2,6-di-tert-butyl-4-methylphenol Thermodynamic Properties vs Temperature (CAS 128-37-0)

Analyze how thermophysical properties change over a temperature range at a constant pressure of 1 atm.

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Property Profile for 2,6-di-tert-butyl-4-methylphenol

Calculated properties vs. Temperature

Profile Data

Equilibrium Thermodynamic and Transport Properties of 2,6-di-tert-butyl-4-methylphenol at 1.01325 bar over -23.15–226.85 °C
Temperature (°C)Specific heat capacity (kJ/kg·K)Density (kg/m³)Dynamic viscosity (cP)Thermal conductivity (W/m·K)Prandtl number ()Molar volume (m³/kmol)Specific enthalpy (kJ)Specific entropy (kJ/kg·K)Phase
-23.151.285331045.84N/A N/A N/A 0.210691-66.8781-0.244108s
-18.0481.307261043.71N/A N/A N/A 0.211122-60.2643-0.21792s
-12.94591.329211041.58N/A N/A N/A 0.211554-53.5386-0.191817s
-7.843881.351161039.45N/A N/A N/A 0.211988-46.701-0.165794s
-2.741841.373121037.32N/A N/A N/A 0.212423-39.7513-0.139848s
2.36021.395091035.19N/A N/A N/A 0.212861-32.6895-0.113977s
7.462241.417081033.05N/A N/A N/A 0.2133-25.5157-0.088177s
12.56431.439071030.92N/A N/A N/A 0.213741-18.2296-0.0624459s
17.66631.461081028.79N/A N/A N/A 0.214184-10.8312-0.0367807s
22.76841.483111026.66N/A N/A N/A 0.214629-3.32051-0.0111789s
27.87041.505151024.53N/A N/A N/A 0.2150754.30260.0143619s
32.97241.527211022.4N/A N/A N/A 0.21552412.03820.039844s
38.07451.549281020.26N/A N/A N/A 0.21597419.88640.0652696s
43.17651.571381018.13N/A N/A N/A 0.21642627.84730.0906409s
48.27861.593481016N/A N/A N/A 0.2168835.92090.11596s
53.38061.615611013.87N/A N/A N/A 0.21733644.10730.141228s
58.48271.637761011.74N/A N/A N/A 0.21779452.40680.166448s
63.58471.659921009.61N/A N/A N/A 0.21825460.81920.191621s
68.68671.682111007.47N/A N/A N/A 0.21871669.34480.216749s
73.78882.0955897.1490.5965090.11949910.46020.245612164.5040.493226l
78.89082.11447894.20.5848980.118510.43670.246422175.2440.523956l
83.99292.13323891.2070.5734020.117510.41010.247249186.080.554515l
89.09492.15177888.170.5620190.11650110.38050.248095197.0120.584906l
94.19692.1701885.0870.5507510.11550210.34780.248959208.0370.615129l
99.2992.18822881.9580.5395960.11450210.31210.249842219.1550.645187l
104.4012.20614878.7830.5285550.11350310.27340.250745230.3650.675081l
109.5032.22384875.560.5176290.11250310.23190.251668241.6660.704813l
114.6052.24132872.290.5068160.11150410.18740.252612253.0570.734384l
119.7072.2586868.970.4961170.11050410.14010.253576264.5370.763796l
124.8092.27567865.6020.4855320.10950510.09010.254563276.1040.793049l
129.9112.29253862.1830.4750610.10850510.03720.255573287.7570.822147l
135.0132.30917858.7140.4647030.1075069.981590.256605299.4960.851088l
140.1152.32561855.1930.4544590.1065069.923290.257662311.320.879876l
145.2172.34183851.6190.4443290.1055079.862330.258743323.2270.908511l
150.3192.35785847.9920.4343120.1045079.798750.25985335.2160.936995l
155.4212.37365844.3120.4244090.1035089.732580.260982347.2860.965327l
160.5232.38924840.5750.4146190.1025089.663860.262142359.4360.99351l
165.6262.40462836.7830.4049420.1015089.592610.26333371.6661.02154l
170.7282.41979832.9340.3953780.1005099.518880.264547383.9731.04943l
175.832.43475829.0270.3859270.09950919.44270.265794396.3571.07717l
180.9322.4495825.0610.3765890.09850959.36410.267072408.8171.10477l
186.0342.46403821.0340.3673630.09750979.283110.268382421.3521.13222l
191.1362.47836816.9460.3582490.096519.199770.269724433.961.15952l
196.2382.49247812.7960.3492470.09551039.11410.271102446.6411.18669l
201.342.50638808.5810.3403570.09451059.026130.272515459.3931.21371l
206.4422.52007804.3020.3315790.09351078.935890.273965472.2161.24059l
211.5442.53355799.9550.3229110.09251098.843410.275454485.1071.26733l
216.6462.54682795.540.3143540.09151118.748720.276982498.0681.29393l
221.7482.55988791.0560.3059070.09051138.651820.278552511.0951.32039l
226.852.57273786.50.297570.08951148.552750.280166524.1891.34671l

Property Profiles for 2,6-di-tert-butyl-4-methylphenol

Heat Capacity (Cp) vs Temperature

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Density vs Temperature

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Thermodynamic Property Profile at Constant Pressure

This page presents the temperature-dependent thermodynamic and transport properties of 2,6-di-tert-butyl-4-methylphenol (CAS 128-37-0) calculated at a constant pressure of 1 atm (101325 Pa) over the temperature range 250-500 K.

The properties shown - specific heat capacity (Cp), density (ρ), dynamic viscosity (μ), thermal conductivity (k), Prandtl number (Pr), molar volume (Vm), specific enthalpy (H), and specific entropy (S) - are among the most commonly used parameters in chemical engineering calculations, process simulation, and thermal system design.

All values are generated programmatically using validated thermodynamic correlations and equations of state and represent equilibrium properties at the specified pressure.


Understanding the Property Trends

  • Specific heat capacity (Cp) indicates the amount of energy required to raise the temperature of 2,6-di-tert-butyl-4-methylphenol and is critical for energy balance and heat-exchanger design.
  • Density (ρ) and molar volume (Vm) describe volumetric behavior and are required for flow calculations, equipment sizing, and storage design.
  • Dynamic viscosity (μ) governs fluid flow resistance, influencing Reynolds number and pressure drop.
  • Thermal conductivity (k) and Prandtl number (Pr) are essential inputs for convective heat-transfer correlations.
  • Specific enthalpy (H) and specific entropy (S) are fundamental thermodynamic properties used in process modeling, compression, and expansion analysis.

Property trends with temperature may vary depending on molecular structure, intermolecular interactions, and phase stability.


Engineering Applications

The temperature-dependent properties of 2,6-di-tert-butyl-4-methylphenol at atmospheric pressure are commonly required in:

  • Heat exchanger and reactor design
  • Process simulation and thermodynamic modeling
  • Fluid flow and pressure-drop calculations
  • Energy balance and equipment sizing
  • Chemical engineering education and research

These profiles are particularly useful when evaluating system performance over a wide operating temperature range under near-ambient pressure conditions.


Frequently Asked Questions

At what pressure are these properties calculated?
All properties on this page are calculated at a constant pressure of 1 atm (101325 Pa).

Can these values be used in process simulation software?
Yes. The data is suitable for preliminary design, validation, and educational use. For licensed simulators, vendor-specific property packages should be referenced.

Can I change the pressure or temperature range?
Yes. Use the interactive controls above to generate custom property profiles at different pressures or temperature ranges.


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