Metathesis of 1-hexene over a WO3/SiO2 catalyst in a gas-phase fixed bed reactor.
The performance of a WO3/SiO2 catalyst has been investigated for the metathesis of 1-hexene in an isothermal, gas-phase fixed bed tubular reactor between 420-500°C and at latm. The reactor was fabricated from stainless steel and was placed in an electric tube furnace. The study focused on the effect...
| Main Author: | |
|---|---|
| Other Authors: | |
| Language: | en |
| Published: |
2008
|
| Subjects: | |
| Online Access: | http://hdl.handle.net/10413/896 |