trans-Isoeugenol Thermodynamic Properties vs Temperature (CAS 5932-68-3)

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

Related Calculators for trans-Isoeugenol

Pure Component Properties

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Properties vs. Pressure

Analyze properties at constant temperature.

Input Conditions

Define the chemical and range for the property profile.

Property Profile for trans-Isoeugenol

Calculated properties vs. Temperature

Profile Data

Equilibrium Thermodynamic and Transport Properties of trans-Isoeugenol 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	1.0757	1367.54	N/A	N/A	N/A	0.120071	-56.3465	-0.205629	s
-18.048	1.09562	1364.37	N/A	N/A	N/A	0.120349	-50.8075	-0.183697	s
-12.9459	1.11558	1361.2	N/A	N/A	N/A	0.120629	-45.1667	-0.161804	s
-7.84388	1.13558	1358.04	N/A	N/A	N/A	0.120911	-39.4239	-0.139948	s
-2.74184	1.15563	1354.87	N/A	N/A	N/A	0.121193	-33.579	-0.118127	s
2.3602	1.17572	1351.7	N/A	N/A	N/A	0.121477	-27.6317	-0.0963382	s
7.46224	1.19586	1348.54	N/A	N/A	N/A	0.121763	-21.5818	-0.0745807	s
12.5643	1.21604	1345.37	N/A	N/A	N/A	0.122049	-15.429	-0.0528519	s
17.6663	1.23626	1342.2	N/A	N/A	N/A	0.122337	-9.17318	-0.0311502	s
22.7684	1.25653	1339.04	N/A	N/A	N/A	0.122626	-2.81403	-0.00947376	s
27.8704	1.27685	1335.87	N/A	N/A	N/A	0.122917	3.64867	0.0121791	s
32.9724	1.29722	1332.7	N/A	N/A	N/A	0.123209	10.2152	0.0338099	s
38.0745	1.70233	1186.2	N/A	0.119497	N/A	0.138426	155.558	0.507594	l
43.1765	1.72209	1182.37	N/A	0.118725	N/A	0.138874	164.294	0.535435	l
48.2786	1.74156	1178.52	N/A	0.117953	N/A	0.139328	173.13	0.563145	l
53.3806	1.76075	1174.65	N/A	0.117181	N/A	0.139787	182.064	0.590723	l
58.4827	1.77966	1170.76	N/A	0.116409	N/A	0.140251	191.096	0.618168	l
63.5847	1.79828	1166.85	N/A	0.115637	N/A	0.140721	200.223	0.645481	l
68.6867	1.81663	1162.92	N/A	0.114865	N/A	0.141197	209.445	0.672662	l
73.7888	1.83469	1158.97	N/A	0.114093	N/A	0.141679	218.76	0.699709	l
78.8908	1.85247	1154.99	N/A	0.113321	N/A	0.142167	228.166	0.726623	l
83.9929	1.86996	1150.99	N/A	0.112549	N/A	0.14266	237.662	0.753404	l
89.0949	1.88717	1146.97	N/A	0.111777	N/A	0.143161	247.247	0.78005	l
94.1969	1.90411	1142.93	N/A	0.111005	N/A	0.143667	256.919	0.806563	l
99.299	1.92076	1138.86	1.1494	0.110233	20.0278	0.14418	266.676	0.832942	l
104.401	1.93712	1134.77	0.999722	0.109461	17.6921	0.1447	276.518	0.859187	l
109.503	1.95321	1130.65	0.872776	0.108689	15.6844	0.145227	286.442	0.885297	l
114.605	1.96901	1126.51	0.764678	0.107916	13.9521	0.145761	296.448	0.911272	l
119.707	1.98453	1122.34	0.672273	0.107144	12.4518	0.146303	306.534	0.937113	l
124.809	1.99977	1118.14	0.592989	0.106372	11.148	0.146852	316.698	0.962818	l
129.911	2.01472	1113.92	0.52472	0.1056	10.011	0.147408	326.939	0.988389	l
135.013	2.02939	1109.67	0.465733	0.104828	9.01624	0.147972	337.256	1.01382	l
140.115	2.04378	1105.4	0.414595	0.104056	8.14315	0.148545	347.646	1.03912	l
145.217	2.05789	1101.09	0.370121	0.103284	7.37454	0.149126	358.11	1.06429	l
150.319	2.07172	1096.76	0.331323	0.102512	6.6959	0.149715	368.645	1.08932	l
155.421	2.08526	1092.39	0.297375	0.101739	6.09501	0.150313	379.25	1.11421	l
160.523	2.09852	1088	0.267584	0.100967	5.56152	0.15092	389.923	1.13896	l
165.626	2.1115	1083.57	0.24137	0.100195	5.08661	0.151537	400.663	1.16359	l
170.728	2.12419	1079.12	0.218241	0.0994229	4.66277	0.152162	411.468	1.18807	l
175.83	2.13661	1074.63	0.19778	0.0986507	4.28359	0.152798	422.337	1.21242	l
180.932	2.14874	1070.1	0.179635	0.0978785	3.94354	0.153444	433.27	1.23663	l
186.034	2.16059	1065.55	0.163503	0.0971063	3.6379	0.1541	444.263	1.2607	l
191.136	2.17215	1060.95	0.149129	0.0963341	3.36257	0.154768	455.316	1.28464	l
196.238	2.18344	1056.32	0.13629	0.0955619	3.11401	0.155446	466.427	1.30844	l
201.34	2.19444	1051.66	0.124798	0.0947896	2.88915	0.156135	477.595	1.33211	l
206.442	2.20516	1046.96	0.114489	0.0940174	2.68533	0.156837	488.819	1.35564	l
211.544	2.2156	1042.21	0.105223	0.0932452	2.50021	0.15755	500.097	1.37903	l
216.646	2.22575	1037.43	0.0968771	0.0924729	2.33176	0.158276	511.427	1.40228	l
221.748	2.23562	1032.61	0.0893452	0.0917007	2.1782	0.159016	522.808	1.4254	l
226.85	2.24522	1027.75	0.082535	0.0909284	2.03796	0.159768	534.239	1.44837	l

Property Profiles for trans-Isoeugenol

Heat Capacity (Cp) vs Temperature

Density vs Temperature

Thermodynamic Property Profile at Constant Pressure

This page presents the temperature-dependent thermodynamic and transport properties of trans-Isoeugenol (CAS 5932-68-3) 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 trans-Isoeugenol 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 trans-Isoeugenol 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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