Dortmund Data Bank
Entropy (S-S0) of Benzene
The experimental data shown in these pages are freely available and have been published already in the DDB Explorer Edition. The data represent a small sub list of all available data in the Dortmund Data Bank. For more data or any further information please search the DDB or contact DDBST.
Component
| Formula |
Molar Mass |
CAS Registry Number |
Name |
| C6H6 |
78.114 |
71-43-2 |
Benzene |
Search the DDB for all data of Benzene
Diagrams
Data Table
| T [K] |
P [kPa] |
Molar Entropy [J/(mol*K)] |
State |
Reference |
| 250.00 |
|
150.24 |
Liquid |
1 |
| 250.00 |
101.325 |
256.84 |
Ideal Gas |
1 |
| 260.00 |
|
155.23 |
Liquid |
1 |
| 260.00 |
101.325 |
259.41 |
Ideal Gas |
1 |
| 280.00 |
|
164.88 |
Liquid |
1 |
| 280.00 |
101.325 |
264.73 |
Ideal Gas |
1 |
| 298.15 |
|
173.27 |
Liquid |
1 |
| 298.15 |
101.325 |
269.64 |
Ideal Gas |
1 |
| 300.00 |
|
174.10 |
Liquid Phase of VLE |
2 |
| 300.00 |
|
174.11 |
Liquid |
1 |
| 300.00 |
|
270.22 |
Ideal Gas |
2 |
| 300.00 |
101.325 |
270.22 |
Ideal Gas |
1 |
| 310.00 |
|
178.62 |
Liquid Phase of VLE |
2 |
| 310.00 |
|
272.96 |
Ideal Gas |
2 |
| 320.00 |
|
183.04 |
Liquid Phase of VLE |
2 |
| 320.00 |
|
183.09 |
Liquid |
1 |
| 320.00 |
|
275.71 |
Ideal Gas |
2 |
| 320.00 |
101.325 |
275.71 |
Ideal Gas |
1 |
| 330.00 |
|
187.39 |
Liquid Phase of VLE |
2 |
| 330.00 |
|
278.53 |
Ideal Gas |
2 |
| 340.00 |
|
191.68 |
Liquid Phase of VLE |
2 |
| 340.00 |
|
191.73 |
Liquid |
1 |
| 340.00 |
|
281.28 |
Ideal Gas |
2 |
| 340.00 |
101.325 |
281.36 |
Ideal Gas |
1 |
| 350.00 |
|
195.92 |
Liquid Phase of VLE |
2 |
| 350.00 |
|
284.02 |
Ideal Gas |
2 |
| 360.00 |
|
200.11 |
Liquid Phase of VLE |
2 |
| 360.00 |
|
200.21 |
Liquid |
1 |
| 360.00 |
|
286.85 |
Ideal Gas |
2 |
| 360.00 |
101.325 |
286.93 |
Ideal Gas |
1 |
| 370.00 |
|
204.25 |
Liquid Phase of VLE |
2 |
| 370.00 |
|
289.59 |
Ideal Gas |
2 |
| 380.00 |
|
208.33 |
Liquid Phase of VLE |
2 |
| 380.00 |
|
208.53 |
Liquid |
1 |
| 380.00 |
|
292.34 |
Ideal Gas |
2 |
| 380.00 |
101.325 |
292.59 |
Ideal Gas |
1 |
| 390.00 |
|
212.35 |
Liquid Phase of VLE |
2 |
| 390.00 |
|
295.00 |
Ideal Gas |
2 |
| 400.00 |
|
216.33 |
Liquid Phase of VLE |
2 |
| 400.00 |
|
216.68 |
Liquid |
1 |
| 400.00 |
|
297.66 |
Ideal Gas |
2 |
| 400.00 |
101.325 |
298.16 |
Ideal Gas |
1 |
| 410.00 |
|
220.28 |
Liquid Phase of VLE |
2 |
| 410.00 |
|
300.23 |
Ideal Gas |
2 |
| 420.00 |
|
224.19 |
Liquid Phase of VLE |
2 |
| 420.00 |
|
224.66 |
Liquid |
1 |
| 420.00 |
|
302.81 |
Ideal Gas |
2 |
| 420.00 |
101.325 |
303.73 |
Ideal Gas |
1 |
| 430.00 |
|
228.07 |
Liquid Phase of VLE |
2 |
| 430.00 |
|
305.39 |
Ideal Gas |
2 |
| 440.00 |
|
231.93 |
Liquid Phase of VLE |
2 |
| 440.00 |
|
232.56 |
Liquid |
1 |
| 440.00 |
|
307.80 |
Ideal Gas |
2 |
| 440.00 |
101.325 |
309.30 |
Ideal Gas |
1 |
| 450.00 |
|
235.78 |
Liquid Phase of VLE |
2 |
| 450.00 |
|
310.21 |
Ideal Gas |
2 |
| 460.00 |
|
239.62 |
Liquid Phase of VLE |
2 |
| 460.00 |
|
240.46 |
Liquid |
1 |
| 460.00 |
|
312.62 |
Ideal Gas |
2 |
| 460.00 |
101.325 |
314.87 |
Ideal Gas |
1 |
| 470.00 |
|
243.46 |
Liquid Phase of VLE |
2 |
| 470.00 |
|
314.87 |
Ideal Gas |
2 |
| 480.00 |
|
247.32 |
Liquid Phase of VLE |
2 |
| 480.00 |
|
248.27 |
Liquid |
1 |
| 480.00 |
|
317.03 |
Ideal Gas |
2 |
| 480.00 |
101.325 |
320.36 |
Ideal Gas |
1 |
| 490.00 |
|
251.20 |
Liquid Phase of VLE |
2 |
| 490.00 |
|
319.02 |
Ideal Gas |
2 |
| 500.00 |
|
255.13 |
Liquid Phase of VLE |
2 |
| 500.00 |
|
256.09 |
Liquid |
1 |
| 500.00 |
|
320.94 |
Ideal Gas |
2 |
| 500.00 |
101.325 |
325.93 |
Ideal Gas |
1 |
| 510.00 |
|
259.11 |
Liquid Phase of VLE |
2 |
| 510.00 |
|
322.68 |
Ideal Gas |
2 |
| 520.00 |
|
263.18 |
Liquid Phase of VLE |
2 |
| 520.00 |
|
264.07 |
Liquid |
1 |
| 520.00 |
|
324.18 |
Ideal Gas |
2 |
| 520.00 |
101.325 |
331.42 |
Ideal Gas |
1 |
| 530.00 |
|
267.38 |
Liquid Phase of VLE |
2 |
| 530.00 |
|
325.34 |
Ideal Gas |
2 |
| 540.00 |
|
271.77 |
Liquid Phase of VLE |
2 |
| 540.00 |
|
272.38 |
Liquid |
1 |
| 540.00 |
|
326.09 |
Ideal Gas |
2 |
| 540.00 |
101.325 |
336.99 |
Ideal Gas |
1 |
| 550.00 |
|
276.55 |
Liquid Phase of VLE |
2 |
| 550.00 |
|
325.26 |
Ideal Gas |
2 |
| 560.00 |
|
282.36 |
Liquid Phase of VLE |
2 |
| 560.00 |
|
324.51 |
Ideal Gas |
2 |
List of References
| Number |
Source |
| 1 |
Chirico R.D.; Steele W.V.: The Importance of the Third Virial Coefficient. Ind.Eng.Chem.Res. 33 (1994) 157-167 |
| 2 |
Steele W.V.; Chirico R.D.; Knipmeyer S.E.; Smith N.K.: High-Temperature Heat-Capacity Measurements and Critical Property Determinations Using a Differential Scanning Calorimeter (Development of Methodology and Application to Pure Organic Compounds). Report (1988) 1-33 |
Pure Component Data Overview
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