Compound Information
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Property Availability
For this compound, WTT contains critically evaluated recommendations for:
(Please note that if more than 50 points are used for
regression, only the 50 most-constraining points are reported)
- Triple point temperature
- Triple point temperature (Crystal 1, Liquid, and Gas)
4 experimental data points - Triple point temperature (Crystal 2, Crystal 1, and Gas)
1 experimental data points - Triple point temperature (Crystal 3, Crystal 2, and Gas)
1 experimental data points - Triple point temperature (Crystal 4, Crystal 3, and Gas)
1 experimental data points - Triple point temperature (Crystal 5, Crystal 4, 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)
4 experimental data points - Critical pressure (Liquid and Gas)
4 experimental data points - Boiling temperature (Liquid in equilibrium with Gas) as a function of Pressure
Pressure from 19.4611 kPa to 2777.5 kPa - Phase boundary pressure
- Phase boundary pressure (Liquid in equilibrium with Gas) as a function of Temperature
Temperature from 233.35 K to 388.37 K
50 experimental data points - Phase boundary pressure (Crystal 1 in equilibrium with Gas) as a function of Temperature
Temperature from 217.03 K to 232.986 K
10 experimental data points - Phase boundary pressure (Crystal 3 in equilibrium with Gas) as a function of Temperature
Temperature from 174.64 K to 214.88 K
9 experimental data points
- Phase boundary pressure (Liquid in equilibrium with Gas) as a function of Temperature
- Critical density (Liquid and Gas)
2 experimental data points - Density
- Density (Liquid in equilibrium with Gas) as a function of Temperature
Temperature from 233.35 K to 388.37 K
23 experimental data points - Density (Gas in equilibrium with Liquid) as a function of Temperature
Temperature from 233.35 K to 388.38 K
3 experimental data points - Density (Liquid) as a function of Temperature and Pressure
Temperature from 233.35 K to 388.37 K
Pressure from 0.06 kPa to 60000 kPa
50 experimental data points - Density (Gas) as a function of Temperature and Pressure
Temperature from 233.35 K to 623 K
Pressure from 0.06 kPa to 2777.5 kPa
35 experimental data points
- Density (Liquid in equilibrium with Gas) as a function of Temperature
- Isobaric coefficient of expansion
- Isobaric coefficient of expansion (Liquid) as a function of Temperature and Pressure
Temperature from 233.35 K to 388.37 K
Pressure from 0.06 kPa to 60000 kPa - Isobaric coefficient of expansion (Gas) as a function of Temperature and Pressure
Temperature from 233.35 K to 623 K
Pressure from 0.06 kPa to 2777.5 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 233.35 K to 388.37 K
Pressure from 0.06 kPa to 60000 kPa - Isothermal compressibility (Gas) as a function of Temperature and Pressure
Temperature from 233.35 K to 623 K
Pressure from 0.06 kPa to 2777.5 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 233.35 K to 388.37 K
Pressure from 0.06 kPa to 60000 kPa - Thermal pressure coefficient (Gas) as a function of Temperature and Pressure
Temperature from 233.35 K to 623 K
Pressure from 0.06 kPa to 2777.5 kPa
- Thermal pressure coefficient (Liquid) as a function of Temperature and Pressure
- 2nd virial coefficient (Gas) as a function of Temperature
Temperature from 233.35 K to 623 K
15 experimental data points - 3rd virial coefficient (Gas) as a function of Temperature
Temperature from 233.35 K to 623 K
11 experimental data points - Enthalpy of phase transition (Crystal 1 to Liquid in equilibrium with Gas)
1 experimental data points - Enthalpy of vaporization or sublimation
- Enthalpy of vaporization or sublimation (Liquid to Gas) as a function of Temperature
Temperature from 233.35 K to 388.37 K
1 experimental data points - Enthalpy of vaporization or sublimation (Crystal 1 to Gas) as a function of Temperature
Temperature from 217.03 K to 232.986 K - Enthalpy of vaporization or sublimation (Crystal 3 to Gas) as a function of Temperature
Temperature from 174.64 K to 214.88 K
- Enthalpy of vaporization or sublimation (Liquid to Gas) as a function of Temperature
- Heat capacity at saturation pressure
- Heat capacity at saturation pressure (Liquid in equilibrium with Gas) as a function of Temperature
Temperature from 233.35 K to 388.2 K
9 experimental data points - Heat capacity at saturation pressure (Crystal 3 in equilibrium with Gas) as a function of Temperature
Temperature from 174.64 K to 214.88 K
18 experimental data points - Heat capacity at saturation pressure (Crystal 4 in equilibrium with Gas) as a function of Temperature
Temperature from 141.31 K to 174.64 K
18 experimental data points - Heat capacity at saturation pressure (Crystal 5 in equilibrium with Gas) as a function of Temperature
Temperature from 18 K to 141.31 K
50 experimental data points - Heat capacity at saturation pressure (Crystal 1 in equilibrium with Gas) as a function of Temperature
Temperature from 217.03 K to 232.986 K
9 experimental data points
- Heat capacity at saturation pressure (Liquid in equilibrium with Gas) as a function of Temperature
- Heat capacity at constant pressure
- Heat capacity at constant pressure (Liquid) as a function of Temperature and Pressure
Temperature from 233.35 K to 388.37 K
Pressure from 0.06 kPa to 60000 kPa
50 experimental data points - Heat capacity at constant pressure (Ideal Gas) as a function of Temperature
Temperature from 298 K to 1000 K - Heat capacity at constant pressure (Gas) as a function of Temperature and Pressure
Temperature from 233.35 K to 623 K
Pressure from 0.06 kPa to 2777.5 kPa
45 experimental data points
- Heat capacity at constant pressure (Liquid) as a function of Temperature and Pressure
- Enthalpy
- Enthalpy (Crystal 5 in equilibrium with Gas) as a function of Temperature
Temperature from 18 K to 141.31 K - Enthalpy (Liquid in equilibrium with Gas) as a function of Temperature
Temperature from 232.986 K to 380 K - Enthalpy (Ideal Gas) as a function of Temperature
Temperature from 298 K to 1000 K
- Enthalpy (Crystal 5 in equilibrium with Gas) as a function of Temperature
- Entropy
- Entropy (Liquid in equilibrium with Gas) as a function of Temperature
Temperature from 233.35 K to 388.37 K
1 experimental data points - Entropy (Crystal 5 in equilibrium with Gas) as a function of Temperature
Temperature from 18 K to 141.31 K - Entropy (Ideal Gas) as a function of Temperature and Pressure
Temperature from 298 K to 1000 K
- Entropy (Liquid in equilibrium with Gas) as a function of Temperature
- Adiabatic compressibility
- Adiabatic compressibility (Liquid) as a function of Temperature and Pressure
Temperature from 233.35 K to 388.37 K
Pressure from 0.06 kPa to 60000 kPa - Adiabatic compressibility (Gas) as a function of Temperature and Pressure
Temperature from 233.35 K to 623 K
Pressure from 0.06 kPa to 2777.5 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 233.35 K to 388.37 K
Pressure from 0.06 kPa to 60000 kPa - Joule-Thomson coefficient (Gas) as a function of Temperature and Pressure
Temperature from 233.35 K to 623 K
Pressure from 0.06 kPa to 2777.5 kPa - Speed of sound
- Speed of sound (Gas) as a function of Temperature and Pressure
Temperature from 233.35 K to 623 K
Pressure from 0.06 kPa to 2777.5 kPa
50 experimental data points - Speed of sound (Liquid) as a function of Temperature and Pressure
Temperature from 233.35 K to 388.37 K
Pressure from 0.06 kPa to 60000 kPa - Speed of sound (Liquid in equilibrium with Gas) as a function of Temperature
Temperature from 233.35 K to 388.37 K - Speed of sound (Gas in equilibrium with Liquid) as a function of Temperature
Temperature from 233.35 K to 388.38 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 233.35 K to 388.37 K
21 experimental data points - Viscosity
- Viscosity (Liquid in equilibrium with Gas) as a function of Temperature
Temperature from 233.35 K to 388.2 K
22 experimental data points - Viscosity (Liquid) as a function of Temperature and Pressure
Temperature from 233.35 K to 388.37 K
Pressure from 0.06 kPa to 60000 kPa
40 experimental data points - Viscosity (Gas) as a function of Temperature and Pressure
Temperature from 233.35 K to 623 K
Pressure from 0.06 kPa to 2777.5 kPa
14 experimental data points
- Viscosity (Liquid in equilibrium with Gas) as a function of Temperature
- Thermal conductivity
- Thermal conductivity (Gas) as a function of Temperature and Pressure
Temperature from 233.35 K to 623 K
Pressure from 0.06 kPa to 2777.5 kPa
45 experimental data points - Thermal conductivity (Liquid) as a function of Temperature and Pressure
Temperature from 233.35 K to 388.37 K
Pressure from 0.06 kPa to 60000 kPa
163 experimental data points - Thermal conductivity (Liquid in equilibrium with Gas) as a function of Temperature
Temperature from 233.35 K to 388.2 K
8 experimental data points
- Thermal conductivity (Gas) as a function of Temperature and Pressure
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.
Distributed by:
Standard Reference Data Program
National Institute of Standards and Technology
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