Dortmund Data Bank

Excess Volume Data

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.

Excess Volume Data Set 13060

Components

No.	Formula	Molar Mass	CAS Registry Number	Name
1	C₃H₆O	58.080	67-64-1	Acetone
2	CH₄O	32.042	67-56-1	Methanol
3	C₆H₁₄	86.177	110-54-3	Hexane

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Constant Value

Temperature	278.150	K
Pressure	1.0132	bar

Data Table

Excess Volume [cm³/mol]	x₁ [mol/mol]	x₂ [mol/mol]
0.0790	0.05600	0.89290
0.3290	0.06890	0.09060
0.1740	0.07330	0.82190
0.4350	0.10140	0.13150
0.1460	0.10560	0.78840
0.2500	0.11670	0.70020
0.4660	0.12150	0.21080
0.4480	0.12160	0.29670
0.3930	0.14150	0.40640
0.2970	0.15170	0.59540
0.3520	0.16180	0.49200
0.5760	0.20040	0.12150
0.3510	0.20310	0.49310
0.0550	0.20460	0.69240
0.4860	0.20540	0.30180
0.4240	0.20930	0.39410
0.2370	0.21220	0.58630
0.5510	0.21480	0.20430
0.3580	0.29600	0.40190
0.0250	0.29780	0.59750
0.2380	0.29960	0.50080
0.4780	0.30260	0.29630
0.6510	0.30640	0.11970
0.5770	0.30940	0.19350
0.2280	0.39670	0.40140
0.0140	0.39700	0.49580
0.4160	0.39930	0.29670
0.7090	0.40450	0.10050
0.5690	0.41220	0.18550
0.4770	0.49230	0.20850
0.3060	0.49700	0.28640
0.6700	0.50020	0.10650
0.0320	0.50680	0.38580
0.5830	0.58210	0.11930
0.3610	0.59860	0.19430
0.0730	0.60720	0.28500
0.2460	0.64320	0.19590
0.4470	0.69090	0.10200
-0.0390	0.74100	0.20760
0.2010	0.79810	0.10250

Reference

Source
Iglesias M.; Orge B.; Pineiro M.M.; Marino G.; Tojo J.: Volumetric properties prediction by cubic EOS for non-ideal mixtures: application to the ternary system acetone + methanol + n-hexane. Thermochim.Acta 328 (1999) 265-275

Excess Volume Data Set 13061

Components

No.	Formula	Molar Mass	CAS Registry Number	Name
1	C₃H₆O	58.080	67-64-1	Acetone
2	CH₄O	32.042	67-56-1	Methanol
3	C₆H₁₄	86.177	110-54-3	Hexane

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Constant Value

Temperature	288.150	K
Pressure	1.0132	bar

Data Table

Excess Volume [cm³/mol]	x₁ [mol/mol]	x₂ [mol/mol]
0.0910	0.05580	0.89340
0.4870	0.06540	0.08440
0.3650	0.07050	0.73330
0.4120	0.09690	0.64650
0.3600	0.09860	0.69650
0.5930	0.10390	0.21760
0.5280	0.10420	0.42240
0.1880	0.10610	0.78540
0.5840	0.10980	0.31370
0.6090	0.11460	0.12460
0.4920	0.11500	0.49120
0.6020	0.11910	0.26140
0.4590	0.12070	0.55200
0.6020	0.19710	0.30430
0.7290	0.20270	0.10860
0.0830	0.20460	0.69290
0.4260	0.20630	0.49680
0.3010	0.21110	0.58760
0.5320	0.21470	0.38750
0.6850	0.21510	0.20460
0.7010	0.28900	0.20730
0.0670	0.28990	0.60130
0.2820	0.29670	0.50370
0.7930	0.29820	0.11850
0.4410	0.29920	0.40380
0.6070	0.30900	0.28360
0.2820	0.38720	0.41660
0.7990	0.38840	0.11870
0.4990	0.39330	0.29960
0.0510	0.39870	0.49390
0.6720	0.40000	0.19940
0.5510	0.48880	0.21460
0.0740	0.49300	0.39500
0.3450	0.49680	0.29520
0.7730	0.50170	0.10570
0.6420	0.57790	0.12440
0.1150	0.59290	0.29550
0.4130	0.59470	0.19980
0.4860	0.69200	0.11360
0.1620	0.68700	0.20540
0.2310	0.79050	0.10860

Reference

Source
Iglesias M.; Orge B.; Pineiro M.M.; Marino G.; Tojo J.: Volumetric properties prediction by cubic EOS for non-ideal mixtures: application to the ternary system acetone + methanol + n-hexane. Thermochim.Acta 328 (1999) 265-275

Excess Volume Data Set 13062

Components

No.	Formula	Molar Mass	CAS Registry Number	Name
1	C₃H₆O	58.080	67-64-1	Acetone
2	CH₄O	32.042	67-56-1	Methanol
3	C₆H₁₄	86.177	110-54-3	Hexane

Search the DDB for all data of this mixture

Constant Value

Temperature	298.150	K
Pressure	1.0132	bar

Data Table

Excess Volume [cm³/mol]	x₁ [mol/mol]	x₂ [mol/mol]
0.4240	0.05310	0.70530
0.4750	0.05370	0.59770
0.5320	0.05470	0.40570
0.5510	0.08780	0.14080
0.5540	0.09430	0.41450
0.5140	0.09740	0.50810
0.1650	0.09950	0.79090
0.5870	0.10030	0.21860
0.4410	0.10030	0.60650
0.5840	0.10180	0.31320
0.3360	0.10190	0.70140
0.7200	0.19180	0.12010
0.6220	0.19220	0.31470
0.2930	0.19660	0.60890
0.0740	0.19730	0.70050
0.0850	0.20060	0.69990
0.6930	0.20070	0.20860
0.4370	0.20080	0.50350
0.5530	0.20120	0.39710
0.4550	0.29030	0.41850
0.2830	0.29100	0.51370
0.0340	0.29130	0.61070
0.8350	0.29420	0.11800
0.7400	0.29530	0.19950
0.5860	0.30760	0.32030
0.8320	0.38370	0.13190
0.2870	0.38570	0.42130
0.5270	0.39010	0.30950
0.7070	0.39550	0.20740
0.0300	0.39750	0.50390
0.5880	0.48660	0.21950
0.0590	0.49370	0.40450
0.3590	0.50250	0.29640
0.8200	0.50310	0.10440
0.6900	0.57640	0.12520
0.4210	0.59390	0.20760
0.1090	0.61190	0.28450
0.1360	0.67820	0.22250
0.4900	0.68750	0.11810
0.2380	0.78850	0.11200

Reference

Source
Iglesias M.; Orge B.; Pineiro M.M.; Marino G.; Tojo J.: Volumetric properties prediction by cubic EOS for non-ideal mixtures: application to the ternary system acetone + methanol + n-hexane. Thermochim.Acta 328 (1999) 265-275

List of All References

Source
Iglesias M.; Orge B.; Pineiro M.M.; Marino G.; Tojo J.: Volumetric properties prediction by cubic EOS for non-ideal mixtures: application to the ternary system acetone + methanol + n-hexane. Thermochim.Acta 328 (1999) 265-275

Excess Volume Data Overview