techniques for approximating the international temperature ... - BIPM
techniques for approximating the international temperature ... - BIPM
techniques for approximating the international temperature ... - BIPM
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60<br />
6. Vapour Pressure Thermometry*<br />
Vapour pressure <strong>the</strong>rmometers are based on <strong>the</strong> saturated vapour pressure in a two-<br />
phase system in an enclosure. A boiling point is an example of a point on a vapour pressure<br />
curve; i.e. <strong>the</strong> <strong>techniques</strong> of vapour pressure <strong>the</strong>rmometry described herein apply also to <strong>the</strong><br />
special case of a boiling or a triple point determination. The behavior of a liquid-vapour<br />
system in equilibrium, <strong>for</strong> example, is describable by an equation P = f(T) (curve tC of<br />
Fig. 6.1). Along <strong>the</strong> curve <strong>for</strong> a pure substance, <strong>the</strong> pressure depends on <strong>the</strong> <strong>temperature</strong><br />
and not on <strong>the</strong> quantity of substance enclosed or vaporized. The <strong>temperature</strong> range<br />
associated with vaporization is limited to <strong>temperature</strong>s between <strong>the</strong> critical point and <strong>the</strong><br />
triple point of <strong>the</strong> substance. The range is even fur<strong>the</strong>r reduced if <strong>the</strong> extreme pressures to<br />
be measured are outside <strong>the</strong> usable range of <strong>the</strong> pressure sensor.<br />
For a given substance, <strong>the</strong> sensitivity of <strong>the</strong> <strong>the</strong>rmometer increases approximately<br />
inversely with <strong>the</strong> <strong>temperature</strong> since uv varies roughly as 1/P (curve tC in Fig. 6.1).<br />
According to <strong>the</strong> Clausius-Clapeyron equation, we have<br />
dP<br />
dT<br />
=<br />
T(<br />
u<br />
where L is <strong>the</strong> molar heat of vaporization which is <strong>temperature</strong> dependent, and uv and uL are<br />
<strong>the</strong> molar volumes of <strong>the</strong> saturated vapour and liquid respectively. Experimental tables<br />
giving P = f(T) have existed <strong>for</strong> a long time <strong>for</strong> commonly-used fluids and interpolation<br />
<strong>for</strong>mulae have been <strong>international</strong>ly agreed upon <strong>for</strong> many of <strong>the</strong>m [Bed<strong>for</strong>d et al. (1984)]. It is<br />
<strong>the</strong>re<strong>for</strong>e easy to obtain <strong>temperature</strong> from measurement of pressure.<br />
L<br />
v −<br />
The sublimation curve can be similarly used, but <strong>the</strong> range of measurable<br />
<strong>temperature</strong>s is <strong>the</strong>n much smaller, limited on <strong>the</strong> high side by <strong>the</strong> triple point <strong>temperature</strong><br />
and on <strong>the</strong> low side by <strong>the</strong> pressure becoming too low to be measured accurately enough.<br />
Here, <strong>the</strong> discussion emphasizes <strong>the</strong>rmometers based on liquid-to-vapour<br />
_________________________________________________________________________<br />
* This chapter is written in more detail and contains ra<strong>the</strong>r more of <strong>the</strong> fundamentals of <strong>the</strong><br />
<strong>the</strong>ory than o<strong>the</strong>r chapters because no self-contained account of vapour pressure<br />
<strong>the</strong>rmometry appears elsewhere, vapour pressure <strong>the</strong>rmometry is one of <strong>the</strong> best means<br />
of <strong>approximating</strong> <strong>the</strong> ITS-90, and <strong>the</strong> <strong>techniques</strong> are moderately commonly used<br />
industrially.<br />
u<br />
L<br />
)