Compound Information
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For this compound, WTT contains critically evaluated recommendations for:
- Triple point temperature
- Triple point temperature (Crystal 1, Liquid, and Gas)
2 experimental data points - Triple point temperature (Crystal 2, Crystal 1, and Gas)
1 experimental data points
- Triple point temperature (Crystal 1, Liquid, and Gas)
- Normal boiling temperature (Liquid and Gas)
- Critical temperature (Liquid and Gas)
2 experimental data points - Critical pressure (Liquid and Gas)
1 experimental data points - Boiling temperature (Liquid in equilibrium with Gas) as a function of Pressure
Pressure from 0.0275117 kPa to 1161.46 kPa - Phase boundary pressure (Liquid in equilibrium with Gas) as a function of Temperature
Temperature from 300 K to 619.23 K
39 experimental data points - Critical density (Liquid and Gas)
- Density
- Density (Liquid) as a function of Temperature and Pressure
Temperature from 300 K to 619.23 K
Pressure from 0.03 kPa to 30000 kPa
42 experimental data points - Density (Liquid in equilibrium with Gas) as a function of Temperature
Temperature from 300 K to 619.23 K
42 experimental data points - Density (Gas) as a function of Temperature and Pressure
Temperature from 300 K to 673 K
Pressure from 0.03 kPa to 1160 kPa - Density (Gas in equilibrium with Liquid) as a function of Temperature
Temperature from 300 K to 619.234 K
- Density (Liquid) as a function of Temperature and Pressure
- Isobaric coefficient of expansion
- Isobaric coefficient of expansion (Liquid) as a function of Temperature and Pressure
Temperature from 300 K to 619.23 K
Pressure from 0.03 kPa to 30000 kPa - Isobaric coefficient of expansion (Gas) as a function of Temperature and Pressure
Temperature from 300 K to 673 K
Pressure from 0.03 kPa to 1160 kPa
- Isobaric coefficient of expansion (Liquid) as a function of Temperature and Pressure
- Isothermal compressibility
- Isothermal compressibility (Liquid) as a function of Temperature and Pressure
Temperature from 300 K to 619.23 K
Pressure from 0.03 kPa to 30000 kPa - Isothermal compressibility (Gas) as a function of Temperature and Pressure
Temperature from 300 K to 673 K
Pressure from 0.03 kPa to 1160 kPa
- Isothermal compressibility (Liquid) as a function of Temperature and Pressure
- Thermal pressure coefficient
- Thermal pressure coefficient (Liquid) as a function of Temperature and Pressure
Temperature from 300 K to 619.23 K
Pressure from 0.03 kPa to 30000 kPa - Thermal pressure coefficient (Gas) as a function of Temperature and Pressure
Temperature from 300 K to 673 K
Pressure from 0.03 kPa to 1160 kPa
- Thermal pressure coefficient (Liquid) as a function of Temperature and Pressure
- 2nd virial coefficient (Gas) as a function of Temperature
Temperature from 300 K to 673 K - 3rd virial coefficient (Gas) as a function of Temperature
Temperature from 300 K to 673 K - Enthalpy of phase transition (Crystal 1 to Liquid in equilibrium with Gas)
1 experimental data points - Enthalpy of vaporization or sublimation (Liquid to Gas) as a function of Temperature
Temperature from 300 K to 619.23 K - Heat capacity at saturation pressure (Liquid in equilibrium with Gas) as a function of Temperature
Temperature from 300 K to 619.1 K
35 experimental data points - Heat capacity at constant pressure
- Heat capacity at constant pressure (Liquid) as a function of Temperature and Pressure
Temperature from 300 K to 619.23 K
Pressure from 0.03 kPa to 30000 kPa
35 experimental data points - Heat capacity at constant pressure (Gas) as a function of Temperature and Pressure
Temperature from 300 K to 673 K
Pressure from 0.03 kPa to 1160 kPa
- Heat capacity at constant pressure (Liquid) as a function of Temperature and Pressure
- Enthalpy (Liquid in equilibrium with Gas) as a function of Temperature
Temperature from 288.78 K to 473.15 K - Adiabatic compressibility
- Adiabatic compressibility (Liquid) as a function of Temperature and Pressure
Temperature from 300 K to 619.23 K
Pressure from 0.03 kPa to 30000 kPa - Adiabatic compressibility (Gas) as a function of Temperature and Pressure
Temperature from 300 K to 673 K
Pressure from 0.03 kPa to 1160 kPa
- Adiabatic compressibility (Liquid) as a function of Temperature and Pressure
- Pressure coefficient of enthalpy (Liquid) as a function of Temperature and Pressure
Temperature from 300 K to 619.23 K
Pressure from 0.03 kPa to 30000 kPa - Joule-Thomson coefficient (Gas) as a function of Temperature and Pressure
Temperature from 300 K to 673 K
Pressure from 0.03 kPa to 1160 kPa - Speed of sound
- Speed of sound (Gas) as a function of Temperature and Pressure
Temperature from 300 K to 673 K
Pressure from 0.03 kPa to 1160 kPa
40 experimental data points - Speed of sound (Liquid) as a function of Temperature and Pressure
Temperature from 300 K to 619.23 K
Pressure from 0.03 kPa to 30000 kPa - Speed of sound (Liquid in equilibrium with Gas) as a function of Temperature
Temperature from 300 K to 619.23 K - Speed of sound (Gas in equilibrium with Liquid) as a function of Temperature
Temperature from 300 K to 619.234 K
- Speed of sound (Gas) as a function of Temperature and Pressure
- Surface tension (Liquid in equilibrium with Gas) as a function of Temperature
Temperature from 293.15 K to 433.15 K
12 experimental data points - Viscosity
- Viscosity (Gas) as a function of Temperature and Pressure
Temperature from 490 K to 920 K
1 experimental data points - Viscosity (Liquid in equilibrium with Gas) as a function of Temperature
Temperature from 284.998 K to 473.15 K
21 experimental data points
- Viscosity (Gas) as a function of Temperature and Pressure
- Thermal conductivity (Liquid in equilibrium with Gas) as a function of Temperature
Temperature from 298.15 K to 343.15 K
2 experimental data points
About WTT
NIST/TRC Web Thermo Tables (WTT)
NIST Standard Reference Subscription Database 3 - Professional Edition
Version 2-2012-1-Pro
This web application provides access to a collection of critically evaluated thermodynamic property data for pure compounds with a primary focus on organics. These data were generated through dynamic data analysis, as implemented in the NIST ThermoData Engine software package [1, 2, 3, 4, 5, 6]. Some critically evaluated data from the historical TRC Thermodynamic Tables archive [7, 8] are included, also. As of May 2012, the Professional Edition contains information on 28432 compounds and total of 531486 evaluated data points. The properties covered by both versions (32 total) are described in Properties and Implemented Models.
Developed by Kenneth Kroenlein, Chris D. Muzny, Andrei F. Kazakov, Vladimir Diky, Robert D. Chirico, Joseph W. Magee, Ilmutdin Abdulagatov and Michael Frenkel.
Thermodynamics Research Center (TRC)
Thermophysical Properties Division
National Institute of Standards and Technology
Boulder CO 80305-3337
Questions and comments should be addressed to Dr. Michael Frenkel .
DISCLAIMER: The National Institute of Standards and Technology (NIST) uses its best efforts to deliver a high-quality copy of the database and to verify that the methods and data contained therein have been selected on the basis of sound scientific judgement. However, NIST makes no warranties to that effect, and NIST shall not be liable for any damage that may result from errors or omissions in the program and database.
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National Institute of Standards and Technology
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