2-(2-hexyloxyethoxy)ethanol Thermodynamic Properties vs Temperature (CAS 112-59-4)

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

Related Calculators for 2-(2-hexyloxyethoxy)ethanol

Pure Component Properties

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Properties vs. Pressure

Analyze properties at constant temperature.

Input Conditions

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Property Profile for 2-(2-hexyloxyethoxy)ethanol

Calculated properties vs. Temperature

Profile Data

Equilibrium Thermodynamic and Transport Properties of 2-(2-hexyloxyethoxy)ethanol 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	2.09027	990.584	1.13475	0.143867	16.487	0.192089	-103.912	-0.379765	l
-18.048	2.10464	988.464	1.11379	0.142868	16.4076	0.192501	-93.2105	-0.337392	l
-12.9459	2.11901	986.3	1.09303	0.141869	16.3259	0.192923	-82.4358	-0.295572	l
-7.84388	2.13338	984.092	1.07245	0.14087	16.2416	0.193356	-71.5879	-0.254286	l
-2.74184	2.14775	981.84	1.05207	0.139871	16.1549	0.193799	-60.6666	-0.213513	l
2.3602	2.16213	979.543	1.03189	0.138872	16.0657	0.194254	-49.672	-0.173233	l
7.46224	2.1765	977.199	1.01189	0.137873	15.974	0.19472	-38.6041	-0.133428	l
12.5643	2.19087	974.809	0.992092	0.136874	15.8799	0.195197	-27.4629	-0.0940817	l
17.6663	2.20524	972.371	0.972484	0.135874	15.7834	0.195687	-16.2483	-0.0551774	l
22.7684	2.21962	969.884	0.95307	0.134875	15.6845	0.196188	-4.96038	-0.0166997	l
27.8704	2.23399	967.348	0.933849	0.133876	15.5831	0.196703	6.40085	0.0213658	l
32.9724	2.24836	964.761	0.914822	0.132877	15.4793	0.19723	17.8354	0.0590331	l
38.0745	2.26273	962.124	0.895988	0.131878	15.3732	0.197771	29.3433	0.0963154	l
43.1765	2.2771	959.434	0.877347	0.130878	15.2646	0.198325	40.9245	0.133225	l
48.2786	2.29148	956.691	0.8589	0.129879	15.1537	0.198894	52.5791	0.169774	l
53.3806	2.30585	953.895	0.840646	0.12888	15.0404	0.199477	64.3069	0.205974	l
58.4827	2.32022	951.043	0.822586	0.127881	14.9247	0.200075	76.1081	0.241836	l
63.5847	2.33459	948.135	0.80472	0.126881	14.8067	0.200689	87.9826	0.277369	l
68.6867	2.34896	945.17	0.787047	0.125882	14.6863	0.201318	99.9305	0.312584	l
73.7888	2.36334	942.148	0.769568	0.124883	14.5636	0.201964	111.952	0.34749	l
78.8908	2.37771	939.065	0.752283	0.123884	14.4386	0.202627	124.046	0.382097	l
83.9929	2.39208	935.923	0.735192	0.122884	14.3113	0.203307	136.214	0.416412	l
89.0949	2.40645	932.719	0.718294	0.121885	14.1817	0.204006	148.455	0.450445	l
94.1969	2.42083	929.453	0.70159	0.120885	14.0499	0.204723	160.77	0.484202	l
99.299	2.4352	926.122	0.685079	0.119886	13.9157	0.205459	173.157	0.517692	l
104.401	2.44957	922.726	0.668763	0.118887	13.7794	0.206215	185.619	0.550922	l
109.503	2.46394	919.264	0.65264	0.117887	13.6407	0.206991	198.153	0.583899	l
114.605	2.47831	915.734	0.636711	0.116888	13.4999	0.207789	210.761	0.61663	l
119.707	2.49269	912.135	0.620976	0.115888	13.3568	0.208609	223.442	0.64912	l
124.809	2.50706	908.466	0.605435	0.114889	13.2115	0.209452	236.196	0.681377	l
129.911	2.52143	904.724	0.590087	0.113889	13.0641	0.210318	249.024	0.713406	l
135.013	2.5358	900.908	0.574933	0.11289	12.9145	0.211209	261.925	0.745212	l
140.115	2.55017	897.018	0.559973	0.11189	12.7627	0.212125	274.9	0.776802	l
145.217	2.56455	893.051	0.545206	0.110891	12.6088	0.213067	287.948	0.808181	l
150.319	2.57892	889.005	0.530633	0.109891	12.4528	0.214037	301.069	0.839354	l
155.421	2.59329	884.88	0.516253	0.108892	12.2947	0.215035	314.263	0.870326	l
160.523	2.60766	880.672	0.502067	0.107892	12.1345	0.216062	327.531	0.901101	l
165.626	2.62204	876.38	0.488073	0.106893	11.9723	0.21712	340.872	0.931684	l
170.728	2.63641	872.003	0.474273	0.105893	11.8079	0.21821	354.286	0.96208	l
175.83	2.65078	867.538	0.460666	0.104893	11.6416	0.219333	367.774	0.992292	l
180.932	2.66515	862.983	0.447251	0.103894	11.4732	0.220491	381.335	1.02233	l
186.034	2.67952	858.336	0.434029	0.102894	11.3028	0.221685	394.969	1.05218	l
191.136	2.6939	853.595	0.420999	0.101894	11.1304	0.222916	408.677	1.08187	l
196.238	2.70827	848.757	0.40816	0.100895	10.9561	0.224187	422.458	1.11139	l
201.34	2.72264	843.819	0.395513	0.099895	10.7797	0.225498	436.312	1.14075	l
206.442	2.73701	838.78	0.383057	0.0988952	10.6014	0.226853	450.24	1.16995	l
211.544	2.75138	833.635	0.370791	0.0978955	10.4212	0.228253	464.241	1.19898	l
216.646	2.76576	828.383	0.358714	0.0968957	10.239	0.2297	478.316	1.22787	l
221.748	2.78013	823.02	0.346827	0.0958959	10.0549	0.231197	492.463	1.25661	l
226.85	2.7945	817.543	0.335127	0.0948961	9.86883	0.232746	506.684	1.28519	l

Property Profiles for 2-(2-hexyloxyethoxy)ethanol

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 2-(2-hexyloxyethoxy)ethanol (CAS 112-59-4) 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 2-(2-hexyloxyethoxy)ethanol 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 2-(2-hexyloxyethoxy)ethanol 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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