Methatesis of Propylene to Ethylene¤
Introduction¤
The methathesis (olefin disproportionation) production of ethylene is a chemical reaction to turn propylene into ethylene and butylene. This disproportionation reaction uses molybdena-alumina catalyst and is affected by temperature and residence time.
ES Model Parameters¤
All the parameters concerning the Metathesis Propylene are listed in the table below.
| entry_key | value | unit | sets | source_reference |
|---|---|---|---|---|
| CO2_A (layer) | 0.557175 | kt/GWh | Towler, Gavin P.; Sinnott, Ray, (2012): "Principles, Practice and Economics of Plant and Process Design" | |
| ETHYLENE (layer) | 1 | - | Towler, Gavin P.; Sinnott, Ray, (2012): "Principles, Practice and Economics of Plant and Process Design" | |
| PROPYLENE (layer) | -3.22581 | - | Towler, Gavin P.; Sinnott, Ray, (2012): "Principles, Practice and Economics of Plant and Process Design" | |
| c_inv | 523 | MCHF/GW | Towler, Gavin P.; Sinnott, Ray, (2012): "Principles, Practice and Economics of Plant and Process Design" | |
| c_maint | 26.2 | MCHF/GW/yr | Towler, Gavin P.; Sinnott, Ray, (2012): "Principles, Practice and Economics of Plant and Process Design" | |
| c_p | 1 | - | Towler, Gavin P.; Sinnott, Ray, (2012): "Principles, Practice and Economics of Plant and Process Design" | |
| gwp_constr | 0 | kt/GWh | Towler, Gavin P.; Sinnott, Ray, (2012): "Principles, Practice and Economics of Plant and Process Design" | |
| lifetime | 25 | y | Towler, Gavin P.; Sinnott, Ray, (2012): "Principles, Practice and Economics of Plant and Process Design" | |
| ref_size | 0.33 | GW | Towler, Gavin P.; Sinnott, Ray, (2012): "Principles, Practice and Economics of Plant and Process Design" | |
| trl | 6 | - | Towler, Gavin P.; Sinnott, Ray, (2012): "Principles, Practice and Economics of Plant and Process Design" |
References¤
| Data Sources |
|---|
| Towler, Gavin P.; Sinnott, Ray. (2012). "Principles, Practice and Economics of Plant and Process Design" |