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preface to fifteenth edition

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5.30 SECTION 5<br />

5.2.1 Vapor-Pressure Equations<br />

Numerous mathematical formulas relating the temperature and pressure of the gas phase in equilibrium<br />

with the condensed phase have been proposed. The An<strong>to</strong>ine equation (Eq. 1) gives good<br />

correlation with experimental values. Equation 2 is simpler and is often suitable over restricted<br />

temperature ranges. In these equations, and the derived differential coefficients for use in the Haggenmacher<br />

and Clausius-Clapeyron equations, the p term is the vapor pressure of the compound in<br />

pounds per square inch (psi), the t term is the temperature in degrees Celsius, and the T term is the<br />

absolute temperature in kelvins ( tC 273.15).<br />

Eq. Vapor-pressure equation dp/dT [d(ln p)/d(1/T)]<br />

1<br />

B<br />

log p A t C<br />

2.303pB<br />

(t C) 2<br />

2.303BT 2<br />

(t C) 2<br />

2<br />

3<br />

B<br />

log p A T<br />

B<br />

log p A C log T<br />

T<br />

2.303pB<br />

T 2<br />

p<br />

<br />

2.303B C<br />

<br />

T2<br />

T<br />

<br />

2.303B<br />

2.303B CT<br />

Equations 1 and 2 are easily rearranged <strong>to</strong> calculate the temperature of the normal boiling<br />

point:<br />

B<br />

t C (5.1)<br />

A log p<br />

B<br />

T (5.2)<br />

A log p<br />

The constants in the An<strong>to</strong>ine equation may be estimated by selecting three widely spaced data<br />

points and substituting in the following equations in sequence:<br />

y3 y2 t2 t1 t3 t1<br />

1 <br />

y y t t t C<br />

In these equations, yi<br />

log p i.<br />

2 1 3 2 3<br />

1<br />

3 1<br />

B<br />

<br />

y3 y1<br />

B (t C)(t3<br />

C)<br />

t t<br />

A y 2 <br />

t C<br />

2

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