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The phase separation of 3He—4He mixtures

✍ Scribed by D.H.N. Wansink


Publisher
Elsevier Science
Year
1957
Weight
46 KB
Volume
23
Category
Article
ISSN
0031-8914

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✦ Synopsis


In our paper concerning the calculation of thermodynamic quantities of 3He-4He mixtures from the vapour pressure 1) we derived the Gibbs-function of mixing zlG as a function of the 3He-concentration X at different temperatures. From such a diagram the unstable concentration regions should be found by determining the pairs of points of the AG-X curves which have a tangent in common. Because this requires the knowledge of ziG at all values of X between 0 and l, whereas our calculations yielded AG up to X = 0.07 only, we had to confine ourselves to an approximation: zIG =,0 was used as criterion for the demixing, since mixtures, for which LIG > 0, are unstable in any case. The T-X curve, obtained in this way and given in fig. 8 of the paper mentioned above, gives only a lower limit of the temperature of demixing. A better result, however, will be obtained by using the points of the AG-X diagram, for which OAG/OX = 0. The results are shown in fig. 1, which should replace the old fig. 8. The agreement with the experimental values is now rather poor.


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