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                <term xml:lang="en">Mixing</term>
                <term xml:lang="en">Phase equilibria</term>
                <term xml:lang="en">Gas chromatography</term>
                <term xml:lang="en">Ethylene</term>
                <term xml:lang="en">Carbon monoxide</term>
                <term xml:lang="en">Vapor-liquid equilibrium data</term>
                <term xml:lang="en">Vapor-liquid equilibrium</term>
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              <p>In this work, vapor-liquid equilibrium data of the carbon monoxide-ethylene binary system have been measured at five isotherms ranging from (233.73 to 273.18) K, with pressure ranging from (1.4 to 6.1) MPa. The measurements were performed using a "static-analytic" apparatus, equipped with two pneumatic rapid on-line sampler-injector (ROLSI) capillary samplers, with phase analysis via gas chromatography. The uncertainties in the measurements were within ± 0.02 K, ± 0.6 kPa, and ± 0.003 for temperature, pressure, and mole fractions, respectively. The measured data are correlated using two models, the Peng-Robinson equation of state with the generalized α function and the van der Waals mixing rules and the Soave-Redlich-Kwong equation of state coupled with the Twu et al. α function and mixing rules.</p>
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