热声发动机单元中重复以上过程;在脉管制冷机单元1中,制冷机主水冷器2和制冷机次水冷器10通过冷却水冷却维持在室温范围;在第N级制冷单元中,从热声发动机中产生的声功传递到制冷机回热器3中发生热声转换,将第N级低温端换热器4的热量泵送到第N-1级的低温端换热器中,第N级低温端换热器4保持低温;如上所述,传递到第N-1级制冷单元中的声功经过热声转换,将第N-1级低温端换热器的热量泵送到第N-2级的低温端换热器中,第N-1级低温端换热器保持低温;最终,所有低温端换热器的热量均泵送到制冷机主水冷器2中,热量由冷却水带走,N级低温端换热器的制冷温度依次降低至气体液化温度;待液化气体按照制冷温度从高到低的顺序依次通过每一制冷单元的低温端换热器,气体热量被吸收,温度梯级降低,最终气体被液化;其中,通过从每级制冷机回热器3旁通到脉冲管7内一部分气体形成膨胀制冷。The heater 18 of each thermoacoustic engine unit 14 is connected with the heat source to absorb the heat of the heat source to form a high-temperature end of the same temperature; the engine main cooler 16 and the engine sub-cooler 22 are all cooled by the water cooler to maintain the room temperature range; therefore, each A temperature gradient is formed on the engine regenerator 17 of the first-stage thermoacoustic engine unit 14; under this temperature gradient, a thermoacoustic effect is generated between the working gas inside the engine regenerator 17 and the solid filler therein, and the input to the heater 18 The heat is converted into sound work; the sound work is propagated and amplified along the positive direction of the temperature gradient, part of the sound work is transferred to the pulse tube refrigerator unit 1, and the other part is transferred to the next-stage thermoacoustic engine unit through the resonant tube 23 to repeat the above Process; in the pulse tube refrigerator unit 1, the refrigerator main water cooler 2 and the refrigerator sub water cooler 10 are cooled by cooling water to maintain the room temperature range; in the Nth stage refrigeration unit, the sound work generated from the thermoacoustic engine Transfer to the refrigerator regenerator 3 for thermoacoustic conversion, and pump the heat of the N-th stage low-temperature end heat exchanger 4 to the N-1th stage low-temperature end heat exchanger, and the N-th stage low-temperature end heat exchanger 4 Keep the low temperature; as mentioned above, the sound work transferred to the N-1th refrigeration unit undergoes thermoacoustic conversion, and the heat of the N-1th low-temperature heat exchanger is pumped to the N-2th low-temperature end Among the heat exchangers, the heat exchanger at the low-temperature end of the N-1 stage keeps the low temperature; finally, the heat of all the heat exchangers at the low-temperature end is pumped to the main water cooler 2 of the refrigerator, and the heat is taken away by the cooling water. The refrigeration temperature of the end heat exchanger is lowered to the gas liquefaction temperature in turn; the liquefied gas passes through the low-temperature end heat exchanger of each refrigeration unit in sequence according to the refrigeration temperature from high to low, the heat of the gas is absorbed, and the temperature is lowered in steps, and the final gas Be liquefied; Wherein, by bypassing the regenerator 3 of each stage refrigerator to a part of the gas in the pulse tube 7 to form expansion refrigeration.

上述装置中,脉管制冷机单元1的脉冲管7与制冷单元的制冷机回热器3属同轴布置。In the above device, the pulse tube 7 of the pulse tube refrigerator unit 1 and the refrigerator regenerator 3 of the refrigeration unit are coaxially arranged.

所述直流抑制器15为弹性隔膜元件或者非对称水力元件。所述旁通气流通道内的气体工质流量由阻力元件调节;阻力元件为阀门、小孔或毛细管组成。所述每级制冷机回热器3的直径相等或者不相等。所述脉冲管7为等直径或非等直径的空管。所述的气体工质为氦气、氢气、氮气或其组合。所述待液化气体为天然气、氮气或氢气。The direct current suppressor 15 is an elastic diaphragm element or an asymmetric hydraulic element. The gas flow rate in the bypass flow channel is regulated by a resistance element; the resistance element is composed of a valve, a small hole or a capillary. The diameters of the regenerators 3 of each refrigerator are equal or unequal. The pulse tube 7 is an empty tube with equal diameter or non-equal diameter. The working gas is helium, hydrogen, nitrogen or a combination thereof. The gas to be liquefied is natural gas, nitrogen or hydrogen.

本发明的环路多级热声发动机驱动气体多级液化装置,其优点在于:其结构简单无运动部件,热声发动机单元工作在行波相位,结构紧凑,能量密度高;采用多个低温端换热器作为梯级冷源,有效减小传热损失,有利于气体液化过程;系统运动部件较少,可靠性高,结构简单;多路旁通结构能够使脉冲管旁通点成为制冷部位,脉冲管中形成膨胀制冷过程,因此能够获得更大的制冷量和更低的制冷温度;在脉冲管旁通点处布置阻力填料,能够减小气流紊乱带来的混合损失。本发明能够高效地实现气体多级液化的整体流程,在液化气体方面具有良好的应用前景。The loop multi-stage thermoacoustic engine-driven gas multi-stage liquefaction device of the present invention has the advantages of simple structure without moving parts, the thermoacoustic engine unit works in the traveling wave phase, compact structure and high energy density; multiple low-temperature ends are used As a cascaded cold source, the heat exchanger effectively reduces heat transfer loss and is beneficial to the gas liquefaction process; the system has fewer moving parts, high reliability, and simple structure; the multi-channel bypass structure can make the bypass point of the pulse tube a cooling part, The expansion refrigeration process is formed in the pulse tube, so greater cooling capacity and lower cooling temperature can be obtained; resistance packing is arranged at the bypass point of the pulse tube, which can reduce the mixing loss caused by the turbulence of the air flow. The invention can efficiently realize the overall process of gas multi-stage liquefaction, and has good application prospects in the aspect of liquefied gas.

附图说明Description of drawings

图1是周远等人提出的多路旁通脉冲管制冷机结构示意图;Figure 1 is a schematic structural diagram of the multiple bypass pulse tube refrigerator proposed by Zhou Yuan et al.

图2是罗二仓等人提出的声学共振型行波热声制冷系统结构示意图;Figure 2 is a schematic structural diagram of the acoustic resonance traveling wave thermoacoustic refrigeration system proposed by Luo Ercang et al.

图3是本发明的环路多级热声发动机驱动的气体多级液化装置(实施例1)结构示意图;Fig. 3 is a schematic structural diagram of a gas multistage liquefaction device (embodiment 1) driven by a loop multistage thermoacoustic engine of the present invention;

图4是本发明的环路多级热声发动机驱动的气体多级液化装置(实施例2)结构示意图。Fig. 4 is a schematic structural diagram of a gas multistage liquefaction device driven by a loop multistage thermoacoustic engine (Example 2) of the present invention.

具体实施方式detailed description

为使本发明的目的、技术方案和优点更加清楚,下面将结合附图及实施例对本发明的技术方案进行清楚、完整地描述,显然,所描述的实施例是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。In order to make the purpose, technical solutions and advantages of the present invention clearer, the technical solutions of the present invention will be clearly and completely described below in conjunction with the accompanying drawings and embodiments. Obviously, the described embodiments are part of the embodiments of the present invention, rather than Full examples. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.

本发明系统对谐振管消耗的声功进行了回收,具有较高的潜在热效率;系统无运动部件,可靠性高,结构紧凑,能量密度高;采用多级冷源,能够梯级降低气体温度,可有效减少传热损失;系统运动部件较少,可靠性高,结构简单;利用多路旁通结构能够使制冷机获得更大的制冷量和更低的制冷温度,提高了制冷机的效率;在脉冲管旁通点处布置阻力填料,能够减小气流紊乱带来的混合损失;本装置能够高效地、可靠地实现气体液化的一体化流程。The system of the present invention recovers the sound power consumed by the resonance tube, and has high potential thermal efficiency; the system has no moving parts, high reliability, compact structure, and high energy density; the multi-stage cold source can reduce the gas temperature step by step, and can Effectively reduce heat transfer loss; the system has fewer moving parts, high reliability, and simple structure; the use of multiple bypass structures can enable the refrigerator to obtain greater cooling capacity and lower cooling temperature, improving the efficiency of the refrigerator; The resistance filler is arranged at the bypass point of the pulse tube, which can reduce the mixing loss caused by the turbulence of the air flow; the device can efficiently and reliably realize the integrated process of gas liquefaction.

实施例1Example 1

图3是本发明的环路多级热声发动机驱动的气体多级(4级)液化装置(实施例1)结构示意图。其由3个热声发动机单元(1#、2#、3#)通过谐振管23首尾相连构成的环路结构及3个脉管制冷机单元1组成;每一热声发动机单元14均由直流抑制器15、发动机主冷却器16、发动机回热器17、加热器18、高温端层流化元件19、热缓冲管20、发动机室温端层流化元件21和发动机次冷却器22组成;每一热声发动机单元14的发动机次冷却器22出口处旁接一个脉管制冷机单元1;Fig. 3 is a schematic structural diagram of a gas multi-stage (four-stage) liquefaction device (embodiment 1) driven by a loop multi-stage thermoacoustic engine of the present invention. It consists of 3 thermoacoustic engine units (1#, 2#, 3#) connected end-to-end through a resonance tube 23 to form a loop structure and 3 pulse tube refrigerator units 1; each thermoacoustic engine unit 14 is composed of DC Suppressor 15, engine main cooler 16, engine regenerator 17, heater 18, high temperature end laminar fluidization element 19, heat buffer pipe 20, engine room temperature end laminar fluidization element 21 and engine secondary cooler 22; A pulse tube refrigerator unit 1 is bypassed at the outlet of the engine subcooler 22 of a thermoacoustic engine unit 14;

本实施例中,每一脉管制冷机单元1均由制冷机主水冷器2、串接的4级制冷单元、连接管5、脉冲管7、制冷机次水冷器10、惯性管11和气库12组成;每一制冷单元均由一个制冷机回热器3和一个低温端换热器4串接而成,第一级制冷单元的制冷机回热器3与制冷机主水冷器2相连,第4级制冷单元的低温端换热器4与连接管5相连;为减小射流带来的损失,所述脉冲管7近连接管5的一端装有低温端导流丝网6,另一端装有制冷机室温端导流丝网9;每级制冷单元的制冷机回热器3通过旁通管路13与脉冲管7相连形成1条旁通气流通道,调整各条旁通气流通道流量的阻力元件为阀门;脉冲管7内还装有阻力填料8,阻力填料8轴向层叠于旁通气体工质进出脉冲管7的接口两侧,以使气体工质均匀顺利通过,所述阻力填料8为丝网;In this embodiment, each pulse tube refrigerator unit 1 is composed of the main water cooler 2 of the refrigerator, the 4-stage refrigeration unit connected in series, the connecting pipe 5, the pulse tube 7, the secondary water cooler 10 of the refrigerator, the inertia tube 11 and the gas storage 12 components; each refrigeration unit is composed of a refrigerator regenerator 3 and a low-temperature end heat exchanger 4 connected in series, the refrigerator regenerator 3 of the first-stage refrigeration unit is connected with the refrigerator main water cooler 2, The low-temperature end heat exchanger 4 of the fourth-stage refrigeration unit is connected to the connecting pipe 5; in order to reduce the loss caused by the jet flow, one end of the pulse tube 7 near the connecting pipe 5 is equipped with a low-temperature end guide wire mesh 6, and the other end Equipped with deflector mesh 9 at the room temperature end of the refrigerator; the regenerator 3 of the refrigerator at each stage of the refrigeration unit is connected to the pulse tube 7 through a bypass pipeline 13 to form a bypass airflow channel, and the flow rate of each bypass airflow channel is adjusted The resistance element is a valve; the pulse tube 7 is also equipped with a resistance packing 8, and the resistance packing 8 is axially stacked on both sides of the interface where the bypass gas working medium enters and exits the pulse tube 7, so that the gas working medium can pass through evenly and smoothly. Filler 8 is silk screen;

本实施例1中,气体工质为氦气,待液化的气体为天然气,加热器18与热源相连并吸收热源热量形成相同温度的高温端(923K);发动机主冷却器16、发动机次冷却器22、制冷机主水冷器2和制冷机次水冷器10通过冷却水冷却以维持在室温范围(310K);每一级热声发动机单元14的发动机回热器17上形成温度梯度,发动机回热器17内部工作气体与其内的固体填料间产生热声效应,将输入到加热器18的热量转化成声功;声功沿着温度梯度的正方向传播并放大,一部分声功传递到脉管制冷机单元1中,另一部分通过谐振管23传递到下一级热声发动机单元14中重复以上过程;传递到脉管制冷机单元1的声功在每级制冷机回热器17中发生热声转换:传递到第4级制冷回热器17中的声功经过热声转换,将第4级低温端换热器4的热量泵送到第3级的低温端换热器4中,第4级低温端换热器保持低温;传递到第3级制冷单元中的声功经过热声转换,将第3级低温端换热器的热量泵送到第2级的低温端换热器中,第3级低温端换热器保持低温;如此,最终所有低温端换热器4的热量均泵送到制冷机主水冷器2中,热量由冷却水带走;相邻制冷单元中低温端换热器4的温度差均为50K,即第1至第4级低温端换热器的制冷温度依次为260K、210K、160K、110K(天然气液化温区);待液化的天然气按照制冷温度从高到低的依次通过每一低温端换热器,气体热量被吸收,温度依次降低,最终被液化;其中,通过从制冷机回热器3旁通到脉冲管7内一部分气体可以有效增加脉冲管7内气体的刚度,同时能够使脉冲管7内压力波动变大,压力波动和体积流率的相位更加接近,有利于提高脉冲管制冷机的效率。In this embodiment 1, the gas working medium is helium, and the gas to be liquefied is natural gas, and the heater 18 is connected to the heat source and absorbs the heat of the heat source to form a high temperature end (923K) of the same temperature; the engine main cooler 16, the engine secondary cooler 22. The main water cooler 2 of the refrigerator and the secondary water cooler 10 of the refrigerator are cooled by cooling water to maintain the room temperature range (310K); a temperature gradient is formed on the engine regenerator 17 of each stage of thermoacoustic engine unit 14, and the engine regenerates heat The thermoacoustic effect is generated between the working gas inside the device 17 and the solid packing inside, and the heat input to the heater 18 is converted into sound work; the sound work is propagated and amplified along the positive direction of the temperature gradient, and a part of the sound work is transferred to the pulse tube cooling In the machine unit 1, the other part is transferred to the next-stage thermoacoustic engine unit 14 through the resonant tube 23 to repeat the above process; Conversion: The sound work transferred to the fourth-stage refrigeration regenerator 17 undergoes thermoacoustic conversion, and the heat of the fourth-stage low-temperature end heat exchanger 4 is pumped to the third-stage low-temperature end heat exchanger 4, and the fourth-stage The heat exchanger at the low-temperature end of the first stage keeps the low temperature; the sound work transferred to the third-stage refrigeration unit undergoes thermoacoustic conversion, and the heat from the low-temperature end heat exchanger of the third stage is pumped to the low-temperature end heat exchanger of the second stage, The heat exchanger at the low-temperature end of the third stage keeps the low temperature; in this way, all the heat of the heat exchanger 4 at the low-temperature end is pumped to the main water cooler 2 of the refrigerator, and the heat is taken away by the cooling water; the heat exchanger at the low-temperature end of the adjacent refrigeration unit The temperature difference of the heater 4 is 50K, that is, the cooling temperatures of the first to fourth stage low-temperature end heat exchangers are 260K, 210K, 160K, and 110K (natural gas liquefaction temperature zone); The gas heat is absorbed, the temperature is lowered in turn, and finally liquefied; wherein, by bypassing a part of the gas from the regenerator 3 of the refrigerator to the pulse tube 7, the pulse tube can be effectively increased. The rigidity of the gas in the pulse tube 7 can also increase the pressure fluctuation in the pulse tube 7, and the phase of the pressure fluctuation and the volume flow rate is closer, which is beneficial to improve the efficiency of the pulse tube refrigerator.

实施例2:Example 2:

图4是本发明的环路多级热声发动机驱动的气体多级(4级)液化装置(实施例2)结构示意图;该装置由3个热声发动机单元(1#、2#、3#)通过谐振管23首尾相连构成的环路结构及3个脉管制冷机单元1组成;每一热声发动机单元14由直流抑制器15、发动机主冷却器16、发动机回热器17、加热器18、高温端层流化元件19、热缓冲管20、发动机室温端层流化元件21和发动机次冷却器22组成;每一热声发动机单元14的发动机次冷却器22出口处旁接一个脉管制冷机单元1;Fig. 4 is the gas multi-stage (4 stage) liquefaction device (embodiment 2) structural representation driven by loop multi-stage thermoacoustic engine of the present invention; The device consists of 3 thermoacoustic engine units (1#, 2#, 3# ) consists of a loop structure connected end to end by resonance tubes 23 and three pulse tube refrigerator units 1; each thermoacoustic engine unit 14 is composed of a DC suppressor 15, an engine main cooler 16, an engine regenerator 17, a heater 18. Composed of a high-temperature end laminar fluidization element 19, a thermal buffer pipe 20, an engine room temperature end laminar fluidization element 21, and an engine subcooler 22; the outlet of the engine subcooler 22 of each thermoacoustic engine unit 14 is bypassed by a pulse Tube refrigerator unit 1;

在每一脉管制冷机单元1中,一个制冷机回热器3及一个与其串接的低温端换热器4构成一级制冷单元,本实施例有依次串接的4级制冷单元;脉冲管7位于第一至第四级制冷单元的制冷机回热器之内,第一级制冷单元的制冷机回热器3热端和脉冲管7热端均与制冷机主水冷器2相接触,脉冲管7冷端与第4级低温端换热器4相接触;气库12通过惯性管11和制冷机主水冷器2相连接;In each pulse tube refrigerator unit 1, a refrigerator regenerator 3 and a low-temperature end heat exchanger 4 connected in series form a first-stage refrigeration unit, and this embodiment has four stages of refrigeration units connected in series; The pipe 7 is located in the refrigerator regenerators of the first to fourth stage refrigeration units, and the hot end of the refrigerator regenerator 3 of the first stage refrigeration unit and the hot end of the pulse tube 7 are in contact with the main water cooler 2 of the refrigerator , the cold end of the pulse tube 7 is in contact with the fourth-stage low-temperature end heat exchanger 4; the gas storage 12 is connected with the main water cooler 2 of the refrigerator through the inertia tube 11;

脉冲管7两端分别装有低温端导流丝网6和制冷机室温端导流丝网9,以减小射流带来的损失;在每级制冷单元的制冷机回热器和脉冲管7共有壁面上开有1个小孔构成制冷机回热器与脉冲管的旁通气流通道;并在每个小孔两侧的脉冲管7内布置阻力填料8,阻力填料为丝网;The two ends of the pulse tube 7 are respectively equipped with a low-temperature end guide wire mesh 6 and a refrigerator room temperature end guide wire mesh 9 to reduce the loss caused by the jet flow; A small hole is opened on the common wall to form a bypass airflow channel between the regenerator of the refrigerator and the pulse tube; and resistance packing 8 is arranged in the pulse tube 7 on both sides of each small hole, and the resistance packing is a wire mesh;

本实施例2中,气体工质为氦气,待液化的气体为天然气,加热器18与热源相连以吸收热源热量形成相同温度的高温端(923K);发动机主冷却器16、发动机次冷却器22、制冷机主水冷器2和制冷机次水冷器10通过冷却水冷却以维持在室温范围(310K);在每一级热声发动机单元14的发动机回热器17上形成温度梯度,发动机回热器17内部工作气体与其内的固体填料间产生热声效应,将输入到加热器18的热量转化成声功;声功沿着温度梯度的正方向传播并放大,一部分声功传递到脉管制冷机单元1中,另一部分通过谐振管23传递到下一级热声发动机单元中重复以上过程;传递到脉管制冷机单元1的声功在每级制冷机回热器3中发生热声转换:传递到第4级制冷机回热器3中的声功经过热声转换,将第4级低温端换热器4的热量泵送到第3级的低温端换热器中,第4级低温端换热器保持低温;传递到第3级制冷单元中的声功经过热声转换,将第3级低温端换热器的热量泵送到第2级的低温端换热器中,第3级低温端换热器保持低温;如上所述,最终所有低温端换热器4的热量均泵送到制冷机主水冷器2中,热量由冷却水带走。相邻制冷单元中的低温端换热器4的温度差均为50K,即第1~4级低温端换热器的制冷温度依次为260K、210K、160K、110K(天然气液化温区)。待液化的天然气按照制冷温度从高到低的顺序依次通过每一低温端换热器,气体热量被吸收,温度依次降低,最终被液化。其中,通过从每级制冷机回热器3旁通到脉冲管7内一部分气体可以有效增加脉冲管内气体的刚度,同时能够使脉冲管内压力波动变大,压力波动和体积流率的相位更加接近,有利于提高脉冲管制冷机的效率。In this embodiment 2, the gas working medium is helium, and the gas to be liquefied is natural gas, and the heater 18 is connected to the heat source to absorb the heat of the heat source to form a high-temperature end (923K) of the same temperature; the engine main cooler 16, the engine secondary cooler 22. The main water cooler 2 of the refrigerator and the secondary water cooler 10 of the refrigerator are cooled by cooling water to maintain the room temperature range (310K); a temperature gradient is formed on the engine regenerator 17 of each stage of thermoacoustic engine unit 14, and the engine regenerator The thermoacoustic effect is generated between the working gas inside the heater 17 and the solid filler inside, and the heat input to the heater 18 is converted into sound work; the sound work is propagated and amplified along the positive direction of the temperature gradient, and a part of the sound work is transmitted to the vessel In the refrigerator unit 1, the other part is transmitted to the next-stage thermoacoustic engine unit through the resonant tube 23 to repeat the above process; Conversion: The sound work transferred to the regenerator 3 of the fourth-stage refrigerator undergoes thermoacoustic conversion, and the heat of the low-temperature end heat exchanger 4 of the fourth stage is pumped to the low-temperature end heat exchanger of the third stage. The heat exchanger at the low-temperature end of the first stage keeps the low temperature; the sound work transferred to the third-stage refrigeration unit undergoes thermoacoustic conversion, and the heat from the low-temperature end heat exchanger of the third stage is pumped to the low-temperature end heat exchanger of the second stage, The third-stage low temperature end heat exchanger keeps the low temperature; as mentioned above, finally all the heat from the low temperature end heat exchanger 4 is pumped to the main water cooler 2 of the refrigerator, and the heat is taken away by the cooling water. The temperature difference between the low-temperature end heat exchangers 4 in adjacent refrigeration units is 50K, that is, the cooling temperatures of the first to fourth-stage low-temperature end heat exchangers are 260K, 210K, 160K, and 110K (natural gas liquefaction temperature range). The natural gas to be liquefied passes through each low-temperature end heat exchanger sequentially according to the order of refrigeration temperature from high to low, the heat of the gas is absorbed, the temperature decreases in turn, and finally is liquefied. Among them, by bypassing a part of the gas in the pulse tube 7 from the regenerator 3 of each refrigerator, the stiffness of the gas in the pulse tube can be effectively increased, and at the same time, the pressure fluctuation in the pulse tube can be increased, and the phase of the pressure fluctuation and the volume flow rate is closer , which is beneficial to improve the efficiency of the pulse tube refrigerator.

最后应说明的是:以上各实施例仅用以说明本发明的技术方案,而非对其限制;尽管参照前述各实施例对本发明进行了详细的说明,本领域的普通技术人员应当理解:其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分或者全部技术特征进行等同替换;而这些修改或者替换,并不使相应技术方案的本质脱离本发明各实施例技术方案的范围。Finally, it should be noted that: the above embodiments are only used to illustrate the technical solutions of the present invention, rather than limiting them; although the present invention has been described in detail with reference to the foregoing embodiments, those of ordinary skill in the art should understand that: It is still possible to modify the technical solutions described in the foregoing embodiments, or perform equivalent replacements for some or all of the technical features; and these modifications or replacements do not make the essence of the corresponding technical solutions deviate from the technical solutions of the various embodiments of the present invention. scope.

Claims (8)

1. the multistage liquefying plant of gas of a loop Multi-stage heat phonomotor driving, its by M thermoacoustic engine unit (14) by resonatron (23) join end to end form loop structure and M vascular refrigerator unit (1) form, M is 3 ~ 6 positive integers; Described thermoacoustic engine unit (14) is made up of the direct current suppressor be connected successively (15), engine primary cooler (16), engine regenerator (17), heater (18), temperature end laminarization element (19), thermal buffer tube (20), engine room temperature end layer fluidisation element (21) and engine time cooler 22; Engine time cooler (22) exit of each thermoacoustic engine unit (14) is other connects a vascular refrigerator unit (1);
Described vascular refrigerator unit (1) is made up of to N level refrigeration unit, tube connector (5), pulse tube (7), refrigeration machine time water cooler (10), inertia tube (11) and air reservoir (12) the refrigeration owner water cooler (2) be connected successively, first, and wherein N is 2 ~ 6 positive integers; Described refrigeration unit is made up of a refrigeration machine regenerator (3) and a low-temperature end heat exchanger (4) being connected in series with it; The refrigeration machine regenerator (3) of the 1st grade of refrigeration unit is connected with refrigeration owner's water cooler (2), and the low-temperature end heat exchanger (4) of N level refrigeration unit is connected with pulse tube (7) cold junction by tube connector (5); Pulse tube (7) two ends are equipped with low-temperature end water conservancy diversion silk screen (6) and refrigeration machine indoor temperature end water conservancy diversion silk screen (9) respectively;
In each vascular refrigerator unit (1), the refrigeration machine regenerator (3) of refrigeration unit is connected to form at least one bypass flow passage by bypass line (13) and pulse tube (7); Pulse tube (7) is built with resistance filler (8), resistance filler (8) is axially laminated in the interface both sides of gas working medium turnover pulse tube (7), and described resistance filler (8) is silk screen or porous media material;
The heater (18) of each thermoacoustic engine unit (14) is connected with thermal source to absorb the temperature end that heat from heat source forms identical temperature; Engine primary cooler (16) and engine time cooler (22) all cool to maintain room temperature range by water cooler; For this reason, the upper formation temperature gradient of the engine regenerator (17) of every one-level thermoacoustic engine unit (14); Under this thermograde, between engine regenerator (17) interior working gas and the solid packing in it, produce thermoacoustic effect, the converting heat Cheng Shenggong of heater (18) will be input to; Sound merit is propagated along the positive direction of thermograde and amplifies, and a part of sound merit is delivered in vascular refrigerator unit (1), and another part is delivered in next stage thermoacoustic engine unit by resonatron (23) and repeats above process; In vascular refrigerator unit (1), refrigeration owner's water cooler (2) and refrigeration machine time water cooler (10) maintain room temperature range by water quench; In N level refrigeration unit, the sound merit produced from thermoacoustic engine is delivered in refrigeration machine regenerator (3) and Sonic heat changing occurs, be pumped in the low-temperature end heat exchanger of N-1 level by the heat of N grade low-temp end heat exchanger (4), N grade low-temp end heat exchanger (4) keeps low temperature; As mentioned above, be delivered to sound merit in N-1 level refrigeration unit through Sonic heat changing, be pumped in the low-temperature end heat exchanger of N-2 level by the heat of N-1 grade low-temp end heat exchanger, N-1 grade low-temp end heat exchanger keeps low temperature; Finally, the heat of all low-temperature end heat exchangers is all pumped in refrigeration owner's water cooler (2), and heat is taken away by cooling water, and the cryogenic temperature of N grade low-temp end heat exchanger is reduced to gas liquefaction temperature successively; Gas to be liquefied passes through the low-temperature end heat exchanger of each refrigeration unit successively according to cryogenic temperature order from high to low, and gas heat is absorbed, and temperature step reduces, and final gas is liquefied; Wherein, swell refrigeration is formed by being bypassed to a part of gas in pulse tube (7) from every grade of refrigeration machine regenerator (3).
2. the multistage liquefying plant of gas of a loop Multi-stage heat phonomotor driving, its by M thermoacoustic engine unit (14) by resonatron (23) join end to end form loop structure and M vascular refrigerator unit (1) form, M is 3 ~ 6 positive integers; Described thermoacoustic engine unit (14) is made up of the direct current suppressor be connected successively (15), engine primary cooler (16), engine regenerator (17), heater (18), temperature end laminarization element (19), thermal buffer tube (20), engine room temperature end layer fluidisation element (21) and engine time cooler 22; Engine time cooler (22) exit of each thermoacoustic engine unit (14) is other connects a vascular refrigerator unit (1);
Described vascular refrigerator unit (1) is by refrigeration owner's water cooler (2), the first order be connected with refrigeration owner's water cooler (2) is to N level refrigeration unit, be positioned at the described first order to N level refrigeration unit refrigeration machine regenerator (3) within pulse tube (7), refrigeration machine time water cooler (10), inertia tube (11) and air reservoir (12) composition, wherein N is the positive integer of 2 ~ 6; Described refrigeration unit is made up of a refrigeration machine regenerator (3) and a low-temperature end heat exchanger (4) being connected in series with it; The refrigeration machine regenerator (3) of the 1st grade of refrigeration unit and pulse tube (7) indoor temperature end are connected with refrigeration owner's water cooler (2), and the low-temperature end heat exchanger (4) of N level refrigeration unit is connected with pulse tube (7) cold junction; Pulse tube (7) two ends are equipped with low-temperature end water conservancy diversion silk screen (6) and refrigeration machine indoor temperature end water conservancy diversion silk screen (9) respectively;
In each vascular refrigerator unit (1), the refrigeration machine regenerator (3) of refrigeration unit is connected by multiple through hole that both common walls are opened or the porous media wall directly made with pulse tube (7); Pulse tube (7) is built with resistance filler (8), resistance filler (8) is axially laminated in the interface both sides of gas working medium turnover pulse tube (7), and described resistance filler (8) is silk screen or porous media material;
The heater (18) of each thermoacoustic engine unit (14) is connected with thermal source to absorb the temperature end that heat from heat source forms identical temperature; Engine primary cooler (16) and engine time cooler (22) all cool to maintain room temperature range by water cooler; For this reason, the upper formation temperature gradient of the engine regenerator (17) of every one-level thermoacoustic engine unit (14); Under this thermograde, between engine regenerator (17) interior working gas and the solid packing in it, produce thermoacoustic effect, the converting heat Cheng Shenggong of heater (18) will be input to; Sound merit is propagated along the positive direction of thermograde and amplifies, and a part of sound merit is delivered in vascular refrigerator unit (1), and another part is delivered in next stage thermoacoustic engine unit by resonatron (23) and repeats above process; In vascular refrigerator unit (1), refrigeration owner's water cooler (2) and refrigeration machine time water cooler (10) maintain room temperature range by water quench; In N level refrigeration unit, the sound merit produced from thermoacoustic engine is delivered in refrigeration machine regenerator (3) and Sonic heat changing occurs, be pumped in the low-temperature end heat exchanger of N-1 level by the heat of N grade low-temp end heat exchanger (4), N grade low-temp end heat exchanger (4) keeps low temperature; As mentioned above, be delivered to sound merit in N-1 level refrigeration unit through Sonic heat changing, be pumped in the low-temperature end heat exchanger of N-2 level by the heat of N-1 grade low-temp end heat exchanger, N-1 grade low-temp end heat exchanger keeps low temperature; Finally, the heat of all low-temperature end heat exchangers is all pumped in refrigeration owner's water cooler (2), and heat is taken away by cooling water, and the cryogenic temperature of N grade low-temp end heat exchanger is reduced to gas liquefaction temperature successively; Gas to be liquefied passes through the low-temperature end heat exchanger of each refrigeration unit successively according to cryogenic temperature order from high to low, and gas heat is absorbed, and temperature step reduces, and final gas is liquefied; Wherein, swell refrigeration is formed by being bypassed to a part of gas in pulse tube (7) from every grade of refrigeration machine regenerator (3).
3., by the multistage liquefying plant of loop Multi-stage heat phonomotor driving gas described in claim 1 or 2, it is characterized in that, described direct current suppressor (15) is elastic diaphragm element or asymmetric hydraulic component.
4., by the multistage liquefying plant of loop Multi-stage heat phonomotor driving gas described in claim 1 or 2, it is characterized in that, the gas working medium flow in described bypass flow passage is regulated by resistance element; Resistance element is valve, aperture or capillary composition.
5. by the multistage liquefying plant of loop Multi-stage heat phonomotor driving gas described in claim 1 or 2, it is characterized in that, the equal diameters of described every grade of refrigeration machine regenerator (3) or unequal.
6., by the multistage liquefying plant of loop Multi-stage heat phonomotor driving gas described in claim 1 or 2, it is characterized in that, described pulse tube (7) is equal diameter blank pipe or non-equal diameter blank pipe.
7. by the multistage liquefaction flow path of a kind of loop Multi-stage heat phonomotor driving gas described in claim 1 or 2 and device, it is characterized in that, described gas working medium is helium, hydrogen, nitrogen or its combination.
8., by the multistage liquefaction flow path of a kind of loop Multi-stage heat phonomotor driving gas described in claim 1 or 2 and device, it is characterized in that, described gas to be liquefied is natural gas, nitrogen or hydrogen.
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