Liquid-Liquid Equilibrium of the Ternary System Water/Formic Acid/1-Pentanol at T= 308.2 K

Hossein Ghanadzadeh, Shahin Asan and Milad Sangashekan
Additional contact information
Hossein Ghanadzadeh: University of Guilan, Rasht, Iran
Shahin Asan: University of Urmia, Urmia, Iran
Milad Sangashekan: University of Guilan, Rasht, Iran

International Journal of Chemoinformatics and Chemical Engineering (IJCCE), 2013, vol. 3, issue 2, 85-93

Abstract: Liquid–liquid equilibrium data for the (water + Formic acid + 1-pentanol) ternary system were determined at T = (308.2) K in ambient pressure. This ternary system exhibits type-1 behavior of LLE. Distribution coefficients and separation factors were measured to evaluate the extracting capacity of the solvent. The consistency of the experimental tie-line data was determined through the Othmer–Tobias and Bachman equations. The raw experimental data were correlated using the NRTL and UNIQUAC models. The average root-mean-square deviation between the experimental and calculated mass fractions was 0.488% and 0.465%.

Date: 2013
References: Add references at CitEc
Citations:

Downloads: (external link)
http://services.igi-global.com/resolvedoi/resolve. ... 018/ijcce.2013070106 (application/pdf)

Related works:
This item may be available elsewhere in EconPapers: Search for items with the same title.

Export reference: BibTeX RIS (EndNote, ProCite, RefMan) HTML/Text

Persistent link: https://EconPapers.repec.org/RePEc:igg:jcce00:v:3:y:2013:i:2:p:85-93

Access Statistics for this article

International Journal of Chemoinformatics and Chemical Engineering (IJCCE) is currently edited by Rama Rao Karri

More articles in International Journal of Chemoinformatics and Chemical Engineering (IJCCE) from IGI Global
Bibliographic data for series maintained by Journal Editor ().