Chemical Properties of Ethane, 1,1'-oxybis[2-methoxy- (CAS 111-96-6)

InChI

InChI=1S/C6H14O3/c1-7-3-5-9-6-4-8-2/h3-6H2,1-2H3

InChI Key

SBZXBUIDTXKZTM-UHFFFAOYSA-N

Formula

C6H14O3

SMILES

COCCOCCOC

Molecular Weight¹

134.17

CAS

111-96-6

Other Names

• (2-Methoxyethyl) ether
• .beta.,.beta.-dimethoxy diethyl ether
• 1,1'-Oxybis(2-methoxy)ethane
• 1,1'-oxybis(2-methoxyethane)
• 1,5-dimethoxydiethyl ether
• 2,2'-Oxybisethanol dimethyl ether
• 2,5,8-Trioxanonane
• 2-(2-Methoxyethoxy)-1-methoxyethane
• 2-methoxyethyl ether
• 3-oxa-1,5-pentanediol, dimethyl ether
• Bis(2-methoxyethyl) ether
• CH3OCH2CH2OCH2CH2OCH3
• Di(2-Methoxyethyl) ether
• Diethyl glycol dimethyl ether
• Diethylene glycol dimethyl ether
• Diglycol methyl ether
• Diglyme
• Dimethoxydiethylene glycol
• Dimethyl carbitol
• Dimethyldigol
• Ethanol, 2,2'-oxybis-, dimethyl ether
• Ether, bis(2-methoxyethyl)
• Glyme-2
• Methyl diglyme
• NSC 59726
• Poly-Solv
• diethylene glycol, dimethyl ether
• diglyme (diethylene glycol dimethyl ether)
• dimethyldiglycol

• PAff : Proton affinity (kJ/mol).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• 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).
• 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_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).
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ : Liquid thermal conductivity (W/m×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
PAff	918.80	kJ/mol	NIST
BasG	870.90	kJ/mol	NIST
ΔcH°liquid	-3805.50 ± 0.90	kJ/mol	NIST
ΔfG°	-315.36	kJ/mol	Joback Calculated Property
ΔfH°gas	[-524.70; -511.70]	kJ/mol
ΔfH°gas	-511.70	kJ/mol	NIST
ΔfH°gas	-524.70	kJ/mol	NIST
ΔfH°liquid	[-569.40; -556.40]	kJ/mol
ΔfH°liquid	-556.40 ± 0.90	kJ/mol	NIST
ΔfH°liquid	-569.40	kJ/mol	NIST
ΔfusH°	14.86	kJ/mol	Joback Calculated Property
ΔvapH°	[44.70; 48.00]	kJ/mol
ΔvapH°	48.00 ± 0.60	kJ/mol	NIST
ΔvapH°	44.70	kJ/mol	NIST
IE	9.80	eV	NIST
log10WS	0.88		Aq. Sol...
logPoct/wat	0.296		Crippen Calculated Property
McVol	113.010	ml/mol	McGowan Calculated Property
Pc	2937.70	kPa	Joback Calculated Property
Inp	[950.90; 951.00]
Inp	951.00		NIST
Inp	950.90		NIST
Inp	950.90		NIST
S°liquid	352.70	J/mol×K	NIST
Tboil	[435.00; 435.20]	K
Tboil	435.20	K	NIST
Tboil	435.15	K	NIST
Tboil	435.00 ± 4.00	K	NIST
Tc	569.71	K	Joback Calculated Property
Tfus	[207.82; 209.15]	K
Tfus	207.82	K	Aq. Sol...
Tfus	209.15	K	NIST
Tfus	209.10 ± 0.20	K	NIST
Vc	0.425	m3/kmol	Joback Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[227.24; 283.44]	J/mol×K	[403.94; 569.71]
Cp,gas	227.24	J/mol×K	403.94	Joback Calculated Property
Cp,gas	237.05	J/mol×K	431.57	Joback Calculated Property
Cp,gas	246.70	J/mol×K	459.20	Joback Calculated Property
Cp,gas	256.17	J/mol×K	486.83	Joback Calculated Property
Cp,gas	265.47	J/mol×K	514.45	Joback Calculated Property
Cp,gas	274.56	J/mol×K	542.08	Joback Calculated Property
Cp,gas	283.44	J/mol×K	569.71	Joback Calculated Property
Cp,liquid	[274.10; 279.84]	J/mol×K	[298.15; 298.15]
Cp,liquid	277.76	J/mol×K	298.15	NIST
Cp,liquid	279.84	J/mol×K	298.15	NIST
Cp,liquid	274.10	J/mol×K	298.15	NIST
η	[0.0004120; 0.0015200]	Pa×s	[273.15; 363.15]
η	0.0015200	Pa×s	273.15	Density...
η	0.0013800	Pa×s	278.15	Density...
η	0.0012600	Pa×s	283.15	Density...
η	0.0011400	Pa×s	288.15	Density...
η	0.0010600	Pa×s	293.15	Density...
η	0.0009760	Pa×s	298.15	Density...
η	0.0009010	Pa×s	303.15	Density...
η	0.0007770	Pa×s	313.15	Density...
η	0.0006760	Pa×s	323.15	Density...
η	0.0005920	Pa×s	333.15	Density...
η	0.0005220	Pa×s	343.15	Density...
η	0.0004640	Pa×s	353.15	Density...
η	0.0004120	Pa×s	363.15	Density...
ΔfusH	[17.78; 17.80]	kJ/mol	[209.10; 209.10]
ΔfusH	17.78	kJ/mol	209.10	NIST
ΔfusH	17.80	kJ/mol	209.10	NIST
ΔfusH	17.80	kJ/mol	209.10	NIST
ΔvapH	[45.40; 47.40]	kJ/mol	[359.50; 402.50]
ΔvapH	47.40	kJ/mol	359.50	NIST
ΔvapH	45.40	kJ/mol	402.50	NIST
n0	[1.39680; 1.41010]		[288.15; 318.15]
n0	1.41010		288.15	Liquid ...
n0	1.40580		298.15	Non-ide...
n0	1.40580		298.15	Liquid ...
n0	1.40570		298.15	Solubil...
n0	1.40600		298.15	Density...
n0	1.40120		308.15	Liquid ...
n0	1.39680		318.15	Liquid ...
ρl	[863.80; 953.70]	kg/m3	[283.15; 373.15]
ρl	953.70	kg/m3	283.15	Thermop...
ρl	953.66	kg/m3	283.15	Volumet...
ρl	952.67	kg/m3	284.15	Volumet...
ρl	951.69	kg/m3	285.15	Volumet...
ρl	950.70	kg/m3	286.15	Volumet...
ρl	949.71	kg/m3	287.15	Volumet...
ρl	948.70	kg/m3	288.15	Thermop...
ρl	950.20	kg/m3	288.15	Thermop...
ρl	948.72	kg/m3	288.15	Volumet...
ρl	947.73	kg/m3	289.15	Volumet...
ρl	946.74	kg/m3	290.15	Volumet...
ρl	945.75	kg/m3	291.15	Volumet...
ρl	944.76	kg/m3	292.15	Volumet...
ρl	943.80	kg/m3	293.15	Thermop...
ρl	945.20	kg/m3	293.15	Excess ...
ρl	945.20	kg/m3	293.15	Thermop...
ρl	943.76	kg/m3	293.15	Volumet...
ρl	942.79	kg/m3	294.15	Volumet...
ρl	941.79	kg/m3	295.15	Volumet...
ρl	940.79	kg/m3	296.15	Volumet...
ρl	939.80	kg/m3	297.15	Volumet...
ρl	938.80	kg/m3	298.15	Thermop...
ρl	938.80	kg/m3	298.15	Volumet...
ρl	940.20	kg/m3	298.15	Thermop...
ρl	939.80	kg/m3	298.15	Excess ...
ρl	938.62	kg/m3	298.15	Excess ...
ρl	937.80	kg/m3	299.15	Volumet...
ρl	936.81	kg/m3	300.15	Volumet...
ρl	935.81	kg/m3	301.15	Volumet...
ρl	934.82	kg/m3	302.15	Volumet...
ρl	933.80	kg/m3	303.15	Thermop...
ρl	935.20	kg/m3	303.15	Thermop...
ρl	935.00	kg/m3	303.15	Excess ...
ρl	933.98	kg/m3	303.15	Surface...
ρl	933.82	kg/m3	303.15	Volumet...
ρl	932.82	kg/m3	304.15	Volumet...
ρl	931.82	kg/m3	305.15	Volumet...
ρl	930.82	kg/m3	306.15	Volumet...
ρl	929.83	kg/m3	307.15	Volumet...
ρl	928.80	kg/m3	308.15	Thermop...
ρl	930.70	kg/m3	308.15	Excess ...
ρl	930.20	kg/m3	308.15	Thermop...
ρl	928.83	kg/m3	308.15	Volumet...
ρl	928.95	kg/m3	308.15	Surface...
ρl	927.82	kg/m3	309.15	Volumet...
ρl	926.83	kg/m3	310.15	Volumet...
ρl	925.82	kg/m3	311.15	Volumet...
ρl	924.82	kg/m3	312.15	Volumet...
ρl	923.80	kg/m3	313.15	Thermop...
ρl	925.20	kg/m3	313.15	Thermop...
ρl	923.97	kg/m3	313.15	Surface...
ρl	925.40	kg/m3	313.15	Excess ...
ρl	923.82	kg/m3	313.15	Volumet...
ρl	922.81	kg/m3	314.15	Volumet...
ρl	921.81	kg/m3	315.15	Volumet...
ρl	920.80	kg/m3	316.15	Volumet...
ρl	919.80	kg/m3	317.15	Volumet...
ρl	920.20	kg/m3	318.15	Thermop...
ρl	918.94	kg/m3	318.15	Surface...
ρl	918.79	kg/m3	318.15	Volumet...
ρl	917.78	kg/m3	319.15	Volumet...
ρl	916.78	kg/m3	320.15	Volumet...
ρl	915.77	kg/m3	321.15	Volumet...
ρl	914.75	kg/m3	322.15	Volumet...
ρl	913.90	kg/m3	323.15	Surface...
ρl	913.70	kg/m3	323.15	Thermop...
ρl	915.20	kg/m3	323.15	Thermop...
ρl	913.75	kg/m3	323.15	Volumet...
ρl	912.73	kg/m3	324.15	Volumet...
ρl	911.72	kg/m3	325.15	Volumet...
ρl	910.70	kg/m3	326.15	Volumet...
ρl	909.69	kg/m3	327.15	Volumet...
ρl	908.84	kg/m3	328.15	Surface...
ρl	908.67	kg/m3	328.15	Volumet...
ρl	910.10	kg/m3	328.15	Thermop...
ρl	907.65	kg/m3	329.15	Volumet...
ρl	906.63	kg/m3	330.15	Volumet...
ρl	905.62	kg/m3	331.15	Volumet...
ρl	904.60	kg/m3	332.15	Volumet...
ρl	905.00	kg/m3	333.15	Thermop...
ρl	903.76	kg/m3	333.15	Surface...
ρl	903.60	kg/m3	333.15	Thermop...
ρl	903.59	kg/m3	333.15	Volumet...
ρl	898.67	kg/m3	338.15	Surface...
ρl	899.90	kg/m3	338.15	Thermop...
ρl	894.80	kg/m3	343.15	Thermop...
ρl	893.55	kg/m3	343.15	Surface...
ρl	893.40	kg/m3	343.15	Thermop...
ρl	889.70	kg/m3	348.15	Thermop...
ρl	888.41	kg/m3	348.15	Surface...
ρl	884.60	kg/m3	353.15	Thermop...
ρl	883.24	kg/m3	353.15	Surface...
ρl	878.04	kg/m3	358.15	Surface...
ρl	879.40	kg/m3	358.15	Thermop...
ρl	872.81	kg/m3	363.15	Surface...
ρl	874.20	kg/m3	363.15	Thermop...
ρl	869.00	kg/m3	368.15	Thermop...
ρl	863.80	kg/m3	373.15	Thermop...
ΔfusS	85.10	J/mol×K	209.10	NIST
γ	[0.02; 0.03]	N/m	[298.15; 318.15]
γ	0.02	N/m	298.15	Volumet...
γ	0.03	N/m	308.15	Volumet...
γ	0.02	N/m	318.15	Volumet...
λ	[0.11; 0.15]	W/m×K	[302.75; 392.16]
λ	0.15	W/m×K	302.75	Thermal...
λ	0.13	W/m×K	332.54	Thermal...
λ	0.12	W/m×K	362.39	Thermal...
λ	0.11	W/m×K	392.16	Thermal...

Datasets

1. Mass density, kg/m3 (2)
2. Speed of sound, m/s (1)

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.69	100.00	953.48
283.69	1000.00	954.15
283.69	5000.00	956.94
283.68	10000.00	960.29
283.68	20000.00	966.68
283.68	30000.00	972.8
283.67	40000.00	978.49
283.67	60000.00	989.12
283.67	80000.00	998.75
283.67	100000.00	1007.71
303.47	100.00	933.69
303.47	1000.00	934.43
303.48	5000.00	937.55
303.48	10000.00	941.31
322.62	30000.00	938.31
322.62	40000.00	945.16
322.62	60000.00	957.74
322.62	80000.00	968.98
322.62	100000.00	979.2
342.49	100.00	894.03
342.49	1000.00	894.98
342.49	5000.00	898.96
342.50	10000.00	903.66
342.50	20000.00	912.57
342.51	30000.00	920.68
342.51	40000.00	928.18
342.51	60000.00	941.77
342.51	80000.00	953.82
303.49	20000.00	948.42
303.49	30000.00	955.17
303.49	40000.00	961.41
303.49	60000.00	973.02
303.50	80000.00	983.33
303.50	100000.00	992.97
322.62	100.00	914.41
322.62	1000.00	915.3
322.62	5000.00	918.77
322.62	10000.00	923.02
322.62	20000.00	930.99
342.52	100000.00	964.68
362.51	100.00	873.45
362.51	1000.00	874.46
362.51	5000.00	879.02
362.52	10000.00	884.41
362.52	20000.00	894.33
362.52	30000.00	903.29
362.52	40000.00	911.53
362.53	60000.00	926.3
362.53	80000.00	939.26
362.53	100000.00	950.89
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	943.5
293.15	5000.00	947.3
293.15	10000.00	950.9
293.15	15000.00	954.4
293.15	20000.00	957.7
293.15	25000.00	960.9
293.15	30000.00	964.0
293.15	35000.00	967.0
293.15	40000.00	969.8
293.15	45000.00	972.8
293.15	50000.00	975.4
293.15	55000.00	978.2
293.15	60000.00	980.9
303.15	100.00	933.7
303.15	5000.00	937.6
303.15	10000.00	941.1
303.15	15000.00	945.0
303.15	20000.00	948.4
303.15	25000.00	951.8
303.15	30000.00	955.2
303.15	35000.00	958.2
303.15	40000.00	961.1
303.15	45000.00	964.0
303.15	50000.00	967.3
303.15	55000.00	970.1
303.15	60000.00	973.2
313.15	100.00	923.7
313.15	5000.00	927.9
313.15	10000.00	931.8
313.15	15000.00	935.7
313.15	20000.00	939.4
313.15	25000.00	942.6
313.15	30000.00	946.5
313.15	35000.00	949.7
313.15	40000.00	952.8
313.15	45000.00	956.1
313.15	50000.00	958.8
313.15	55000.00	961.9
313.15	60000.00	964.9
323.15	100.00	913.7
323.15	5000.00	918.2
323.15	10000.00	922.7
323.15	15000.00	926.4
323.15	20000.00	930.5
323.15	25000.00	934.2
323.15	30000.00	937.6
323.15	35000.00	941.0
323.15	40000.00	944.4
323.15	45000.00	947.6
323.15	50000.00	951.0
323.15	55000.00	953.9
323.15	60000.00	956.7
333.15	100.00	903.6
333.15	5000.00	908.3
333.15	10000.00	912.8
333.15	15000.00	917.3
333.15	20000.00	921.0
333.15	25000.00	925.3
333.15	30000.00	928.9
333.15	35000.00	932.6
333.15	40000.00	936.4
333.15	45000.00	939.8
333.15	50000.00	942.9
333.15	55000.00	946.0
333.15	60000.00	949.1
343.15	100.00	893.6
343.15	5000.00	898.5
343.15	10000.00	903.2
343.15	15000.00	907.8
343.15	20000.00	912.3
343.15	25000.00	916.2
343.15	30000.00	920.5
343.15	35000.00	924.2
343.15	40000.00	928.0
343.15	45000.00	931.4
343.15	50000.00	934.8
343.15	55000.00	938.2
343.15	60000.00	941.4
353.15	100.00	883.3
353.15	5000.00	888.7
353.15	10000.00	893.9
353.15	15000.00	898.7
353.15	20000.00	903.2
353.15	25000.00	907.6
353.15	30000.00	911.6
353.15	35000.00	915.5
353.15	40000.00	919.5
353.15	45000.00	923.1
353.15	50000.00	927.0
353.15	55000.00	930.4
353.15	60000.00	933.6
Reference

Speed of sound, m/s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
293.15	100.00	1298.9
293.15	10000.00	1344.9
293.15	20000.00	1386.5
293.15	30000.00	1426.6
293.15	40000.00	1463.9
293.15	50000.00	1499.2
293.15	60000.00	1532.5
293.15	70000.00	1565.1
293.15	80000.00	1595.5
293.15	90000.00	1624.9
293.15	100000.00	1653.4
303.15	100.00	1259.3
303.15	10000.00	1306.7
303.15	20000.00	1350.6
303.15	30000.00	1392.0
303.15	40000.00	1430.4
303.15	50000.00	1466.9
303.15	60000.00	1501.5
303.15	70000.00	1534.3
303.15	80000.00	1565.8
303.15	90000.00	1595.9
303.15	100000.00	1625.1
313.15	100.00	1219.9
313.15	10000.00	1269.5
313.15	20000.00	1315.4
313.15	30000.00	1357.6
313.15	40000.00	1397.8
313.15	50000.00	1435.3
313.15	60000.00	1470.5
313.15	70000.00	1504.4
313.15	80000.00	1536.7
313.15	90000.00	1567.6
313.15	100000.00	1597.0
323.15	100.00	1180.9
323.15	10000.00	1232.5
323.15	20000.00	1280.2
323.15	30000.00	1324.4
323.15	40000.00	1365.5
323.15	50000.00	1404.0
323.15	60000.00	1440.6
323.15	70000.00	1475.2
323.15	80000.00	1508.2
323.15	90000.00	1539.8
323.15	100000.00	1569.9
333.15	100.00	1142.4
333.15	10000.00	1196.4
333.15	20000.00	1246.0
333.15	30000.00	1291.4
333.15	40000.00	1333.7
333.15	50000.00	1373.6
333.15	60000.00	1410.9
333.15	70000.00	1446.2
333.15	80000.00	1480.1
333.15	90000.00	1512.3
333.15	100000.00	1543.1
343.15	100.00	1104.2
343.15	10000.00	1160.8
343.15	20000.00	1212.0
343.15	30000.00	1259.5
343.15	40000.00	1303.1
343.15	50000.00	1343.9
343.15	60000.00	1382.1
343.15	70000.00	1418.6
343.15	80000.00	1452.9
343.15	90000.00	1485.9
343.15	100000.00	1517.4
353.15	100.00	1066.6
353.15	10000.00	1125.7
353.15	20000.00	1179.3
353.15	30000.00	1228.1
353.15	40000.00	1273.4
353.15	50000.00	1314.9
353.15	60000.00	1354.4
353.15	70000.00	1391.3
353.15	80000.00	1426.7
353.15	90000.00	1460.4
353.15	100000.00	1492.3
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.67]	kPa	[322.72; 461.92]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.56921e+01
Coefficient B			-4.43052e+03
Coefficient C			-3.51090e+01
Temperature range, min.			322.72
Temperature range, max.			461.92
Pvap	1.33	kPa	322.72	Calculated Property
Pvap	2.93	kPa	338.19	Calculated Property
Pvap	5.95	kPa	353.65	Calculated Property
Pvap	11.33	kPa	369.12	Calculated Property
Pvap	20.38	kPa	384.59	Calculated Property
Pvap	34.88	kPa	400.05	Calculated Property
Pvap	57.14	kPa	415.52	Calculated Property
Pvap	90.06	kPa	430.99	Calculated Property
Pvap	137.18	kPa	446.45	Calculated Property
Pvap	202.67	kPa	461.92	Calculated Property

Similar Compounds

Find more compounds similar to Ethane, 1,1'-oxybis[2-methoxy-.

Mixtures

• Carbon dioxide + Ethane, 1,1'-oxybis[2-methoxy-
• Ethane, 1,1'-oxybis[2-methoxy- + 1-Butanol
• Ethanol + Ethane, 1,1'-oxybis[2-methoxy-
• Ethane, 1,1'-oxybis[2-methoxy- + Cyclohexane + «beta» Carotene
• n-Hexane + Ethane, 1,1'-oxybis[2-methoxy- + «beta» Carotene
• Toluene + Ethane, 1,1'-oxybis[2-methoxy- + «beta» Carotene
• 1-Hexene + Ethane, 1,1'-oxybis[2-methoxy- + «beta» Carotene
• Ethane, 1,1'-oxybis[2-methoxy- + Water
• Ethane, 1,1'-oxybis[2-methoxy- + Ethane, 1,2-dichloro-
• Ethane, 1,1'-oxybis[2-methoxy- + Norflurane
• Difluoromethane + Ethane, 1,1'-oxybis[2-methoxy-
• Ethane, 1,1'-oxybis[2-methoxy- + Ethane, 1,1-difluoro-
• Ethane, 1,1'-oxybis[2-methoxy- + Propane, 1,1,1,3,3-pentafluoro
• Methane + Ethane, 1,1'-oxybis[2-methoxy-
• Ethane + Ethane, 1,1'-oxybis[2-methoxy-
• Ethane, 1,1'-oxybis[2-methoxy- + Propane, 1,1,1,3,3,3-hexafluoro-

Sources

• Crippen Method
• Temperature and Pressure Dependences of Thermophysical Properties of Some Ethylene Glycol Dimethyl Ethers from Ultrasonic Measurements
• Density, viscosity and solubility of carbon dioxide in glymes
• Vapor-liquid equilibria of difluoromethane + N,N-dimethylacetamide, difluoromethane + dimethylether diethylene glycol and 1,1-difluoroethane + dimethylether diethylene glycol systems
• Vapor-liquid equilibrium measurement of1,1,1,3,3-pentafluoropropane + N,N-dimethylformamide/diethyleneglycol dimethyl ether/N-methyl-2-pyrrolidone working fluids forabsorption power cycle
• Surface tension of four oxygenated fuels: experiment and correlation
• Excess molar enthalpies and volumes of binary mixtures of nonafluorobutylmethylether with ethylene glycol ethers at T = 298.15 K
• Non-ideal behaviour of a room temperature ionic liquid in an alkoxyethanol or poly ethers at T = (298.15 to 318.15) K
• Thermophysical properties of glycols and glymes
• Isothermal Vapor Liquid Equilibrium of HFC-161 + DMETrEG within the Temperature Range of 293.15 353.15 K and Comparison for HFC-161 Combined with Different Absorbents
• Compressed Liquid Densities of Binary Mixtures of 1-Butanol and Diethylene Glycol Dimethyl Ether from (283 to 363) K at Pressures up to 100 MPa
• Liquid Densities and Refractive Indices of Binary Mixtures for the Dimethyl Ether of a Glycol + Ethanol from T=288.15 K to 318.15 K
• Volumetric Properties of Monoethylene Glycol Dimethyl Ether and Diethylene Glycol Dimethyl Ether up to 60 MPa
• Solubility Study of Methane and Ethane In Promising Physical Solvents for Natural Gas Sweetening Operations
• Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with 2,5,8-Trioxanonane, 2-Propanone, and Cyclohexanone
• Volumetric and Surface Properties of Aqueous Mixtures of Polyethers at T = (298.15, 308.15, and 318.15) K
• Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
• Excess Properties and Spectral Investigation for the Binary System Diethylene Glycol Dimethyl Ether + Water at T = (293.15, 298.15, 303.15, 308.15 and 313.15) K
• Measurement and Correlation of Isothermal Vapor Liquid Equilibrium of 1,1,1,3,3-Pentafluoropropane + N,N-Dimethylacetamide and 1,1,1,3,3,3-Hexafluoropropane + N,N-Dimethylacetamide/Diethylene Glycol Dimethyl Ether Systems
• Thermal Conductivity Measurement of Polyglycol Alkyl Ethers at Temperatures from (303.15 to 393.15) K
• p-T-x Measurements for Some Working Fluids for an Absorption Heat Transformer: 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylether Diethylene Glycol (DMEDEG) and Dimethylether Triethylene Glycol (DMETrEG)
• Density, Speed of Sound, and Refractive Index of Aqueous Binary Mixtures of Some Glycol Ethers at T = 298.15 K
• Joback Method
• Aqueous Solubility Prediction Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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