Chemical Properties of Butane, 1,1'-[oxybis(2,1-ethanediyloxy)]bis- (CAS 112-73-2)

Butane, 1,1'-[oxybis(2,1-ethanediyloxy)]bis-

InChI
InChI=1S/C12H26O3/c1-3-5-7-13-9-11-15-12-10-14-8-6-4-2/h3-12H2,1-2H3
InChI Key
KZVBBTZJMSWGTK-UHFFFAOYSA-N
Formula
C12H26O3
SMILES
CCCCOCCOCCOCCCC
Molecular Weight1
218.33
CAS
112-73-2
Other Names
  • 2,2'-dibutoxyethyl ether
  • 2-(2-butoxyethoxy)-1-butoxyethane
  • 2-butoxyethyl ether
  • 5,8,11-trioxapentadecane
  • Butyl diglyme
  • Dibutylether diethylenglykolu
  • Diethylene glycol di-n-butyl ether
  • Ether, bis(butoxyethyl)
  • bis(2-butoxyethyl) ether
  • butex
  • dibutyl carbitol
  • diethylene glycol dibutyl ether
  • ether, bis(2-butoxyethyl)
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Physical Properties

Property Value Unit Source
ω 0.7115 Relay (1.0) Calculated Property
Δf -264.84 kJ/mol Joback Calculated Property
Δfgas -667.39 kJ/mol Relay (1.0) Calculated Property
Δfus 30.40 kJ/mol Joback Calculated Property
Δvap 73.80 ± 1.70 kJ/mol NIST
IE 9.44 eV Relay (1.0) Calculated Property
log10WS -2.53 Relay (1.0) Calculated Property
logPoct/wat 2.636 Crippen Calculated Property
McVol 197.550 ml/mol McGowan Calculated Property
Pc 1706.12 kPa Joback Calculated Property
I [1727.00; 1727.00]   Show Hide
I 1727.00 NIST
I 1727.00 NIST
Tboil [529.15; 529.20] K Show Hide
Tboil 529.20 K NIST
Tboil 529.15 K NIST
Tboil 529.15 K NIST
Tc 687.10 K Relay (1.0) Calculated Property
Tfus [212.95; 212.95] K Show Hide
Tfus 212.95 K NIST
Tfus 212.95 K NIST
Vc 0.769 m3/kmol Relay (1.0) Calculated Property

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,gas [493.15; 581.42] J/mol×K [541.42; 702.57] Show Hide
Cp,gas 493.15 J/mol×K 541.42 Joback Calculated Property
Cp,gas 509.14 J/mol×K 568.28 Joback Calculated Property
Cp,gas 524.63 J/mol×K 595.14 Joback Calculated Property
Cp,gas 539.60 J/mol×K 622.00 Joback Calculated Property
Cp,gas 554.06 J/mol×K 648.86 Joback Calculated Property
Cp,gas 568.00 J/mol×K 675.71 Joback Calculated Property
Cp,gas 581.42 J/mol×K 702.57 Joback Calculated Property
Cp,liquid [456.53; 517.89] J/mol×K [312.57; 421.48] Show Hide
Cp,liquid 456.53 J/mol×K 312.57 Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
Cp,liquid 460.90 J/mol×K 322.47 Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
Cp,liquid 465.49 J/mol×K 332.37 Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
Cp,liquid 470.51 J/mol×K 342.27 Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
Cp,liquid 475.75 J/mol×K 352.18 Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
Cp,liquid 480.33 J/mol×K 362.08 Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
Cp,liquid 486.88 J/mol×K 371.98 Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
Cp,liquid 493.65 J/mol×K 381.88 Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
Cp,liquid 500.42 J/mol×K 391.78 Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
Cp,liquid 505.44 J/mol×K 401.68 Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
Cp,liquid 512.21 J/mol×K 411.58 Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
Cp,liquid 517.89 J/mol×K 421.48 Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
η [0.0001156; 0.0020127] Pa×s [291.69; 541.42] Show Hide
η 0.0020127 Pa×s 291.69 Joback Calculated Property
η 0.0009287 Pa×s 333.31 Joback Calculated Property
η 0.0005088 Pa×s 374.93 Joback Calculated Property
η 0.0003144 Pa×s 416.55 Joback Calculated Property
η 0.0002120 Pa×s 458.18 Joback Calculated Property
η 0.0001527 Pa×s 499.80 Joback Calculated Property
η 0.0001156 Pa×s 541.42 Joback Calculated Property
ΔvapH 56.60 kJ/mol 410.50 NIST
Pvap [2.50; 25.58] kPa [403.15; 473.15] Show Hide
Pvap 2.50 kPa 403.15 Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap 3.61 kPa 413.15 Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap 5.26 kPa 423.15 Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap 7.39 kPa 433.15 Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap 10.43 kPa 443.15 Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap 14.23 kPa 453.15 Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap 16.61 kPa 458.15 Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap 19.19 kPa 463.15 Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap 22.18 kPa 468.15 Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap 25.58 kPa 473.15 Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
ρl 878.55 kg/m3 298.15 Speeds of Sound and Isentropic Compressibilities of n-Alkoxyethanols and Polyethers with Propylamine at 298.15K

Datasets

Mass density, kg/m3

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
283.15 100.00 891.3
283.15 1000.00 891.8
283.15 3000.00 893.2
283.15 5000.00 894.3
283.15 10000.00 897.7
283.15 15000.00 900.9
283.15 20000.00 904.3
283.15 25000.00 906.9
283.15 30000.00 909.9
283.15 35000.00 912.8
283.15 40000.00 915.3
283.15 50000.00 920.5
283.15 60000.00 925.4
293.15 100.00 882.9
293.15 1000.00 883.1
293.15 3000.00 884.8
293.15 5000.00 885.9
293.15 10000.00 889.6
293.15 15000.00 892.9
293.15 20000.00 896.1
293.15 25000.00 899.3
293.15 30000.00 902.3
293.15 35000.00 905.1
293.15 40000.00 907.9
293.15 50000.00 913.6
293.15 60000.00 918.2
303.15 100.00 874.5
303.15 1000.00 875.1
303.15 3000.00 876.6
303.15 5000.00 878.2
303.15 10000.00 881.8
303.15 15000.00 885.2
303.15 20000.00 888.42
303.15 25000.00 891.8
303.15 30000.00 894.9
303.15 35000.00 897.9
303.15 40000.00 900.8
303.15 50000.00 906.4
303.15 60000.00 911.8
313.15 100.00 866.1
313.15 1000.00 866.41
313.15 3000.00 868.1
313.15 5000.00 869.8
313.15 10000.00 873.5
313.15 15000.00 877.2
313.15 20000.00 880.7
313.15 25000.00 884.1
313.15 30000.00 887.1
313.15 35000.00 890.5
313.15 40000.00 893.3
313.15 50000.00 899.4
313.15 60000.00 904.9
323.15 100.00 857.2
323.15 1000.00 858.2
323.15 3000.00 859.8
323.15 5000.00 861.5
323.15 10000.00 865.4
323.15 15000.00 869.2
323.15 20000.00 873.1
323.15 25000.00 876.5
323.15 30000.00 879.8
323.15 35000.00 883.1
323.15 40000.00 886.3
323.15 50000.00 892.4
323.15 60000.00 898.8
333.15 100.00 849.1
333.15 1000.00 850.0
333.15 3000.00 851.6
333.15 5000.00 853.3
333.15 10000.00 857.5
333.15 15000.00 861.4
333.15 20000.00 865.4
333.15 25000.00 869.0
333.15 30000.00 872.6
333.15 35000.00 875.9
333.15 40000.00 879.5
333.15 50000.00 885.5
333.15 60000.00 891.6
343.15 100.00 840.4
343.15 1000.00 841.7
343.15 3000.00 843.5
343.15 5000.00 845.5
343.15 10000.00 849.8
343.15 15000.00 853.7
343.15 20000.00 857.9
343.15 25000.00 861.6
343.15 30000.00 865.3
343.15 35000.00 868.9
343.15 40000.00 872.3
343.15 50000.00 878.9
343.15 60000.00 884.7
353.15 100.00 832.4
353.15 1000.00 833.0
353.15 3000.00 835.1
353.15 5000.00 836.7
353.15 10000.00 841.4
353.15 15000.00 846.0
353.15 20000.00 850.3
353.15 25000.00 854.0
353.15 30000.00 857.9
353.15 35000.00 861.6
353.15 40000.00 865.1
353.15 50000.00 871.5
353.15 60000.00 878.2
363.15 100.00 823.4
363.15 1000.00 824.8
363.15 3000.00 827.1
363.15 5000.00 828.7
363.15 10000.00 833.5
363.15 15000.00 838.4
363.15 20000.00 842.8
363.15 25000.00 846.8
363.15 30000.00 850.9
363.15 35000.00 854.9
363.15 40000.00 858.5
363.15 50000.00 865.6
363.15 60000.00 872.0
Reference

Correlations

Property Value Unit Temperature (K) Source
Pvap [1.33; 202.64] kPa [398.87; 559.05] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Pvp) = A + B/(T + C)
Coefficient A1.69660e+01
Coefficient B-6.19763e+03
Coefficient C-2.72730e+01
Temperature range, min.398.87
Temperature range, max.559.05
Pvap 1.33 kPa 398.87 Calculated Property
Pvap 2.86 kPa 416.67 Calculated Property
Pvap 5.73 kPa 434.47 Calculated Property
Pvap 10.84 kPa 452.26 Calculated Property
Pvap 19.48 kPa 470.06 Calculated Property
Pvap 33.45 kPa 487.86 Calculated Property
Pvap 55.18 kPa 505.66 Calculated Property
Pvap 87.83 kPa 523.45 Calculated Property
Pvap 135.35 kPa 541.25 Calculated Property
Pvap 202.64 kPa 559.05 Calculated Property

Similar Compounds

1,2-Dibutoxyethane. 1-Butoxy-2-ethoxyethane. 2,5-Dioxanonane. Butane, 1-(2-methoxyethoxy)-. Ethanol, 2-(2-butoxyethoxy)-. 3,6,9,12,15-Pentaoxanonadecan-1-ol. 2-(2-(2-(2-(2-(2-Butoxy-ethoxy)-ethoxy)-ethoxy)-ethoxy)-ethoxy)-ethoxy)-ethanol. 3,6,9,12-Tetraoxahexadecan-1-ol. Ethanol, 2-[2-(2-butoxyethoxy)ethoxy]-. Heptaethylene glycol, butyl ether, acetate. 2-(2-(2-(2-(2-(2-(2-(2-Butoxy-ethoxy)-ethoxy)-ethoxy)-ethoxy)-ethoxy)-ethoxy)-ethoxy)-ethoxy)-ethyl acetate. 2-[2-[2-[2-(2-Butoxyethoxy)ethoxy]ethoxy]ethoxy]ethyl acetate. 2-[2-(2-Butoxyethoxy)ethoxy]ethyl acetate. 2-(2-(2-(2-(2-(2-(2-Butoxy-ethoxy)-ethoxy)-ethoxy)-ethoxy)-ethoxy)-ethoxy)-ethoxy)-ethyl acetate. 2-[2-[2-(2-Butoxyethoxy)ethoxy]ethoxy]ethyl acetate.

Find more compounds similar to Butane, 1,1'-[oxybis(2,1-ethanediyloxy)]bis-.

Mixtures

Sources

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