1-hexanol Thermodynamic Properties vs Temperature (CAS 111-27-3)

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

Related Calculators for 1-hexanol

Pure Component Properties

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Properties vs. Pressure

Analyze properties at constant temperature.

Input Conditions

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Property Profile for 1-hexanol

Calculated properties vs. Temperature

Profile Data

Equilibrium Thermodynamic and Transport Properties of 1-hexanol 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	2.0691	849.703	28.2474	0.156962	372.363	0.120248	-106.036	-0.387128	l
-18.048	2.09259	846.237	22.3838	0.156178	299.916	0.12074	-95.4196	-0.345093	l
-12.9459	2.11772	842.748	17.9259	0.155385	244.31	0.12124	-84.6798	-0.303409	l
-7.84388	2.14456	839.234	14.4992	0.154581	201.152	0.121748	-73.8074	-0.26203	l
-2.74184	2.1732	835.697	11.8376	0.153767	167.301	0.122263	-62.7935	-0.220911	l
2.3602	2.20373	832.135	9.74999	0.152944	140.485	0.122786	-51.6287	-0.180008	l
7.46224	2.23624	828.548	8.09745	0.15211	119.044	0.123318	-40.3031	-0.139277	l
12.5643	2.27081	824.934	6.77786	0.151267	101.749	0.123858	-28.8064	-0.0986757	l
17.6663	2.30754	821.294	5.71543	0.150413	87.6821	0.124407	-17.1278	-0.0581624	l
22.7684	2.3465	817.627	4.85335	0.14955	76.151	0.124965	-5.25626	-0.0176958	l
27.8704	2.3878	813.931	4.14866	0.148676	66.6289	0.125532	6.81999	0.0227648	l
32.9724	2.43137	810.207	3.56858	0.147793	58.7075	0.12611	19.1129	0.0632589	l
38.0745	2.47696	806.452	3.0879	0.146899	52.067	0.126697	31.6334	0.103821	l
43.1765	2.52425	802.668	2.68706	0.145996	46.459	0.127294	44.3909	0.144479	l
48.2786	2.57291	798.852	2.3508	0.145082	41.6894	0.127902	57.3933	0.185254	l
53.3806	2.62262	795.004	2.0671	0.144159	37.6059	0.128521	70.6468	0.226163	l
58.4827	2.67308	791.122	1.82644	0.143225	34.0876	0.129152	84.156	0.267214	l
63.5847	2.72395	787.206	1.62123	0.142282	31.0381	0.129794	97.9239	0.308412	l
68.6867	2.77493	783.255	1.44539	0.141328	28.3797	0.130449	111.952	0.349757	l
73.7888	2.82569	779.268	1.294	0.140365	26.0495	0.131116	126.239	0.391243	l
78.8908	2.87592	775.243	1.16307	0.139391	23.9964	0.131797	140.784	0.432861	l
83.9929	2.92529	771.179	1.04935	0.138408	22.1784	0.132492	155.584	0.474598	l
89.0949	2.97349	767.075	0.950179	0.137414	20.5608	0.1332	170.632	0.516435	l
94.1969	3.0202	762.93	0.863344	0.13641	19.1149	0.133924	185.923	0.55835	l
99.299	3.06511	758.742	0.787027	0.135397	17.8167	0.134663	201.448	0.60032	l
104.401	3.10789	754.508	0.719708	0.134373	16.646	0.135419	217.196	0.642316	l
109.503	3.14822	750.229	0.660121	0.13334	15.5858	0.136191	233.157	0.684306	l
114.605	3.1858	745.902	0.607201	0.132296	14.6219	0.136982	249.316	0.726257	l
119.707	3.22029	741.524	0.560048	0.131243	13.7419	0.13779	265.659	0.76813	l
124.809	3.25138	737.095	0.517904	0.130179	12.9353	0.138618	282.17	0.809887	l
129.911	3.2788	732.611	0.480124	0.129105	12.1934	0.139467	298.831	0.851485	l
135.013	3.30269	728.071	0.446155	0.128022	11.5098	0.140336	315.621	0.892881	l
140.115	3.32356	723.471	0.415528	0.126928	10.8804	0.141229	332.526	0.934041	l
145.217	3.34194	718.81	0.387836	0.125825	10.3011	0.142144	349.531	0.974936	l
150.319	3.35836	714.084	0.362731	0.124711	9.76803	0.143085	366.624	1.01555	l
155.421	3.37332	709.29	0.33991	0.123587	9.27784	0.144052	383.798	1.05586	l
160.523	2.05371	2.8712	0.00901527	0.0207495	0.892294	35.5861	840.972	2.11888	g
165.626	2.07293	2.83781	0.0091204	0.0212594	0.889299	36.0048	851.573	2.14318	g
170.728	2.09201	2.80519	0.00922527	0.0217749	0.886312	36.4234	862.27	2.16742	g
175.83	2.11092	2.77332	0.0093299	0.0222959	0.883333	36.8421	873.062	2.19159	g
180.932	2.12967	2.74216	0.00943427	0.0228224	0.88036	37.2607	883.948	2.2157	g
186.034	2.14827	2.71169	0.00953838	0.0233544	0.877393	37.6794	894.927	2.23974	g
191.136	2.1667	2.68189	0.00964225	0.023892	0.874431	38.0981	905.999	2.26372	g
196.238	2.18497	2.65274	0.00974587	0.024435	0.871473	38.5167	917.162	2.28764	g
201.34	2.20308	2.62421	0.00984925	0.0249836	0.868519	38.9354	928.417	2.31148	g
206.442	2.22103	2.5963	0.00995238	0.0255376	0.865567	39.354	939.762	2.33527	g
211.544	2.23881	2.56897	0.0100553	0.0260971	0.862618	39.7727	951.197	2.35898	g
216.646	2.25643	2.54221	0.0101579	0.0266621	0.859671	40.1914	962.721	2.38263	g
221.748	2.27389	2.516	0.0102603	0.0272325	0.856726	40.61	974.332	2.40622	g
226.85	2.29118	2.49033	0.0103625	0.0278084	0.853783	41.0287	986.031	2.42974	g

Property Profiles for 1-hexanol

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 1-hexanol (CAS 111-27-3) 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 1-hexanol 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 1-hexanol 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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