Please use this identifier to cite or link to this item: https://hdl.handle.net/10321/4690
Title: Vapor-liquid equilibrium data for binary systems of 1H-Pyrrole with Butan-1-ol, Propan-1-ol, or Pentan-1-ol
Authors: Zawadzki, Maciej 
Ngema, Peterson Thokozani
Domanska, Urszula 
Naidoo, Paramespri
Ramjugernath, Deresh
Keywords: 0904 Chemical Engineering;Chemical Engineering
Issue Date: Sep-2012
Publisher: American Chemical Society (ACS)
Source: Zawadzki, M. et al. 2012. Vapor-liquid equilibrium data for binary systems of 1H-Pyrrole with Butan-1-ol, Propan-1-ol, or Pentan-1-ol. Journal of Chemical and Engineering Data. 57(9): 2520-2527. doi:10.1021/je3004194
Journal: Journal of Chemical and Engineering Data; Vol. 57, Issue 9 
Abstract: 
Isobaric and isothermal vapor-liquid equilibrium (VLE) data are presented for binary systems comprising 1H-pyrrole (pyrolle) with light alcohols. The systems measured include 1H-pyrrole + butan-1-ol at 40 kPa and T = (353.2, 363.2, and 373.2) K; 1H-pyrrole + propan-1-ol at 40 kPa and T = (348.2, 358.2, and 368.2) K; and 1H-pyrrole + pentan-1-ol at 40 kPa and T = (353.2, 363.2, and 373.2) K. Measurements were undertaken on a low-pressure dynamic still, with analysis of the equilibrium samples by gas chromatography. The 1H-pyrolle + butan-1-ol and 1H-pyrolle + pentan-1-ol systems exhibited azeotropic behavior for both the isobaric and the isothermal measurements. The measured data were modeled using the Wilson and nonrandom two-liquid (NRTL) excess Gibbs energy models, with both models correlating the data well. © 2012 American Chemical Society.
URI: https://hdl.handle.net/10321/4690
ISSN: 0021-9568
1520-5134 (Online)
DOI: 10.1021/je3004194
Appears in Collections:Research Publications (Engineering and Built Environment)

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