2-Chloro-1-[4-(1,1-dimethylethyl)phenyl]ethanone Thermodynamic Properties vs Temperature (CAS 21886-62-4)

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

Related Calculators for 2-Chloro-1-[4-(1,1-dimethylethyl)phenyl]ethanone

Pure Component Properties

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Properties vs. Pressure

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Input Conditions

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Property Profile for 2-Chloro-1-[4-(1,1-dimethylethyl)phenyl]ethanone

Calculated properties vs. Temperature

Profile Data

Equilibrium Thermodynamic and Transport Properties of 2-Chloro-1-[4-(1,1-dimethylethyl)phenyl]ethanone 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	1.02221	1245	N/A	N/A	N/A	0.169236	-53.6269	-0.195696	s
-18.048	1.04148	1242.15	N/A	N/A	N/A	0.169626	-48.3624	-0.17485	s
-12.9459	1.0608	1239.29	N/A	N/A	N/A	0.170017	-42.9994	-0.154036	s
-7.84388	1.08017	1236.43	N/A	N/A	N/A	0.17041	-37.5378	-0.13325	s
-2.74184	1.09958	1233.57	N/A	N/A	N/A	0.170804	-31.9773	-0.11249	s
2.3602	1.11904	1230.72	N/A	N/A	N/A	0.171201	-26.3175	-0.0917555	s
7.46224	1.13856	1227.86	N/A	N/A	N/A	0.171599	-20.5584	-0.0710437	s
12.5643	1.15812	1225	N/A	N/A	N/A	0.171999	-14.6995	-0.0503529	s
17.6663	1.17773	1222.15	N/A	N/A	N/A	0.172402	-8.74075	-0.0296817	s
22.7684	1.1974	1219.29	N/A	N/A	N/A	0.172806	-2.68177	-0.00902848	s
27.8704	1.21711	1216.43	N/A	N/A	N/A	0.173211	3.47768	0.0116083	s
32.9724	1.23688	1213.57	N/A	N/A	N/A	0.173619	9.73786	0.0322301	s
38.0745	1.6318	1080.69	N/A	0.111052	N/A	0.194968	106.436	0.34504	l
43.1765	1.65115	1077.37	N/A	0.110337	N/A	0.195569	114.811	0.371732	l
48.2786	1.67021	1074.03	N/A	0.109622	N/A	0.196176	123.284	0.398303	l
53.3806	1.68898	1070.68	N/A	0.108907	N/A	0.196791	131.853	0.424754	l
58.4827	1.70746	1067.31	N/A	0.108192	N/A	0.197412	140.518	0.451084	l
63.5847	1.72564	1063.92	N/A	0.107477	N/A	0.198041	149.276	0.477291	l
68.6867	1.74354	1060.52	N/A	0.106762	N/A	0.198676	158.126	0.503376	l
73.7888	1.76114	1057.1	2.35403	0.106047	39.0936	0.19932	167.067	0.529337	l
78.8908	1.77845	1053.65	2.15807	0.105332	36.4373	0.19997	176.096	0.555174	l
83.9929	1.79547	1050.2	1.98335	0.104617	34.0388	0.200629	185.214	0.580886	l
89.0949	1.8122	1046.72	1.82711	0.103902	31.8674	0.201296	194.417	0.606473	l
94.1969	1.82863	1043.22	1.68702	0.103187	29.8966	0.201971	203.705	0.631933	l
99.299	1.84478	1039.7	1.56108	0.102472	28.1038	0.202654	213.076	0.657268	l
104.401	1.86063	1036.17	1.44757	0.101757	26.469	0.203345	222.529	0.682475	l
109.503	1.87619	1032.61	1.34503	0.101042	24.9751	0.204046	232.062	0.707555	l
114.605	1.89146	1029.04	1.25216	0.100327	23.607	0.204755	241.673	0.732507	l
119.707	1.90644	1025.44	1.16788	0.0996116	22.3517	0.205473	251.362	0.75733	l
124.809	1.92113	1021.82	1.09121	0.0988965	21.1975	0.206201	261.126	0.782025	l
129.911	1.93553	1018.18	1.02134	0.0981814	20.1344	0.206938	270.965	0.80659	l
135.013	1.94963	1014.51	0.957515	0.0974663	19.1533	0.207685	280.876	0.831025	l
140.115	1.96345	1010.83	0.899115	0.0967512	18.2464	0.208443	290.858	0.85533	l
145.217	1.97697	1007.12	0.845574	0.0960361	17.4067	0.20921	300.911	0.879505	l
150.319	1.9902	1003.39	0.796398	0.0953209	16.6279	0.209989	311.031	0.903549	l
155.421	2.00314	999.631	0.751153	0.0946058	15.9045	0.210778	321.218	0.927462	l
160.523	2.01579	995.851	0.709454	0.0938906	15.2316	0.211578	331.471	0.951243	l
165.626	2.02814	992.045	0.67096	0.0931755	14.6047	0.21239	341.787	0.974892	l
170.728	2.04021	988.213	0.635369	0.0924603	14.0199	0.213213	352.165	0.998409	l
175.83	2.05198	984.356	0.602412	0.0917451	13.4736	0.214049	362.605	1.02179	l
180.932	2.06346	980.472	0.571849	0.0910299	12.9626	0.214896	373.104	1.04504	l
186.034	2.07465	976.56	0.543465	0.0903147	12.4841	0.215757	383.66	1.06816	l
191.136	2.08555	972.62	0.517067	0.0895995	12.0355	0.216631	394.273	1.09115	l
196.238	2.09616	968.652	0.492485	0.0888843	11.6143	0.217519	404.941	1.114	l
201.34	2.10648	964.655	0.469563	0.0881691	11.2185	0.21842	415.662	1.13672	l
206.442	2.1165	960.628	0.448162	0.0874538	10.8461	0.219336	426.435	1.1593	l
211.544	2.12623	956.57	0.428157	0.0867386	10.4955	0.220266	437.258	1.18175	l
216.646	2.13568	952.481	0.409434	0.0860233	10.1649	0.221212	448.131	1.20406	l
221.748	2.14483	948.359	0.391891	0.085308	9.85298	0.222173	459.05	1.22624	l
226.85	2.15369	944.205	0.375435	0.0845928	9.55837	0.223151	470.016	1.24829	l

Property Profiles for 2-Chloro-1-[4-(1,1-dimethylethyl)phenyl]ethanone

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 2-Chloro-1-[4-(1,1-dimethylethyl)phenyl]ethanone (CAS 21886-62-4) 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-Chloro-1-[4-(1,1-dimethylethyl)phenyl]ethanone 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-Chloro-1-[4-(1,1-dimethylethyl)phenyl]ethanone 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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