Abstract
This article presents the findings of our research regarding the supercritical water gasification of a real biomass, olive mill wastewater, with Ni/Al2O3 and Ru/Al2O3 catalysts. The experiments were performed at five reaction temperatures between 400 and 600 °C, for five reaction times ranging from 30 to 150 s and at a constant pressure of 25 MPa. It was seen that the employment of catalysts enhanced the gasification and biofuel production yield, which mainly involved methane and hydrogen. Ni/Al2O3 was selective for hydrogen formation, whereas Ru/Al2O3 favored the formation of methane. The highest calorific value of the produced biofuel was obtained as 56123 kJ/m3 with Ru/Al2O3 at 600 °C and 60 s. Apart from biofuel production, the simultaneous treatment of the wastewater was also accomplished. At elevated temperatures and times, treatment efficiencies greater than 97% based on total organic carbon conversion were reached. Moreover, the kinetic evaluation of the catalytic supercritical water gasification of olive mill wastewater was performed based on first order reaction kinetics.
| Original language | English |
|---|---|
| Pages (from-to) | 155-164 |
| Number of pages | 10 |
| Journal | Renewable Energy |
| Volume | 124 |
| DOIs | |
| Publication status | Published - Aug 2018 |
| Externally published | Yes |
Bibliographical note
Publisher Copyright:© 2017 Elsevier Ltd
Keywords
- Biofuel
- Ni/AlO
- Olive mill wastewater
- Ru/AlO
- Supercritical water