Chemical Properties of Diethyl carbitol (CAS 112-36-7)

InChI

InChI=1S/C8H18O3/c1-3-9-5-7-11-8-6-10-4-2/h3-8H2,1-2H3

InChI Key

RRQYJINTUHWNHW-UHFFFAOYSA-N

Formula

C8H18O3

SMILES

CCOCCOCCOCC

Molecular Weight¹

162.23

CAS

112-36-7

Other Names

• .beta.,.beta.'-diethoxy diethyl ether
• 1,1'-oxybis[2-ethoxyethane]
• 1-Ethoxy-2-(«beta»-ethoxyethoxy)ethane
• 2-(2-Ethoxyethoxy)-1-ethoxyethane
• 2-ethoxyethyl ether
• 3,6,9-trioxaundecane
• 3-oxa-1,5-pentanediol, diethyl ether
• Diethyldiethylene glycol
• Diethylether diethylenglykolu
• Ethane, 1,1'-oxybis[2-ethoxy-
• Ethanol, 2,2'-oxybis-, diethyl ether
• Ether, bis(2-ethoxyethyl)
• Ethyl diglyme
• bis(2-ethoxyethyl) ether
• diethylene glycol diethyl ether

• ω : Acentric Factor.
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• ε_r : Dielectric Constant (Relative permittivity).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion 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).
• 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_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.6807		ChemSep v8.3 pure component data Compiled value
εr	5.70		NCMS SOLV-DB
Tflash,cc	355.15	K	NCMS SOLV-DB
ΔfG°	-299.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-580.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfusH°	20.04	kJ/mol	Joback Calculated Property
ΔvapH°	[48.95; 58.40]	kJ/mol
ΔvapH°	48.95	kJ/mol	NCMS SOLV-DB
ΔvapH°	56.40 ± 1.40	kJ/mol	NIST
ΔvapH°	58.40 ± 0.04	kJ/mol	NIST
IE	9.32	eV	Relay (1.0) Calculated Property
log10WS	-0.80		Relay (1.0) Calculated Property
logPoct/wat	0.999		NCMS SOLV-DB
McVol	141.190	ml/mol	McGowan Calculated Property
NFPA Fire	2		NCMS SOLV-DB
NFPA Health	1		NCMS SOLV-DB
NFPA Safety	0		NCMS SOLV-DB
Pc	2370.00	kPa	ChemSep v8.3 pure component data Compiled value
Ptriple	7.60e-05	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[174.83; 1081.40]
Inp	1081.00		NIST
Inp	1081.40		NIST
Inp	1058.00		NIST
Inp	174.83		NIST
Inp	179.46		NIST
Inp	1081.40		NIST
Inp	1058.00		NIST
Tboil	[458.20; 462.15]	K
Tboil	462.15	K	ChemSep v8.3 pure component data Compiled value
Tboil	462.05	K	NCMS SOLV-DB
Tboil	458.20	K	NIST
Tboil	462.15	K	NIST
Tboil	462.15	K	NIST
Tc	[612.00; 624.00]	K
Tc	612.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc	624.00	K	ChemSep v8.3 pure component data Compiled value
Tfus	[228.00; 229.15]	K
Tfus	229.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	229.15	K	ChemSep v8.3 pure component data Compiled value
Tfus	228.85	K	NCMS SOLV-DB
Tfus	228.85	K	NIST
Tfus	228.85	K	NIST
Tfus	Outlier 228.00 ± 2.00	K	NIST
Ttriple	228.85	K	ChemSep v8.3 pure component data Compiled value
UQi	5.69		ChemSep v8.3 pure component data Compiled value
URi	6.64		ChemSep v8.3 pure component data Compiled value
Vc	0.528	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2550000		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[347.50; 384.80]	J/mol×K	[298.10; 421.48]
Cp,liquid	347.50	J/mol×K	298.10	NIST
Cp,liquid	349.11	J/mol×K	312.57	Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
Cp,liquid	351.22	J/mol×K	322.47	Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
Cp,liquid	353.33	J/mol×K	332.37	Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
Cp,liquid	355.44	J/mol×K	342.27	Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
Cp,liquid	358.68	J/mol×K	352.18	Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
Cp,liquid	360.79	J/mol×K	362.08	Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
Cp,liquid	364.85	J/mol×K	371.98	Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
Cp,liquid	368.90	J/mol×K	381.88	Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
Cp,liquid	372.15	J/mol×K	391.78	Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
Cp,liquid	377.01	J/mol×K	401.68	Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
Cp,liquid	380.75	J/mol×K	411.58	Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
Cp,liquid	384.80	J/mol×K	421.48	Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
η	0.0014000	Pa×s	298.15	NCMS SOLV-DB
ΔvapH	[43.18; 48.30]	kJ/mol	[273.00; 395.50]
ΔvapH	43.18	kJ/mol	273.00	NIST
ΔvapH	48.30	kJ/mol	395.50	NIST
Pvap	[0.05; 84.21]	kPa	[293.15; 453.15]
Pvap	0.05	kPa	293.15	NCMS SOLV-DB
Pvap	2.61	kPa	363.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	4.29	kPa	373.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	6.69	kPa	383.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	10.08	kPa	393.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	15.08	kPa	403.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	22.08	kPa	413.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	31.51	kPa	423.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	37.58	kPa	428.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	44.45	kPa	433.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	52.47	kPa	438.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	61.68	kPa	443.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	72.21	kPa	448.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	84.21	kPa	453.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
n0	1.41100		298.15	NCMS SOLV-DB
ρl	[831.60; 926.40]	kg/m3	[273.15; 373.15]
ρl	926.40	kg/m3	273.15	Below the room temperature measurements of CO2 solubilities in six physical absorbents
ρl	916.30	kg/m3	283.15	Below the room temperature measurements of CO2 solubilities in six physical absorbents
ρl	916.36	kg/m3	283.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	917.00	kg/m3	283.15	Thermophysical properties of glycols and glymes
ρl	915.39	kg/m3	284.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	914.43	kg/m3	285.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	913.46	kg/m3	286.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	912.50	kg/m3	287.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	911.53	kg/m3	288.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	912.20	kg/m3	288.15	Thermophysical properties of glycols and glymes
ρl	914.40	kg/m3	288.15	Thermophysical properties of glycols and glymes
ρl	910.57	kg/m3	289.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	909.60	kg/m3	290.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	908.63	kg/m3	291.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	907.67	kg/m3	292.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	906.71	kg/m3	293.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	906.73	kg/m3	293.15	Thermodynamics of 1-alkanol + linear polyether mixtures
ρl	907.40	kg/m3	293.15	Thermophysical properties of glycols and glymes
ρl	909.60	kg/m3	293.15	Thermophysical properties of glycols and glymes
ρl	905.75	kg/m3	294.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	904.78	kg/m3	295.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	903.81	kg/m3	296.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	902.85	kg/m3	297.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	902.76	kg/m3	298.15	Speeds of Sound and Isentropic Compressibilities of n-Alkoxyethanols and Polyethers with Propylamine at 298.15K
ρl	904.70	kg/m3	298.15	Thermophysical properties of glycols and glymes
ρl	902.60	kg/m3	298.15	Thermophysical properties of glycols and glymes
ρl	902.88	kg/m3	298.15	Thermodynamics of 1-alkanol + linear polyether mixtures
ρl	901.88	kg/m3	298.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	900.92	kg/m3	299.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	899.95	kg/m3	300.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	898.98	kg/m3	301.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	898.02	kg/m3	302.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	897.05	kg/m3	303.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	897.70	kg/m3	303.15	Thermophysical properties of glycols and glymes
ρl	897.22	kg/m3	303.15	Thermodynamics of 1-alkanol + linear polyether mixtures
ρl	899.80	kg/m3	303.15	Thermophysical properties of glycols and glymes
ρl	896.08	kg/m3	304.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	895.12	kg/m3	305.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	894.15	kg/m3	306.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	893.18	kg/m3	307.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	892.90	kg/m3	308.15	Thermophysical properties of glycols and glymes
ρl	892.21	kg/m3	308.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	895.00	kg/m3	308.15	Thermophysical properties of glycols and glymes
ρl	893.08	kg/m3	308.50	Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Ethers and Benzyl Alcohol at 308.15 K and Atmospheric Pressure
ρl	891.25	kg/m3	309.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	890.28	kg/m3	310.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	889.31	kg/m3	311.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	888.34	kg/m3	312.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	887.37	kg/m3	313.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	890.10	kg/m3	313.15	Thermophysical properties of glycols and glymes
ρl	888.10	kg/m3	313.15	Thermophysical properties of glycols and glymes
ρl	886.40	kg/m3	314.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	885.43	kg/m3	315.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	884.46	kg/m3	316.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	883.48	kg/m3	317.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	882.51	kg/m3	318.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	885.30	kg/m3	318.15	Thermophysical properties of glycols and glymes
ρl	881.54	kg/m3	319.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	880.57	kg/m3	320.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	879.60	kg/m3	321.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	878.63	kg/m3	322.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	880.40	kg/m3	323.15	Thermophysical properties of glycols and glymes
ρl	878.40	kg/m3	323.15	Thermophysical properties of glycols and glymes
ρl	877.66	kg/m3	323.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	876.70	kg/m3	324.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	875.73	kg/m3	325.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	874.75	kg/m3	326.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	873.78	kg/m3	327.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	872.81	kg/m3	328.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	875.60	kg/m3	328.15	Thermophysical properties of glycols and glymes
ρl	871.84	kg/m3	329.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	870.87	kg/m3	330.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	869.89	kg/m3	331.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	868.92	kg/m3	332.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	868.70	kg/m3	333.15	Thermophysical properties of glycols and glymes
ρl	870.70	kg/m3	333.15	Thermophysical properties of glycols and glymes
ρl	867.94	kg/m3	333.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	865.90	kg/m3	338.15	Thermophysical properties of glycols and glymes
ρl	858.90	kg/m3	343.15	Thermophysical properties of glycols and glymes
ρl	861.00	kg/m3	343.15	Thermophysical properties of glycols and glymes
ρl	856.10	kg/m3	348.15	Thermophysical properties of glycols and glymes
ρl	851.20	kg/m3	353.15	Thermophysical properties of glycols and glymes
ρl	846.30	kg/m3	358.15	Thermophysical properties of glycols and glymes
ρl	841.40	kg/m3	363.15	Thermophysical properties of glycols and glymes
ρl	836.50	kg/m3	368.15	Thermophysical properties of glycols and glymes
ρl	831.60	kg/m3	373.15	Thermophysical properties of glycols and glymes
γ	[0.03; 0.03]	N/m	[293.15; 298.15]
γ	0.03	N/m	293.15	Physical-Chemical Properties and Liquid-Liquid Equilibria for Binary Mixture of Diethylene Glycol Diethyl Ether with Water
γ	0.03	N/m	298.15	NCMS SOLV-DB

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[182.89; 562.91]	J/mol×K	[255.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			9.00000e+01
Coefficient B			-5.00000e+02
Coefficient C			6.49224e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			255.00
Temperature range, max.			1500.00
Cp,gas	182.89	J/mol×K	255.00	Calculated Property
Cp,gas	275.13	J/mol×K	393.33	Calculated Property
Cp,gas	347.70	J/mol×K	531.67	Calculated Property
Cp,gas	402.93	J/mol×K	670.00	Calculated Property
Cp,gas	445.56	J/mol×K	808.33	Calculated Property
Cp,gas	479.19	J/mol×K	946.67	Calculated Property
Cp,gas	506.30	J/mol×K	1085.00	Calculated Property
Cp,gas	528.57	J/mol×K	1223.33	Calculated Property
Cp,gas	547.17	J/mol×K	1361.67	Calculated Property
Cp,gas	562.91	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[332.09; 403.34]	J/mol×K	[283.15; 462.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K
Coefficient A			2.19400e+02
Coefficient B			3.98000e-01
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			283.15
Temperature range, max.			462.15
Cp,liquid	332.09	J/mol×K	283.15	Calculated Property
Cp,liquid	340.01	J/mol×K	303.04	Calculated Property
Cp,liquid	347.93	J/mol×K	322.93	Calculated Property
Cp,liquid	355.84	J/mol×K	342.82	Calculated Property
Cp,liquid	363.76	J/mol×K	362.71	Calculated Property
Cp,liquid	371.67	J/mol×K	382.59	Calculated Property
Cp,liquid	379.59	J/mol×K	402.48	Calculated Property
Cp,liquid	387.50	J/mol×K	422.37	Calculated Property
Cp,liquid	395.42	J/mol×K	442.26	Calculated Property
Cp,liquid	403.34	J/mol×K	462.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0043077; 0.0002063]	Pa×s	[228.85; 500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-2.25690e+00
Coefficient B			8.60490e+02
Coefficient C			-1.27930e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			228.85
Temperature range, max.			500.00
η	0.0043077	Pa×s	228.85	Calculated Property
η	0.0023744	Pa×s	258.98	Calculated Property
η	0.0014589	Pa×s	289.11	Calculated Property
η	0.0009704	Pa×s	319.23	Calculated Property
η	0.0006854	Pa×s	349.36	Calculated Property
η	0.0005070	Pa×s	379.49	Calculated Property
η	0.0003892	Pa×s	409.62	Calculated Property
η	0.0003078	Pa×s	439.74	Calculated Property
η	0.0002494	Pa×s	469.87	Calculated Property
η	0.0002063	Pa×s	500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[62.84; 0.00]	kJ/mol	[228.85; 624.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			7.47540e+01
Coefficient B			3.80010e-01
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			6.24000e+02
Temperature range, min.			228.85
Temperature range, max.			624.00
ΔvapH	62.84	kJ/mol	228.85	Calculated Property
ΔvapH	60.09	kJ/mol	272.76	Calculated Property
ΔvapH	57.12	kJ/mol	316.66	Calculated Property
ΔvapH	53.87	kJ/mol	360.57	Calculated Property
ΔvapH	50.26	kJ/mol	404.47	Calculated Property
ΔvapH	46.17	kJ/mol	448.38	Calculated Property
ΔvapH	41.39	kJ/mol	492.28	Calculated Property
ΔvapH	35.48	kJ/mol	536.19	Calculated Property
ΔvapH	27.27	kJ/mol	580.09	Calculated Property
ΔvapH	0.00	kJ/mol	624.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[342.30; 489.93]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.65189e+01
Coefficient B			-5.34545e+03
Coefficient C			-1.29720e+01
Temperature range, min.			342.30
Temperature range, max.			489.93
Pvap	1.33	kPa	342.30	Calculated Property
Pvap	2.88	kPa	358.70	Calculated Property
Pvap	5.80	kPa	375.11	Calculated Property
Pvap	11.00	kPa	391.51	Calculated Property
Pvap	19.77	kPa	407.91	Calculated Property
Pvap	33.91	kPa	424.32	Calculated Property
Pvap	55.82	kPa	440.72	Calculated Property
Pvap	88.56	kPa	457.12	Calculated Property
Pvap	135.95	kPa	473.53	Calculated Property
Pvap	202.65	kPa	489.93	Calculated Property
Pvap	[7.60e-05; 2367.19]	kPa	[228.85; 624.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			6.95812e+01
Coefficient B			-8.58250e+03
Coefficient C			-7.68470e+00
Coefficient D			3.60090e-06
Coefficient E			2.00000e+00
Temperature range, min.			228.85
Temperature range, max.			624.00
Pvap	7.60e-05	kPa	228.85	Calculated Property
Pvap	8.94e-03	kPa	272.76	Calculated Property
Pvap	0.24	kPa	316.66	Calculated Property
Pvap	2.72	kPa	360.57	Calculated Property
Pvap	16.83	kPa	404.47	Calculated Property
Pvap	69.68	kPa	448.38	Calculated Property
Pvap	217.45	kPa	492.28	Calculated Property
Pvap	553.14	kPa	536.19	Calculated Property
Pvap	1210.47	kPa	580.09	Calculated Property
Pvap	2367.19	kPa	624.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[963.87; 290.56]	kg/m3	[228.85; 624.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			7.41053e+01
Coefficient B			2.55040e-01
Coefficient C			6.24000e+02
Coefficient D			2.85700e-01
Temperature range, min.			228.85
Temperature range, max.			624.00
ρl	963.87	kg/m3	228.85	Calculated Property
ρl	926.37	kg/m3	272.76	Calculated Property
ρl	887.03	kg/m3	316.66	Calculated Property
ρl	845.38	kg/m3	360.57	Calculated Property
ρl	800.78	kg/m3	404.47	Calculated Property
ρl	752.18	kg/m3	448.38	Calculated Property
ρl	697.79	kg/m3	492.28	Calculated Property
ρl	634.03	kg/m3	536.19	Calculated Property
ρl	551.10	kg/m3	580.09	Calculated Property
ρl	290.56	kg/m3	624.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.01]	N/m	[228.15; 461.15]	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			6.18624e-02
Coefficient B			-1.17600e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			228.15
Temperature range, max.			461.15
γ	0.04	N/m	228.15	Calculated Property
γ	0.03	N/m	254.04	Calculated Property
γ	0.03	N/m	279.93	Calculated Property
γ	0.03	N/m	305.82	Calculated Property
γ	0.02	N/m	331.71	Calculated Property
γ	0.02	N/m	357.59	Calculated Property
γ	0.02	N/m	383.48	Calculated Property
γ	0.01	N/m	409.37	Calculated Property
γ	0.01	N/m	435.26	Calculated Property
γ	0.01	N/m	461.15	Calculated Property
γ	[0.04; 0.00]	N/m	[228.85; 624.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is γ in N/m, T in K
Coefficient A			7.02760e-02
Coefficient B			1.48500e+00
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			6.24000e+02
Temperature range, min.			228.85
Temperature range, max.			624.00
γ	0.04	N/m	228.85	Calculated Property
γ	0.03	N/m	272.76	Calculated Property
γ	0.02	N/m	316.66	Calculated Property
γ	0.02	N/m	360.57	Calculated Property
γ	0.01	N/m	404.47	Calculated Property
γ	0.01	N/m	448.38	Calculated Property
γ	0.01	N/m	492.28	Calculated Property
γ	0.00	N/m	536.19	Calculated Property
γ	0.00	N/m	580.09	Calculated Property
γ	0.00	N/m	624.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.02; 0.06]	W/m×K	[462.15; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K
Coefficient A			1.63700e-04
Coefficient B			9.44000e-01
Coefficient C			7.16000e+02
Coefficient D			0.00000e+00
Temperature range, min.			462.15
Temperature range, max.			1000.00
λgas	0.02	W/m×K	462.15	Calculated Property
λgas	0.03	W/m×K	521.91	Calculated Property
λgas	0.03	W/m×K	581.67	Calculated Property
λgas	0.03	W/m×K	641.43	Calculated Property
λgas	0.04	W/m×K	701.19	Calculated Property
λgas	0.04	W/m×K	760.96	Calculated Property
λgas	0.05	W/m×K	820.72	Calculated Property
λgas	0.05	W/m×K	880.48	Calculated Property
λgas	0.06	W/m×K	940.24	Calculated Property
λgas	0.06	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.16; 0.12]	W/m×K	[228.85; 462.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λliquid in W/m×K, T in K
Coefficient A			2.02400e-01
Coefficient B			-1.87500e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			228.85
Temperature range, max.			462.15
λliquid	0.16	W/m×K	228.85	Calculated Property
λliquid	0.15	W/m×K	254.77	Calculated Property
λliquid	0.15	W/m×K	280.69	Calculated Property
λliquid	0.14	W/m×K	306.62	Calculated Property
λliquid	0.14	W/m×K	332.54	Calculated Property
λliquid	0.14	W/m×K	358.46	Calculated Property
λliquid	0.13	W/m×K	384.38	Calculated Property
λliquid	0.13	W/m×K	410.31	Calculated Property
λliquid	0.12	W/m×K	436.23	Calculated Property
λliquid	0.12	W/m×K	462.15	Calculated Property

Similar Compounds

Find more compounds similar to Diethyl carbitol.

Mixtures

• Diethyl carbitol + Methyl Alcohol
• Diethyl carbitol + 1-Butanol
• Diethyl carbitol + 1-Decanol
• Carbon dioxide + Diethyl carbitol
• Propylamine + Diethyl carbitol
• Diethyl carbitol + Ethane, 1,2-dichloro-
• Benzyl alcohol + Diethyl carbitol
• Diethyl carbitol + Water

Sources

• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 ChEDL chemicals 1.5.2, from Kudchadker, A. P.; Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 7. Oxygen Compounds Other Than Alkanols and Cycloalkanols. J. Chem. Eng. Data 2001, 46, 457-479.
• 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)
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Crippen Method
• Speeds of Sound and Isentropic Compressibilities of n-Alkoxyethanols and Polyethers with Propylamine at 298.15K
• Solubilities of CO2 capture absorbents 2-ethoxyethyl ether, 2-butoxyethyl acetate and 2-(2-ethoxyethoxy)ethyl acetate
• Thermodynamics of 1-alkanol + linear polyether mixtures
• Below the room temperature measurements of CO2 solubilities in six physical absorbents
• Thermophysical properties of glycols and glymes
• Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
• Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
• Physical-Chemical Properties and Liquid-Liquid Equilibria for Binary Mixture of Diethylene Glycol Diethyl Ether with Water
• Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Ethers and Benzyl Alcohol at 308.15 K and Atmospheric Pressure
• Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
• Fast Determination of Binary Vapor Liquid Equilibrium of CO2-Based Mixtures at Elevated Pressures
• Joback Method
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure

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