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Valorization of glycerol via continuous etherification with ethanol: Thermodynamic modeling and process optimization
Carolina M Marinho1, Caroline O T Lemos1, Karen A Resende1
1Faculdade de Engenharia Química, Universidade Federal de Uberlândia, Av. João Naves de Ávila 2121, Campus Santa Mônica - Bloco 1K, 38400-902 Uberlândia, MG, Brazil.
Glycerol valorization into chemicals is key for sustainable biorefineries. Superheated vapor-phase conversion using ethanol achieved 50% ether yield and 83% glycerol conversion, reducing mass-transfer limits.
Area of Science:
- Chemical Engineering
- Catalysis
- Sustainable Chemistry
Background:
- Glycerol valorization is crucial for biodiesel sustainability.
- Existing methods face challenges like mass-transfer limitations.
Purpose of the Study:
- Optimize superheated vapor-phase conversion of glycerol with ethanol.
- Investigate thermodynamic and experimental parameters for efficient ether production.
Main Methods:
- Integrated thermodynamic modeling (Peng-Robinson equation of state) with experimental etherification.
- Evaluated effects of temperature, catalyst loading, molar ratio, and pressure over a β-zeolite catalyst.
Main Results:
- Achieved maximum ether yield of 50% and glycerol conversion of 83% under optimized conditions.
- Identified optimal conditions: 319°C, 7.9 MPa, single-phase superheated vapor state.
- Demonstrated competitive performance compared to existing glycerol upgrading technologies.
Conclusions:
- Superheated vapor-phase processing offers an efficient route for glycerol waste valorization.
- Results provide guidance for process optimization and scale-up for sustainable chemical production.
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