Calculating Enthelpy of Vaporization using Clapeyron Equation

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SUMMARY

This discussion focuses on calculating the enthalpy of vaporization (Δhvap) of heptane using the Clapeyron equation and the Antoine equation. The user initially calculated Δhvap as 198.348 ft3•psi/lb, which equates to 36.703 BTU/lb, but later corrected this to 136.6 BTU/lb after realizing that Tsat must be converted to Kelvin for accurate results. The Antoine coefficients used were A = 6.89385, B = 1264.37, and C = 216.636, with a saturation pressure (Psat) of 15.5597 psia (804.592 mmHg). The discussion highlights the importance of unit consistency in thermodynamic calculations.

PREREQUISITES
  • Understanding of the Antoine equation for vapor pressure calculations
  • Familiarity with the Clapeyron equation for phase change analysis
  • Knowledge of thermodynamic properties, specifically enthalpy of vaporization
  • Experience with unit conversions, particularly between Celsius and Kelvin
NEXT STEPS
  • Study the derivation and application of the Clapeyron equation in phase transitions
  • Learn about the Rackett equation for estimating liquid volumes
  • Explore the Peng-Robinson equation of state for real gas behavior
  • Investigate the implications of empirical parameters in the Antoine equation
USEFUL FOR

Chemical engineers, thermodynamics students, and professionals involved in process design and optimization will benefit from this discussion, particularly those focused on vapor-liquid equilibrium calculations.

cjc0117
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Hi everyone. I am having a problem that hopefully someone here can help me with. For the purposes of flash calculations, I’m trying to find the enthalpy of vaporization of a compound using the Antoine equation and Clapeyron equation. I am using heptane at 15.5597 psia as an example. For the Antoine equation in the form log10(Psat) = A-B/(Tsat+C), where Psat is in units of mmHg and Tsat is in units of °C, I have Antoine coefficients for heptane of A = 6.89385, B = 1264.37, and C = 216.636. At Psat = 15.5597 psia = 804.592 mmHg, this gives me a saturation temperature of Tsat = 100.386 °C. The Clapeyron equation for a vapor-liquid phase change is dPsat/dTsat=Δhvap/(TsatΔνvap). Rearranging yields Δhvap = (dPsat/dTsat)(Tsat•Δνvap). Using the Rackett equation and the Peng-Robinson equation of state, I have found within reasonable accuracy that Δνvap = 4.385 ft3/lb. Taking the derivative of the Antoine equation with respect to temperature yields dPsat/dTsat = BPsatln(10)/(C+Tsat)2. Thus, Δhvap = BPsatTsatΔνvapln(10)/(C+Tsat)2. Plugging everything in results in a value of Δhvap = 198.348 ft3•psi/lb, which is equivalent to 36.703 BTU/lb. The actual value of Δhvap for heptane at 15.5597 psia should be somewhere around 135 BTU/lb. I’ve looked over my method and calculations multiple times but I can’t find an error. Perhaps the Antoine equation cannot be differentiated because it uses empirical parameters? Thanks. Any help would be much appreciated.
 
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In the Clapyron equation, you did remember that Tsat is absolute temperature, correct?
 
Perfect, that's exactly what I did wrong. I left the Tsat in the denominator in °C because the Antoine coefficients are for temperatures in °C, but I converted the other Tsat to Kelvin and now I'm getting 136.6 BTU/lb. Thanks a lot. It didn't make sense to me at first that I should convert to Kelvin because then the temperature units wouldn't seem to cancel out (K/ °C). But then I remembered that "per degree celsius" is the same as "per degree Kelvin" because a degree Kelvin is equal to a degree Celsius. Thanks again.
 

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