Ternary Solubility Data for Systems Involving 1-Propanol and Water

Soluting-In, Soluting-Out, and Washing-Out Effects of Various Additives on Aqueous 1-Butanol Solutions

“…The experimental cloud point data obtained for ternary systems of {1-butanol in the PEG aqueous solutions} and {1-butanol in the IL aqueous solutions} are novel, and there are no data in the available literature for comparison. The graphical comparisons of the data obtained here for {1-butano in the amino acid aqueous solutions} and {1-butanol in the 1-/2-propanol aqueous solutions} with the relevant data reported in the literature ,− are provided in Figures S10–S23 of the Supporting Information, as 1-butanol mass fraction against water mass fraction at different temperatures. From these figures, it can be seen that the liquid–liquid equilibrium data of {1-butanol + water + glycine} (Figure S11), {1-butanol + water + serine} (Figure S12), {1-butanol + water + alanine} ( Figure S13), {1-butanol + water + 1-propanol} (Figures S14–S19), − and {1-butanol + water + 2-propanol} (Figures S20–S22) are generally in a good consistency with the literature data.…”

“…The graphical comparisons of the data obtained here for {1-butano in the amino acid aqueous solutions} and {1-butanol in the 1-/2-propanol aqueous solutions} with the relevant data reported in the literature ,− are provided in Figures S10–S23 of the Supporting Information, as 1-butanol mass fraction against water mass fraction at different temperatures. From these figures, it can be seen that the liquid–liquid equilibrium data of {1-butanol + water + glycine} (Figure S11), {1-butanol + water + serine} (Figure S12), {1-butanol + water + alanine} ( Figure S13), {1-butanol + water + 1-propanol} (Figures S14–S19), − and {1-butanol + water + 2-propanol} (Figures S20–S22) are generally in a good consistency with the literature data. However, Figure S10 shows a clear discrepancy between our data and ref for the {1-butanol + water + glycine} system at 313.1 K. To investigate this disagreement, the liquid–liquid equilibrium data of the binary system of {1-butanol + water} at 313.1 K were also taken from the other literature , and sketched in Figure S10.…”

IUPAC-NIST Solubility Data Series. 81. Hydrocarbons with Water and Seawater-Revised and Updated. Part 5. C7 Hydrocarbons with Water and Heavy Water

“…2 Chen and Wagner 15 Sawamura et al 55 Stephenson 58 318. 2 Dohanyosova et al 18 Ma et al 37 Sanemasa et al 51 Sanemasa et al 52 Sawamura et al 55 Bradley et al 10 318.…”

“…2 Englin et al 19 Glasoe and Schultz 21 Chen and Wagner 15 Glasoe and Schultz 21 Jones The analytical method was used. The equilibrium cell, about 140 mL, was filled with a mixture of ͑1͒ and ͑2͒, temperature controllers were set at the desired temperature, liquids were degassed, agitated and allowed to reach equilibrium for 2 h. Details of the apparatus and sampling procedures were described in the paper.…”

Phase equilibrium and PVT-properties of 0.7223H2O + 0.1242 n-C6H14 + 0.1535 n-C3H7OH ternary system

“…The measurements were performed in the range of temperature from 309.26 to 678.82 K, density from 81.0 to 485.0 kg/m 3 , and pressure up to 60 MPa. The data on phase equilibrium in the watern-hexane-n-propyl alcohol, which are available in the literature, relate largely to close-to-room temperatures [1][2][3][4]. In the widest range of parameters of state, the C v -PVT properties of the 0.3950 (by weight) H 2 O + 0.2789 n-C 6 H 14 + 0.3261 n-C 3 H 7 OH mixture were investigated in [5], and the PVT-properties of the mixture of 0.3265 H 2 O + 0.4778 n-C 6 H 14 + 0.1957 n-C 3 H 7 OH -in [6].…”