1978
DOI: 10.1021/je60076a009
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Extraction of acetonitrile from aqueous solutions. 1. Ternary liquid equilibriums

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Cited by 18 publications
(11 citation statements)
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“…For the systems acetonitrile-aromatic hydrocarbons and water-acetonitrile, the values of the parameters were obtained by submitting to regression vapor-liquid equilibrium (VLE) data of each examined binary system: In particular, two sets of Isobarlc VLE data at 28.0 and 101.3 kPa (9), for the system acetonitrile-aromatic hydrocarbons, and two sets of VLE data, one Isobarlc at 101.3 kPa (10) and the other isothermal at 60 °C (11), for the system acetronltrlle-water. The calculation procedure, described In detail elsewhere (9), was based on the minimization of the objective function, S: (5) The weighting factors FP, FT, and Fri used for each binary system are given in Table VII. acetonitrile (l)-m-xylene (3) 1 1 60 acetonitrile (l)-p-xylene (3) 1 1 60 acetonitrile (l)-ethylbenzene (3) 1 1 60 acetonitrile (l)-water (2) 0.75…”
Section: Resultsmentioning
confidence: 99%
See 1 more Smart Citation
“…For the systems acetonitrile-aromatic hydrocarbons and water-acetonitrile, the values of the parameters were obtained by submitting to regression vapor-liquid equilibrium (VLE) data of each examined binary system: In particular, two sets of Isobarlc VLE data at 28.0 and 101.3 kPa (9), for the system acetonitrile-aromatic hydrocarbons, and two sets of VLE data, one Isobarlc at 101.3 kPa (10) and the other isothermal at 60 °C (11), for the system acetronltrlle-water. The calculation procedure, described In detail elsewhere (9), was based on the minimization of the objective function, S: (5) The weighting factors FP, FT, and Fri used for each binary system are given in Table VII. acetonitrile (l)-m-xylene (3) 1 1 60 acetonitrile (l)-p-xylene (3) 1 1 60 acetonitrile (l)-ethylbenzene (3) 1 1 60 acetonitrile (l)-water (2) 0.75…”
Section: Resultsmentioning
confidence: 99%
“…Francis (3) reported in small triangular graphs the binodal curves for the systems acetonitrile-water-benzene and acetonitrile-water-toluene at 25 °C. Rao et al (4) reported complete LLE data for the system acetonitrile-water-toluene at 30 °C, and Rao et al (5) reported similar data for the system acetonitrile-water-mixture of xylenes at 31 °C.…”
Section: Introductionmentioning
confidence: 89%
“…However, the comparison between ACN and acetone shows that ACN exhibits a slightly faster mass transfer. The marginal difference can be explained by a slightly larger ACN mixing gap as the EFCE test system under otherwise comparable physical properties …”
Section: Resultsmentioning
confidence: 99%
“…The marginal difference can be explained by a slightly larger ACN mixing gap as the EFCE test system under otherwise comparable physical properties. [33,36,37] At constant volumetric flow _ V = 14 μL Á s −1 and concentration c ACN,0 = 10 wt% with varied droplet size (see Figure 7), the mass transfer is faster with a higher surface to droplet volume ratio at 0 mm rising height. Under the same conditions as in Figure 7, the Raman measurement inside the droplet clearly shows a similar influence of the volume to surface ratio after droplet formation (see Figure 8).…”
Section: Droplet Suction (Fixed Hanging and Moving Droplet)mentioning
confidence: 99%
“…A large reflux ratio is usually accompanied by large condensing and reboiling requirements, and hence, a higher operating cost [9]. The extraction of acetonitrile from its aqueous solution by multiple solvents has also been tested [10][11][12].…”
Section: Introductionmentioning
confidence: 99%