Numerical Simulation of Injection of Supercritical Ethylene/Methane into Nitrogen

dc.contributor.advisorDr. Jack R. Edwards, Committee Chairen_US
dc.contributor.advisorDr. Richard D. Gould, Committee Memberen_US
dc.contributor.advisorDr. Hassan A. Hassan, Committee Memberen_US
dc.contributor.authorStar, Ana Mariaen_US
dc.date.accessioned2010-04-02T18:02:56Z
dc.date.available2010-04-02T18:02:56Z
dc.date.issued2005-12-13en_US
dc.degree.disciplineAerospace Engineeringen_US
dc.degree.levelthesisen_US
dc.degree.nameMSen_US
dc.description.abstractThe present study investigates the physical mechanisms of supercritical fluid injection for pure ethylene and ethylene/methane mixtures, as well as onset of condensation upon fluid expansion. These mechanisms are considered a key enabling technology in the design of hydrocarbon-fueled scramjet engines. The numerical method combines a solution of the compressible Navier-Stokes equations for the supercritical fluid with two different approaches for condensate growth: one based on a homogeneous equilibrium assumption and the other on classical aerosol dynamics. The thermodynamic behavior of the supercritical fluid is described using the Peng-Robinson equation of state. Computational results are compared with shadowgraph and direct-lighting imaging data, mass flow measurements, mole fraction measurements and temperature measurements in the jet mixing zone, and pressure distributions within a three-dimensional injector geometry. Qualitative results involving jet structure, the appearance of a condensed phase, and the general effects of back pressure and injectant temperature are in good agreement with experimental results for pure ethylene injection. Quantitative results also display reasonable agreement with experimental results but do indicate the need for improving the model. Qualitative trends for ethylene/methane mixture injection are in moderate agreement with the experimental data, suggesting that the thermodynamic interaction between ethylene and methane as modeled by the chosen mixing rules are not sufficiently accurate. For conditions where both are applicable, a finite-rate (nucleation/growth) phase-transition model presents essentially the same bulk fluid response as a homogeneous equilibrium model with additional predictions of number density and average droplet size.en_US
dc.identifier.otheretd-12122005-154752en_US
dc.identifier.urihttp://www.lib.ncsu.edu/resolver/1840.16/1287
dc.rightsI hereby certify that, if appropriate, I have obtained and attached hereto a written permission statement from the owner(s) of each third party copyrighted matter to be included in my thesis, dissertation, or project report, allowing distribution as specified below. I certify that the version I submitted is the same as that approved by my advisory committee. I hereby grant to NC State University or its agents the non-exclusive license to archive and make accessible, under the conditions specified below, my thesis, dissertation, or project report in whole or in part in all forms of media, now or hereafter known. I retain all other ownership rights to the copyright of the thesis, dissertation or project report. I also retain the right to use in future works (such as articles or books) all or part of this thesis, dissertation, or project report.en_US
dc.subjectmethane/ethylene mixtureen_US
dc.subjectfluid injectionen_US
dc.subjectsupercritical fluidsen_US
dc.subjectPeng-Robinson Equation of Stateen_US
dc.titleNumerical Simulation of Injection of Supercritical Ethylene/Methane into Nitrogenen_US

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