High Selectivities to Ethylene by Partial Oxidation of Ethane
A. S. Bodke,
1
D. A. Olschki,
1
L.
D. Schmidt,
1*
E. Ranzi
2
At least 85 percent selectivity to ethylene at greater than 70 percent conversion can be obtained by partial oxidation of ethane by
adding large amounts of H2 to the reaction mixture and using a platinum-tin catalyst operating at 950°C with a contact time
of ~10
3 seconds. This system almost totally shuts off
the reactions that form undesired CO and CO2, which fall
from 20 percent without H2 to 5 percent when H2
is added. Although a 2/1 H2/O2 mixture should
be explosive at high temperatures, no flames or explosions occur in the
presence of ethane. The successive reactions on the catalyst generate
more H2 than used in the feed, so with recycle no
additional H2 would be needed. These results are unexpected because ethylene is a nonequilibrium product and entropy considerations argue that all reaction channels open at high temperatures so the
products should approach equilibrium, which predicts only a few percent
ethylene. This process is promising for the replacement of steam
cracking in the production of ethylene.
1 Department of Chemical Engineering and
Materials Science, University of Minnesota, Minneapolis, MN 55455, USA.
2 Departmento di Chemica Industriale e Ingegneria
Chemica, Politechnico di Milano, Milan, Italy.
*
To whom correspondence should be addressed.