Chemical Properties of Erythritol (CAS 149-32-6)

InChI

InChI=1S/C4H10O4/c5-1-3(7)4(8)2-6/h3-8H,1-2H2/t3-,4+

InChI Key

UNXHWFMMPAWVPI-ZXZARUISSA-N

Formula

C4H10O4

SMILES

OCC(O)C(O)CO

Molecular Weight¹

122.12

CAS

149-32-6

Other Names

• (R*,S*)-1,2,3,4-butanetetrol
• 1,2,3,4-Butanetetrol, (2R,3S)-rel-
• 1,2,3,4-Butanetetrol, (R*,S*)-
• 1,2,3,4-Tetrahydroxybutane, (R*,S*)-
• 2(R),3(S)-1,2,3,4-Butanetetrol
• Antierythrite
• C*Eridex
• Erythrit
• Erythrite
• Erythritol, meso-
• Erythroglucin
• Erythrol
• L-Erythritol
• Lichen sugar
• NIK 242
• NSC 8099
• Paycite
• Phycitol
• TETRAHYDOXYBUTANE
• meso-1,2,3,4-butanetetrol
• meso-Erythritol

• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• Δ_cH°_solid : Standard solid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,solid : Solid phase heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_subH° : Enthalpy of sublimation at standard conditions (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_{solid,1 bar} : Solid phase molar entropy at standard conditions (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ΔcH°liquid	-2092.80 ± 1.30	kJ/mol	NIST
ΔcH°solid	-2118.00	kJ/mol	NIST
ΔfG°	-569.36	kJ/mol	Joback Calculated Property
ΔfH°gas	-745.37	kJ/mol	Joback Calculated Property
ΔfH°liquid	-910.48 ± 0.54	kJ/mol	NIST
ΔfusH°	39.93	kJ/mol	Measure...
ΔsubH°	[135.00; 157.00]	kJ/mol
ΔsubH°	140.00	kJ/mol	NIST
ΔsubH°	157.00	kJ/mol	NIST
ΔsubH°	135.00	kJ/mol	NIST
ΔvapH°	93.30	kJ/mol	NIST
log10WS	[0.70; 0.70]
log10WS	0.70		Aq. Sol...
log10WS	0.70		Estimat...
logPoct/wat	-2.307		Crippen Calculated Property
McVol	90.700	ml/mol	McGowan Calculated Property
Pc	6740.71	kPa	Joback Calculated Property
S°solid,1 bar	[166.50; 177.80]	J/mol×K
S°solid,1 bar	166.50	J/mol×K	NIST
S°solid,1 bar	177.80	J/mol×K	NIST
Tboil	603.70	K	NIST
Tc	819.90	K	Joback Calculated Property
Tfus	[390.50; 394.90]	K
Tfus	394.90	K	Aq. Sol...
Tfus	392.05	K	KDB
Tfus	390.50	K	Solid-l...
Tfus	394.82	K	Heat ca...
Tfus	390.90 ± 0.20	K	NIST
Tfus	391.60 ± 0.20	K	NIST
Vc	0.324	m3/kmol	Joback Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[248.93; 277.70]	J/mol×K	[658.76; 819.90]
T(K) Ideal gas heat capacity (J/mol×K) 250 255 260 265 270 275 280 700 750 800
Cp,gas	248.93	J/mol×K	658.76	Joback Calculated Property
Cp,gas	254.30	J/mol×K	685.62	Joback Calculated Property
Cp,gas	259.43	J/mol×K	712.47	Joback Calculated Property
Cp,gas	264.33	J/mol×K	739.33	Joback Calculated Property
Cp,gas	269.00	J/mol×K	766.19	Joback Calculated Property
Cp,gas	273.46	J/mol×K	793.04	Joback Calculated Property
Cp,gas	277.70	J/mol×K	819.90	Joback Calculated Property
Cp,solid	[161.90; 170.70]	J/mol×K	[291.70; 303.00]
Cp,solid	161.90	J/mol×K	291.70	NIST
Cp,solid	170.70	J/mol×K	303.00	NIST
η	[0.0000022; 0.0672433]	Pa×s	[348.12; 658.76]
T(K) Dynamic viscosity (Pa×s) 0 0.01 0.02 0.03 0.04 0.05 0.06 0.07 400 500 600
η	0.0672433	Pa×s	348.12	Joback Calculated Property
η	0.0039218	Pa×s	399.89	Joback Calculated Property
η	0.0004388	Pa×s	451.67	Joback Calculated Property
η	0.0000770	Pa×s	503.44	Joback Calculated Property
η	0.0000187	Pa×s	555.21	Joback Calculated Property
η	0.0000058	Pa×s	606.99	Joback Calculated Property
η	0.0000022	Pa×s	658.76	Joback Calculated Property
ΔfusH	[38.90; 42.36]	kJ/mol	[381.60; 396.00]
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 39 39.5 40 40.5 41 41.5 42 42.5 385 390 395
ΔfusH	42.36	kJ/mol	381.60	NIST
ΔfusH	39.40	kJ/mol	390.90	NIST
ΔfusH	38.90	kJ/mol	391.20	NIST
ΔfusH	40.30	kJ/mol	392.20	NIST
ΔfusH	42.36	kJ/mol	396.00	NIST
ΔvapH	[93.30; 113.60]	kJ/mol	[397.50; 412.50]
ΔvapH	93.30	kJ/mol	397.50	NIST
ΔvapH	97.00 ± 1.00	kJ/mol	398.00	NIST
ΔvapH	113.60 ± 1.10	kJ/mol	412.50	NIST
ΔfusS	[100.80; 111.00]	J/mol×K	[381.60; 390.90]
ΔfusS	111.00	J/mol×K	381.60	NIST
ΔfusS	100.80	J/mol×K	390.90	NIST

Similar Compounds

Find more compounds similar to Erythritol.

Mixtures

• Vitamin C + Erythritol + Water
• Erythritol + Water
• Ethanol + Erythritol + Methyl Alcohol
• Ethanol + Erythritol
• Erythritol + Methyl Alcohol
• Acetone + Erythritol
• Ethanol + Erythritol + Water
• Erythritol + Methyl Alcohol + Water
• Erythritol + Tetrahydrofuran + Water

Sources

• Crippen Method
• Isopiestic determination of osmotic and activity coefficients of aqueous solutions of aliphatic polyols at 298.15K
• Solubility of erythritol in methanol, ethanol and methanol + ethanol: Experimental measurement and thermodynamic modeling
• Solid-liquid phase equilibria in binary mixtures of functionalized ionic liquids with sugar alcohols: New experimental data and modelling
• Partitioning of diuron in a novel aqueous two-phase system based on polyols and tetrahydrofuran
• Apparent molar volumes and apparent molar heat capacities of aqueous adonitol, dulcitol, glycerol, meso-erythritol, myo-inositol, D-sorbitol, and xylitol at temperatures from (278.15 to 368.15) K and at the pressure 0.35 MPa
• Heat capacities of some sugar alcohols as phase change materials for thermal energy storage applications
• Enthalpies of dilution of aqueous solutions of n-butanol, butanediols, 1,2,4-butanetriol, and 1,2,3,4-butanetetrol at 298.15K
• Measurement of enthalpy curves of phase change materials via DSC and T-History: When are both methods needed to estimate the behaviour of the bulk material in applications?
• Densities and Viscosities of Sugar Alcohols in Vitamin B6 Aqueous Solutions at (293.15 to 323.15) K
• Solubility of Erythritol in Different Solvents
• Densities and Viscosities of Erythritol, Xylitol, and Mannitol in l-ascorbic Acid Aqueous Solutions at T = (293.15 to 323.15) K
• Densities and Viscosities of Sugar Alcohol Aqueous Solutions
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook

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