There is an equation for estimating the boiling point of pure component at different pressure.
ln(P1/P2)=-Hevap/R X (1/T1-1/T2)
Since the enthalpy of vaporation is changing with pressure/temperature (boiling point), is the equation reliable?
|
|
Posted 07 May 2018 - 09:26 AM
There is an equation for estimating the boiling point of pure component at different pressure.
ln(P1/P2)=-Hevap/R X (1/T1-1/T2)
Since the enthalpy of vaporation is changing with pressure/temperature (boiling point), is the equation reliable?
Posted 07 May 2018 - 10:30 AM
I think a lot depends on what you mean by "reliable"?
A quick check based on water (using NIST's REFPROP for the reference calculations), it appears that your simplified equation (appears to be based on the Clausius-Clapeyron equation) is off by about 1 C at 0.25 atm and about 0.25 C at 3 atm. Is that "reliable"? For organics (tested on methanol, toluene, octane), the errors are larger (2-3 C at 0.25 atm and 1.5 to 2.5 C at 3 atm). I suggest that you perform similar calculations for test compounds that make sense to you, then determine exactly what "reliable" means in terms of those errors.
Heat Of Dilution Of Hydrogen Chloride In Hydrochloric Acid Solution (3Started by Guest_fredlan54_* , 21 Nov 2025 |
|
|
||
Shell And Tube Heat Exchanger In HtriStarted by Guest_Sanjayr126_* , 28 Sep 2021 |
|
|
||
Heat Loss Calculation From Cylindrical Tan;Started by Guest_rasprocess2026_* , 23 Jul 2025 |
|
|
||
Steam Pressure In Heat ExchangerStarted by Guest_mvanrijnbach_* , 15 Apr 2025 |
|
|
||
Heat Exchanger Steam FlowStarted by Guest_aliebrahem17_* , 25 Nov 2024 |
|
|