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Condensation stage of a pulse tube pre-cooled dilution refrigerator

机译:脉冲管预冷稀释机的冷凝阶段

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摘要

In our article, experiments with a pulse tube (PTR) pre-cooled dilution refrigerator (DR) are presented, where an upgraded ~3He condensation stage has been tested. The DR had a ~3He flow rate of up to 1.1 mmol/s. The ~3He gas entering the refrigerator was first pre-cooled to a temperature of approx 50 KAPPA at the first stage of the PTR. In the next cooling step, the ~3He was run through a recently installed heat exchanger, which was attached to the regenerator of the second stage of the pulse tube cryocooler; at the outlet of this heat exchanger the temperature of the ~3He was as low as approx 4 KAPPA. Due to the non-ideality of the helium gas, the second regenerator of a two stage PTR has excess cooling power which can be made use of without affecting the base temperature of this stage, and it is this effect which was put to work, here. Finally, the ~3He was further cooled in a heat exchanger, mounted at the second stage of the PTR, before it entered the dilution unit of the cryostat. The installation of a heat exchanger at the regenerator of the second stage of the PTR is especially important for the construction of DRs with high refrigeration capacities; in addition, it allows for a plain design of the subsequent Joule-Thomson (JT) stage, and herewith facilitates considerably the construction of "dry" DRs. The condensation rate of the ~(3,4)He mash prior to an experiment was increased. The pressure during condensation could be kept near 1 bar, and thus a compressor was no longer necessary with the modified apparatus.
机译:在我们的文章中,介绍了使用脉冲管(PTR)预冷的稀释冰箱(DR)进行的实验,其中已测试了升级的〜3He冷凝阶段。 DR的〜3He流速高达1.1 mmol / s。在PTR的第一阶段,首先将进入冰箱的〜3He气体预冷至约50 KAPPA的温度。在下一个冷却步骤中,〜3He通过最近安装的热交换器运行,该热交换器连接到脉冲管低温冷却器第二级的再生器上;在该热交换器的出口处,〜3He的温度低至约4 KAPPA。由于氦气的不理想性,两级PTR的第二个蓄冷器具有过量的冷却功率,可以在不影响该阶段的基础温度的情况下利用该冷却器,正是这种作用在这里发挥了作用。 。最后,〜3He在安装到PTR第二阶段的热交换器中进一步冷却,然后进入低温恒温器的稀释装置。在PTR第二阶段的再生器上安装热交换器对于高制冷量DR的构造尤为重要。另外,它允许随后的焦耳-汤姆逊(JT)阶段的简单设计,从而大大简化了“干” DR的构造。实验之前〜(3,4)He mash的冷凝速率增加了。冷凝过程中的压力可以保持在1 bar附近,因此,改进的设备不再需要压缩机。

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