techniques for approximating the international temperature ... - BIPM
techniques for approximating the international temperature ... - BIPM techniques for approximating the international temperature ... - BIPM
62 transitions, but it could be applied also to those based on solid-to-vapour transitions (sublimation) with suitable changes. 6.1 Two-Phase Equilibrium The number of parameters that can be arbitrarily imposed on a system is given by Gibb's phase rule: v = c + 2 - Φ where c is the number of constituents of the system, Φ is the number of phases, and v is the number of degrees of freedom (or variance). For a pure substance with two phases (c = 1, Φ = 2), v = 1. The data for the pressure therefore fix the value of the temperature at the intersection in Fig. 6.1 of a line T = constant with the curve tC; this is the measurement principle of the thermometers described here. In fact, the points of this curve are a series of equilibrium states that are distinguished by the distribution between the two phases of the total number of moles of the substance enclosed. The equilibrium is regulated by the Gibbs-Duhem relationship, which holds in the simple case described here, by the simultaneous realization of three conditions: PL = Pv TL = Tv and µL(TL,PL) = µv(Tv,Pv) , where the indices L and v refer to the liquid and vapour phases respectively; P and T are the pressure and temperature at the separation surface; and µ, the chemical potential, is identical for a pure substance to the free molar enthalpy. Any variation of one of the three quantities causes displacement of the equilibrium. If the substance is not pure but contains soluble impurities, the variance of the system, becomes equal to the number of constituents present. Suppose that: each constituent is present at the same time in both liquid and vapour phases; the vapour phase is a mixture of perfect vapours; the surface-tension is negligible; the liquid phase is an ideal solution, that is to say, the substances mix without change of volume or enthalpy. This last assumption is realistic so long as the molar fractions xi (i = 2 to n) of the (n - 1) impurities present (solutes) are very small with respect to that (x1 ~ 1) of the pure substance (solvent) filling the thermometer. (Note that the respective concentrations denoted xi L and xi v (i = 1 to n) are generally not equal, as will be seen later.) Under these conditions, the deviation
63 from an ideal solution is less than 1 % so long as the molar fractions of solutes are less than 10 -3 . The equilibrium of such a system must always satisfy the Gibbs-Duhem relation; that is, each constituent must have the same chemical potential in the two phases: µiv = µi L for i = 1 to n. The chemical potential is a function of pressure, temperature, and molar fractions of constituents. The influence of the impurities present is as follows: a) At temperature T, the pressure P above the liquid is different from the saturated vapour pressure Π1 of the pure substance since it is equal to the sum of the partial pressures pi of the various constituents (Dalton's Law): i.e. n P = ∑p i = ∑ x This can be used to determine the calibration errors of the apparatus. i= 1 b) At temperature T, the saturated vapour pressure Πi of a pure substance is higher than the partial pressure pi of this substance in the mixture: expression by pi = xi L Πi n i= 1 v i ⋅P (Raoult's Law) . For the solvent, for which xi L ~ 1, we can write: n L ⎛ L ⎞ p1 = x1 Π1 = ⎜1 x ⎟ ⎜ − ∑ i ⎟ Π ⎝ i= 2 ⎠ For a weak concentration of solute (xi L → 0) it is necessary to replace the above pi = xi L ki (Henry's Law) , where ki (≠ Πi) is a constant that depends on the temperature and the nature of the constituents present. As a result of the above, the quantity of every dissolved impurity is proportional to its own partial pressure. We can write 1
- Page 31 and 32: 11 Fig. 2.1: One form of apparatus
- Page 33 and 34: 13 Fig. 2.3: Flow cryostat, shown w
- Page 35 and 36: 15 Fig. 2.4: Stirred liquid bath fo
- Page 37 and 38: 17 contained within a cylindrical c
- Page 39 and 40: 19 Fig. 2.5: Schematic drawing of a
- Page 41 and 42: 21 device SRM 767 [Schooley et al.
- Page 43 and 44: 23 Table 3.1 : Current Best Estimat
- Page 45: 25 The widely-used, but not very re
- Page 48 and 49: 28 fraction of sample melted) can g
- Page 50 and 51: 30 Fig. 3.2a: Apparatus for the cal
- Page 52 and 53: 32 Fig. 3.3: Sealed cell for realiz
- Page 54 and 55: 34 Final readings of the thermomete
- Page 56 and 57: 36 temperatures differ (usually) sy
- Page 58 and 59: 38 Fig. 3.4: Cross sectional drawin
- Page 60 and 61: 40 Fig. 3.5: Miniature graphite bla
- Page 62 and 63: 42 4. Germanium Resistance Thermome
- Page 64 and 65: 44 Fig. 4.3: Example of the Π-type
- Page 66 and 67: 46 Fig. 4.4: Differences between dc
- Page 68 and 69: 48 - conversely, p-doped thermomete
- Page 70 and 71: 50 Fig. 4.6: Effect of a radio-freq
- Page 72 and 73: 52 that it will not be subject to m
- Page 74 and 75: ln R n = ∑ i= 0 54 ⎛ ln T - P
- Page 76 and 77: 56 Fig. 5.1: Resistance (Ω) and s
- Page 78 and 79: 58 thermometer wires) caused a more
- Page 80 and 81: 60 6. Vapour Pressure Thermometry*
- Page 84 and 85: n ∑ i= 2 64 L x [ Π − k ] P =
- Page 86 and 87: 66 Fig. 6.3: Diagram at constant pr
- Page 88 and 89: 68 Fig. 6.4: Schematic construction
- Page 90 and 91: 70 Fig. 6.6: Use of an evacuated ja
- Page 92 and 93: 72 Following this, the connecting t
- Page 94 and 95: 74 Fig. 6.9: (c) N2, CO, Ar, O2, CH
- Page 96 and 97: 76 the Weber-Schmidt equation [Webe
- Page 98 and 99: 78 Table 6.1: Temperature values (K
- Page 100 and 101: 80 into the bulb (hydrous ferric ox
- Page 102 and 103: 82 Fig. 6.12: Effect on the vapour
- Page 104 and 105: 84 the remaining liquid increases.
- Page 106 and 107: 86 Curie constant (C⊥ is about 0.
- Page 108 and 109: 8.1 General Remarks 88 8. Platinum
- Page 110 and 111: 90 For a group of 45 thermometers h
- Page 112 and 113: 92 More recently, Seifert [(1980),
- Page 114 and 115: 94 For thermometers with W(4.2 K) <
- Page 116 and 117: 96 after 500 h at 1700 °C in air,
- Page 118 and 119: 98 normally extends about 50 cm bac
- Page 120 and 121: 100 inhomogeneities result from the
- Page 122 and 123: 9.5 Approximations to the ITS-90 10
- Page 124 and 125: 104 10. Infrared Radiation Thermome
- Page 126 and 127: 106 almost negligible. The final ac
- Page 128 and 129: 108 11. Carbon Resistance Thermomet
- Page 130 and 131: 110 Fig. 11.1: Resistance-temperatu
62<br />
transitions, but it could be applied also to those based on solid-to-vapour transitions<br />
(sublimation) with suitable changes.<br />
6.1 Two-Phase Equilibrium<br />
The number of parameters that can be arbitrarily imposed on a system is given by<br />
Gibb's phase rule:<br />
v = c + 2 - Φ<br />
where c is <strong>the</strong> number of constituents of <strong>the</strong> system, Φ is <strong>the</strong> number of phases, and v is <strong>the</strong><br />
number of degrees of freedom (or variance). For a pure substance with two phases (c = 1,<br />
Φ = 2), v = 1. The data <strong>for</strong> <strong>the</strong> pressure <strong>the</strong>re<strong>for</strong>e fix <strong>the</strong> value of <strong>the</strong> <strong>temperature</strong> at <strong>the</strong><br />
intersection in Fig. 6.1 of a line T = constant with <strong>the</strong> curve tC; this is <strong>the</strong> measurement<br />
principle of <strong>the</strong> <strong>the</strong>rmometers described here. In fact, <strong>the</strong> points of this curve are a series of<br />
equilibrium states that are distinguished by <strong>the</strong> distribution between <strong>the</strong> two phases of <strong>the</strong><br />
total number of moles of <strong>the</strong> substance enclosed.<br />
The equilibrium is regulated by <strong>the</strong> Gibbs-Duhem relationship, which holds in <strong>the</strong><br />
simple case described here, by <strong>the</strong> simultaneous realization of three conditions:<br />
PL = Pv TL = Tv and µL(TL,PL) = µv(Tv,Pv) ,<br />
where <strong>the</strong> indices L and v refer to <strong>the</strong> liquid and vapour phases respectively; P and T are <strong>the</strong><br />
pressure and <strong>temperature</strong> at <strong>the</strong> separation surface; and µ, <strong>the</strong> chemical potential, is<br />
identical <strong>for</strong> a pure substance to <strong>the</strong> free molar enthalpy. Any variation of one of <strong>the</strong> three<br />
quantities causes displacement of <strong>the</strong> equilibrium.<br />
If <strong>the</strong> substance is not pure but contains soluble impurities, <strong>the</strong> variance of <strong>the</strong><br />
system, becomes equal to <strong>the</strong> number of constituents present. Suppose that: each<br />
constituent is present at <strong>the</strong> same time in both liquid and vapour phases; <strong>the</strong> vapour phase<br />
is a mixture of perfect vapours; <strong>the</strong> surface-tension is negligible; <strong>the</strong> liquid phase is an ideal<br />
solution, that is to say, <strong>the</strong> substances mix without change of volume or enthalpy. This last<br />
assumption is realistic so long as <strong>the</strong> molar fractions xi (i = 2 to n) of <strong>the</strong> (n - 1) impurities<br />
present (solutes) are very small with respect to that (x1 ~ 1) of <strong>the</strong> pure substance (solvent)<br />
filling <strong>the</strong> <strong>the</strong>rmometer. (Note that <strong>the</strong> respective concentrations denoted xi L and xi v (i = 1 to<br />
n) are generally not equal, as will be seen later.) Under <strong>the</strong>se conditions, <strong>the</strong> deviation