1992
DOI: 10.1007/bf00114918
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Experimental techniques: Methods for cooling below 300 mK

Abstract: There are at present three methods for cooling samples to temperatures below 300 mK: dilution, Pomeranchuk, and nuclear refrigeration. We give the basic principles of these methods with more details concerning dilutions refrigerators. This should allow the construction of a simple all plastic refrigerator for temperatures lower than 15 mK, or an even simpler Pomeranchuk cell. The source of heat leaks and other important points for reaching temperatures in the microkelvin range with nuclear refrigerators are gi… Show more

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Cited by 43 publications
(10 citation statements)
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“…The dilution refrigerator followed a PSI design [19] with the substitution of a coiled heat exchanger made of 0.7-mm-innerdiameter × 0.15-mm wall teflon tubing [20]. The refrigerator operation was monitored with RuO resistance thermometers referenced to a calibrated germanium thermometer.…”
Section: Experimental Methodsmentioning
confidence: 99%
“…The dilution refrigerator followed a PSI design [19] with the substitution of a coiled heat exchanger made of 0.7-mm-innerdiameter × 0.15-mm wall teflon tubing [20]. The refrigerator operation was monitored with RuO resistance thermometers referenced to a calibrated germanium thermometer.…”
Section: Experimental Methodsmentioning
confidence: 99%
“…The ideal cooling capacity-temperature curve ( ݊ = 1 × 10 ିସ ‫݈݉‬ ‫ݏ‬ ⁄ ) is shown in Figure 5, with complete heat exchange and no heat leakage. Now for a specific dilution refrigerator, assuming that the material of the tube heat exchanger is CuNi alloy (ܴ ெ = 12 × 10 ିଷ ‫ܭ‬ ସ ݉ ଶ ܹ ⁄ ), the following analysis is based on this premise) [13], the influence of 3 He purity on cooling capacity (݊ = 1 × 10 ିସ ‫݈݉‬ ‫ݏ‬ ⁄ and the heat exchange area is 100ܿ݉ ଶ ) is shown in Figure 6. The flow rate increases with the temperature rising.…”
Section: Figure 6 Influence Of 3 He Purity On Cooling Capacitymentioning
confidence: 99%
“…CuNi tube-in-tube continuous counterflow heat exchangers have been shown to be well suited to DRs with flow rates on the order of a few μmol/s with 100 mK base temperatures [9]. Several models [9,[18][19][20] estimated the efficiency of the heat exchanger as where the enthalpy coefficients of the diluted and the concentrated phase of the 3 He∕ 4 He mixture are D = 107 J∕K 2 ∕mol and C = 23 J∕K 2 ∕mol [9], respectively, and f is a dimensionless factor given by where A is the surface area of the heat exchanger inner tube, a K is the Kapitza resistivity and T m is the MDR lowest achievable temperature. The area A > 40 cm 2 has been chosen to suit the cooling power requirements, in order to minimize the effect of Kapitza resistance.…”
Section: Designmentioning
confidence: 99%