Chemical Properties of D-Limonene (CAS 5989-27-5)

InChI

InChI=1S/C10H16/c1-8(2)10-6-4-9(3)5-7-10/h4,10H,1,5-7H2,2-3H3/t10-/m0/s1

InChI Key

XMGQYMWWDOXHJM-JTQLQIEISA-N

Formula

C10H16

SMILES

C=C(C)[C@H]1CC=C(C)CC1

Molecular Weight¹

136.24

CAS

5989-27-5

Other Names

• (+)-(4R)-limonene
• (+)-(R)-Limonene
• (+)-(R)-p-mentha-1,8-diene
• (+)-.alpha.-limonene
• (+)-4-isopropenyl-1-methylcyclohexene
• (+)-dipentene
• (+)-limonene
• (+)-p-mentha-1,8-diene
• (4R)-(+)-limonene
• (4R)-Limonene
• (R)-(+)-limonene
• (R)-(+)-p-mentha-1,8-diene
• (R)-1-methyl-4-(1-methylethenyl)cyclohexene
• (R)-4-isopropenyl-1-methyl-1-cyclohexene
• (R)-limonene
• (R)-p-mentha-1,8-diene
• 4-Isopropenyl-1-methyl-1-cyclohexene-, (R)-
• Biogenic SE 374
• Cyclohexene, 1-methyl-4-(1-methylethenyl)-, (4R)-
• Cyclohexene, 1-methyl-4-(1-methylethenyl)-, (R)-
• D-(+)-limonene
• Dextro-limonene
• EC 7
• Glidesafe
• Glidsafe
• Limonene, (D)-
• Refchole
• carvene
• cyclohexene, 1-methyl-4-(1-methylethenyl)-, (R)-,
• limonene, (+)-
• p-mentha-1,8-diene, (R)-(+)-

• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• ε_r : Dielectric Constant (Relative permittivity).
• Δ_fH°_gas : 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_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety Rating.
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• γ : Surface Tension (N/m).
• 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.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Datasets
4. Correlations
5. Similar Compounds
6. Mixtures
7. Sources

Physical Properties

Property	Value	Unit	Source
ΔcH°liquid	-6167.20 ± 2.10	kJ/mol	NIST
εr	2.38		NCMS SOLV-DB
ΔfH°gas	44.31	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	11.73	kJ/mol	Joback Calculated Property
ΔvapH°	[48.12; 49.90]	kJ/mol
ΔvapH°	48.12	kJ/mol	NCMS SOLV-DB
ΔvapH°	49.50	kJ/mol	NIST
ΔvapH°	49.60	kJ/mol	NIST
ΔvapH°	49.90	kJ/mol	NIST
ΔvapH°	49.60	kJ/mol	NIST
ΔvapH°	48.90 ± 0.10	kJ/mol	NIST
IE	8.65	eV	Relay (1.0) Calculated Property
log10WS	-4.26		Estimated Solubility
logPoct/wat	4.830		NCMS SOLV-DB
McVol	132.300	ml/mol	McGowan Calculated Property
NFPA Fire	2		NCMS SOLV-DB
NFPA Health	1		NCMS SOLV-DB
NFPA Safety	0		NCMS SOLV-DB
Tboil	[448.00; 452.00]	K
Tboil	449.15	K	NCMS SOLV-DB
Tboil	449.00	K	NIST
Tboil	451.00	K	NIST
Tboil	449.40 ± 2.00	K	NIST
Tboil	448.00 ± 4.00	K	NIST
Tboil	451.00 ± 0.50	K	NIST
Tboil	451.00 ± 0.50	K	NIST
Tboil	451.00 ± 1.00	K	NIST
Tboil	449.40 ± 3.00	K	NIST
Tboil	451.00 ± 3.00	K	NIST
Tboil	449.00 ± 3.00	K	NIST
Tboil	451.00 ± 2.00	K	NIST
Tboil	449.90 ± 3.00	K	NIST
Tboil	449.70 ± 3.00	K	NIST
Tboil	449.50 ± 3.00	K	NIST
Tboil	452.00 ± 3.00	K	NIST
Tboil	449.00 ± 6.00	K	NIST
Tboil	448.00 ± 4.00	K	NIST
Tboil	449.00 ± 4.00	K	NIST
Tc	653.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Tfus	[198.65; 198.85]	K
Tfus	198.85	K	NCMS SOLV-DB
Tfus	198.65 ± 0.15	K	NIST
Vc	0.470	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value

Cheméo can also estimate Critical Pressure, Standard Gibbs free energy of formation, Acentric Factor for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
η	[0.0003820; 0.0010780]	Pa×s	[283.15; 373.15]
η	0.0010780	Pa×s	283.15	Density, Viscosity, and Refractive Index in the Range (283.15 to 353.15) K and Vapor Pressure of r-Pinene, d-Limonene, (()-Linalool, and Citral Over the Pressure Range 1.0 kPa Atmospheric Pressure
η	0.0009020	Pa×s	293.15	Density, viscosity, vapour liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures
η	0.0009320	Pa×s	293.15	Density, Viscosity, and Refractive Index in the Range (283.15 to 353.15) K and Vapor Pressure of r-Pinene, d-Limonene, (()-Linalool, and Citral Over the Pressure Range 1.0 kPa Atmospheric Pressure
η	0.0008900	Pa×s	298.15	Density, viscosity, vapour liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures
η	0.0009230	Pa×s	298.15	NCMS SOLV-DB
η	0.0008970	Pa×s	298.15	Density, Viscosity, and Refractive Index in the Range (283.15 to 353.15) K and Vapor Pressure of r-Pinene, d-Limonene, (()-Linalool, and Citral Over the Pressure Range 1.0 kPa Atmospheric Pressure
η	0.0007930	Pa×s	303.15	Density, viscosity, vapour liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures
η	0.0008160	Pa×s	303.15	Density, Viscosity, and Refractive Index in the Range (283.15 to 353.15) K and Vapor Pressure of r-Pinene, d-Limonene, (()-Linalool, and Citral Over the Pressure Range 1.0 kPa Atmospheric Pressure
η	0.0007020	Pa×s	313.15	Density, viscosity, vapour liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures
η	0.0007220	Pa×s	313.15	Density, Viscosity, and Refractive Index in the Range (283.15 to 353.15) K and Vapor Pressure of r-Pinene, d-Limonene, (()-Linalool, and Citral Over the Pressure Range 1.0 kPa Atmospheric Pressure
η	0.0006450	Pa×s	323.15	Density, Viscosity, and Refractive Index in the Range (283.15 to 353.15) K and Vapor Pressure of r-Pinene, d-Limonene, (()-Linalool, and Citral Over the Pressure Range 1.0 kPa Atmospheric Pressure
η	0.0006280	Pa×s	323.15	Density, viscosity, vapour liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures
η	0.0005660	Pa×s	333.15	Density, viscosity, vapour liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures
η	0.0005800	Pa×s	333.15	Density, Viscosity, and Refractive Index in the Range (283.15 to 353.15) K and Vapor Pressure of r-Pinene, d-Limonene, (()-Linalool, and Citral Over the Pressure Range 1.0 kPa Atmospheric Pressure
η	0.0005000	Pa×s	343.15	Density, viscosity, vapour liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures
η	0.0005240	Pa×s	343.15	Density, Viscosity, and Refractive Index in the Range (283.15 to 353.15) K and Vapor Pressure of r-Pinene, d-Limonene, (()-Linalool, and Citral Over the Pressure Range 1.0 kPa Atmospheric Pressure
η	0.0004520	Pa×s	353.15	Density, viscosity, vapour liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures
η	0.0004760	Pa×s	353.15	Density, Viscosity, and Refractive Index in the Range (283.15 to 353.15) K and Vapor Pressure of r-Pinene, d-Limonene, (()-Linalool, and Citral Over the Pressure Range 1.0 kPa Atmospheric Pressure
η	0.0004130	Pa×s	363.15	Density, viscosity, vapour liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures
η	0.0003820	Pa×s	373.15	Density, viscosity, vapour liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures
ΔfusH	11.38	kJ/mol	199.20	NIST
ΔvapH	[37.90; 49.20]	kJ/mol	[305.50; 417.00]
ΔvapH	47.70	kJ/mol	305.50	NIST
ΔvapH	49.20	kJ/mol	342.00	NIST
ΔvapH	44.50	kJ/mol	367.50	NIST
ΔvapH	46.10 ± 0.20	kJ/mol	417.00	NIST
ΔvapH	43.50 ± 0.20	kJ/mol	417.00	NIST
ΔvapH	40.90 ± 0.30	kJ/mol	417.00	NIST
ΔvapH	37.90 ± 0.60	kJ/mol	417.00	NIST
Pvap	[1.01e-03; 2.67]	kPa	[238.20; 341.15]
Pvap	1.01e-03	kPa	238.20	Thermodynamic study of selected monoterpenes III
Pvap	1.01e-03	kPa	238.20	Thermodynamic study of selected monoterpenes III
Pvap	1.01e-03	kPa	238.20	Thermodynamic study of selected monoterpenes III
Pvap	1.76e-03	kPa	243.20	Thermodynamic study of selected monoterpenes III
Pvap	1.76e-03	kPa	243.20	Thermodynamic study of selected monoterpenes III
Pvap	1.76e-03	kPa	243.20	Thermodynamic study of selected monoterpenes III
Pvap	2.96e-03	kPa	248.15	Thermodynamic study of selected monoterpenes III
Pvap	2.96e-03	kPa	248.15	Thermodynamic study of selected monoterpenes III
Pvap	2.96e-03	kPa	248.15	Thermodynamic study of selected monoterpenes III
Pvap	4.89e-03	kPa	253.15	Thermodynamic study of selected monoterpenes III
Pvap	4.89e-03	kPa	253.15	Thermodynamic study of selected monoterpenes III
Pvap	4.89e-03	kPa	253.15	Thermodynamic study of selected monoterpenes III
Pvap	7.90e-03	kPa	258.15	Thermodynamic study of selected monoterpenes III
Pvap	7.90e-03	kPa	258.15	Thermodynamic study of selected monoterpenes III
Pvap	7.90e-03	kPa	258.15	Thermodynamic study of selected monoterpenes III
Pvap	0.01	kPa	263.15	Thermodynamic study of selected monoterpenes III
Pvap	0.01	kPa	263.15	Thermodynamic study of selected monoterpenes III
Pvap	0.01	kPa	263.15	Thermodynamic study of selected monoterpenes III
Pvap	0.02	kPa	268.15	Thermodynamic study of selected monoterpenes III
Pvap	0.02	kPa	268.15	Thermodynamic study of selected monoterpenes III
Pvap	0.02	kPa	268.15	Thermodynamic study of selected monoterpenes III
Pvap	0.03	kPa	273.15	Thermodynamic study of selected monoterpenes III
Pvap	0.03	kPa	273.15	Thermodynamic study of selected monoterpenes III
Pvap	0.03	kPa	273.15	Thermodynamic study of selected monoterpenes III
Pvap	0.03	kPa	273.65	Thermodynamic study of selected monoterpenes III
Pvap	0.03	kPa	273.65	Thermodynamic study of selected monoterpenes III
Pvap	0.03	kPa	273.65	Thermodynamic study of selected monoterpenes III
Pvap	0.04	kPa	278.15	Thermodynamic study of selected monoterpenes III
Pvap	0.04	kPa	278.15	Thermodynamic study of selected monoterpenes III
Pvap	0.04	kPa	278.15	Thermodynamic study of selected monoterpenes III
Pvap	0.07	kPa	283.15	Thermodynamic study of selected monoterpenes III
Pvap	0.07	kPa	283.15	Thermodynamic study of selected monoterpenes III
Pvap	0.07	kPa	283.15	Thermodynamic study of selected monoterpenes III
Pvap	0.09	kPa	288.15	Thermodynamic study of selected monoterpenes III
Pvap	0.09	kPa	288.15	Thermodynamic study of selected monoterpenes III
Pvap	0.09	kPa	288.15	Thermodynamic study of selected monoterpenes III
Pvap	0.13	kPa	293.15	Thermodynamic study of selected monoterpenes III
Pvap	0.13	kPa	293.15	Thermodynamic study of selected monoterpenes III
Pvap	0.13	kPa	293.15	Thermodynamic study of selected monoterpenes III
Pvap	0.19	kPa	298.15	Thermodynamic study of selected monoterpenes III
Pvap	0.19	kPa	298.15	Thermodynamic study of selected monoterpenes III
Pvap	0.19	kPa	298.15	Thermodynamic study of selected monoterpenes III
Pvap	0.26	kPa	303.15	Thermodynamic study of selected monoterpenes III
Pvap	0.26	kPa	303.15	Thermodynamic study of selected monoterpenes III
Pvap	0.26	kPa	303.15	Thermodynamic study of selected monoterpenes III
Pvap	0.36	kPa	308.15	Thermodynamic study of selected monoterpenes III
Pvap	0.36	kPa	308.15	Thermodynamic study of selected monoterpenes III
Pvap	0.36	kPa	308.15	Thermodynamic study of selected monoterpenes III
Pvap	2.67	kPa	341.15	NCMS SOLV-DB
n0	[1.47000; 1.47300]		[293.20; 298.15]
n0	1.47300		293.20	Vapor Liquid Equilibrium Data for Binary Systems of 1-Methyl-4-(1-methylethenyl)-cyclohexene + {Ethanol, Propan-1-ol, Propan-2-ol, Butan-1-ol, Pentan-1-ol, or Hexan-1-ol} at 40 kPa
n0	1.47081		298.15	Deterpenation of Citrus Essential Oil by Liquid-Liquid Extraction with 1-Alkyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)amide Ionic Liquids
n0	1.47000		298.15	NCMS SOLV-DB
ρl	[837.31; 841.35]	kg/m3	[298.15; 298.20]
ρl	838.68	kg/m3	298.15	Improved concentration of citrus essential oil by solvent extraction with acetate ionic liquids
ρl	837.31	kg/m3	298.15	Ternary and quaternary (liquid + liquid) equilibria for (water + ethanol + a-pinene, +b-pinene, or +limonene) and (water + ethanol + a-pinene + limonene) at the temperature 298.15 K
ρl	837.31	kg/m3	298.15	Temperature dependence on mutual solubility of binary (methanol + limonene) mixture and (liquid + liquid) equilibria of ternary (methanol + ethanol + limonene) mixture
ρl	837.31	kg/m3	298.15	Mutual Solubilities of Terpene in Methanol and Water and Their Multicomponent Liquid-Liquid Equilibria
ρl	841.35	kg/m3	298.20	Fractionation of orange essential oil using liquid-liquid extraction: Equilibrium data for model and real systems at 298.2 K.
ρl	840.73	kg/m3	298.20	Deterpenation of Citrus Essential Oils Using Glycerol-Based Deep Eutectic Solvents
ρl	841.35	kg/m3	298.20	Physical Behavior of the Phases from the Liquid-Liquid Equilibrium of Citrus Essential Oils Systems at 298.2 K
γ	0.03	N/m	298.15	NCMS SOLV-DB

Datasets

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	20000.00	862.0
283.15	25000.00	864.9
283.15	30000.00	867.7
283.15	35000.00	870.4
283.15	40000.00	873.3
298.15	20000.00	851.5
298.15	25000.00	854.5
298.15	30000.00	857.6
298.15	35000.00	860.9
298.15	40000.00	863.4
313.15	20000.00	841.0
313.15	25000.00	844.2
313.15	30000.00	847.2
313.15	35000.00	850.3
313.15	40000.00	853.3
328.15	20000.00	830.5
328.15	25000.00	833.8
328.15	30000.00	837.2
328.15	35000.00	840.4
328.15	40000.00	843.8
343.15	20000.00	820.1
343.15	25000.00	823.7
343.15	30000.00	827.3
343.15	35000.00	831.1
343.15	40000.00	834.6
358.15	20000.00	810.2
358.15	25000.00	813.9
358.15	30000.00	817.6
358.15	35000.00	821.3
358.15	40000.00	824.8
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	298.20	838.59
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
101.80	298.15	838.59
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	839.1
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	20000.00	862.0
283.15	25000.00	864.9
283.15	30000.00	867.7
283.15	35000.00	870.4
283.15	40000.00	873.3
298.15	20000.00	851.5
298.15	25000.00	854.5
298.15	30000.00	857.6
298.15	35000.00	860.9
298.15	40000.00	863.4
313.15	20000.00	841.0
313.15	25000.00	844.2
313.15	30000.00	847.2
313.15	35000.00	850.3
313.15	40000.00	853.3
328.15	20000.00	830.5
328.15	25000.00	833.8
328.15	30000.00	837.2
328.15	35000.00	840.4
328.15	40000.00	843.8
343.15	20000.00	820.1
343.15	25000.00	823.7
343.15	30000.00	827.3
343.15	35000.00	831.1
343.15	40000.00	834.6
358.15	20000.00	810.2
358.15	25000.00	813.9
358.15	30000.00	817.6
358.15	35000.00	821.3
358.15	40000.00	824.8
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[165.92; 457.19]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			-5.24100e+01
Coefficient B			9.40340e-01
Coefficient C			-5.46640e-04
Coefficient D			1.15900e-07
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	165.92	J/mol×K	273.00	Calculated Property
Cp,gas	216.98	J/mol×K	353.78	Calculated Property
Cp,gas	262.50	J/mol×K	434.56	Calculated Property
Cp,gas	302.87	J/mol×K	515.33	Calculated Property
Cp,gas	338.44	J/mol×K	596.11	Calculated Property
Cp,gas	369.58	J/mol×K	676.89	Calculated Property
Cp,gas	396.66	J/mol×K	757.67	Calculated Property
Cp,gas	420.04	J/mol×K	838.44	Calculated Property
Cp,gas	440.10	J/mol×K	919.22	Calculated Property
Cp,gas	457.19	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[324.43; 480.94]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.42584e+01
Coefficient B			-3.89401e+03
Coefficient C			-4.57090e+01
Temperature range, min.			324.43
Temperature range, max.			480.94
Pvap	1.33	kPa	324.43	Calculated Property
Pvap	3.03	kPa	341.82	Calculated Property
Pvap	6.28	kPa	359.21	Calculated Property
Pvap	12.06	kPa	376.60	Calculated Property
Pvap	21.71	kPa	393.99	Calculated Property
Pvap	36.95	kPa	411.38	Calculated Property
Pvap	59.91	kPa	428.77	Calculated Property
Pvap	93.16	kPa	446.16	Calculated Property
Pvap	139.63	kPa	463.55	Calculated Property
Pvap	202.63	kPa	480.94	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.01]	N/m	[176.65; 451.15]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			5.48756e-02
Coefficient B			-9.29000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			176.65
Temperature range, max.			451.15
γ	0.04	N/m	176.65	Calculated Property
γ	0.04	N/m	207.15	Calculated Property
γ	0.03	N/m	237.65	Calculated Property
γ	0.03	N/m	268.15	Calculated Property
γ	0.03	N/m	298.65	Calculated Property
γ	0.02	N/m	329.15	Calculated Property
γ	0.02	N/m	359.65	Calculated Property
γ	0.02	N/m	390.15	Calculated Property
γ	0.02	N/m	420.65	Calculated Property
γ	0.01	N/m	451.15	Calculated Property

Similar Compounds

Find more compounds similar to D-Limonene.

Mixtures

• Carbon dioxide + D-Limonene
• D-Limonene + Ethanol + Water
• D-Limonene + Bicyclo[3.1.1]heptane, 6,6-dimethyl-2-methylene-, (1S)-
• Acetonitrile + D-Limonene
• D-Limonene + Water
• D-Limonene + Water + Linalool
• D-Limonene + Acetone + Water
• D-Limonene + 1-Pentanol
• D-Limonene + Methyl Alcohol
• D-Limonene + Ethanol + Methyl Alcohol
• Carbon dioxide + D-Limonene + Ethanol
• Acetonitrile + D-Limonene + Water
• D-Limonene + Methyl Alcohol + Water
• D-Limonene + Water + (1S)-2,6,6-Trimethylbicyclo[3.1.1]hept-2-ene
• D-Limonene + Methyl Alcohol + (1S)-2,6,6-Trimethylbicyclo[3.1.1]hept-2-ene
• D-Limonene + (1S)-2,6,6-Trimethylbicyclo[3.1.1]hept-2-ene
• D-Limonene + 1-Hexanol
• D-Limonene + Ethanol
• 1-Propanol + D-Limonene
• 2-Propanol + D-Limonene

Find more mixtures with D-Limonene.

Sources

• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 ChEDL chemicals 1.5.2, from Tsonopoulos, C.; Ambrose, D. Vapor-Liquid Critical Properties of Elements and Compounds. 6. Unsaturated Aliphatic Hydrocarbons. J. Chem. Eng. Data 1996, 41, 645-656.
• Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
• Cheméo Relay (1.0)
• Cheméo Relay (1.0, beta) Beta: served but experimental, data-limited and below our cross-validation release bar; the Joback value is recommended where available.
• Measurement of activity coefficients at infinite dilution for acetonitrile, water, limonene, limonene epoxide and their binary pairs
• Density, viscosity, vapour liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures
• Improved concentration of citrus essential oil by solvent extraction with acetate ionic liquids
• Fractionation of orange essential oil using liquid-liquid extraction: Equilibrium data for model and real systems at 298.2 K.
• Solubility of three natural compounds with insecticidal activity in supercritical carbon dioxide: Experimental measurements and predictive modeling with the GC-EoS
• Ternary and quaternary (liquid + liquid) equilibria for (water + ethanol + a-pinene, +b-pinene, or +limonene) and (water + ethanol + a-pinene + limonene) at the temperature 298.15 K
• (Liquid + liquid) equilibria of (water + linalool + limonene) ternary system at T = (298.15, 308.15, and 318.15) K
• Temperature dependence on mutual solubility of binary (methanol + limonene) mixture and (liquid + liquid) equilibria of ternary (methanol + ethanol + limonene) mixture
• (Ternary liquid + liquid) equilibria for (water + acetone + alpha-pinene, or beta-pinene, or limonene) mixtures
• P, rho, and T measurements of the (limonene + beta-pinene) mixtures
• Deterpenation of eucalyptus essential oil by liquid + liquid extraction: Phase equilibrium and physical properties for model systems at T = 298.2 K
• Viscosities and densities of systems involved in the deterpenation of essential oils by liquid-liquid extraction: New UNIFAC-VISCO parameters
• Thermodynamic study of selected monoterpenes III
• Deterpenation of Citrus Essential Oils Using Glycerol-Based Deep Eutectic Solvents
• Physical Behavior of the Phases from the Liquid-Liquid Equilibrium of Citrus Essential Oils Systems at 298.2 K
• Physical Properties of Model and Real Systems Composed of Essential Oils and Hydroalcoholic Solvents at 298.2 K and Atmospheric Pressure
• Liquid-Liquid Equilibrium for the Water + Acetonitrile + Limonene System at different temperatures
• Entrainer Effect of Ethanol on High-Pressure Vapor-Liquid Equilibria for Supercritical Carbon Dioxide + Limonene + Linalool System
• Mutual Solubilities of Terpene in Methanol and Water and Their Multicomponent Liquid-Liquid Equilibria
• P, rho, and T Measurements of the Limonene + alpha-Pinene Mixtures
• Deterpenation of Citrus Essential Oil by Liquid-Liquid Extraction with 1-Alkyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)amide Ionic Liquids
• Vapor Liquid Equilibrium Data for Binary Systems of 1-Methyl-4-(1-methylethenyl)-cyclohexene + {Ethanol, Propan-1-ol, Propan-2-ol, Butan-1-ol, Pentan-1-ol, or Hexan-1-ol} at 40 kPa
• Vapor Liquid Equilibria Measurements of Bitter Orange Aroma Compounds Highly Diluted in Boiling Hydro-Alcoholic Solutions at 101.3 kPa
• Henry s Law Constants for Fragrance and Organic Solvent Compounds in Aqueous Industrial Surfactants
• Density, Viscosity, and Refractive Index in the Range (283.15 to 353.15) K and Vapor Pressure of r-Pinene, d-Limonene, (()-Linalool, and Citral Over the Pressure Range 1.0 kPa Atmospheric Pressure
• Joback Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure

Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.
Calculated This icon marks a calculated value or equation: a prediction, not a measurement.
Compiled This icon marks a compiled value or equation: taken from a data compilation such as ChemSep, not from an original measurement report.
These property values are available through the Cheméo API. A free account gives you an access key.