共查询到19条相似文献,搜索用时 93 毫秒
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斯特林制冷机的计算机辅助调机 总被引:2,自引:0,他引:2
通过对双自由度斯特林制冷机振动系统模型的分析 ,建立了计算机仿真调相角模型。在模型求解过程中 ,通过改变弹簧参数来优化斯特林制冷机的压力波和制冷机回热器位移之间的相位差 ,使其接近最优相角要求 ,来辅助调节系统的工作参数。模型模拟的结果与实验结果能较好的吻合 相似文献
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为满足低温存储领域对小型化、大冷量、高效率斯特林制冷机的应用需求,研究基于斯特林制冷机的特点,结合实际现状,设计了一台可用于低温存储领域的-80℃自由活塞式斯特林制冷机。根据其运行原理,通过数值模拟及实验验证重点分析了设备运行频率和工作压力对整机性能的影响,在此基础上讨论并提出了制冷机的优化思路。实验结果表明回热器采用丝网填充,工作压力为2.9 MPa,运行频率为63 Hz时,该制冷机在175.1 W输入功率下,可在-85℃提供29 W冷量输出,COP为0.166;当使用PET材料时,无热负载状态下最快可在42分钟左右冷端温度达到-86℃,其性能表现满足现有小型低温冰箱的冷量需求。通过数值模拟和实验结果的对比,讨论了出现性能差异的原因。 相似文献
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《真空与低温》2016,(6)
自由活塞斯特林制冷机具有高效紧凑,适合中低温制冷等优点。对用于低温冰箱自由活塞式斯特林制冷机进行了一维建模,并实现整机性能的模拟与优化。在考虑各种空体积的情况下,模拟分析了压缩活塞PV功和相位角的变化对整机性能的影响,获得了制冷机运行的最佳相位。对比了环形回热器的填料及填充方式对自由活塞式斯特林制冷机的性能影响,及对应材料下回热器的轴向导热损失情况。模拟了制冷机性能随回热器空隙率和制冷温度的变化情况,计算分析了回热器内部的不可逆损失随空隙率的变化情况,并且获得了不同温度下的最佳空隙率。最后,为了获得好的制冷性能,优化不同制冷温度的回热器设计参数及膨胀活塞与气缸壁的密封间隙宽度。 相似文献
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《低温学》1987,27(3):152-155
The results of experimental investigations on the cyclic flow characteristic of the regenerator of a split cycle Stirling cryocooler is presented. A mathematical model has been proposed to describe the action of regenerator and other main components of the cryocooler system on its dynamic response. 相似文献
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《低温学》2003,43(10-11):575-581
This paper describes an experimental apparatus developed to investigate detailed thermal and hydrodynamic characteristics of a regenerator at cryogenic temperature under oscillating flow and pulsating pressure conditions. Cold-end of the regenerator is maintained at approximately 85 K for G-M cryocooler type and 100 K for Stirling cryocooler type operations by means of two cryogenic heat exchangers. At both ends of the regenerator, fine hot wire probes are installed to measure the fast oscillating gas temperature and mass flow rate. The gas temperature sensors installed very close to the ends of the regenerator matrix assure precise gas temperature measurement in the regenerator. In this study, thermal and hydrodynamic behaviors of the well-defined wire-screen regenerator are fully characterized. First, pressure drop characteristics are discussed for different frequencies under room temperature. Second, ineffectiveness of the regenerator is obtained for different cold-end temperatures. 相似文献
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《低温学》2014
A mathematical model based on thermodynamic theory of variable mass is developed for the split Stirling refrigerator, in which, the whole machine is considered by one-dimensional approach while the processes in the regenerator are simulated by two-dimensional approach. First, the influence of the ideal frost layer distributions on the flow and heat transfer in the regenerator and the performance of the Stirling cryocooler are simulated. Then, the distribution of the contaminated water vapor and its coagulated and deposited process is qualitatively analyzed. Finally, the lifetime of the refrigerator is evaluated based on the calculated data. The results show that when the refrigerator is operated at uniform distribution of the water vapor partial pressure in the regenerator, the cooling capacity is reduced over 10% at about 631 h, and the power consumption of compressor is increased over 20% at about 1168 h. However, for the linear distribution of water vapor partial pressure, the refrigerator can work properly because the frost never reaches the criterion of failure. Also, it is found that when the Stirling cryocooler restarts after a shutdown, the cooling capacity is reduced by 10% once the frost mass is over 7.05 mg, and there is no cooling capacity once the frost mass reaches 41.2 mg. 相似文献
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P.C.T. de Boer 《低温学》2011,(2):105-113
The key component of a regenerative cryocooler is its regenerative heat exchanger. This device is subject to losses due to imperfect heat transfer between the regenerator material and the gas, as well as due to viscous dissipation. The relative magnitudes of these losses can be characterized by the ratio of the Stanton number St to the Fanning friction factor f. Using available data for the ratio St/f, results are developed for the optimal cooling rate and Carnot efficiency. The variations of pressure and temperature are taken to be sinusoidal in time, and to have small amplitudes. The results are applied to the case of the Stirling cryocooler, with flow being generated by pistons at both sides of the regenerator. The performance is found to be close to optimal at large ratio of the warm space volume to the regenerator void volume. The results are also applied to the Orifice Pulse Tube Refrigerator. In this case, optimal performance additionally requires a large ratio of the regenerator void volume to the cold space volume. 相似文献
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In this paper, an isothermal model is used for modeling the Stirling cryocooler. Various losses including regenerator imperfection thermal loss, piston finite speed loss, gas spring hysteresis loss, displacer shuttle heat loss, clearance heat pump loss, heat conduction loss, and flow viscosity loss are taken into consideration at the same time step, as they could interact with each other. Energy and exergy balance analysis of the cryocooler shows that the mechanical friction loss is the biggest mechanical loss; conduction loss is the biggest heat loss. Effects of parameters consisting of cold end temperature, hot end temperature, average pressure, rotation speed, displacer clearance size, phase shift between piston and displacer, and ratio between diameter and stroke of piston on the cryocooler's performance are investigated. It shows that, there is optimum displacer clearance size, optimum phase shift between piston and displacer, and optimum ratio between diameter and stroke of piston for the studied cryocooler. The isothermal model was verified by the PPC-102 Stirling cryocooler. 相似文献
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The hydrodynamic parameters associated with steady longitudinal and lateral (radial) flow of helium in several widely-used pulse tube and Stirling cryocooler regenerator fillers were measured and correlated in this investigation. Pressure drops in test sections packed with regenerator fillers were experimentally measured. Computational fluid dynamics (CFD) models of the regenerator test sections and their vicinities were developed and simulations were performed in which the regenerator test sections were modeled as porous media. By iterative repetition of the simulations, the longitudinal and radial permeability and Forchheimer inertial coefficients were determined such that they would lead to agreement between experimental measurements and the simulations. The regenerator fillers included 325 and 400 mesh stainless steel screens, stainless steel metal foam, sintered 400 mesh stainless steel screens, and a stack of micromachined perforated plates. The hydrodynamic response of the regenerator fillers were also correlated as friction factors. The results confirm that the aforementioned regenerator fillers are anisotropic. 相似文献
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