Sammanfattning
Bio-ethanol is well known for its use as a gasoline additive. However, it can be blended in low portions to traditional gasoline although it has a corrosive nature. By taking advantage of modern continuous reactor technology and heterogeneous alumina catalysts, ethanol can be upgraded to 1-butanol in fixed beds. Butanol has more feasible properties as fuel component in comparison to ethanol. Mathematical modeling of reaction kinetics revealed a simple kinetic model could be used to describe the complex reaction process on a Cu/alumina catalyst. The reaction kinetics model is based on five parallel reactions in which ethanol reacts to 1-butanol, acetealdehyde, ethyl acetate, diethyl ether and diethoxyethane, respectively.
| Originalspråk | Odefinierat/okänt |
|---|---|
| Sidor (från-till) | 1425–1429 |
| Tidskrift | Topics in Catalysis |
| Volym | 57 |
| Nummer | 17-20 |
| DOI | |
| Status | Publicerad - 2014 |
| MoE-publikationstyp | A1 Tidskriftsartikel-refererad |
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