The kinetics of ethylene epoxidation network were studied experiment
ally over a cesium-dopedsilver cat
alyst supported on
![](/images/gifchars/<font color=)
alpha.gif" BORDER=0>-Al
2O
3 pellets in a differenti
al reactor. A variety of rate functionswere considered and among these, expressions based on a du
al-site Langmuir-Hinselwoodmechanism:
ri =
kiPE![](/isubscribe/journ<font color=)
als/iecred/39/i07/eqn/ie990939xe10001.gif">/(1 +
![](/isubscribe/journ<font color=)
als/iecred/39/i07/eqn/ie990939xe10002.gif">
PE)
2, fitted the data best with an average error of 13.0 and10.7% for the epoxidation and the complete combustion reactions, respectively. Under theexperiment
al conditions, both reactants influence both reaction rates; however, product influenceis negligible because of their sm
all parti
al pressures present in the reactor. High oxygen/ethyleneratios and lower temperature favored selectivity to the epoxidation reaction. The kineticparameters obtained from the differenti
al reactor experiments were refined to match the fixed-bed reactor experiments. With this, the average error in predicting both ethylene conversionand selectivity to ethylene oxide was 4.3%. The apparent activation energies for the epoxidationand combustion reactions were 60.7 and 73.2 kJ/mol, respectively.