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AN607 Datasheet(PDF) 27 Page - Silicon Laboratories |
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AN607 Datasheet(HTML) 27 Page - Silicon Laboratories |
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27 / 41 page ![]() AN607 Rev. 1.7 27 Humidity-Related Calculations While the above expressions are physically based, they are difficult to solve and manipulate. Hence, many approximate formulas have been developed. The two most common are the Antoine Equation and the Magnus equation. Many of these formulas contain coefficients that can vary depending on their source, its age and, in some cases, the context of the equations use. Antoine Equation This equation calculates saturation vapor pressure. Additionally; coefficients are available for this equation for a wide variety of vapors other than water. The coefficients used in the following equation are for an air-water system and are optimized for use over the temperature range 0 to 100 °C. Magnus Equation This equation calculates saturation vapor pressure as does the Antoine Equation. It has the advantage that it can be easily manipulated to find the dew point (tdp) or frost point. Where: P’s is pressure in Pascals Nm –2 T is temperature in °C Over the range of –40 to +50 °C, the best fit constants are as follows: For air with a vapor pressure P’, the dew point is defined as the temperature at which the water vapor would be saturated. Thus, Utilizing the relationship RH = 100 x P’/P’s A1 B1 C1 Reference 17.625 243.04 610.94 Alduchov, Oleg A., Robert E. Eskridge, 1996: Improved Magnus Form Approximation of Saturation Vapor Pressure. J. Appl. Meteor., 35, 601–609 p s 23.19 3830 T 44.83 – ------------------------ – exp = t dp 3830 23.19 Ps ln – -------------------------------------- 44.83 + = Where: Pressure in Pascals Nm 2 – Temperature in °K (°C + 273.15) P sC 1 e A1T B 1 T + ----------------- = T d B 1 In P C 1 ------- A1 P C 1 ------- ln – -------------------------------- = |
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