Abstract
Applications of bio-oil are limited by its challenging properties including high moisture content, low pH, high viscosity, high oxygen content, and low heating value. Separation of switchgrass bio-oil components by adding water, organic solvents (hexadecane and octane), and sodium hydroxide may help to overcome these issues. Acetic acid and phenolic compounds were extracted in aqueous and organic phases, respectively. Polar chemicals, such as acetic acid, did not partition in the organic solvent phase. Acetic acid in the aqueous phase after extraction is beneficial for a microbial-electrolysis-cell application to produce hydrogen as an energy source for further hydrodeoxygenation of bio-oil. Organic solvents extracted more chemicals from bio-oil in combined than in sequential extraction; however, organic solvents partitioned into the aqueous phase in combined extraction. When sodium hydroxide was added to adjust the pH of aqueous bio-oil, organic-phase precipitation occurred. As the pH was increased, a biphasic aqueous/organic dispersion was formed, and phase separation was optimized at approximately pH 6. The neutralized organic bio-oil had approximately 37% less oxygen and 100% increased heating value than the initial centrifuged bio-oil. The less oxygen content and increased heating value indicated a significant improvement of the bio-oil quality through neutralization.
| Original language | English |
|---|---|
| Pages (from-to) | 2164-2173 |
| Number of pages | 10 |
| Journal | Energy and Fuels |
| Volume | 30 |
| Issue number | 3 |
| DOIs | |
| State | Published - Mar 17 2016 |
Funding
This work was funded by the U.S. Department of Energy, BioEnergy Technologies Office, under the CHASE program. The manuscript has been coauthored by UT-Battelle, LLC, under Contract No. DEAC05-00OR22725 with the U.S. Department of Energy.
| Funders | Funder number |
|---|---|
| U.S. Department of Energy | |
| Bioenergy Technologies Office | |
| UT-Battelle | DEAC05-00OR22725 |
