Multicomponent gas transport in a Stefan diffusion column containing an azeotropic liquid mixture of acetone-n-hexane
Author:
Affiliation:
1. Department of Chemical Engineering, University of Puerto Rico, Mayagüez, Puerto Rico
Publisher
Informa UK Limited
Subject
General Chemical Engineering,General Chemistry
Link
https://www.tandfonline.com/doi/pdf/10.1080/00986445.2020.1852400
Reference60 articles.
1. Vapor−Liquid Equilibrium of the Ternary System Ethyl Acetate + Hexane + Acetone at 101.32 kPa
2. Densities, Speeds of Sound, Refractive Indices, and the Corresponding Changes of Mixing at 25 °C and Atmospheric Pressure for Systems Composed by Ethyl Acetate, Hexane, and Acetone
3. Application of Diffusion Cells to Production of Known Concentration of Gaseous Hydrocarbons
4. Measurement of gaseous diffusion coefficients at and above the normal boiling point temperature of the liquid by the Stefan-Winkelmann method.
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1. A steady two‐dimensional cylindrical mass transport model to determine binary gas diffusivities: A proof‐of‐concept theoretical development;The Canadian Journal of Chemical Engineering;2024-03-13
2. Quantitative relationship between interfacial curvature due to a liquid’s surface tension and the binary gas diffusivity estimates obtained in an isothermal Stefan column;Chemical Engineering Communications;2023-04-04
3. Theoretical reassessment of the first Stefan diffusion column experiment with a two-component liquid phase, consisting of a high-density volatile solvent and a low-density nonvolatile diluent;Chemical Engineering Communications;2022-05-19
4. Chemical engineering contributions resulting in an improved understanding of the Stefan diffusion column: A 150-year perspective;Chemical Engineering Communications;2022-04-18
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