2-Bromo-1-[3-(trifluoromethyl)phenyl]ethanone Thermodynamic Properties vs Temperature (CAS 2003-10-3)

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

Related Calculators for 2-Bromo-1-[3-(trifluoromethyl)phenyl]ethanone

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-Bromo-1-[3-(trifluoromethyl)phenyl]ethanone

Calculated properties vs. Temperature

Profile Data

Equilibrium Thermodynamic and Transport Properties of 2-Bromo-1-[3-(trifluoromethyl)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	0.59331	1693.86	N/A	N/A	N/A	0.157654	-112.452	-0.389167	s
-18.048	0.605849	1689.76	N/A	N/A	N/A	0.158036	-109.393	-0.377054	s
-12.9459	0.618446	1685.67	N/A	N/A	N/A	0.158419	-106.27	-0.364933	s
-7.84388	0.631101	1681.58	N/A	N/A	N/A	0.158805	-103.083	-0.352801	s
-2.74184	0.643814	1677.48	N/A	N/A	N/A	0.159193	-99.8303	-0.340659	s
2.3602	0.656585	1673.39	N/A	N/A	N/A	0.159582	-96.513	-0.328506	s
7.46224	0.669415	1669.29	N/A	N/A	N/A	0.159973	-93.1304	-0.316341	s
12.5643	0.682304	1665.2	N/A	N/A	N/A	0.160367	-89.6822	-0.304164	s
17.6663	0.695251	1661.11	N/A	N/A	N/A	0.160762	-86.168	-0.291973	s
22.7684	0.961006	1479.31	N/A	0.104636	N/A	0.180518	-2.15164	-0.00724375	l
27.8704	0.975314	1474.53	N/A	0.103963	N/A	0.181104	2.78806	0.00930642	l
32.9724	0.989361	1469.72	N/A	0.10329	N/A	0.181696	7.8001	0.0258167	l
38.0745	1.00315	1464.89	N/A	0.102618	N/A	0.182295	12.8831	0.0422842	l
43.1765	1.01667	1460.03	N/A	0.101945	N/A	0.182902	18.0359	0.0587059	l
48.2786	1.02994	1455.14	N/A	0.101272	N/A	0.183517	23.2569	0.0750792	l
53.3806	1.04294	1450.22	N/A	0.1006	N/A	0.184139	28.545	0.0914015	l
58.4827	1.05568	1445.28	N/A	0.0999268	N/A	0.184769	33.8987	0.10767	l
63.5847	1.06817	1440.3	N/A	0.0992541	N/A	0.185407	39.3168	0.123883	l
68.6867	1.08039	1435.3	N/A	0.0985814	N/A	0.186053	44.7979	0.140038	l
73.7888	1.09235	1430.27	N/A	0.0979086	N/A	0.186708	50.3407	0.156133	l
78.8908	1.10405	1425.2	N/A	0.0972359	N/A	0.187372	55.9439	0.172165	l
83.9929	1.11548	1420.1	N/A	0.0965631	N/A	0.188044	61.6061	0.188134	l
89.0949	1.12666	1414.98	N/A	0.0958904	N/A	0.188726	67.326	0.204036	l
94.1969	1.13758	1409.82	N/A	0.0952176	N/A	0.189417	73.1022	0.21987	l
99.299	1.14823	1404.62	N/A	0.0945448	N/A	0.190117	78.9335	0.235635	l
104.401	1.15863	1399.39	N/A	0.0938721	N/A	0.190828	84.8184	0.251328	l
109.503	1.16876	1394.13	N/A	0.0931993	N/A	0.191548	90.7558	0.266948	l
114.605	1.17864	1388.83	N/A	0.0925265	N/A	0.192279	96.7441	0.282495	l
119.707	1.18825	1383.5	N/A	0.0918537	N/A	0.19302	102.782	0.297965	l
124.809	1.1976	1378.12	N/A	0.0911809	N/A	0.193772	108.869	0.313358	l
129.911	1.20669	1372.71	N/A	0.0905081	N/A	0.194536	115.002	0.328672	l
135.013	1.21552	1367.27	N/A	0.0898353	N/A	0.195311	121.181	0.343906	l
140.115	1.22409	1361.78	N/A	0.0891624	N/A	0.196098	127.405	0.35906	l
145.217	1.2324	1356.25	N/A	0.0884896	N/A	0.196898	133.672	0.37413	l
150.319	1.24044	1350.68	N/A	0.0878168	N/A	0.197709	139.98	0.389118	l
155.421	1.24823	1345.07	N/A	0.0871439	N/A	0.198534	146.329	0.40402	l
160.523	1.25575	1339.42	N/A	0.0864711	N/A	0.199372	152.717	0.418837	l
165.626	1.26302	1333.72	N/A	0.0857982	N/A	0.200224	159.142	0.433567	l
170.728	1.27002	1327.97	N/A	0.0851254	N/A	0.20109	165.604	0.448209	l
175.83	1.27676	1322.18	N/A	0.0844525	N/A	0.201971	172.101	0.462762	l
180.932	1.28324	1316.34	N/A	0.0837796	N/A	0.202867	178.632	0.477226	l
186.034	1.28946	1310.46	N/A	0.0831067	N/A	0.203778	185.195	0.491599	l
191.136	1.29542	1304.52	N/A	0.0824338	N/A	0.204706	191.789	0.505881	l
196.238	1.30112	1298.53	N/A	0.0817609	N/A	0.20565	198.413	0.52007	l
201.34	1.30656	1292.49	N/A	0.081088	N/A	0.206611	205.065	0.534166	l
206.442	1.31174	1286.39	N/A	0.0804151	N/A	0.20759	211.745	0.548167	l
211.544	1.31665	1280.24	N/A	0.0797422	N/A	0.208588	218.45	0.562075	l
216.646	1.32131	1274.03	N/A	0.0790692	N/A	0.209604	225.18	0.575886	l
221.748	1.3257	1267.76	N/A	0.0783963	N/A	0.210641	231.932	0.589602	l
226.85	1.32984	1261.43	N/A	0.0777233	N/A	0.211698	238.707	0.60322	l

Property Profiles for 2-Bromo-1-[3-(trifluoromethyl)phenyl]ethanone

Heat Capacity (Cp) vs Temperature

Density vs Temperature

Thermal Conductivity vs Temperature

Thermodynamic Property Profile at Constant Pressure

This page presents the temperature-dependent thermodynamic and transport properties of 2-Bromo-1-[3-(trifluoromethyl)phenyl]ethanone (CAS 2003-10-3) 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 2-Bromo-1-[3-(trifluoromethyl)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-Bromo-1-[3-(trifluoromethyl)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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