Dozens of these formulas have been developed. One that I use from time to time was published by V Ganapathy, Hydrocarbon Processing, Nov 1988, pgs 105-108. Ganapathy references his source as V Gonzales-Pozo, Chem Eng, May 12, 1986, pg 123.
It has the form
T = Ax + B/x + C(x^0.5) + D(ln(x)) + E(x^2) + F(x^3) + G
where
T is temperature in Fahrenheit
x is pressure in psia
A = -0.17724
B = 3.83986
C = 11.48345
D = 31.1311
E = 8.762969E-5
F = -2.78794E-8
G = 86.594
For quick estimates in the field you can use
T (deg C) = 100 * (bar(abs)^0.25)
This is easy to do with a hand held calculator because you enter the pressure in bar(abs), hit the square root button twice, and mutiply by 100. The answer is within 1 or 2 degrees for "normal" plant pressures. For example, this short cut gives the temperature for 15 bar(abs) steam as 196.8 C, but a more accurate formula will give 198.3 C
regards
Harvey
Katmar Software
Engineering & Risk Analysis Software