glycerol 1-monooleate Thermodynamic Properties vs Temperature (CAS 111-03-5)

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

Input Conditions

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Property Profile for glycerol 1-monooleate

Calculated properties vs. Temperature

Profile Data

Equilibrium Thermodynamic and Transport Properties of glycerol 1-monooleate 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
-23.151.28972980.964N/A N/A N/A 0.363459-67.0964-0.244906s
-18.0481.31169978.705N/A N/A N/A 0.364298-60.4601-0.218629s
-12.94591.33366976.445N/A N/A N/A 0.365141-53.7118-0.192437s
-7.843881.35564974.186N/A N/A N/A 0.365988-46.8513-0.166328s
-2.741841.37763971.926N/A N/A N/A 0.366838-39.8786-0.140296s
2.36021.39964969.667N/A N/A N/A 0.367693-32.7938-0.11434s
7.462241.42165967.408N/A N/A N/A 0.368552-25.5966-0.0884569s
12.56431.44367965.148N/A N/A N/A 0.369415-18.2871-0.0626431s
17.66631.46571962.889N/A N/A N/A 0.370281-10.8653-0.0368963s
22.76841.48776960.63N/A N/A N/A 0.371152-3.3309-0.0112139s
27.87041.50983958.37N/A N/A N/A 0.3720274.3160.0144066s
32.97241.53191956.111N/A N/A N/A 0.37290612.07550.0399674s
38.07451.96175852.0060.8733870.2005438.543670.418471187.720.6099l
43.17651.98219850.4890.8606440.1995458.549270.419218197.7810.641966l
48.27862.00242848.9480.8479920.1985478.552330.419978207.9460.673843l
53.38062.02245847.3830.8354340.1975498.552910.420754218.2140.705535l
58.48272.04226845.7950.8229680.1965518.551020.421544228.5830.737045l
63.58472.06186844.1810.8105940.1955538.546690.42235239.0530.768375l
68.68672.08126842.5430.7983140.1945558.539970.423171249.6220.799527l
73.78882.10045840.880.7861260.1935578.530870.424008260.290.830503l
78.89082.11942839.1920.774030.1925598.519430.424861271.0550.861305l
83.99292.13819837.4780.7620280.1915628.505690.425731281.9160.891936l
89.09492.15675835.7380.7501180.1905648.489660.426617292.8730.922397l
94.19692.17511833.9710.7383010.1895658.471390.427521303.9230.95269l
99.2992.19325832.1780.7265770.1885678.45090.428442315.0670.982817l
104.4012.21118830.3570.7149460.1875698.428220.429381326.3031.01278l
109.5032.22891828.510.7034080.1865718.403390.430339337.631.04258l
114.6052.24643826.6340.6919620.1855738.376440.431315349.0471.07222l
119.7072.26373824.730.680610.1845758.34740.432311360.5521.1017l
124.8092.28083822.7980.6693510.1835778.316290.433326372.1461.13102l
129.9112.29773820.8370.6581850.1825798.283160.434361383.8261.16018l
135.0132.31441818.8470.6471120.1815818.248020.435417395.5921.18919l
140.1152.33088816.8260.6361320.1805828.210930.436494407.4421.21804l
145.2172.34715814.7760.6252450.1795848.171890.437592419.3761.24674l
150.3192.3632812.6950.6144520.1785868.130960.438713431.3921.27529l
155.4212.37905810.5830.6037510.1775888.088150.439856443.491.30369l
160.5232.39469808.440.5931440.1765898.04350.441022455.6681.33193l
165.6262.41012806.2650.582630.1755917.997040.442212467.9251.36003l
170.7282.42534804.0580.5722090.1745937.94880.443426480.261.38798l
175.832.44035801.8180.5618810.1735947.898820.444665492.6731.41579l
180.9322.45516799.5440.5516470.1725967.847120.445929505.1621.44345l
186.0342.46975797.2370.5415060.1715977.793740.447219517.7251.47096l
191.1362.48414794.8960.5314580.1705997.738710.448537530.3631.49833l
196.2382.49832792.520.5215040.16967.682060.449881543.0731.52556l
201.342.51229790.1080.5116420.1686027.623820.451254555.8551.55264l
206.4422.52605787.6610.5018740.1676037.564030.452656568.7081.57958l
211.5442.5396785.1780.49220.1666057.502710.454088581.6311.60639l
216.6462.55294782.6580.4826180.1656067.439910.45555594.6221.63305l
221.7482.56607780.10.473130.1646087.375640.457044607.6811.65957l
226.852.579777.5040.4637350.1636097.309940.45857620.8061.68596l

Thermodynamic Property Profile at Constant Pressure

This page presents the temperature-dependent thermodynamic and transport properties of glycerol 1-monooleate (CAS 111-03-5) 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 glycerol 1-monooleate 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 glycerol 1-monooleate 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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