butyl nonanoate Thermodynamic Properties vs Temperature (CAS 50623-57-9)

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

Related Calculators for butyl nonanoate

Pure Component Properties

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Properties vs. Pressure

Analyze properties at constant temperature.

Input Conditions

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Property Profile for butyl nonanoate

Calculated properties vs. Temperature

Profile Data

Equilibrium Thermodynamic and Transport Properties of butyl nonanoate 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
-23.15	1.75785	854.321	0.723025	0.102169	12.4399	0.250894	-89.6505	-0.327416	l
-18.048	1.78038	852.087	0.709809	0.10117	12.4912	0.251552	-80.6243	-0.291676	l
-12.9459	1.80273	849.814	0.696713	0.100171	12.5384	0.252225	-71.4836	-0.256199	l
-7.84388	1.8249	847.502	0.68374	0.0991717	12.5818	0.252913	-62.2294	-0.220978	l
-2.74184	1.84689	845.151	0.670887	0.0981724	12.6212	0.253617	-52.8625	-0.186008	l
2.3602	1.86869	842.759	0.658156	0.0971732	12.6567	0.254337	-43.3839	-0.151282	l
7.46224	1.89031	840.326	0.645547	0.0961738	12.6883	0.255073	-33.7946	-0.116796	l
12.5643	1.91175	837.852	0.633059	0.0951745	12.7161	0.255826	-24.0953	-0.0825421	l
17.6663	1.93301	835.336	0.620692	0.0941751	12.7401	0.256597	-14.2872	-0.0485171	l
22.7684	1.95409	832.777	0.608448	0.0931758	12.7604	0.257385	-4.37104	-0.0147156	l
27.8704	1.97498	830.176	0.596325	0.0921764	12.7769	0.258192	5.65218	0.0188668	l
32.9724	1.9957	827.531	0.584323	0.091177	12.7898	0.259017	15.7816	0.0522344	l
38.0745	2.01623	824.841	0.572443	0.0901775	12.799	0.259861	26.0161	0.0853914	l
43.1765	2.03658	822.107	0.560685	0.0891781	12.8045	0.260726	36.355	0.118342	l
48.2786	2.05675	819.327	0.549049	0.0881786	12.8065	0.26161	46.7973	0.151089	l
53.3806	2.07674	816.501	0.537535	0.0871791	12.8049	0.262516	57.342	0.183636	l
58.4827	2.09654	813.628	0.526142	0.0861796	12.7998	0.263443	67.9882	0.215988	l
63.5847	2.11617	810.707	0.514871	0.08518	12.7912	0.264392	78.735	0.248147	l
68.6867	2.13561	807.738	0.503721	0.0841804	12.7791	0.265364	89.5814	0.280115	l
73.7888	2.15487	804.72	0.492694	0.0831808	12.7637	0.266359	100.527	0.311897	l
78.8908	2.17395	801.653	0.481788	0.0821812	12.7448	0.267378	111.57	0.343495	l
83.9929	2.19285	798.534	0.471004	0.0811816	12.7226	0.268422	122.709	0.374911	l
89.0949	2.21157	795.365	0.460342	0.0801819	12.6971	0.269492	133.945	0.406148	l
94.1969	2.2301	792.143	0.449801	0.0791822	12.6683	0.270588	145.276	0.43721	l
99.299	2.24845	788.868	0.439383	0.0781825	12.6362	0.271711	156.701	0.468097	l
104.401	2.26663	785.539	0.429085	0.0771828	12.6009	0.272863	168.219	0.498812	l
109.503	2.28462	782.155	0.41891	0.076183	12.5625	0.274043	179.83	0.529357	l
114.605	2.30242	778.716	0.408856	0.0751832	12.5209	0.275254	191.531	0.559735	l
119.707	2.32005	775.219	0.398923	0.0741834	12.4761	0.276495	203.323	0.589948	l
124.809	2.3375	771.665	0.389112	0.0731836	12.4283	0.277769	215.205	0.619997	l
129.911	2.35476	768.052	0.379422	0.0721837	12.3774	0.279075	227.175	0.649885	l
135.013	2.37184	764.379	0.369853	0.0711838	12.3235	0.280416	239.233	0.679612	l
140.115	2.38874	760.645	0.360405	0.0701839	12.2666	0.281793	251.377	0.709181	l
145.217	2.40546	756.848	0.351079	0.069184	12.2067	0.283206	263.608	0.738594	l
150.319	2.422	752.989	0.341872	0.068184	12.1438	0.284658	275.923	0.767851	l
155.421	2.43835	749.064	0.332787	0.067184	12.078	0.28615	288.321	0.796956	l
160.523	2.45453	745.073	0.323821	0.066184	12.0094	0.287682	300.803	0.825908	l
165.626	2.47052	741.014	0.314976	0.065184	11.9378	0.289258	313.367	0.85471	l
170.728	2.48633	736.886	0.306251	0.0641839	11.8634	0.290878	326.012	0.883362	l
175.83	2.50196	732.688	0.297645	0.0631838	11.7861	0.292545	338.738	0.911867	l
180.932	2.5174	728.417	0.289158	0.0621837	11.7061	0.29426	351.542	0.940225	l
186.034	2.53267	724.072	0.280789	0.0611836	11.6232	0.296026	364.425	0.968438	l
191.136	2.54775	719.651	0.272539	0.0601834	11.5375	0.297845	377.386	0.996507	l
196.238	2.56266	715.151	0.264407	0.0591832	11.4489	0.299719	390.422	1.02443	l
201.34	2.57738	710.571	0.256392	0.058183	11.3576	0.301651	403.535	1.05222	l
206.442	2.59192	705.909	0.248494	0.0571827	11.2635	0.303643	416.722	1.07986	l
211.544	2.60627	701.162	0.240712	0.0561824	11.1665	0.305699	429.983	1.10737	l
216.646	2.62045	696.327	0.233045	0.0551821	11.0667	0.307821	443.316	1.13473	l
221.748	2.63444	691.401	0.225493	0.0541818	10.964	0.310014	456.722	1.16196	l
226.85	2.64826	686.382	0.218053	0.0531814	10.8583	0.312281	470.198	1.18905	l

Property Profiles for butyl nonanoate

Heat Capacity (Cp) vs Temperature

Density vs Temperature

Thermal Conductivity vs Temperature

Viscosity vs Temperature

Thermodynamic Property Profile at Constant Pressure

This page presents the temperature-dependent thermodynamic and transport properties of butyl nonanoate (CAS 50623-57-9) 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 butyl nonanoate 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 butyl nonanoate 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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