Can anyone please explain the suitability to apply PV = nRT to fluegas since there is high water vapor content and the remaining gases are not air (High CO2 content) ?
I found in this webpage explaining that it can be applied
http://fluegasknowho...ity-calculator/
But I got this question. What if the temperature is reduced to a point where the flue gas is saturated with water vapor.
Are there any equations/ data tables to be applied for flue gases? e.g. coefficient of compressibility.
Please tell me any references with flue gas calculations applying PV = nRT.
Also is there a way to determine the moisture content of a flue gas by flue gas analyzer provided that only O2, CO2, CO, and excess air percentages in flue gas are measured and the fuel is C11 to C16.
Edited by cheminst, 17 June 2019 - 06:18 AM.