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

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 press...

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Bibliographic Details
Main Authors: Braeuer, A.S (Author), Fechter, M.H.H (Author), Koschack, J. (Author)
Format: Article
Language:English
Published: Elsevier Ltd 2022
Subjects:
Online Access:View Fulltext in Publisher
LEADER 02115nam a2200217Ia 4500
001 10.1016-j.fuel.2022.124352
008 220517s2022 CNT 000 0 und d
020 |a 00162361 (ISSN) 
245 1 0 |a 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 
260 0 |b Elsevier Ltd  |c 2022 
856 |z View Fulltext in Publisher  |u https://doi.org/10.1016/j.fuel.2022.124352 
520 3 |a 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. © 2022 The Author(s) 
650 0 4 |a Equations of state 
650 0 4 |a High temperature and pressure 
650 0 4 |a Microfluidics 
650 0 4 |a Raman 
650 0 4 |a Vapor–liquid equilibria (VLE) 
700 1 |a Braeuer, A.S.  |e author 
700 1 |a Fechter, M.H.H.  |e author 
700 1 |a Koschack, J.  |e author 
773 |t Fuel