Calculation of vapor pressure

Understanding Vapor Pressure Calculation: Fundamentals and Applications

Vapor pressure calculation determines the pressure exerted by a vapor in equilibrium with its liquid. This article explores key formulas, data, and real-world applications.

Learn how to accurately compute vapor pressure using empirical and theoretical models. Detailed tables, formulas, and examples guide expert-level understanding.

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  • Calculate vapor pressure of water at 80°C using Antoine equation.
  • Determine vapor pressure of ethanol at 25°C with Clausius-Clapeyron relation.
  • Estimate vapor pressure of benzene at 50°C from tabulated constants.
  • Find vapor pressure of acetone at 30°C using empirical correlations.

Comprehensive Tables of Vapor Pressure Values for Common Substances

Accurate vapor pressure data is essential for chemical engineering, environmental science, and process design. The following tables present vapor pressure values for widely used substances across typical temperature ranges.

SubstanceTemperature (°C)Vapor Pressure (kPa)Vapor Pressure (mmHg)Reference
Water00.6114.58CRC Handbook
Water253.1723.8CRC Handbook
Water5012.3592.6CRC Handbook
Water100101.3760Standard Atmospheric Pressure
Ethanol00.584.35NIST
Ethanol257.8759.0NIST
Ethanol5024.0180.0NIST
Ethanol78.4101.3760Boiling Point
Benzene00.131.0Yaws’ Handbook
Benzene2512.795.3Yaws’ Handbook
Benzene5047.0352.5Yaws’ Handbook
Benzene80101.3760Boiling Point
Acetone00.32.25NIST
Acetone2524.0180.0NIST
Acetone56101.3760Boiling Point

These values serve as benchmarks for validating vapor pressure calculations using various models. Note that vapor pressure increases exponentially with temperature, approaching atmospheric pressure at the boiling point.

Key Formulas for Vapor Pressure Calculation and Variable Definitions

Vapor pressure can be calculated using several empirical and theoretical equations. Each formula has specific variables and applicability ranges. Below are the most widely used equations with detailed explanations.

Antoine Equation

The Antoine equation is an empirical relationship widely used for vapor pressure estimation:

P = 10A – (B / (C + T))
  • P: Vapor pressure (usually in mmHg or kPa depending on constants)
  • T: Temperature (°C)
  • A, B, C: Substance-specific Antoine constants

The constants A, B, and C are determined experimentally and vary with the temperature range. For example, for water between 1°C and 100°C:

  • A = 8.07131
  • B = 1730.63
  • C = 233.426

These constants yield vapor pressure in mmHg.

Clausius-Clapeyron Equation

The Clausius-Clapeyron equation relates vapor pressure to temperature based on enthalpy of vaporization:

ln(P) = – (Ī”Hvap / R) * (1/T) + C
  • P: Vapor pressure (Pa or atm)
  • Ī”Hvap: Enthalpy of vaporization (J/mol)
  • R: Universal gas constant (8.314 J/molĀ·K)
  • T: Absolute temperature (Kelvin)
  • C: Integration constant determined from reference data

This equation assumes ΔHvap is constant over the temperature range, which is an approximation valid for small intervals.

Antoine Constants Table for Common Substances

SubstanceTemperature Range (°C)ABCUnits of PReference
Water1 – 1008.071311730.63233.426mmHgCRC Handbook
Ethanol0 – 78.38.204171642.89230.3mmHgNIST
Benzene10 – 806.905651211.033220.79mmHgYaws’ Handbook
Acetone10 – 567.024471161.0224.0mmHgNIST

Other Empirical Correlations

Additional models include the Wagner equation, Antoine extended forms, and the DIPPR correlation, which provide higher accuracy over wider temperature ranges but require more parameters.

Detailed Explanation of Variables and Typical Values

  • Temperature (T): Usually in °C for Antoine, Kelvin for Clausius-Clapeyron. Accurate temperature measurement is critical.
  • Vapor Pressure (P): Pressure exerted by vapor in equilibrium, units vary (kPa, mmHg, atm). Conversion factors: 1 atm = 101.325 kPa = 760 mmHg.
  • Enthalpy of Vaporization (Ī”Hvap): Energy required to vaporize one mole, typically 30-50 kJ/mol for common liquids.
  • Constants A, B, C: Empirically derived, substance and temperature range dependent.
  • Gas Constant (R): 8.314 J/molĀ·K, universal constant used in thermodynamic equations.

Real-World Applications: Case Studies in Vapor Pressure Calculation

Case 1: Vapor Pressure of Water at 80°C Using Antoine Equation

Objective: Calculate the vapor pressure of water at 80°C.

Given Antoine constants for water (1-100°C): A = 8.07131, B = 1730.63, C = 233.426.

Applying the Antoine equation:

P = 108.07131 – (1730.63 / (233.426 + 80))

Calculate denominator:

233.426 + 80 = 313.426

Calculate fraction:

1730.63 / 313.426 ā‰ˆ 5.523

Calculate exponent:

8.07131 – 5.523 = 2.54831

Calculate vapor pressure:

P = 102.54831 ā‰ˆ 354.3 mmHg

Convert to kPa:

354.3 mmHg Ɨ (101.325 kPa / 760 mmHg) ā‰ˆ 47.3 kPa

This matches well with tabulated data (~47.4 kPa), confirming the accuracy of the Antoine equation for this temperature.

Case 2: Estimating Vapor Pressure of Ethanol at 25°C Using Clausius-Clapeyron Equation

Objective: Calculate vapor pressure of ethanol at 25°C using Clausius-Clapeyron, given vapor pressure at 20°C.

Known data:

  • Vapor pressure at 20°C (P1) = 5.95 kPa
  • Temperature T1 = 293.15 K (20°C)
  • Temperature T2 = 298.15 K (25°C)
  • Enthalpy of vaporization Ī”Hvap = 38.56 kJ/mol = 38560 J/mol
  • Gas constant R = 8.314 J/molĀ·K

Clausius-Clapeyron rearranged for P2:

ln(P2/P1) = – (Ī”Hvap / R) * (1/T2 – 1/T1)

Calculate the right side:

1/T2 – 1/T1 = (1/298.15) – (1/293.15) ā‰ˆ 0.003355 – 0.003412 = -0.000057 K-1

Calculate exponent:

– (38560 / 8.314) Ɨ (-0.000057) ā‰ˆ -4638.5 Ɨ (-0.000057) ā‰ˆ 0.264

Calculate P2:

ln(P2/5.95) = 0.264 → P2/5.95 = e0.264 ā‰ˆ 1.302 → P2 ā‰ˆ 7.75 kPa

Tabulated vapor pressure of ethanol at 25°C is approximately 7.87 kPa, showing good agreement.

Additional Considerations and Advanced Topics

For precise engineering applications, vapor pressure calculations must consider:

  • Non-ideal behavior: Real gases and mixtures deviate from ideality; activity coefficients and fugacity corrections may be necessary.
  • Temperature range validity: Empirical constants are valid only within specified temperature ranges.
  • Mixture effects: Raoult’s law and Dalton’s law govern vapor pressures in mixtures, requiring component vapor pressures and mole fractions.
  • Pressure units consistency: Always ensure units of vapor pressure and constants match to avoid calculation errors.

Advanced models such as the Wagner equation or DIPPR correlations provide enhanced accuracy for industrial process simulations. These models incorporate additional parameters and temperature dependencies.

References and Further Reading

  • NIST Chemistry WebBook – Authoritative source for thermophysical properties.
  • CHERIC Database – Chemical engineering research information center.
  • Engineering Toolbox: Vapor Pressure of Water – Practical data and calculators.
  • Yaws, C.L., “Thermophysical Properties of Chemicals and Hydrocarbons,” Elsevier, 2015.
  • Poling, B.E., Prausnitz, J.M., O’Connell, J.P., “The Properties of Gases and Liquids,” 5th Edition, McGraw-Hill, 2000.