Isobaric Vapor–Liquid Equilibria of Binary Systems Containing Oxygenated Biofuel Compounds (Ethanol + Cyclopentanone, Propyl Butanoate + 4-Methylphenol, Cyclopentanone + Propane-1,2-diol) at Atmospheric Pressure
Author:
Affiliation:
1. School of Mechanical, Medical and Process Engineering, Queensland University of Technology, 2 George Street, Brisbane, Queensland4000, Australia
Funder
Queensland University of Technology
Publisher
American Chemical Society (ACS)
Subject
General Chemical Engineering,General Chemistry
Link
https://pubs.acs.org/doi/pdf/10.1021/acs.jced.2c00624
Reference39 articles.
1. Fractionation of bio-oil produced from hydrothermal liquefaction of microalgae by liquid-liquid extraction
2. A review of fractional distillation to improve hydrothermal liquefaction biocrude characteristics; future outlook and prospects
3. Phase equilibria of systems containing oxygenated compounds: Polar or “pseudo-association” approach?
4. Kiran, E.; Brennecke, J. F. Supercritical Fluid Engineering Science: Fundamentals and Applications; American Chemical Society: Washington, United States, 1993; p 422.
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1. Effect of thermodynamic models on process modelling and techno-economics for biofuel. A case study using fractional distillation of an algae biocrude;Journal of Cleaner Production;2024-07
2. Isobaric Vapor–Liquid Equilibrium of Ethyl Acetate + 1-Hexanol, Methanol + 1-Hexanol, and n-Heptane + Cyclohexanol Binary System at 101.3 kPa;Journal of Chemical & Engineering Data;2023-07-31
3. Correlation and Prediction of Isobaric Vapor–Liquid Equilibria of Binary and Ternary Systems Containing Oxygenated Biofuel Compounds (Butan-2-one + 2-Methylpropan-1-ol + Cyclopentanone) at Atmospheric Pressure;Journal of Chemical & Engineering Data;2023-05-08
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