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Dortmund Data Bank
Thermophysical Data for Process Design
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DDB#	Name	CAS-RN	Formula
84	Acetic acid	64-19-7	C₂H₄O₂	Overview	Details
174	Water	7732-18-5	H₂O	Overview	Details

Databank		Sets	Points	Temperature Range	Pressure Range
Vapor-Liquid Equilibria	VLE	184	2525	273-598 K	1-7440 kPa
Heats of Mixing	HE	37	480	281-353 K	100 kPa (const.)
Gas Solubilities	GLE	5	11	293-313 K	0 kPa (const.)
Activity Coefficients at Infinite Dilution (Pure Solvents)	ACT	12	12	298-391 K	n.a.
Heat Capacities of Mixtures, Excess Heat Capacities	CPE	36	345	273-393 K	n.a.
(A)zeotropic Data	AZD	159	159	293-503 K	1-6865 kPa
Solid-Liquid Equilibria	SLE	22	255	243-290 K	85 kPa (const.)
Vapor-Liquid Equilibria of Electrolyte Systems	ELE	2	36	270-298 K	1 kPa (const.)
Densities and Volumes of Mixtures, Excess Volumes	VE	109	1122	278-368 K	95-101 kPa
Critical Data of Mixtures	CRI	2	18	593-649 K	n.a.
Mixture Viscosities	VIS	78	1227	273-473 K	100-3200 kPa
Mixture Surface Tensions	MSFT	17	276	283-323 K	101 kPa (const.)
Mixture Speeds of Sound	MSOS	7	117	283-353 K	101 kPa (const.)
Mixture Thermal Conductivities	MTCN	4	56	293-425 K	n.a.
Mixture Dielectric Constants	MDEC	2	36	293-298 K	91 kPa (const.)
Mixture P-v-T Data	MPVT	1	262	373-503 K	6-2779 kPa
Mixture Flash Points	MFLP	1	8	314-343 K	n.a.
Electrical Conductivities	ECND	20	380	278-821 K	100-20821 kPa
Diffusion Coefficients	DIF	3	16	288-318 K	n.a.
Further Thermodynamic Properties	X	61	626	246-674 K	100-32300 kPa
Total		762	7967

n.a. = not available or not given

Some data for this system can be found in our DDB Explorer Version.

Dortmund Data Bank Version: February 2024

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