lawrencium Thermodynamic Properties vs Temperature (CAS 22537-19-5)

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

Input Conditions

Define the chemical and range for the property profile.

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Property Profile for lawrencium

Calculated properties vs. Temperature

Profile Data

Equilibrium Thermodynamic and Transport Properties of lawrencium 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
-23.150.0323635N/A N/A N/A N/A N/A -1.73323-0.00632133s
-18.0480.0331207N/A N/A N/A N/A N/A -1.56619-0.00565989s
-12.94590.0338828N/A N/A N/A N/A N/A -1.39526-0.00499649s
-7.843880.0346496N/A N/A N/A N/A N/A -1.22043-0.00433114s
-2.741840.0354212N/A N/A N/A N/A N/A -1.04168-0.00366381s
2.36020.0361976N/A N/A N/A N/A N/A -0.858985-0.00299449s
7.462240.0369789N/A N/A N/A N/A N/A -0.672312-0.00232315s
12.56430.0377649N/A N/A N/A N/A N/A -0.481642-0.0016498s
17.66630.0385557N/A N/A N/A N/A N/A -0.286948-9.7440e-4s
22.76840.0393514N/A N/A N/A N/A N/A -0.0882077-2.9696e-4s
27.87040.0401519N/A N/A N/A N/A N/A 0.1146053.8254e-4s
32.97240.0409572N/A N/A N/A N/A N/A 0.3215140.00106412s
38.07450.0417673N/A N/A N/A N/A N/A 0.5325430.00174779s
43.17650.0425823N/A N/A N/A N/A N/A 0.7477190.00243355s
48.27860.0434021N/A N/A N/A N/A N/A 0.9670650.00312141s
53.38060.0442268N/A N/A N/A N/A N/A 1.190610.0038114s
58.48270.0450562N/A N/A N/A N/A N/A 1.418370.0045035s
63.58470.0458906N/A N/A N/A N/A N/A 1.650370.00519774s
68.68670.0467297N/A N/A N/A N/A N/A 1.886650.00589413s
73.78880.0475737N/A N/A N/A N/A N/A 2.127210.00659266s
78.89080.0484226N/A N/A N/A N/A N/A 2.37210.00729336s
83.99290.0492763N/A N/A N/A N/A N/A 2.621330.00799622s
89.09490.0501348N/A N/A N/A N/A N/A 2.874930.00870125s
94.19690.0509982N/A N/A N/A N/A N/A 3.132920.00940847s
99.2990.0518665N/A N/A N/A N/A N/A 3.395330.0101179s
104.4010.0527396N/A N/A N/A N/A N/A 3.662180.0108295s
109.5030.0536175N/A N/A N/A N/A N/A 3.933490.0115433s
114.6050.0545003N/A N/A N/A N/A N/A 4.20930.0122593s
119.7070.055388N/A N/A N/A N/A N/A 4.489630.0129775s
124.8090.0562805N/A N/A N/A N/A N/A 4.774490.0136979s
129.9110.0571779N/A N/A N/A N/A N/A 5.063930.0144206s
135.0130.0580801N/A N/A N/A N/A N/A 5.357950.0151455s
140.1150.0589872N/A N/A N/A N/A N/A 5.656590.0158726s
145.2170.0598991N/A N/A N/A N/A N/A 5.959870.0166019s
150.3190.0608159N/A N/A N/A N/A N/A 6.267810.0173335s
155.4210.0617376N/A N/A N/A N/A N/A 6.580450.0180674s
160.5230.0626641N/A N/A N/A N/A N/A 6.89780.0188035s
165.6260.0635955N/A N/A N/A N/A N/A 7.219880.0195418s
170.7280.0645318N/A N/A N/A N/A N/A 7.546740.0202825s
175.830.0654729N/A N/A N/A N/A N/A 7.878380.0210253s
180.9320.0664189N/A N/A N/A N/A N/A 8.214840.0217705s
186.0340.0673697N/A N/A N/A N/A N/A 8.556130.0225179s
191.1360.0683254N/A N/A N/A N/A N/A 8.902290.0232676s
196.2380.069286N/A N/A N/A N/A N/A 9.253340.0240195s
201.340.0702514N/A N/A N/A N/A N/A 9.60930.0247738s
206.4420.0712217N/A N/A N/A N/A N/A 9.97020.0255303s
211.5440.0721969N/A N/A N/A N/A N/A 10.33610.0262892s
216.6460.0731769N/A N/A N/A N/A N/A 10.70690.0270503s
221.7480.0741618N/A N/A N/A N/A N/A 11.08280.0278137s
226.850.0751515N/A N/A N/A N/A N/A 11.46370.0285794s

Property Profiles for lawrencium

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 lawrencium (CAS 22537-19-5) 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 lawrencium 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 lawrencium 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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