germanium tetraethoxide Thermodynamic Properties vs Temperature (CAS 14165-55-0)

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

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Property Profile for germanium tetraethoxide

Calculated properties vs. Temperature

Profile Data

Equilibrium Thermodynamic and Transport Properties of germanium tetraethoxide 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
-23.150.910935N/A N/A 0.138919N/A N/A -47.7912-0.174412l
-18.0480.928962N/A N/A 0.137968N/A N/A -43.0975-0.155827l
-12.94590.946712N/A N/A 0.137016N/A N/A -38.3125-0.137255l
-7.843880.964187N/A N/A 0.136065N/A N/A -33.4376-0.118702l
-2.741840.981385N/A N/A 0.135113N/A N/A -28.4743-0.100172l
2.36020.998306N/A N/A 0.134161N/A N/A -23.424-0.0816701l
7.462241.01495N/A N/A 0.13321N/A N/A -18.288-0.0631994l
12.56431.03132N/A N/A 0.132258N/A N/A -13.0678-0.044764l
17.66631.04741N/A N/A 0.131306N/A N/A -7.76479-0.0263677l
22.76841.06323N/A N/A 0.130355N/A N/A -2.38037-0.0080138l
27.87041.07877N/A N/A 0.129403N/A N/A 3.084030.0102944l
32.97241.09403N/A N/A 0.128452N/A N/A 8.627020.0285537l
38.07451.10902N/A N/A 0.1275N/A N/A 14.24720.0467612l
43.17651.12373N/A N/A 0.126548N/A N/A 19.94310.0649141l
48.27861.13817N/A N/A 0.125597N/A N/A 25.71340.0830098l
53.38061.15233N/A N/A 0.124645N/A N/A 31.55660.101046l
58.48271.16621N/A N/A 0.123693N/A N/A 37.47130.119019l
63.58471.17982N/A N/A 0.122742N/A N/A 43.45620.136928l
68.68671.19315N/A N/A 0.12179N/A N/A 49.50980.154771l
73.78881.2062N/A N/A 0.120839N/A N/A 55.63070.172544l
78.89081.21898N/A N/A 0.119887N/A N/A 61.81750.190246l
83.99291.23148N/A N/A 0.118935N/A N/A 68.06880.207876l
89.09491.2437N/A N/A 0.117984N/A N/A 74.38310.225431l
94.19691.25565N/A N/A 0.117032N/A N/A 80.75910.242909l
99.2991.26732N/A N/A 0.11608N/A N/A 87.19540.260309l
104.4011.27872N/A N/A 0.115129N/A N/A 93.69050.27763l
109.5031.28984N/A N/A 0.114177N/A N/A 100.2430.294869l
114.6051.30068N/A N/A 0.113226N/A N/A 106.8520.312025l
119.7071.31125N/A N/A 0.112274N/A N/A 113.5150.329097l
124.8091.32154N/A N/A 0.111322N/A N/A 120.2310.346083l
129.9111.33155N/A N/A 0.110371N/A N/A 126.9990.362982l
135.0131.34129N/A N/A 0.109419N/A N/A 133.8180.379792l
140.1151.35075N/A N/A 0.108467N/A N/A 140.6860.396514l
145.2171.35994N/A N/A 0.107516N/A N/A 147.6010.413144l
150.3191.36884N/A N/A 0.106564N/A N/A 154.5620.429682l
155.4211.37748N/A N/A 0.105613N/A N/A 161.5680.446128l
160.5231.38583N/A N/A 0.104661N/A N/A 168.6170.462479l
165.6261.39391N/A N/A 0.103709N/A N/A 175.7090.478735l
170.7281.40172N/A N/A 0.102758N/A N/A 182.8410.494895l
175.831.40924N/A N/A 0.101806N/A N/A 190.0110.510958l
180.9321.41649N/A N/A 0.100854N/A N/A 197.220.526923l
186.0341.42347N/A N/A 0.0999028N/A N/A 204.4650.542789l
191.1361.37053.11587N/A N/A N/A 38.0981N/A N/A g
196.2381.381753.082N/A N/A N/A 38.5167N/A N/A g
201.341.392843.04886N/A N/A N/A 38.9354N/A N/A g
206.4421.40383.01642N/A N/A N/A 39.354N/A N/A g
211.5441.41462.98467N/A N/A N/A 39.7727N/A N/A g
216.6461.425272.95358N/A N/A N/A 40.1914N/A N/A g
221.7481.435792.92313N/A N/A N/A 40.61N/A N/A g
226.851.446172.8933N/A N/A N/A 41.0287N/A N/A g

Property Profiles for germanium tetraethoxide

Heat Capacity (Cp) vs Temperature

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Thermodynamic Property Profile at Constant Pressure

This page presents the temperature-dependent thermodynamic and transport properties of germanium tetraethoxide (CAS 14165-55-0) 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 germanium tetraethoxide 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 germanium tetraethoxide 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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