Chemical Properties of Ethanol, 2-(1-methylethoxy)- (CAS 109-59-1)

Ethanol, 2-(1-methylethoxy)-

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InChI
InChI=1S/C5H12O2/c1-5(2)7-4-3-6/h5-6H,3-4H2,1-2H3
InChI Key
HCGFUIQPSOCUHI-UHFFFAOYSA-N
Formula
C5H12O2
SMILES
CC(C)OCCO
Molecular Weight1
104.15
CAS
109-59-1
Other Names
  • 2-Isopropoxyethanol
  • 2-[(1-Methylethyl)oxy]ethanol
  • 4-Methyl-3-oxa-1-pentanol
  • Dowanal EiPAT
  • Dowanol EiPAT
  • Ethanol, 2-isopropoxy-
  • Ethylene glycol isopropyl ether
  • Ethylene glycol monisopropyl ether
  • Ethylene glycol monoisopropyl
  • Ethylene glycol monoisopropyl ether
  • Isopropyl Cellosolve
  • Isopropyl Oxitol
  • Isopropyl glycol
  • Monoisopropyl ether of ethylene glycol
  • NSC 1259
  • Ucar AC
  • «beta»-Hydroxyethyl isopropyl ether
  • «beta»-Hydroxyethyl isopropyl ether
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Contents

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

Physical Properties

Property Value Unit Source
Δf -253.04 kJ/mol Joback Calculated Property
Δfgas -436.26 kJ/mol Joback Calculated Property
Δfus 10.46 kJ/mol Joback Calculated Property
Δvap [50.10; 50.14] kJ/mol Show Hide
Δvap 50.14 kJ/mol NIST
Δvap 50.10 ± 0.10 kJ/mol NIST
log10WS -0.38 Crippen Calculated Property
logPoct/wat 0.404 Crippen Calculated Property
McVol 93.050 ml/mol McGowan Calculated Property
Pc 3834.03 kPa Joback Calculated Property
Inp 768.00 NIST
Tboil 414.70 K NIST
Tc 593.40 K Joback Calculated Property
Tfus 214.16 K Joback Calculated Property
Vc 0.346 m3/kmol Joback Calculated Property

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,gas [191.34; 238.21] J/mol×K [427.96; 593.40] Show Hide
Cp,gas 191.34 J/mol×K 427.96 Joback Calculated Property
Cp,gas 199.79 J/mol×K 455.53 Joback Calculated Property
Cp,gas 207.98 J/mol×K 483.11 Joback Calculated Property
Cp,gas 215.92 J/mol×K 510.68 Joback Calculated Property
Cp,gas 223.60 J/mol×K 538.25 Joback Calculated Property
Cp,gas 231.03 J/mol×K 565.83 Joback Calculated Property
Cp,gas 238.21 J/mol×K 593.40 Joback Calculated Property
Cp,liquid 238.80 J/mol×K 298.15 NIST
η [0.0002180; 0.1081645] Pa×s [214.16; 427.96] Show Hide
η 0.1081645 Pa×s 214.16 Joback Calculated Property
η 0.0183815 Pa×s 249.79 Joback Calculated Property
η 0.0048625 Pa×s 285.43 Joback Calculated Property
η 0.0017280 Pa×s 321.06 Joback Calculated Property
η 0.0007551 Pa×s 356.69 Joback Calculated Property
η 0.0003835 Pa×s 392.33 Joback Calculated Property
η 0.0002180 Pa×s 427.96 Joback Calculated Property
ΔvapH [40.42; 45.10] kJ/mol [377.00; 414.70] Show Hide
ΔvapH 45.10 kJ/mol 377.00 NIST
ΔvapH 40.42 kJ/mol 414.70 NIST
Pvap [60.00; 100.00] kPa [398.12; 414.21] Show Hide
Pvap 60.00 kPa 398.12 Isobari...
Pvap 80.00 kPa 407.13 Isobari...
Pvap 100.00 kPa 414.21 Isobari...
n0 1.40790 298.15 Density...

Pressure Dependent Properties

Property Value Unit Pressure (kPa) Source
Tboilr [316.20; 417.20] K [1.70; 99.10] Show Hide
Tboilr 316.20 K 1.70 NIST
Tboilr 417.20 K 99.10 NIST

Datasets

  1. Viscosity, Pa*s (1)
  2. Mass density, kg/m3 (1)

Viscosity, Pa*s

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Viscosity, Pa*s - Liquid
293.15 20000.00 0.0029
293.15 40000.00 0.0035
293.15 60000.00 0.0041
293.15 80000.00 0.0047
293.15 100000.00 0.0052
303.15 20000.00 0.0023
303.15 40000.00 0.0027
303.15 60000.00 0.0031
303.15 80000.00 0.0036
303.15 100000.00 0.0040
313.15 20000.00 0.0019
313.15 40000.00 0.0022
313.15 60000.00 0.0025
313.15 80000.00 0.0028
313.15 100000.00 0.0032
323.15 20000.00 0.0015
323.15 40000.00 0.0017
323.15 60000.00 0.0020
323.15 80000.00 0.0023
323.15 100000.00 0.0026
333.15 20000.00 0.0013
333.15 40000.00 0.0015
333.15 60000.00 0.0017
333.15 80000.00 0.0020
333.15 100000.00 0.0022
343.15 20000.00 0.0010
343.15 40000.00 0.0012
343.15 60000.00 0.0014
343.15 80000.00 0.0017
343.15 100000.00 0.0019
353.15 20000.00 0.0009
353.15 40000.00 0.0011
353.15 60000.00 0.0012
353.15 80000.00 0.0014
353.15 100000.00 0.0015
Reference

Mass density, kg/m3

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
293.15 100.00 904.0
293.15 5000.00 907.3
293.15 10000.00 910.8
293.15 15000.00 914.1
293.15 20000.00 917.3
293.15 25000.00 920.4
293.15 30000.00 923.6
293.15 35000.00 926.4
293.15 40000.00 929.2
293.15 45000.00 932.0
293.15 50000.00 934.5
293.15 55000.00 937.1
293.15 60000.00 939.6
303.15 100.00 895.0
303.15 5000.00 898.4
303.15 10000.00 902.1
303.15 15000.00 905.5
303.15 20000.00 908.8
303.15 25000.00 912.1
303.15 30000.00 915.2
303.15 35000.00 918.2
303.15 40000.00 921.2
303.15 45000.00 924.0
303.15 50000.00 927.0
303.15 55000.00 929.7
303.15 60000.00 932.1
313.15 100.00 885.5
313.15 5000.00 889.2
313.15 10000.00 893.2
313.15 15000.00 896.9
313.15 20000.00 900.4
313.15 25000.00 903.7
313.15 30000.00 907.2
313.15 35000.00 910.2
313.15 40000.00 913.3
313.15 45000.00 916.2
313.15 50000.00 919.1
313.15 55000.00 921.9
313.15 60000.00 924.8
323.15 100.00 875.9
323.15 5000.00 880.1
323.15 10000.00 884.3
323.15 15000.00 888.2
323.15 20000.00 891.9
323.15 25000.00 895.4
323.15 30000.00 899.0
323.15 35000.00 902.3
323.15 40000.00 905.4
323.15 45000.00 908.5
323.15 50000.00 911.4
323.15 55000.00 914.5
323.15 60000.00 917.3
333.15 100.00 866.4
333.15 5000.00 871.0
333.15 10000.00 875.2
333.15 15000.00 879.4
333.15 20000.00 883.3
333.15 25000.00 887.0
333.15 30000.00 890.7
333.15 35000.00 894.2
333.15 40000.00 897.4
333.15 45000.00 900.7
333.15 50000.00 903.6
333.15 55000.00 906.9
333.15 60000.00 910.0
343.15 100.00 856.8
343.15 5000.00 861.5
343.15 10000.00 866.1
343.15 15000.00 870.5
343.15 20000.00 874.7
343.15 25000.00 878.6
343.15 30000.00 882.5
343.15 35000.00 886.1
343.15 40000.00 889.5
343.15 45000.00 893.1
343.15 50000.00 896.4
343.15 55000.00 899.4
343.15 60000.00 902.5
353.15 100.00 846.8
353.15 5000.00 851.9
353.15 10000.00 856.7
353.15 15000.00 861.6
353.15 20000.00 865.8
353.15 25000.00 870.0
353.15 30000.00 874.1
353.15 35000.00 877.8
353.15 40000.00 881.6
353.15 45000.00 885.2
353.15 50000.00 888.3
353.15 55000.00 891.7
353.15 60000.00 894.9
Reference

Correlations

Property Value Unit Temperature (K) Source
Pvap [1.33; 202.65] kPa [320.62; 436.38] The Yaw... Show Hide
Equationln(Pvp) = A + B/(T + C)
Coefficient A1.67352e+01
Coefficient B-4.32941e+03
Coefficient C-5.73960e+01
Temperature range, min.320.62
Temperature range, max.436.38
Pvap 1.33 kPa 320.62 Calculated Property
Pvap 2.87 kPa 333.48 Calculated Property
Pvap 5.77 kPa 346.34 Calculated Property
Pvap 10.92 kPa 359.21 Calculated Property
Pvap 19.62 kPa 372.07 Calculated Property
Pvap 33.68 kPa 384.93 Calculated Property
Pvap 55.51 kPa 397.79 Calculated Property
Pvap 88.20 kPa 410.66 Calculated Property
Pvap 135.66 kPa 423.52 Calculated Property
Pvap 202.65 kPa 436.38 Calculated Property

Similar Compounds

2-(2-isopropoxyethoxy)ethanol. 1-Propanol, 2-ethoxy-. Ethanol, 2-(1,1-dimethylethoxy)-. Ethanol, 2-ethoxy-. 1-Propanol, 2,2'-oxybis-. Isopropoxyacetic acid. Propane, 2-ethoxy-. 2-(1-methylpropoxy)ethanol. 2-Propanol, 1-(1-methylethoxy)-. Heptaethylene glycol monoethyl ether. Hexaethylene glycol monoethyl ether. Ethanol, 2-[2-(2-ethoxyethoxy)ethoxy]-. Pentaethylene glycol, monoethyl ether. 3,6,9,12-Tetraoxatetradecan-1-ol. Ethanol, 2-(2-ethoxyethoxy)-.

Find more compounds similar to Ethanol, 2-(1-methylethoxy)-.

Mixtures

Sources

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