Vapor-Liquid equilibria of the systems 1-octanol/nitrogen and 1-octanol/oxygen at pressures from 3 to 9 MPa and temperatures up to 613 K – Measured in a microcapillary with Raman spectroscopy
[Display omitted] •Acquisition of new vapor–liquid equilibrium (VLE) data at elevated temperature and pressure conditions for the binary system 1-octanol/nitrogen and 1-octanol/oxygen, which are scarce / not available in the archival literature.•Use of an in situ Raman Spectroscopy unit.•Applying a...
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Published in | Fuel (Guildford) Vol. 323; p. 124352 |
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Main Authors | , , |
Format | Journal Article |
Language | English |
Published |
Kidlington
Elsevier Ltd
01.09.2022
Elsevier BV |
Subjects | |
Online Access | Get full text |
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Summary: | [Display omitted]
•Acquisition of new vapor–liquid equilibrium (VLE) data at elevated temperature and pressure conditions for the binary system 1-octanol/nitrogen and 1-octanol/oxygen, which are scarce / not available in the archival literature.•Use of an in situ Raman Spectroscopy unit.•Applying a precise calibration and spectral evaluation procedure.•Modelling using the Peng-Robinson equation of state (PR-EOS) as well as the perturbed-chain statistical associating fluid theory (PC-SAFT)
Vapor-liquid equilibria (VLE) of the binary systems 1-octanol/nitrogen and 1-octanol/oxygen were investigated at engine-relevant temperatures (T=303to613K for 1-octanol/nitrogen; T=303to493K for 1-octanol/oxygen) and pressures (p=3to9MPa). In order to acquire vapor–liquid equilibrium data, the pressurized fuel (1-octanol) and gas (nitrogen or oxygen) are mixed in a T-junction, where a Taylor flow of alternating liquid-phase and vapor-phase segments is formed. This segmented flow passes into a microcapillary that is inserted in a steal heating block, in which the equilibrium compositions of both phases are measured by in situ Raman spectroscopy. The measured Raman signal ratios are correlated to mole fractions by a calibration, performed in the unsaturated vapor and liquid phase regimes. The obtained VLE data agree well with the few available literature data points. The VLE compositions calculated by the Peng-Robinson equation of state (PR-EoS) and perturbed-chain statistical associating fluid theory (PC-SAFT) were furthermore compared to the here obtained experimental data. Both models show good agreement as indicated by the absolute average deviations (AAD), that are at maximum 9.5 % for the saturated vapor phase and 4.2 % for the saturated liquid phase. |
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ISSN: | 0016-2361 1873-7153 |
DOI: | 10.1016/j.fuel.2022.124352 |