SDS Volume (3748)

Volume 69. Ternary Alcohol-Hydrocarbon-Water Systems, p None

Original Measurements

Arda, N.; Sayar, A. A.; Fluid Phase Equilib. 73, 129-138 (1992).

Variables:

Room Temp: 293 $\pu{K}$

Prepared by:

A. Skrzecz

Method/Apparatus/Procedure:

Solubility measurements were made in an equilibrium cell with a stirrer [1] by titration of binary mixtures of known composition with the third component. This was done using 2-propanol for heterogeneous hydrocarbon-water mixtures, until the turbidity had disappeared and 2,2,4-trimethylpentane for homogeneous alcohol-water mixtures until cloudiness was observed. Tie lines were measured in the same cell filled with ternary heterogeneous mixtures of known composition. Mixtures were stirred for 1 h and after separation the samples of each phase were twice analyzed; 2-propanol concentration was determined by GLC using Supelco Carbopack-C 0.2%, CW-1500, 60/80 column on Aerograph Hydrogen-Flame, Model 600-C ($\ce{N2}$, 12-13 mL/s, 373 K). Water was determined by the Karl Fischer method.

Source and Purity of Materials:
  1. Merck, dried over anhydrous $\ce{K2CO3}$, distilled, with middle $\pu{80\%}$ collected;
    impurities $\le \pu{0.1\%}$ by GLC; BP = $\pu{355.7 \pm 0.1 K}$,
    $n_{D}^{25} = \pu{1.3756 \pm 0.0005}$
    $\rho^{25} = \pu{783.2 \pm 0.1 kg m-3}$.
  2. Merck, dried over anhydrous $\ce{K2CO3}$, distilled, with middle $\pu{60\%}$ collected;
    impurities $\le \pu{0.2\%}$ by GLC; BP = $\pu{37 \pm 0.1 K}$,
    $n(\pu{293 K},D) = \pu{1.3890 \pm 0.0005}$,
    $\rho(\pu{293 K}) = \pu{695.8 \pm 0.1 kg m-3}$
  3. Source not specified.
Estimated Errors:

Ambient temperature: $\pu{\pm 0.1 K}$.
Solubility: Solubility curve $x = \pu{\pm 0.0025}$
2-propanol $x = \pu{\pm 0.0050}$
water $x = \pu{\pm 0.0025}$

References

1 Sayar, A. A.; J. Chem. Eng. Data 36, 61 (1991).

Components:
  1. 2-Propanol, $\ce{ C3H8O }$; [67-63-0] NIST WebBook
  2. 2,2,4-Trimethylpentane, $\ce{ C8H18 }$; [540-84-1] NIST WebBook
  3. Water, $\ce{ H2O }$; [7732-18-5] NIST WebBook
Experimental Data
Compositions along the saturation curve
$T$ (°C) $T$ ($\pu{K}$) w1 w2 $x_{1}$ $x_{2}$
25.0293.2 0.00002.8 x 10-3 0.00004 x 10-4
25.0293.2 0.01456.0 x 10-3 4.4 x 10-31.0 x 10-3
25.0293.2 0.04069.4 x 10-3 0.01261.5 x 10-3
25.0293.2 0.11520.0125 0.03802.2 x 10-3
25.0293.2 0.15820.0151 0.05412.7 x 10-3
25.0293.2 0.19070.0207 0.06733.8 x 10-3
25.0293.2 0.25930.0193 0.09693.8 x 10-3
25.0293.2 0.28110.0218 0.10744.4 x 10-3
25.0293.2 0.32920.0210 0.13134.4 x 10-3
25.0293.2 0.38740.0251 0.16415.6 x 10-3
25.0293.2 0.43800.0297 0.19657.0 x 10-3
25.0293.2 0.46320.0312 0.21387.6 x 10-3
25.0293.2 0.50860.0320 0.24718.2 x 10-3
25.0293.2 0.56840.0573 0.30770.0163
25.0293.2 0.58930.0739 0.33640.0222
25.0293.2 0.61730.1137 0.39210.0380
25.0293.2 0.62080.1389 0.41510.0489
25.0293.2 0.61560.1667 0.43060.0613
25.0293.2 0.59300.2147 0.44010.0838
25.0293.2 0.57440.2521 0.44670.1031
25.0293.2 0.53510.3088 0.43920.1333
25.0293.2 0.51040.3388 0.42830.1496
25.0293.2 0.50670.3547 0.43850.1615
25.0293.2 0.46120.4269 0.43550.2121
25.0293.2 0.40960.4913 0.41020.2588
25.0293.2 0.36160.5580 0.39160.3179
25.0293.2 0.26500.6886 0.33890.4632
25.0293.2 0.19330.7752 0.27370.5775
25.0293.2 0.05850.9294 0.09950.8318
25.0293.2 0.02740.9606 0.04780.8823
25.0293.2 0.00000.9921 0.00000.9519

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