Liquid–Liquid Equilibrium Measurements for Model Systems Related to Catalytic Fast Pyrolysis of Biomass
Abstract
Here in this paper we report liquid-liquid mutual solubilities for binary aqueous mixtures involving 2-, 3-, and 4-ethylphenol, 2-, 3-, and 4-methoxyphenol, benzofuran, and 1H-indene for the temperature range (300 < T/K < 360). Measurements in the water-rich phase for (2-ethylphenol + water) were extended to T = 440 K to facilitate comparison with literature values. Liquid-liquid equilibrium tie-line determinations were made for four ternary systems involving (water + toluene) mixed with a third component; phenol, 3-ethylphenol, 4-methoxyphenol, or 2,4-dimethylphenol. Literature values at higher temperatures are available for the three (ethylphenol + water) systems, and, in general, good agreement is seen. The ternary system (water + toluene + phenol) has been studied previously with inconsistent results reported in the literature, and one report is shown to be anomalous. All systems are modeled with the predictive methods NIST-Modified-UNIFAC and NIST-COSMO-SAC, with generally good success in the temperature range of interest (300 < T/K < 360). This work is part of a larger project on the testing and development of predictive phase equilibrium models for compound types occurring in catalytic fast pyrolysis of biomass, and background information for the larger project is provided.
- Authors:
-
- Wiltec Research Company, Provo, UT (United States)
- National Inst. of Standards and Technology (NIST), Boulder, CO (United States). Thermodynamics Research Center, Applied Chemicals and Materials Division
- National Renewable Energy Lab. (NREL), Golden, CO (United States). National Bioenergy Center
- Publication Date:
- Research Org.:
- National Renewable Energy Laboratory (NREL), Golden, CO (United States)
- Sponsoring Org.:
- USDOE Office of Energy Efficiency and Renewable Energy (EERE), Sustainable Transportation Office. Bioenergy Technologies Office (BETO)
- OSTI Identifier:
- 1340649
- Report Number(s):
- NREL/JA-5100-66653
Journal ID: ISSN 0021-9568
- Grant/Contract Number:
- AC36-08GO28308
- Resource Type:
- Accepted Manuscript
- Journal Name:
- Journal of Chemical and Engineering Data
- Additional Journal Information:
- Journal Volume: 62; Journal Issue: 1; Journal ID: ISSN 0021-9568
- Publisher:
- American Chemical Society
- Country of Publication:
- United States
- Language:
- English
- Subject:
- 09 BIOMASS FUELS; catalytic; fast pyrolysis; biomass
Citation Formats
Jasperson, Louis V., McDougal, Rubin J., Diky, Vladimir, Paulechka, Eugene, Chirico, Robert D., Kroenlein, Kenneth, Iisa, Kristiina, and Dutta, Abhijit. Liquid–Liquid Equilibrium Measurements for Model Systems Related to Catalytic Fast Pyrolysis of Biomass. United States: N. p., 2016.
Web. doi:10.1021/acs.jced.6b00625.
Jasperson, Louis V., McDougal, Rubin J., Diky, Vladimir, Paulechka, Eugene, Chirico, Robert D., Kroenlein, Kenneth, Iisa, Kristiina, & Dutta, Abhijit. Liquid–Liquid Equilibrium Measurements for Model Systems Related to Catalytic Fast Pyrolysis of Biomass. United States. https://doi.org/10.1021/acs.jced.6b00625
Jasperson, Louis V., McDougal, Rubin J., Diky, Vladimir, Paulechka, Eugene, Chirico, Robert D., Kroenlein, Kenneth, Iisa, Kristiina, and Dutta, Abhijit. Wed .
"Liquid–Liquid Equilibrium Measurements for Model Systems Related to Catalytic Fast Pyrolysis of Biomass". United States. https://doi.org/10.1021/acs.jced.6b00625. https://www.osti.gov/servlets/purl/1340649.
@article{osti_1340649,
title = {Liquid–Liquid Equilibrium Measurements for Model Systems Related to Catalytic Fast Pyrolysis of Biomass},
author = {Jasperson, Louis V. and McDougal, Rubin J. and Diky, Vladimir and Paulechka, Eugene and Chirico, Robert D. and Kroenlein, Kenneth and Iisa, Kristiina and Dutta, Abhijit},
abstractNote = {Here in this paper we report liquid-liquid mutual solubilities for binary aqueous mixtures involving 2-, 3-, and 4-ethylphenol, 2-, 3-, and 4-methoxyphenol, benzofuran, and 1H-indene for the temperature range (300 < T/K < 360). Measurements in the water-rich phase for (2-ethylphenol + water) were extended to T = 440 K to facilitate comparison with literature values. Liquid-liquid equilibrium tie-line determinations were made for four ternary systems involving (water + toluene) mixed with a third component; phenol, 3-ethylphenol, 4-methoxyphenol, or 2,4-dimethylphenol. Literature values at higher temperatures are available for the three (ethylphenol + water) systems, and, in general, good agreement is seen. The ternary system (water + toluene + phenol) has been studied previously with inconsistent results reported in the literature, and one report is shown to be anomalous. All systems are modeled with the predictive methods NIST-Modified-UNIFAC and NIST-COSMO-SAC, with generally good success in the temperature range of interest (300 < T/K < 360). This work is part of a larger project on the testing and development of predictive phase equilibrium models for compound types occurring in catalytic fast pyrolysis of biomass, and background information for the larger project is provided.},
doi = {10.1021/acs.jced.6b00625},
journal = {Journal of Chemical and Engineering Data},
number = 1,
volume = 62,
place = {United States},
year = {Wed Nov 02 00:00:00 EDT 2016},
month = {Wed Nov 02 00:00:00 EDT 2016}
}
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